NOVELTY - The new type utility claims have one kind turner comprises one three dimension moving device and used for organic fertilizer and turning wheel device, the three dimension walking device device for sports and three troughs of direction. Using said structure of the utility model is new type by three dimension walking device automatically control disc device for organic fertilizer in storing groove by turning action, no need to manual operation, saves labour arrangement, increase work efficiency. The utility model is new type has simple structure and novel structure, working efficiency high, automatic degree high, effect is obvious.
NOVELTY - Fertilizer comprises humic acid, microorganism, farmyard manure, straw, kitchen garbage produced object, nitrogen fertilizer, phosphate fertilizer, potash fertilizer, micronutrient fertilizer and saline-alkali improvement conditioner. Saline-alkali improvement conditioning agent comprises calcium phosphate, ferrous sulfate, fly ash and phosphorus.    USE - Fertilizer used for planting sweet potato in saline-alkali soil (claimed).    ADVANTAGE - The fertilizer is prepared in a simple and cost-effective manner, reduces soil salt content and pH value, and increases soil organic matter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing straw and farmyard manure and adding 5-6% ferrous sulfate and microorganism to carry out fermentation to obtain fermented product;    (B) mixing kitchen garbage produced object, ferrous sulfate, calcium superphosphate, microorganism and humic acid, and then pelletizing to obtain mixed granule; and    (C) mixing remaining components, and then adding all products and stirring uniformly to obtain final product.
NOVELTY - 3-Hydroxy-2-butanone, ammonium acetate, hydrogen peroxide and water are added to reactor. The content of hydrogen peroxide is 28-33 wt.%. The mixed material in reactor is heated at 80-90 degrees C for 0.8-1.2 hours and cooled to room temperature, to obtain mixed solution. The mixed material is stirred during heating. 1.8-2.1 mol/L Sodium hydroxide solution is added to mixed solution, pH is adjusted to 9-10, cooled to 10-15 degrees C, stirred for 10-20 minutes, crystallized and filtered, to obtain cake. The filter cake is washed with water, to obtain tetramethylpyrazine.    USE - Preparation of tetramethylpyrazine (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of tetramethylpyrazine with yield of 91%, within short period of time.
NOVELTY - Fuel rod from waste soil comprises 58-62 pts. wt. dehydrated waste soil, 38-42 pts. wt. straw, 0.04 -0.06 pt. wt. efficient plant grain, 0.03 kg red phosphorus, and 0.03 kg high potassium permanganate.    USE - Fuel rod.    ADVANTAGE - The fuel rod has high thermal efficiency, which uses agricultural wastes that saves fuel cost and method for cleaning up river and dust.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fuel rod from waste soil comprising mixing dehydrated waste soil using blender, adding and stirring straw, efficient plant grain, red phosphorus, and high potassium permanganate; and charging in molding machine, molding, and drying.
NOVELTY - Reagent comprises specific amplification primers having 18 and 21 nucleobases (SEQ ID NOs: 1-2), given in the specification that are gygtttyggatatgttgg and craaacracccaaacactcac, where the 5' end of the primer having (SEQ ID NO: 2) is labeled with biotin. The sequencing primer comprises 20 nucleobases (SEQ ID NOs: 3), given in the specification that are gatagttygygtttttagaa.    USE - Reagent used for detecting methylation status of MGMT gene promoter (claimed).    ADVANTAGE - The reagent is eco-friendly, has short testing cycle, high specificity, high accuracy and also guide doctors in the treatment of a disease associated with prognosis.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of detecting methylation status of O-6-methylguanine-deoxyribonucleic acid methyltransferase (MGMT) gene promoter, which involves:    (A) extracting deoxyribonucleic acid (DNA) from the sample;    (B) treating the template DNA with bisulfite and recovering by purification;    (C) taking the purified product as a template and performing polymerase chain reaction (PCR) amplification using specific amplification primers (SEQ ID NOs: 1-2);    (D) purifying the single-stranded PCR product and placing in a pyrosequencing instrument; and    (E) obtaining methylation status of the MGMT promoter using a software.
NOVELTY - Zerovalent iron-activated sludge coupling chlorinated hydrocarbons/dioxane composite pollute comprises continuously sending wastewater from the bottom of fixed bed reactor filled with activated sludge containing microorganism, discharging from the top, culturing activated sludge, filling into fixed bed reactor filled with activated sludge containing microorganism, processing, discharging, and degrading trichloroethane and dioxane.    USE - Method for zerovalent iron-activated sludge coupling chlorinated hydrocarbons/dioxane composite pollute (claimed).
NOVELTY - Substrate comprises 60-120 pts. wt. corn straw, 80-160 pts. wt. rice straw, 40-80 pts. wt. cassava residue, 15-30 pts. wt. bagasse, 15-30 pts. wt. farmyard manure, 24-48 pts. wt. plant ash, 5-15 pts. wt. vermiculite, 10-18 pts. wt. potato, 1-2.5 pts. wt. calcium superphosphate, 0.5-1.5 pts. wt. potassium chloride, 0.5-1.5 pts. wt. ferrous sulfate heptahydrate, 4-12 pts. wt. quicklime and 0.1-0.5 pt. wt. biofermentation agent.    USE - The substrate is useful for cultivation of corn (claimed).    ADVANTAGE - The substrate simply and cost-effectively enables soilless cultivation of corn, provides nutritional components to the corn plant, improves quality of corn, is performed environmentally-friendly, and saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the substrate, which involves (a) respectively crushing the corn straw, rice straw, cassava residue, bagasse and farmyard manure to obtain powders having 40-60 mesh size, mixing the powders, stacking and fermenting obtained mixture for 4 hours, crushing the potato, adding crushed potato, calcium superphosphate, ferrous sulfate heptahydrate and biofermentation agent to fermented product, and mixing obtained mixture, (c) mixing plant ash with water to obtain plant ash solution, uniformly mixing the plant ash solution with the mixture obtained in step (b), uniformly stirring obtained mixture, sealing the mixture, and heating and fermenting the mixture at 28-35 degrees C for 25-35 days, and (d) stirring fermented product at 80-120 revolutions/minute (rpm) for 5-8 minutes, adding quicklime and vermiculite powder during stirring process, regulating pH value of obtained mixture, and drying obtained product.
NOVELTY - Method for collecting human excrement, involves collecting the excrement into plastic bottle, which is sealed by bottle cap through a hopper, placing the plastic bottle in a circulating box, taking the excrement as raw materials for generating methane, fertilizers and drugs, delivering the excrement to a special factory, and obtaining corresponding payment.    USE - The method is useful for collecting human excrement (claimed).    ADVANTAGE - The method achieves human disease prevention and reasonable diet.
NOVELTY - Separating and classifying whole-plant corn component, involves pretreating corn straws or corncobs, adding diluted acid to pretreated materials, boiling mixture to obtain glycan solution and plug material, transforming obtained glycan solution to generate functional sugar, dividing plug material as carbon source to prepare biological catalysis transforming agent and high polymer material lignin and derivatives, taking generated solid residue as raw material to transform into bioethanol, and collecting carbon dioxide generated in fermentation process.    USE - The biorefinery integrated method is useful for separating and classifying whole-plant corn component (claimed).    ADVANTAGE - The method promotes rapid expansion of biomass industry, and is economical to perform.    DETAILED DESCRIPTION - Biorefinery integrated method for separating and classifying whole-plant corn component, involves pretreating corn straws or corncobs as raw materials by using extractant to obtain pretreated materials and an extract liquid, adding diluted acid into the pretreated materials, boiling mixture to obtain glycan solution, separating plug material, transforming obtained glycan solution to generate functional sugar, dividing the plug material into A portion and B portion, taking the A portion as a carbon source to prepare biological catalysis transforming agent, transforming the B portion into a high polymer material lignin and derivatives, taking generated solid residue as raw material to transform into bioethanol, taking the extractant and vinasse waste solution generated during production of bioethanol, taking the vinasse as an organic fodder or a fertilizer, and collecting carbon dioxide generated in the fermentation process to obtain food-grade carbon dioxide.
NOVELTY - The utility model claims a novel angle relux mixed stirring and filtering fermentation tank, belonging to fermentation equipment field, the device comprising: a tank body, a stirring device, driving device, a filtering device, relux device, paddle stir leaf generating radial acting force with strong cutting effect, large particle diameter of solid object and dispersing and biogas slurry full mixing, avoiding crusting, bottom liquid extraction under force in tank body in relux screw pump and liquid product flow of circle direction, forming liquid stirring, cutting small effect, which avoids damage to the mechanical stirring crushing material is methane fungus and relux extract biogas liquid spray form a common function, using the biogas slurry and material in fermentation tank full mixing, increase stirring effect, reducing stirring power consume, equipped with two of a discharging port, can in the fermentation tank and biogas slag discharge, increase fermentation efficiency, filter device can save the fermentation raw material, further reducing cost, the utility model is new type structure is simple, suitable operation.
NOVELTY - This utility model claims a multi-parameter gas measuring device comprises single chip machine, single chip machine and power information transmission device connected with the monitoring module and single chip machine and electric connection of the internal message transmission device is set with zigbee coordinator and has zigbee terminal module, monitor module internal is set with output end with the flow rate monitoring device and concentration monitoring device, single chip and liquid crystal display and an audible and visual alarm connected with phase, input end of single chip machine and regulating switch, signal amplifier and power source mutually connected with the input end of signal amplifier and collecting unit power connected, internal acquisition unit set with methane sensor, oxygen sensor, vulcanization hydrogen sensor and carbon monoxide sensor, methane sensor, oxygen sensor, vulcanization hydrogen sensor and carbon monoxide sensor and signal amplifier are electric connected.
NOVELTY - The smart-transformer has an insulating oil deterioration diagnostic sensor (110) for measuring amount of combustible gas present in insulating oil of a smart-transformer body. A database part (140) stores data about temperature characteristic of the combustible gas and combustible gas amount. A workload monitoring sensor (120) measures three-phase current/voltage of the smart-transformer body. A determining unit (130) determines an attention section and an abnormal section about the insulating oil. An alarm part (150) produces an alarm signal when the attention section is determined.    USE - Smart-transformer for use in an electric power sub-station and a smart grid net managing post.    ADVANTAGE - The insulating oil deterioration diagnostic sensor measures the amount of the combustible gas present in the insulating oil of the smart-transformer body, and the workload monitoring sensor measures the three-phase current/voltage of the smart-transformer body so as to effectively perform accuracy about check point of time prediction of the smart-transformer.    DETAILED DESCRIPTION - The combustible gas is hydrogen, acetylene, ethylene, methane, ethane or propane material. An INDEPENDENT CLAIM is also included for a method for performing real-time workload monitoring and insulating oil deterioration diagnosing operations about a smart transformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a smart-transformer. '(Drawing includes non-English language text)'    Insulating oil deterioration diagnostic sensor (110)    Workload monitoring sensor (120)    Determining unit (130)    Database part (140)    Alarm part (150)
NOVELTY - The apparatus (A) has a pair of mount frame (5a) that includes a trolley (3) which is installed in an upper portion of a composting tank which stores livestock dung such that a horizontal displacement is possible and a reciprocation is enabled to right and left in top of a traveling rail (4) from a H-steel. A four shafts screw type stirring housing (1) is provided to suspend down to the trolley and to stir the livestock dung such that an inclination is made possible at 8 degrees with respect to the stirring advancing direction.    USE - Fermentation stirring apparatus of livestock dung used for fermenting and composting livestock farming excretion installed in composting facility.    ADVANTAGE - The running cost is reduced and the fermentation stirring apparatus works economically, since the frequency of a movement in the unit area of the manure tank of the screw type stirring apparatus is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a stirring method using the fermentation stirring apparatus of the livestock dung.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the fermentation stirring apparatus of livestock dung.    Screw type stirring housing (1)    Trolley (3)    Rack rail (5)    Mount frames (5a)    Fermentation stirring apparatus (A)
NOVELTY - A composition comprises porous metal complex (A) which can change structurally with adsorption and thermoplastic resin (B) with density of less than or equal to 1 g/cm3.    USE - A composition for adsorbent, occlusion material and separation material (all claimed).    ADVANTAGE - Gas-adsorption performance, gas occlusion capacity, and gas-separation performance are outstanding.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) adsorbent comprising composition;    (2) occlusion material comprising composition;    (3) separation material comprising composition;    (4) separation process which involves making separation material and mixed gas to contact by 0.01-10 MPa pressure range and using separation material; and    (5) manufacture of porous metal complex which involves molding in heated state the thermoplastic resin at Vicat softening point of less than or equal to 1 g/cm3 and changing structurally with adsorption in which density of molded object is less than or equal to 1 g/cm3.
NOVELTY - Tetrahydro-1H-benzo(d)azepine hydrochloride synthesis involves adding 2-nitrobenzene sulfonylchloride to a solution of 4-chIoro phenethylamine at 0-5 degrees C, and then stirring at 25-30 degrees C for period 10-12 hours to obtain amine compound (II). The obtained amine compound is added to a solution of racemic propylene oxide to obtain a solution of alcohol compound (III). The obtained alcohol compound solution is mixed with thionyl chloride at 45-50 degrees C for 10-12 hours to obtain chloride compound (IV).    USE - Method for synthesizing tetrahydro-1H-benzo(d)azepine hydrochloride for treating obesity.    ADVANTAGE - The method synthesizes tetrahydro-1H-benzo(d)azepine hydrochloride in a simple, precise and eco-friendly manner without using racemic mixture resolution, and expensive, corrosive and inflammable reagents.    DETAILED DESCRIPTION - Tetrahydro-1H-benzo(d)azepine hydrochloride synthesis involves adding 2-nitrobenzene sulfonylchloride to a solution of 4-chIoro phenethylamine at 0-5 degrees C, and then stirring at 25-30 degrees C for period 10-12 hours to obtain amine compound of formula (I). The obtained amine compound is added to a solution of racemic propylene oxide to obtain a solution of alcohol compound of formula (II). The obtained alcohol compound solution is mixed with thionyl chloride at 45-50 degrees C for 10-12 hours to obtain chloride compound of formula (III). The obtained chloride compound is reacted with aluminum chloride in inert atmosphere to obtain azepine compound of formula (IV). The obtained azepine compound deprotected with nosyl group by adding thiophenol to obtain tetrahydro-1H-benzo(d)azepine hydrochloride of general formula (V).
NOVELTY - Generating methane in a biogas plant, comprises fermentation of materials, which are characterized by their mass flow of organic dry substance and which are supplied to a fermentation process, where the stability of the fermentation process is monitored based on indicators. The methane stream formed during the fermentation is adjusted using the mass flow of the organic dry substance at any time to a value, which corresponds to a largest economic profit of the biogas plant determined on the basis of the available data.    USE - The method is useful for generating methane in a biogas plant (claimed).    ADVANTAGE - The method can be performed in an economical and optimal manner, i.e., the plant can be operated with a maximum profit, and thus stability of the biological process can be ensured at any time.    DETAILED DESCRIPTION - Generating methane in a biogas plant, comprises fermentation of materials, which are characterized by their mass flow of organic dry substance and which are supplied to a fermentation process, where the stability of the fermentation process is monitored based on indicators. The methane stream formed during the fermentation is adjusted using the mass flow of the organic dry substance at any time to a value, which corresponds to a largest economic profit of the biogas plant determined on the basis of the available data, where regularly and in a relatively short time intervals at least one of the stability of the fermentation process characteristic parameters are determined and automated or partially automated with the highest priority are considered, and the mass flow of the supplied organic substances is adapted on the basis of an action strategy such that the parameters achieves values which correspond to a stable fermentation process.
NOVELTY - Biogas plant (1) comprises a container containing an input (21) and an output. The container has sacks having bulk material.    USE - Used as biogas plant.    DESCRIPTION OF DRAWING(S) - The drawing shows an overall view of the biogas plant.    Biogas plant (1)    Fermenter (2)    Line (4)    Motor (6)    Input (21)
NOVELTY - A plant (P1) exhibiting artificially down-regulated folylpolyglutamate synthetases (FPGS1) gene expression, where the plant exhibits reduced lignin content, is new.    USE - As plant (P1) exhibiting artificially down-regulated FPGS1 gene expression has reduced lignin content. The method (M2) is useful for improving forage crop or biofuel crop having beneficial trait chosen from increased sugar release, increased forage digestibility, and increased saccharification efficiency. The method (M4) is useful for making commodity product chosen from paper, paper pulp, ethanol, butanol, biodiesel, biogas, silage, carbon fiber, animal feed, and fermentable biofuel feedstock (all claimed).    ADVANTAGE - No suitable example given.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) plant part of the plant;    (2) method (M1) of reducing lignin content in plant;    (3) plant (P2) produced by the method (M1) or its part or seed;    (4) method (M2) of improving forage crop or biofuel crop comprising down-regulating expression of the FPGS1 gene in plant;    (5) plant (P3) produced by the method (M2) or its plant part or seed;    (6) method (M3) of producing plant biomass; and    (7) method (M4) of making commodity product.
NOVELTY - The utility model claims a new energy chemical industry technology area, especially relates to a natural gas in one system and purification device. Purification device comprises for containing the ammine liquid and absorbing tower for the absorption tower is pressed natural gas to the natural gas entering pipe, the gas entering tube and the absorption tower connected, the gas entering tube comprises vertical tube vertical section, said vertical pipe section vertical on the gas entering tube and connected interface edge side of the absorption tower, a top end position of the vertical pipe section is higher than vertical ammine liquid of the absorption tower internal preset liquid level height. More than by structure provided with, when stop running when whole system, the pressure imbalance then result in the ammine liquid backflow enter gas entering pipe, then through ammine liquid connected interface flow into the vertical pipe section vertical gravity factor cannot be raised to the top end of the vertical pipe section vertical to avoid ammine liquid flow to natural gas for other seat and other device enter the tube. The utility model is new application obvious increase of safety and system operation stability and working efficiency.
NOVELTY - Method for at least partially decreasing amount of organic acids in water-based fluid involves adding preset amount of bacteria (B) to the water-based fluid comprising organic acids to at least partially consume the organic acids. The bacteria (B) is chosen from facultative bacteria, spore-forming bacteria, phenol degrading bacteria, denitrifying bacteria, organic acid-degrading bacteria and/or high-temperature bacteria, and organic acids are glycolic acid, malic acid, acetic acid, lactic acid, butyric acid, propionic acid succinic acid, fumaric acid and/or benzoic acid.    USE - Method for partially decreasing organic acids in water-based fluid e.g. desalter wash water, overhead water from atmospheric or vacuum process units, strip sour water, coker water blowdown, cooling water blowdown, boiler water blowdown, oily water sewers, equalization tank water, cleaning solutions used for scale removal, water bottoms from storage tanks, API unit water and/or dissolved gas flotation unit water (all claimed).    ADVANTAGE - The method enables the metabolization of dissolved oxygen, reduction of bacteria amount and degradation of phenols.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water treatment system (10), which has at least one bacterial additive zone (2) comprising the influent wastewater stream, chosen from equalization tank, aeration basin (16) and/or return activated sludge (RAS) line (20), and an effluent wastewater (18) stream flowing out of the water treatment system. The effluent wastewater stream comprises reduced amount of at least one organic acid as compared to an identical effluent wastewater stream without the bacteria (B).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a water treatment system.    Water treatment system (10)    Influent waste water (12)    Aeration basin (16)    Effluent waste water (18)    Return activated sludge line (20)
NOVELTY - Chlamydomonas reinhardtii CrM001 (KCTC12584BP) having enhanced biomass, starch and lipid by gamma -ray radiation, is new.    USE - The Chlamydomonas reinhardtii CrM001 and microbial agent are useful for manufacturing biomass, starch and lipid (claimed) and for bio-energy production.    ADVANTAGE - The Chlamydomonas reinhardtii CrM001 has enhanced biomass, starch and lipid content from nutritional deficiency (nitrogen deficiency) culture conditions, increased cell saturation more than 20% compared to Chlamydomonas reinhardtii CrM001 without gamma -rays irradiation (claimed); contributes as a raw material for various chemical products provided with fuel for transport.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) microbial agent comprising Chlamydomonas reinhardtii CrM001 or its culture liquid; (2) producing starch, comprising culturing Chlamydomonas reinhardtii CrM001 and separating starch from the culture medium; (3) producing lipid, comprising culturing Chlamydomonas reinhardtii CrM001 and separating lipids from the culture medium; (4) producing bioethanol, comprising (a) preparing Chlamydomonas reinhardtii CrM001, separating starch from the culture medium, converting the separated starch to bioethanol; (5) producing biodiesel, comprising (i) preparing Chlamydomonas reinhardtii CrM001, separating lipids from the culture medium, converting the separated lipids to biodiesel.
NOVELTY - Method for preparing organic fertilizer involves (a) mixing wheat straw, crushed water hyacinth, shell powder, and animal manure, adding fermenting agent to mixture, and fermenting mixture, (b) stacking fermented mixture, adding earthworms to stacked material and culturing earthworms, spraying soybean residue and vitamin solution on stacked material, (c) separating earthworms from fermented material to obtain earthworm manure, and (d) adding crushed neem leaves, crushed Blumea balsamifera to earthworm manure, mixing mixture and fermenting mixture.    USE - The method is useful for preparing organic fertilizer for wheat (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer, which provides nutrients required for the growth of wheat, enables plant to absorb element in compound state, and is soluble in soil, and easily absorbed by plants.    DETAILED DESCRIPTION - Method for preparing organic fertilizer involves (a) mixing 50-100 parts wheat straw, 30-50 parts crushed water hyacinth, 10-20 parts shell powder, and 30-69 parts animal manure, adding 1-3 parts fermenting agent to mixture, and fermenting mixture for 20-30 days, (b) spreading fermented mixture obtained in the step (a), until fermented mixture reaches room temperature, stacking fermented mixture into thickness of 20-30 cm, and width of 1-2 m, adding 0.5-30000 earthworms/m2 stacked material, maintaining stacked material at 20-26 degrees C and spraying soybean residue (every day) for 20-30 days, and 10-20 ppm vitamin solution (every 3 days), and culturing earthworms for 20-30 days, (c) separating earthworm from fermented material to obtain earthworm manure, and (d) adding 5-10 parts crushed neem leaves, 2-5 parts crushed Blumea balsamifera to earthworm manure, mixing mixture and fermenting mixture for 10-20 days.
NOVELTY - Preparing catalyst comprises (i) washing abalone shell distilled water, drying at 90-110 degrees C for 12-15 hours, calcining in a muffle furnace at 700-900 degrees C for 3-5 hours, pulverizing and sieving through 160-180 meshes sieve to obtain white powder; (ii) soaking the white powder in anhydrous ethanol at 20-160 degrees C for 2-4 hours; (iii) ultrasonic processing the obtained suspension for 15-20 minutes and stirring for 2-3 hours; (iv) adding sodium silicate into the suspension, stirring, filtering, washing the solid with distilled water and drying.    USE - The method provide catalyst which is useful for producing biodiesel oil (claimed).    ADVANTAGE - The method is simple, economical and easy to operate. The catalyst has biodiesel oil production rate of more than 92% and has good performance of 83% when reused for four times.    DETAILED DESCRIPTION - Preparing catalyst comprises (i) washing abalone shell distilled water, drying at 90-110 degrees C for 12-15 hours, calcining in a muffle furnace at 700-900 degrees C for 3-5 hours, pulverizing and sieving through 160-180 meshes sieve to obtain white powder; (ii) soaking the white powder in anhydrous ethanol at 20-160 degrees C for 2-4 hours; (iii) ultrasonic processing the obtained suspension for 15-20 minutes and stirring for 2-3 hours; (iv) adding sodium silicate into the suspension, where the mass ratio of sodium silicate and white powder is 1-3:100, stirring for 3-5 minutes, filtering, washing the solid with distilled water and drying at 70-90 degrees C for 4-6 hours. An INDEPENDENT CLAIM is also included for the catalyst prepared by the above method.
NOVELTY - Composition comprises microorganisms or their culture broth.    USE - The composition is useful for removing odor or waste (food waste or sewage sludge) decomposition (all claimed), and useful as compost.    ADVANTAGE - The composition has excellent effect on odor removal by efficiently decomposing ammonia, hydrogen sulfide and mercaptan generated during fermentation decomposition, has throughput of 95% by decomposing moisture and salinity contained in organic waste having halophilic, eosinophilic and thermophilic properties, and has high energy efficiency which is exhibited at optimum growth temperature (relatively low temperature of 35-40 degrees C) and self-heating up to 80 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for removing odor or waste decomposition, comprising spraying the composition on waste.
NOVELTY - Composite microbial fertilizer liquid culture medium comprises 62-68 pts. wt. edible brown sugar, 5-6 pts. wt. black beans, 5-6 pts. wt. leaf and twig of fruticose breynia, 1-2 pts. wt. salt, 0.01-0.02 pts. wt. cobalt chloride , 5-6 pts. wt. ammonium sulfate, 4-5 pts. wt. hide glue, 0.5-1 pts. wt. potassium dihydrogen phosphate, 0.5-1 pts. wt. dipotassium hydrogenphosphate, 4-5 pts. wt. composite amino acid powder, 2-3 pts. wt. lime, 0.5-1 pts. wt. multi-vitamins and 0.5-1 pts. wt. magnesium sulfate.    USE - The liquid culture medium is useful in fruits and vegetables and cash crops cultivation fields.    ADVANTAGE - The liquid culture medium is clear, rich in nutrients, and economical; has raw materials having wide source of physical and chemical factors; can meet the nutritional requirements of bacteria, actinomycetes, yeasts and fungi class; and improves the product quality. The method solves excess production of single microorganism species in composite microbial agent-containing liquid fermentation medium; and is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing liquid culture medium, comprising (i) grinding soy beans, and soaking in warm water, filtering through 150 mesh, to obtain filtered dregs; (ii) dissolving edible brown sugar, salt, ammonium sulfate, magnesium sulfate, potassium dihydrogen phosphate, dipotassium phosphate, composite amino acid powder and cobalt chloride in cold water; (iii) dissolving hot hide glue at 100 degrees C, and stirring to melt; (iv) adding leaf and twig of fruticose breynia with cold water, and completely stirring uniformly; (v) dissolving lime by adding cold water, adding the solution into a closed container, carrying out continuous sterilization at 121 degrees C for 1 hour, cooling to room temperature, and adding aqueous solution of composite vitamin under aseptic conditions, and stirring, to obtain the final product.
NOVELTY - Capsule comprises 120-150 pts. wt. Stemona japonica, 120-150 pts. wt. rehmanniae, 120-150 pts. wt. ophiopogon root, 150-180 pts. wt. loquat leaf, 40-60 pts. wt. bitter almond, 200-240 pts. wt. Fritillaria thunbergii bulb, 40-60 pts. wt. radix peucedani, 40-60 pts. wt. shizandra berry, 40-60 pts. wt. liquorice and 1-2 pts. wt. chlorphenamine maleate.    USE - The capsule is useful for treating cough (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the capsule comprising: (a) crushing Fritillaria thunbergii bulb and chlorpheniramine maleate, respectively into powder; (b) adding bitter almond, radix peucedani and shizandra berry into 80 wt.% ethanol, extracting twice (each time for 2 hours), adding 8 times of ethanol, mixing extract, filtering to obtain filtrate and dregs, recycling ethanol, concentrating to relative density of 1.25-1.30 to clear paste; (c) adding dreg and Stemona japonica, rehmanniae, ophiopogon root, loquat leaf and liquorice, adding 8 times of water, decocting for 3 times (each time for 1.5 hours), mixing decoction, filtering to obtain filtrate and dregs, concentrating to relative density of 1.25-1.30 to clear paste; and (d) mixing two clear paste and Fritillaria thunbergii bulb powder, drying, grinding, adding chlorpheniramine maleate powder, granulating and loading into capsule to obtain the product.
NOVELTY - The utility model claims a a a a a a a water decomposing hydrogen and oxygen in the device, a solar energy collecting device (1), a solar energy collecting device and energy conversion device (2) connected with the energy conversion device and the electrolytic device (3), the electrolytic device through a pipe. (4) and a hydrogen storage device (5) and oxygen storage device (6) connected with, on the pipe provided with a pump (7). The utility model is a beneficial effect is, a reasonable design, energy saving effect is good.
NOVELTY - The device has a hydrogen water storage tank that stores hydrogen water ejected in hydrogen dissolution unit (40) which is connected to magnesium contact unit (20) dissolves hydrogen in hydrogen water flowing through connection line. The connection line in which hydrogen water ejected in magnesium contact unit flows and enhances hydrogen concentration of hydrogen water. The magnesium contact unit which is contacted with magnesium filter enhances hydrogen concentration of hydrogen water. A hydrogen water supply line (13) is connected to hydrogen water generating unit.    USE - Device for manufacturing high concentration hydrogen water used in beverage, health care, cosmetics and agriculture.    ADVANTAGE - The hydrogen water is produced by using electrolysis magnesium contact unit and hydrogen dissolution unit, such that hydrogen concentration of hydrogen water is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for manufacturing high concentration hydrogen water.    Hydrogen water generating unit (10)    Hydrogen water supply line (13)    Magnesium contact unit (20)    Micro bubble production unit (30)    Hydrogen dissolution unit (40)
NOVELTY - This utility model new supply of one with a biogas digester with heating device, marsh gas belongs to technology area. It solves the later of organic object and fermentation in the biogas digester, need for manual work and from pool take out it, cleaning it and not suitable, which wastes equal technology problem. Marsh gas pool of the belt heating device, comprising internal cavity and comprises pool body, pool body upper part is set with with pool cover, pool body middle part formed with the cavity inside for pool body is divided into left cavity and the right cavity clapboard, pool body two side wall are set with outwards inclined is inclined face, middle part clapboard hinged with working plate, working plate of the left cavity, upper working plate is provided with, working plate the other end extending to the side wall of pool body position, and the working plate end can drive the upper and lower lifting and lifting structure connection, upper part is set with clapboard recovery port, upper recycling port is in the working plate, upper clapboard hinged with can also make recovery port closed by the door plate, the left inner cavity also set with heating device. This new utility model has fast cleaning, is suitable.
NOVELTY - Medicinal fertilizer comprises A: 5-20% active extract of Areca catechu nuts and/or pumpkin seed, where the relative density of active extract is 1.03-1.07, B: 1-5% polysorbate 80, and 0.5-2% sodium dodecylbenzenesulfonate, and C: balance of water.    USE - The fertilizer is useful for preventing and controlling plant pathogenic nematode (claimed).    ADVANTAGE - The fertilizer has multi-functional eco-friendly fertilizers, is environmentally-friendly, and effectively reduces highly toxic pesticides.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use method of medicinal fertilizer, comprising diluting the medicinal fertilizer for 1-10 times, and directly irrigating crop after planting.
NOVELTY - A soil conditioner comprises 3-7 wt.% enzyme, 5-9 wt.% sintered plastic shell powder and 80-90 wt.% red clay. The fermented plastic shell is obtained by fermenting plastic shell powder and pulverizing.    USE - Conditioner is used for mudflat soil (claimed).    ADVANTAGE - The soil conditioner is environmentally-friendly and has high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of soil conditioner.
NOVELTY - The device has centre shaft (130) which is fixed with membrane portion. Membrane portion is provided between air chambers (120a,120b). Regulating and control valve (200) is provided with valve sleeve provided with separating plate. Upper portion of valve sleeve is provided with air inlet groove with left and right air grooves. Air chamber is provided with sliding sleeve connected with piston rod connected with piston baffle plate. Control shaft is provided with heave portions. Air grooves are connected with discharge channel and separately connected with air chamber.    USE - Energy-saving type liquid extraction device.    ADVANTAGE - The automatic extraction of slurry is performed using the biogas-power instead of manual operation. The pneumatic diaphragm pump efficiently extracts the liquid containing particles, so that the blocking problem during extraction of the liquid is eliminated efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy-saving type liquid extraction device.    Pump (100)    Liquid cavities (110a,110b)    Air chambers (120a,120b)    Centre shaft (130)    Regulating and control valve (200)
NOVELTY - This utility model relates to a marsh gas pool, belonging to the marsh gas engineering field. A heat preservation marsh gas pool, comprising biogas pool main body, said marsh gas pool main body is interlayer structure, set with air inlet and air outlet in the marsh gas pool main body outer under side, the temperature induction device is set on the air outlet end. Compared with the prior art, this utility model has the following advantages: the marsh gas pool by the weather change and no influence, and it can better produce marsh gas.
NOVELTY - This new utility model claims a novel marsh gas tank, comprising organic matter pool, the upper pool is set with organic matter with separating pipe and marsh slag pipe, the separating pipe the other end set with separator, the marsh slag pipe the other end set with biogas residue storage pool, the pool one side provided with organic matter with regulating pool pipe, regulating the other end set with regulating pool pipe pool, regulating pool the other end set with regulating tube, the regulating pipe the other end set with heat exchanger, on the separator set with marsh gas pipe and gas pipe, the gas pipe the other end set with liquid storage box, the liquid storage box is set with bottom with heat output pipe, the output heat pipe the other end set with heat pump, the heat pump heat pump through pipe and heat exchanger connected with together, the utility model new structure design reasonable, can carry out industrial production, not only sealing performance, but also is easy to converying and installation, suitable operation, a slag is simple, the raw materials are fermented, biogas generated can supply enough people use, one is a kind of green environmental protection device.
NOVELTY - This utility model claims a device for fast preparing biological nitrogen by using simulate month of soil as filler The device comprises biologic film Anaerobic ammonia oxidation reactor, the reactor comprises the third phase separator and reaction area, the reaction area is filled with simulation lunar particle, the three phase separator upper part the reaction zone, reaction zone and constant temperature circulation water bath connected with realize constant temperature control. For digested sludge and Anaerobic ammonia oxidation sludge is composed of the mixed sludge added with a small amount of UASB reactor, then adding particle diameter is 2-4 mm, the specific gravity is 75/202/2, average inner friction angle is 33.3 stimulate the lunar soil grain, low closeness in light-shielding condition, for monitoring waste water pump enter continuous UASB reactor for culturing start up. This new utility model has simple structure, easy implementation, monitoring lunar soil filler is added to retain sludge, the biological amount to the inside of Anaerobic ammonia oxidation reactor, which is good for rapid start up biological membrane Anaerobic ammonia oxidation process for preparing nitrogen.
NOVELTY - This utility model claims a marsh gas manufacturing system, comprising section for marsh gas pool of pot shape, wherein said marsh gas pool is embedded in side of step-shaped floor of high order, the marsh gas pool is set with pot nozzle with one buffer in the feedstock and the buffering cavity end and discharge end of one stirring pool connected with the side stirring pool is set with with pulverizer, the discharging end of the pulverizer extending to the stirring tank, in marsh gas pool set with one discharging pipeline, the discharging pipeline comprises one trumpet suction mouth slag, the slag discharging pipeline extending to one slag containing groove in the inner of slag containing groove embedded in the low level side of the step-shaped floor, marsh gas pool side of wall is also set with one arrange liquid pipeline, a liquid discharging pipeline dividing two path output, one path is connected with import and the circulation pump, the circulation pump outlet through circulation pipeline extending to upper part of the stirring pool, another one connected to irrigating pipeline, this utility new type can make dejecta, sewage, the garbage collective get in marsh gas pool, carrying out to manufacture marsh gas, and discharging the liquid can used for cultivating fish or irrigation.
NOVELTY - The utility model claims a of a biologic reactor of a BOD online analysis, comprising main control module, temperature control module, controlling a pH value, culturing box, a box, a main control module and a MSP430F149 single chip machine as core processor, a control module via the main control module a command signal controlling temperature of a tank, a pH control module accept main control module used for a command signal controlling pH value of culture tank, culturing tank and a test box is set with a water pump with a transfusion pipe connected with. The utility model is a new device can be fast and determine a value of BOD in water, any chemistry medicament added, green environmental protection, suitable and practical.
NOVELTY - Collecting excessive biogas through biogas collection system comprises (i) connecting gas storage plate of biogas fermentation system to air inlet of biogas collection system, conveying biogas into pump cavity, using airflow channel to ensure that air guide cylinder is slidably connected to upper and lower ends of gas guiding piston, (ii) driving the gas guiding piston to install at the upper end of piston connecting rod to move upwards, setting annular gas groove on the piston connecting rod, and (iii) moving the gas guiding piston downwards, and separating the annular groove and the airbag.    USE - The method is useful for collecting excessive biogas through biogas collection system (claimed).    DETAILED DESCRIPTION - Collecting excessive biogas through biogas collection system comprises (i) connecting gas storage plate of biogas fermentation system at the top part to an air inlet of biogas collection system, conveying biogas into a pump cavity, using an airflow channel to ensure that air guide cylinder is slidably connected to upper and lower ends of gas guiding piston, (ii) since the lower end of the gas guiding piston area is larger than the upper end of the area, under atmospheric pressure condition, when axial force of the gas guiding piston is more than its original gravity, driving the gas guiding piston to install at the upper end of piston connecting rod to move upwards, setting an annular gas groove on the piston connecting rod connected to an external air bag, and (iii) when axial force of the gas guiding piston is less than its original gravity, moving the gas guiding piston downwards, and separating the annular groove and the airbag.
NOVELTY - Recombinant Trichoderma reesei strain-containing artificial zinc finger transcription factor, having a preservation number of CGMCC NO. 10649, is new.    USE - The recombinant Trichoderma reesei strain is useful in biomass degradation (claimed).    ADVANTAGE - The recombinant Trichoderma reesei has increased cellulase activity of up to 35%, enzyme activity reaching up to 8.4 units/ml, and beta -glucosidase content reaching up to more than 3.5 times and activity reaching up to 8.8 units/ml than wild type C30 strain; and utilizes microbial resources during biomass degradation.
NOVELTY - Surfactant producing Bacillus tequilensis FJAT-14262a (CGMCC NO: 1073) is new.    USE - Used as surfactant producing Bacillus tequilensis FJAT-14262a.    ADVANTAGE - The strain is environmentally friendly, non-toxic or low toxic, reduces biological surfactant raw material cost, and produces surfactant having characteristic of reducing the surface tension.
NOVELTY - Enzyme based biological pretreatment to improve the residual sludge produced short-chain fatty acid comprises e.g. allowing to stand wastewater treatment plant obtained residual activated sludge and concentrating, adding proteinase K to the concentrated sludge, subjecting resulting product for hydrolysis reaction, stirring, inoculating the hydrolyzate in anaerobic granular sludge, subjecting resulting product to alkaline sludge pretreatment, adjusting the pH, subjecting resulting product for anaerobic fermentation, stirring continuously to produce short-chain fatty acids.    USE - The method is useful for enzyme based biological pretreatment to improve the residual sludge produced short-chain fatty acid (claimed).    ADVANTAGE - The method makes acid-producing microorganisms strict anaerobic bacteria and enrich Clostridium, and reduce the proportion of facultative microbes, and improves acid production rate and acid production substrate.    DETAILED DESCRIPTION - Enzyme based biological pretreatment to improve the residual sludge produced short-chain fatty acid comprises (i) allowing to stand wastewater treatment plant obtained residual activated sludge and concentrating, adding proteinase K to the concentrated sludge, where the proteinase K concentration is 0.004-0.04 U/gVSS, (ii) subjecting step (i) resulting product for hydrolysis reaction at 30-40 degrees C, stirring at a rate of 100-200 revolutions/minute for 2-48 hours, under the conditions of hydrolysis, inoculating the inoculum hydrolyzate in anaerobic granular sludge, anaerobic granular sludge is thickened sludge mass of 8-15%, (iii) subjecting step (ii) resulting product to alkaline sludge pretreatment, adjusting the initial pH value to 8-12, and (iv) subjecting step (iii) resulting product for anaerobic fermentation at 30-40 degrees C, stirring continuously under anaerobic fermentation conditions at 100-200 revolutions/minute for 1-12 days to produce short-chain fatty acids.
NOVELTY - The bottle has a sleeve body (1) connected with a hanging ring (2). A cotton thread part is bundled with an iron silk part (3).    USE - Environmental protection medicine transfusion bottle.    ADVANTAGE - The bottle is simple in structure, easy to use and inexpensive. The bottle ensures environmental protection process and reduces medical personnel working difficulty.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an environmental protection medicine transfusion bottle.    Sleeve body (1)    Hanging ring (2)    Iron silk part (3)
NOVELTY - A KIT-6 type polydimethylsiloxane(PDMS) composite film comprises 60-64.5 mass% polyvinylidene fluoride (PVDF) base membrane and 32.3-34.9 mass% PDMS prepolymer, where surface of the PVDF base membrane is coated with 0.7-8 mass% KIT-6 type mesoporous material, sieve surface of the mesoporous material is hydrophobic and aperture is 5.5-7.75 nm, and ratio of the PDMS film and the mesoporous material is 2-25%.    USE - KIT-6 type PDMScomposite film for separating organic steam, n-butane/nitrogen, propylene/nitrogen and acetone/nitrogen.    ADVANTAGE - The composite film has better permeationcoefficientand high separation factor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing KIT-6 type polydimethylsiloxanecomposite film for separating organic steam.
NOVELTY - Scraper comprises organic material storage bin, high temperature aerobic fermentation tank, vibration sieve roller, vibration machine and granulator. High temperature aerobic fermentation tank comprises stirrer (5), and tank body (11) having feeding port (1), discharge port (9) and exhaust port. Tank is made of steam heating layer having steam import and steam outlet (13), and temperature sensor. Stirrer has rotating shaft, hollow vertical pipe and hollow transverse pipe. Hollow transverse pipe is fixed on rotating shaft. Outer wall of hollow vertical pipe has oxygen injector.    USE - Scraper.    ADVANTAGE - The scraper ensures easy organic waste disposal, good sterilization and environmental protection.    DETAILED DESCRIPTION - Scraper comprises organic material storage bin, high temperature aerobic fermentation tank, vibration sieve roller, vibration machine and granulator. High temperature aerobic fermentation tank comprises stirrer, and tank body having feeding port, discharge port and exhaust port. Tank is made of steam heating layer having steam import and steam outlet, and temperature sensor. Stirrer has rotating shaft, hollow vertical pipe and hollow transverse pipe. Hollow transverse pipe is fixed on rotating shaft. Outer wall of hollow vertical pipe has oxygen injector. Rotating shaft and motor output shaft are connected to sterilizing filter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of scraper.    Feeding port (1)    Stirrer (5)    Discharge port (9)    Tank body (11)    Steam outlet (13)
NOVELTY - The method involves cleaning and draining initial gas flow, and cooling the gas with the use of refrigerant. The compression and expansion of nitrogen are performed to increase the pressure of nitrogen. The heat exchanging of low and high pressure nitrogen and the liquefied gas is performed. A refrigerant pre-cooling circuit is used for further cooling the flow of high pressure nitrogen by maintaining working parameters of main cooling circuit, in order to ensure 100 percent liquefaction and super-cooling of natural gas without formation of gaseous phase.    USE - Method for liquefying natural gas.    ADVANTAGE - The refrigerant pre-cooling circuit is used for further cooling the flow of high pressure nitrogen by maintaining working parameters of main cooling circuit, so as to ensure 100 percent liquefaction and super-cooling of natural gas without formation of gaseous phase.
NOVELTY - The station has a hydrolysis chamber (3) located in an inferior part of hydrolysis deposit (1) and a methanogenesis deposit (2), and producing phase of hydrolysis and acidogenic of an organic substrate. A methanogenesis chamber is located in a superior part of deposit of hydrolysis and methanogenesis. A control system drives and/or activates a remote control valve, a sifting part (6) and a crushing part (5). A hydrolysis gas conduction part is connected with another hydrolysis chamber through a hydrolysis gas entrance.    USE - Station for processing an organic substrate for production of biogas from organic matter of residues generated in a small industry, a farm and a hotel.    ADVANTAGE - The control system drives and/or activates the remote control valve, a sifting part and the crushing part, thus reducing greenhouse gas spills in industries and carbon track in a chain of agro-industrial production, diminishing dependancy of agriculture of mineral installments and increasing fertility of grounds and productivity of cultures.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a station for processing an organic substrate for production of biogas from organic matter of residues.    Hydrolysis deposit (1)    Methanogenesis deposit (2)    Hydrolysis chamber (3)    Crushing part (5)    Sifting part (6)
NOVELTY - Twin chambered in-vessel composting apparatus comprises composting chambers with body portion, at least one sidewall from bottom, and top with lid; air distribution system positioned in-between composting chambers with interconnected ducts with valves, blower and suction device; blower device outlet coupled to inlet line of air distribution system; suction device inlet coupled to outlet line of the air distribution system; and leachate recirculation pump and wastage line with valve provided at the bottom of each chamber to remove excess leachate.    USE - Twin chambered in-vessel composting apparatus used for passive and active compositing (claimed).    DETAILED DESCRIPTION - Twin chambered in-vessel composting apparatus comprises composting chambers with body portion, at least one sidewall from bottom, and top with lid; first composting chamber for receiving the waste material and second composting chamber for harvest compost material; air distribution system positioned in-between composting chambers with interconnected ducts with valves, blower and suction device; blower device outlet coupled to inlet line of air distribution system for positive aeration by blowing air to composting chambers; suction device inlet coupled to outlet line of the air distribution system, and outlet line further including carbon filter and polyethylene filter before suction device; and leachate recirculation pump and wastage line with valve provided at the bottom of each chamber to remove excess leachate.
NOVELTY - Method for determining withaferin A from rat plasma by high performance thin layer chromatographic technique (HPTLC) involves (a) selecting plants comprising withaferin A, where the selected plant is authenticated and extracted, (b) selecting animals and administering defined dose of extracts, (c) collecting blood sample from animals, and (d) detecting withaferin A in blood plasma.    USE - The method is useful for determining withaferin A from rat plasma by HPTLC (claimed). The determined withaferin A is used for analyzing herbal medicine.    ADVANTAGE - The method enables to determine withaferin A in a cost-effective and environmentally-friendly manner.
NOVELTY - Biological fermentation of organic sewage comprises adding organic sewage into Pantoea agglomerans and Enterobacter amnigenus, and stirring.    USE - Method for biologically fermenting organic sewage.    ADVANTAGE - The method is simple, reduces waste liquid permeability, does not need filter device, saves cost and saves time.
NOVELTY - Biologic removal of heavy metal in organic sewage comprises adding organic sewage with gram-negative fungus, and stirring uniformly.    USE - Method for biologic removal of heavy metal in organic sewage (claimed).    ADVANTAGE - The method has simple operation and good effect. It reduces waste liquid permeability on earth, does not need filter device, saves cost, and saves time.
NOVELTY - Biologic deodorization of organic sewage comprises adding deodorant and Bacillus cereus into organic sewage, and stirring.    USE - Method for biologic deodorization of organic sewage (claimed).    ADVANTAGE - The method is simple, reduces waste liquid permeation to atmosphere, does not need filter device, saves cost and saves time.
NOVELTY - Biologic absorption of organic matter in organic sewage comprises adding organic sewage with aquatic microbacteria, and stirring uniformly.    USE - Method for biologic absorption of organic matter in organic sewage (claimed).    ADVANTAGE - The method is simple, reduces waste liquid permeation on earth, does not need filter device, saves cost, and saves time.
NOVELTY - Preparation of biogas and municipal sludge comprises putting the municipal sludge into dry anaerobic fermentation tank, and from steam boiler to dry anaerobic fermentation pot into steam, dry municipal sludge anaerobic fermentation, and anaerobic fermentation to produce biogas and sludge fermentation; anaerobic fermentation of modified sludge conditioning and dewatering, drying and pulverizing to obtain dry sludge powder; mixing the dry sludge powder with sediment and extruding the brick building; and drying and calcining the sludge to obtain a sintered brick.    USE - Method for preparing biogas and municipal sludge used for producing sintered brick (claimed).    ADVANTAGE - The method has no secondary pollution.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for preparing biogas and municipal sludge (Drawing includes non-English language text).
NOVELTY - Fertilizer comprises 80-100 pts. wt. cow dung, 30-40 pts. wt. brandy, 200-300 pts. wt. straw, 30-40 pts. wt. urea, 20-30 pts. wt. monoammonium phosphate, 10-20 pts. wt. potassium chloride, 3-7 pts. wt. zinc sulfate, 2-6 pts. wt. magnesium sulfate, 5-9 pts. wt. ferrous sulfate, 3-5 pts. wt. borax, 2-4 pts. wt. chlorothalonil and 6-10 pts. wt. medicinal preparation.    USE - Fertilizer used for lettuce plant (claimed).    ADVANTAGE - The fertilizer enhances disease resistance ability of lettuce.
NOVELTY - Culture material comprises 10-20 pts. wt. sawdust, 35-40 pts. wt. corn cob, 10-20 pts. wt. bagasse, 15-25 pts. wt. wheat bran, 3-8 pts. wt. corn flour, 2-7 pts. wt. bean pulp, 30-40 pts. wt. Pleurotus eryngii residue, 8-12 pts. wt. dairy manure, 9-12 pts. wt. corn stover, 1-5 pts. wt. calcium carbonate, 1-5 pts. wt. lime, 2-3 pts. wt. gypsum, 1-5 pts. wt. compound fertilizer, 2-6 pts. wt. calcium superphosphate and 11-20 pts. wt. bentonite. The pH value of culture material is 7.5-8 and water content of culture material is 65-68%.    USE - Culture material used for cultivating edible mushroom (claimed).    ADVANTAGE - The culture material ensures improved yield, color and nutritional value in low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing culture material, which involves:    (A) mixing sawdust, corn cob, bagasse, wheat bran, corn flour, bean pulp, Pleurotus eryngii residue, dairy manure and corn stover for 5 minutes;    (B) mixing additive with obtained mixture;    (C) stirring remaining materials with obtained mixture;    (D) fermenting obtained mixture at 62-65 degrees C for 8-10 hours; and    (E) introducing air in fermented material at 35-45 degrees C for 12 hours to obtain culture material.
NOVELTY - Organic composite fertilizer comprises 12-20 pts. wt. potato plant powder, 6-10 pts. wt. fermented seaweed grain, 4-8 pts. wt. banana fruit peel powder, 6-8 pts. wt. potassium nitrate, 6-8 pts. wt. potassium sulfate, 3-5 pts. wt. calcium hydrophosphate, 10-15 pts. wt. urea, 13-15 pts. wt. bentonite, 0.2-0.4 pts. wt. sodium borate and 4-8 pts. wt. poultry excrement grain.    USE - Organic composite fertilizer used for planting potato (claimed), sweet potato, cassava and Chinese yam.    ADVANTAGE - The organic composite fertilizer promotes plant growth, and ensures good nutrient element absorption, long-term use and increased yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic composite fertilizer, which involves mixing raw materials, where obtained mixture is granulated and then granules are coated.
NOVELTY - Organic composite fertilizer comprises 15-20 pts. wt. mushroom fungus slag, 7-10 pts. wt. pine forest surface soil grain, 5-8 pts. wt. corn straw grain, 3-4 pts. wt. silkworm, 0.1-0.2 pts. wt. potassium sulfate, 0.2-0.3 pts. wt. potassium dihydrogen phosphate, 1.0-1.15 pts. wt. urea, 0.01-0.02 pts. wt. sodium borate, 3-5 pts. wt. plant ash and 60-80 pts. wt. distilled water.    USE - Organic composite fertilizer used for growth of lettuce (claimed).    ADVANTAGE - The organic composite fertilizer enhances plant root system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic composite fertilizer, which involves:    (A) crushing mushroom with a pulverizer and drying;    (B) harvesting corn straw for 10-12 days, mixing components and fermenting anaerobic fermentation for 30-45 days, and filtering to obtain filtered liquid; and    (C) drying the filtered liquid by airing to obtain final product.
NOVELTY - Compound fertilizer comprises 40-60 pts. wt. rotten chicken manure, 30-45 pts. wt. plant ash, 2-4 pts. wt. borax, 8-10 pts. wt. ferrous sulfate, 25-40 pts. wt. canal mud, 50-60 pts. wt. colza cake, 10-30 pts. wt. furfural residue, 15-20 pts. wt. shell powder, 12-18 pts. wt. ammonium phosphate, 15-24 pts. wt. urea, 10-15 pts. wt. silkworm excreta, and 1-1.5 pts. wt. water-retaining agent.    USE - Compound fertilizer used for increasing yield of pomegranate (claimed).    ADVANTAGE - The compound fertilizer is economic, and increases harvest peiod of pomegranate.
NOVELTY - Processing threonine-based fermentation liquor, comprises (i) preparing threonine crystals, and mother liquor; (ii) preparing protein granules; (iii) preparing chicken feed; and (iv) preparing fertilizer.    USE - The method is useful for processing threonine-based fermentation liquor (claimed).    ADVANTAGE - The method completely utilizes yeast liquid component, does not produces waste, is environmental friendly, and converts waste into useful materials.
NOVELTY - Preparation of botanical algicide comprises extracting Macleaya and/or small Macleaya pod using anhydrous methanol or ethanol.    USE - Method for preparing botanical algaecide (claimed).    ADVANTAGE - The algaecide restrains growth of algae and removes algae in water body. It is environment-friendly, and has good biological safety.
NOVELTY - Preparation of protein feed comprises taking tomato waste slag and bran, mixing, adding water, uniformly mixing to obtain fermentation matrix mixture; inoculating Trichoderma viride and Aspergillus niger in potato dextrose agar (PDA) liquid culture medium, activating to obtain liquid-I; mixing liquid-I with fermentation matrix, fermenting to obtain solid fermented product; activating Candida utilis yeast in culture medium to obtain liquid-II; mixing solid fermented product with liquid-II, fermenting; and drying.    USE - Method for preparing protein feed (claimed).    ADVANTAGE - The feed has high protein content.    DETAILED DESCRIPTION - Preparation of protein feed comprises taking tomato waste slag and bran at a weight ratio of 85:15, mixing, adding water, uniformly mixing to obtain fermentation matrix mixture, where mixture contains 35-55 wt.% fermented matrix and balance water; inoculating Trichoderma viride and Aspergillus niger in potato dextrose agar (PDA) liquid culture medium, activating at 28 plus minus 0.5 degrees C for 36-60 hours to obtain liquid-I, where weight ratio of Trichoderma viride and Aspergillus niger is 1-3:2-5; mixing 5-10 wt.% liquid-I with fermentation matrix, fermenting in natural temperature for 1-3 days to obtain solid fermented product; activating Candida utilis yeast in culture medium at 28 plus minus 0.5 degrees C for 6-18 hours to obtain liquid-II; mixing solid fermented product with 5-10 wt.% liquid-II, fermenting in natural temperature for 3-5 days; and drying to a water content of 15-20%.
NOVELTY - Processing residues generated during composting process of organic wastes, comprises (a) fermenting the organic wastes, and collecting the residues in one place by collecting the debris generated during screening, (b) introducing the collected residues into a crusher, and crushing the residues, (c) spheroidizing the residues adhered with oil by adding wastewater generated during processing organic waste into the crushed product, and (d) introducing the spheroidized crushed product into a pellet machine, and solidifying the residues into pellet form by compressing.    USE - The method is useful for processing residues generated during composting process of organic wastes (claimed).    ADVANTAGE - The method reduces energy consumption, and is environmentally friendly and economical.
NOVELTY - A rain water purification treatment microbial filter bed comprises bed body for absorbing microorganism flora and filtering, and processing rainwater/sewage, microorganism fungus filter bed, microorganism fungus filter bed supply device connected to supply gear pump (4) and hollow pipe (2).    USE - Rain water purification treatment microbial filter bed.    ADVANTAGE - The filter bed is low-cost and has improved treatment efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of rain water purification treatment microbial filter bed.    Hollow pipe (2)    Supply gear pump (4)
NOVELTY - Producing biogas involves pouring fermentation material into inner discharge port for biogas fermentation. The biogas is placed into the inner cylinder through the inlet. The gas piston is provided to maintain pressure. The effective area of the bottom (S1) is greater than above the effective area (S2). The piston overcomes the elastic force of the air spring, and make upward movement. The gas spring release elastic energy when the pressure inside the cylinder decreases. The annular groove and the air balloon are removed, when piston rod moves downward.    USE - Method for producing biogas (claimed).    ADVANTAGE - The method enables to produce biogas by saving energy.    DETAILED DESCRIPTION - The thrust is representd by formula F=P(S1-S2), where F is thurst and P is pressure. An INDEPENDENT CLAIM is included for methane fermentation system, which comprises ferment pool body, air board, partition board, inner separating board, gas plate, feeding port and discharging port.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of methane fermentation system.    Fermentation pool body (10)    Discharging port (14)    Stirring groove (16)    Storage plate (20)    Separating plate (30)
NOVELTY - Producing organic fertilizer using agricultural waste comprises adjusting the agricultural waste in high nitrogen containing material, then adjusting low nitrogen containing material to the carbon and nitrogen ratio of the agricultural waste, adjusting agricultural waste water content, inoculating decayed microbial agent, fermenting for 7-9 days, and then granulating.    USE - The fertilizer is useful in field of agricultural production.    ADVANTAGE - The method produces product with good particle size, is easy to apply, and increase crop yields of about 30%.
NOVELTY - Special fertilizer and its preparation method are claimed. The special fertilizer comprises 5.5 pts. wt. bacterial enzymes, 30 pts. wt. bean pulp, 28 pts. wt. rabbit manure, 22 pts. wt. cassava residue, 31 pts. wt. protein mud and 37 pts. wt. water. The fertilizer is prepared by stirring the weighed components at 50 degrees C in a sealed tank and fermenting the mixture for 50-80 days, drying the fermented mixture at 70 degrees C, granulating and crushing the dried mixture and packing.    USE - The special fertilizer is useful for crop (claimed).    ADVANTAGE - The special fertilizer is environmentally-friendly.
NOVELTY - Preparing crop organic fertilizer, comprises taking 10.5 pts. wt. effective microorganism (em) probiotics, 26 pts. wt. mushroom waste residue, 35 pts. wt. plant ash, 28 pts. wt. wheat bran, 31 pts. wt. worse vinegar and 34.5 pts. wt. water, mixing components, stirring at 50 degrees C, fermenting in a sealed tank for 50-80 days, drying at 70 degrees C, granulating using a granulator and packing.    USE - The method is useful for preparing crop organic fertilizer (claimed).    ADVANTAGE - The fertilizer is environmentally friendly.
NOVELTY - Soil conditioning agent comprises 100-500 pts. wt. organic humic acid of concentration 45%, 0.5-2 pts. wt. ferrous sulfate, 8-100 pts. wt. polyglutamic acid, 15-150 pts. wt. polyaspartate, 1-50 pts. wt. earthworm powder, 12-180 pts. wt. shell powder, 10-50 pts. wt. soybean meal, 1-10 pts. wt. amino oligosaccharins, 10-30 pts. wt. attapulgite powder and 10-20 pts. wt. microbial complex. Microbial complex comprises Trichoderma, Aspergillus niger, Aspergillus oryzae, Streptomyces powder, Bacillus amyloliquefaciens and Saccharomyces cerevisiae.    USE - Soil conditioning agent.    ADVANTAGE - The soil conditioning agent ensures improved absorption of heavy metal in soil and improved physical and chemical property of soil and fertility of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil conditioning agent, which involves:    (A) fermenting raw material at 60 plus minus 5 degrees C for 16 hours;    (B) adding soybean meal and microbial complex to fermented product; and    (C) crushing and drying obtained mixture to obtain final product.
NOVELTY - Microbial agent comprises Bacillus thuringiensis (KCCM11562P) as first morning A strain, B.simplex (KCCM11563P) as first morning B strain, Lysinibacillus xylanilyticus (KCCM11564P) as first morning C strain, B.methylotrophicus (KCCM11565P) as first morning D strain, Debaryomyces polymorphus (KCCM11566P) as first morning E strain, and Mucor circinelloides (KCCM11567P) as first morning F strain.    USE - The microbial agent and method are useful for decomposing organic sludge. The organic sludge is food waste, sewage sludge or milk sludge (all claimed).    ADVANTAGE - The microbial agent rapidly decomposes organic sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for decomposing the organic sludge, which involves culturing the above-mentioned microorganisms to obtain microbial agent, mixing the microbial agent with the organic sludge, and subjecting obtained mixture to fermentation.
NOVELTY - The venous set has a guide slot formed in an inner side of a three-way valve (170) that is equipped in a sap tube. A fluid path is guided in a guide projection part (176) that is fixed in an upper portion and a lower part of a valve body (170a). An operating knob (174) is formed in a chamber body and a sealing cap. The valve body is arranged in branches (171, 172) that are connected to a drip chamber. A hinge shaft is inserted into the guide slot that is formed in an outer periphery of the sap tube. A fixed stopper is equipped with a tooth form.    USE - Venous set for supplying sap to a patient.    ADVANTAGE - The venous set improves assembling structure of the operating knob so as to manipulate rotation of the three-way valve of the of the valve body and improve switching process of the fluid path. The venous set intensifies fastening force so as to improve assemblability with an allophone assembly of the sap tube with the three-way valve. The venous set provides an environment-friendly medical appliance.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective and sectional views of a venous set.    Three-way valve (170)    Valve body (170a)    Branches (171, 172)    Operating knob (174)    Guide projection part (176)
NOVELTY - Eye drop comprises 5-15 g sea tangle, 5-15 g dendrobe, 7-12 g sodium chloride, 0.3-0.7 g ethyl hydroxybenzoate, 0.2-0.5 g vitamin B2 and 0.2-0.5 g vitamin C.    USE - The eye drop is useful for treating senile cataract (claimed), softening hardness to dissipate stagnation, purifying cloudy lens and nourishing lens, and inhibiting or delaying the onset of age-related cataracts.    ADVANTAGE - The eye drop is rich in medicinal raw material, safe, cost-effective and easy to use, and reduces surgical treatment rate of senile cataract.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing eye drop, which involves (a) washing sea tangle and dendrobe, chopping the washed materials, soaking the chopped materials for 2 times (each time for 24 hours), where the chopped materials are soaked in 300-400 ml 95% alcohol and then in 200-300 ml 95% alcohol, filtering the mixture, combining the filtrates, and recovering alcohol from the filtrate, (b) adding sodium chloride, ethyl hydroxybenzoate, vitamin B2 and vitamin C to the filtrate obtained in step (a), mixing at room temperature to completely dissolve, regulating osmotic pressure with distilled water that is equivalent to osmotic pressure of 0.8-1.2 sodium chloride concentration, filtering the precipitate, and adjusting the pH value to 7, and (c) filtering the solution through ultrafilter with 10 k molecular weight cutoff membrane, filling with nitrogen gas, encapsulating, sterilizing solution at 110-120 degrees C for 20-30 minutes, and packing 8 ml finished product per bottle.
NOVELTY - Method for preparing fertilizer, involves (a) preparing Dosidicus gigas broth by performing enzymolysis, (b) preparing Saccharina japonica broth by performing enzymolysis, (c) mixing D.gigas broth and S.japonica broth, inoculating nitrogen fixing bacteria, Bacillus licheniformis and effective microorganism into mixture, adding water, cattle manure, corn stalks, wheat straw, urea and glucose to mixture, mixing mixture and fermenting mixture, and (d) drying fermented mixture, crushing, packing and storing product.    USE - The method is useful for preparing fertilizer for potato (claimed) for promoting growth of potato.    ADVANTAGE - The fertilizer increases protein content of potato and is rich in amino acid, protein and nutrient content.
NOVELTY - An agriculture organic base fertilizer comprises 1200-1800 pts. wt. crop residues, 800-1200 pts. wt. sugar cane bagasse, 500-800 pts. wt. sugar filtered mud, 500-800 pts. wt. pond sludge, 1500-2000 pts. wt. animal manure, 30-60 pts. wt. phosphate fertilizer, and 30-60 pts. wt. composite bacteria.    USE - Agriculture organic base fertilizer.    ADVANTAGE - The agriculture organic base fertilizer is safe, environment-friendly, non-polluting, and non-toxic, and has no side effect. The method is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of agriculture organic base fertilizer comprising mixing crop residues, sugar cane bagasse, sugar filtered mud, pond sludge, animal manure, phosphate fertilizer, and composite bacteria, covering with plastic sheeting, heating, drying, fermenting for 1 month, turning, mixing, pouring 0.2 wt.% aqueous urea solution, covering with film, and standing for 1 month.
NOVELTY - Preparation of coin-shaped copper nicotinate micromaterial comprises preparing 30 mM/L copper nitrate aqueous solution at room temperature to obtain stock solution, taking 5-15 mL copper nitrate solution into bottle, adding 5-15 mL ultra-purified water, heating to boil, adding 10-30 mL 0.1-0.3 M/L nicotinic acid, magnetically stirring while keeping boiling state until color of solution is pale blue, precipitating solid, centrifuging, discarding supernatant, removing unreacted nicotinic acid reducing agent, cleaning precipitate, discarding supernatant, repeating for 3-4 times and drying.    USE - Method for preparing coin-shaped copper nicotinate micromaterial used as catalyst for degradation of p-nitrophenol wastewater (claimed).    ADVANTAGE - The copper nicotinate has particle size of 3-9 mu m, wall thickness of 1-5 mu m and hollow intermediate portion with quadrangle, hexagon or octagon shape. The copper nicotinate catalyst has high efficiency, simple and easy operation and synthesis, and high yield.    DETAILED DESCRIPTION - Preparation of coin-shaped copper nicotinate micromaterial comprises preparing 30 mM/L copper nitrate aqueous solution at room temperature to obtain stock solution, taking 5-15 mL copper nitrate solution into bottle, adding 5-15 mL ultra-purified water, heating to boil, adding 10-30 mL 0.1-0.3 M/L nicotinic acid, magnetically stirring at speed of 30-70 revolutions/minute (rpm) while keeping boiling state until color of solution is pale blue, precipitating solid, centrifuging at speed of 6000-7500 rpm for 10-15 minutes, discarding supernatant, removing unreacted nicotinic acid reducing agent, cleaning precipitate, discarding supernatant, repeating for 3-4 times and drying.
NOVELTY - The kitchen and agriculture waste after preparing the liquid fertile manufacturing device of food and agriculture waste liquid fertile after manufacture of the new utility model claims use of food and agriculture waste fast ferment in organic fertile and device, comprising: removing food and agriculture waste odour oil dividing separating, crushing, removing food and agriculture waste device and foreign matter (1), kitchen and using agriculture waste pre-treatment device (1) handle (70), and using food and agriculture waste pre-treatment device (1) processing organic fertile manufacturing the organic fertile manufacturing device (140). The utility model is new kitchen and using agriculture waste fast ferment in organic fertile device in removing odour after separating rough impure object and oil dividing separating, crushing and removing small or object, using the food and agriculture waste can be fast in liquid fertile and organic fertile, again using food and agriculture processing waste resources, not make food and agriculture waste pollute underground and ocean, to protect environment.
NOVELTY - The utility model relates to a recovery processing device for ecological agriculture, comprising fermentation pool, burning pool and storage tank, fermentation pool comprises an outer pool body and an inner pool body, inner pool body processes small straw and incombustible straw, generated marsh gas is stored in gas storage cavity between inner pool and outer pool for burning large straw in burning and household use, slag generated in fermentation pool and ash generated after burning in burning pool are discharged to material type storage, can be used as farmland fertilizer, the device not only solves farmland waste treatment, but also turns the waste into treasure and returns to farmland as fertilizer.
NOVELTY - Preparation of nicosulfuron (I) involves reacting (2E)-3-(dimethlyamino)prop-2-enal (II) and 2-cyano-N,N-dimethylacetamide (III), and reacting obtained N,N-dimethyl-2-sulfamoylpyridine-3-carboxamide (IV) with 4,6-dimethoxypyrimidin-2-amine (V) in the presence alkyl carbonate (VI).    USE - Preparation of nicosulfuron (claimed).    ADVANTAGE - The method is continuous, safe, environmentally-friendly, does not use toxic phosgene or polymers as in isocyanate method, and toxic reagents, such as chlorocarbonylamine and ethyl chloroformate, and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - Preparation of nicosulfuron of formula (I) involves reacting (2E)-3-(dimethlyamino)-prop-2-enal of formula (II) and 2-cyano-N,N-dimethylacetamide of formula (III), and reacting obtained N,N-dimethyl-2-sulfamoylpyridine-3-carboxamide of formula (IV) with 4,6-dimethoxypyrimidin-2-amine of formula (V) in the presence of alkyl carbonate of formula (VI).    R=methyl, ethyl, phenyl, benzyl and t-butyl.
NOVELTY - The new type utility claims have droppings organic chemical process equipment, comprising fermentation tank, the fermentation tank top part set with main motor, transmission motor, upright post and enter hopper, the enter hopper bottom set with transmission belt wheel, a hopper enter one side set with energy storage device, the energy storage device lower end set with transmission motor, the fermentation tank outside enter one end set with hopper ladder, the ladder top part set with sun shield, upper end two side equipped with straight ladder with protection plate, said the top of column end set with solar energy photoelectric plate, on the solar energy photoelectric plate set with two of solar energy collecting device, the utility model is new type structure using modern advanced manufacturing technique and manufacturing, simple operation, using suitable, it can make body and livestock excrement equal substance into internal process processing process, thus production out of high-quality organic fertilizer, relieving have environmental pollute, increase have resource use rate, equipment operation and low cost, can be used in animal husbandry and cultivation equal work.
NOVELTY - The new type utility claims have droppings fermentation composting device, comprising fermentation tank, supporting frame, and ladder distribution under the fermentation device end set with pedestal, the top end set with enter hopper, set with guardrail; the supporting frame top end set with slider, said slider through control line connected with transmission motor, supporting frame two side over square set with baffle plate, the support frame upper end set with stench absorbing machine, lower end set with bracket, on the bracket set with groove, the utility model is new type structure design can make animal body and excrement equal organic waste by Anaerobic fermentation to make conversion is energy of other form and the corresponding crop fertilizer, equipment operation, operation cost is low, effect is good, the conversion to environment and human without dangerous, can widely applied to breeding equal organic waste and waster processing.
NOVELTY - The biogas recovery system has a harmless treatment pool that is connected with aerobic fermentation pool. A filter pool is connected with a negative pressure concentration reactor and a harmless treatment pool. The negative pressure concentration reactor is connected with the filter pool and the network distribution pool. The negative pressure concentration reactor is set with a Chinese medicine adding device that is connected with a metering and weighing device and is set with a stirrer.    USE - Biogas recovery system.    ADVANTAGE - The liquid compound fertilizer can effectively retains the active component in the biogas liquid, provides variety of essential trace elements in natural complex state, provides enzymes and plant growth hormone peptides, and promotes the growth of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing liquid compound fertilizer using biogas recovery system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the biogas recovery system. (Drawing includes non-English language text)
NOVELTY - In one heating plant type organic fertilizer fermentation bed, it comprises fermentation bed (1), insulating plate (2), pipe (3), electric heating belt (4), convex edge (5), wherein the fermentation bed set on floor (1), wherein fermentation bed (1) internal of lower bottom in turn equipped with insulating plate (2), horizontal pipe (3), wherein pipe (3) is set with electric heating belt (4) or connecting hot water circulation, and in fermentation bed (1) and front, rear edge set with convex edge (5). The utility model is new type of beneficial effect is: fermentation time and using fertilizer of greatly shortened, organic fertilizer to obtain mass increase, which is good for carrying out harmless of agriculture, at the same time, but also reducing have to livestock waste and pollute environment.
NOVELTY - The new type utility claims have one kind automatic sludge treatment system, said system comprises matrix array in the fermentation pool and a discharging pool, shift by travelling crane, for self-motion, buffer bin, a conveyor, a mixing machine, mixing front conveyor, a sludge conveyor, auxiliary material feeding machine and turn machine finish mixing and transporting fill material in the pool, by air blower and deodorizing device realize the aerobic fermented material and discharge gas harmless discharging, the processing process comprises the following control in the PLC controller, after the sludge and complement material will deliver to mix in fermentation pool, sludge and auxiliary material after fermentation in fermentation in pool, again by the PLC controller control, shift of travelling crane and the material after self-motion for discharging machine for fermentation deliver to discharge pool. The system and the automatic processing process with automatic level high, it can save manpower and material resources, material fermentation full, uniform, fermentation effect, short period, it will not generate second time pollute, it will not cause environmental pollute, can continue production, low energy consumption.
NOVELTY - The utility model is new type relates to one kind turning is easy to discharge fertilizer throwing circle machine, comprising power cabin, power cabin fixedly connected with internal power supply of motor, power cabin upper end set and motor phase matching with the rotating disk, upper end motor shaft rotate through power cabin upper wall and rotating plate and rotating plate fixedly connected with the rotary plate on the hinge connected with the centrifugal force for fertilizer extrusion formation by uniform particle size and polishing circular bucket, internal polishing circular bucket set with connected with lead screw, inner lead screw connected with the bottom and polishing the round bucket bottom fixedly connected. The utility model is new type of one kind is easy to discharge fertilizer turning round polishing machine by funnel on bucket cover bottom mounted lighting device, suitable night use and maintain a circular polishing machine, and bucket cover on top end equipped with solar energy battery, it is more energy saving and environment-friendly, but also for polishing round bucket hinge connected on rotating disc on the fixing seat by fixing, no influence on normal use and under suitable condition raw material, greatly simplify operation steps and improve production efficiency.
NOVELTY - A one process intensification cultivating Anaerobic reaction tank of cattle excrement, Anaerobic reaction tank except the layer design has jacket structure, Anaerobic reaction tank provided with internal stirring, the stirring plate of stirring plate main pole, end stirring, stirring rod and stirring plate wing plate composed of pole, main pole fixed on stirring at rotation axis, adjacent stirring between main pole angle is 30 to 90 degrees, the rotating shaft end provided with two sealing ring, and through bearing and connected with the tank body. Anaerobic reaction tank using the horizontal design, longer diameter than is 1: 1 to 4. The jacket and Anaerobic reaction tank body in interval is 20 to 40 mm. The stirring end section is round or oval. Anaerobic reaction tank using the jacket design, for Anaerobic reaction tank provide heat energy, using material heated uniformly, using multi-stirring plate cross the whole structure design, effective increase stirring efficiency, make organic matter metabolism more thoroughly.
NOVELTY - The utility model provide an organic fertilizer processing device using pig manure as raw material, it has a fermentation tank, a belt transporting machine, the raw material sieving mechanism, a stirring mechanism, a spiral transporting machine, weighing machine, wherein, ferment tank entrance and material separation machine connected with, to fermentation tank outlet set with belt transport mechanism, a belt transporting machine output end inclined lifting mechanism and a sieving mechanism connected with the raw material, the raw material through transmitter and sieving raw material stirring machine connected with the raw material stirring machine spiral transporting machine and a weighing mechanism connected with, the scheme and structure is simple, the automatic degree high, use effect is good.
NOVELTY - The new type utility claims have A one casing reaction liquid circulation again using system, comprising a reaction kettle, sediment tank, a filtering device, a neutralizing device, drying device and separating device, the reaction kettle and sediment tank connected, said sediment tank and filtering device connected, the filter device and device and connection, the neutralizing device and drying device connected, the drying device and separating device connected, the filter device and the reaction kettle connected. The casing because of reaction liquid circulation again using system using filtering device, and device, separating device and drying device in turn by re-processing process, can active the reaction liquid and filtering again after use, can at the same time the residue of reaction liquid and after production for organic fertilizer, which greatly reduce have production cost, reducing have environmental pollute, and can the waste again using, increase have production benefit.
NOVELTY - The new type utility claims have ocean biological fungus fertilizer high-efficient generator, comprising shell and set in internal shell and inner shell, wherein the inner shell near bottom provided with bi-direction packing auger, packing auger part bi-direction rotating leaf is clockwise, rotating leaf part is anticlockwise, bi-direction and different rotating to the auger vane near intersection is provided with parallel arranged above the power cutter and thermal transfer, in transfer hot hob comprises can containing the hot liquid and cavity, cavity through pipeline connected with can to heat-conducting liquid temperature control by the temperature control part. The utility model is new type with production efficiency high, temperature control effect is good, the homogenizing effect is good.
NOVELTY - An energy-saving environmentally-friendly S type fertilizer production device, wherein the target is that the integration degree is high, little power consumption, low cost, the utility model comprises a big particle storehouse, small particle storehouse, finished product bin, grain bin,, gear, drum, air preheater, air inlet pipe, coal combustion nozzle, elevator, a spiral propeller, a vibration ball, blade propeller, filter screen and small particle filter screen, a draught fan, a drum outside drum, the transfer drum and inner drum, elevator a. install a grain cabin, the other end extends into the inner inner drum, inner drum installed with inner spiral propeller blade and propeller, inner drum front end opening, transfer drum back end open mouth, to drum discharging port installed with big and small particle filter screen, filter screen of big cabin provided with a big particle filter screen outside, provided with small particle cabin side of a small particle filter screen, a small particle chamber equipped with finished product cabin, drum and transfer drum are installed with a vibration ball, coal combustion nozzle install a drum rear end, a pre-heater install on coal combustion nozzle, air inlet tube and air pre-heater connected with.
NOVELTY - The pool has retting pool main structure whose bottom portion is set with inclined structure and top portion is mounted with top seal of sun panel curved roof (2). A separating mechanism (3) is provided to separate upper and lower portions of sunlight greenhouse. A bottom portion of sunlight greenhouse is mounted with light absorbing film. A marsh gas collecting room is connected to ignition room. The sunlight greenhouse is arranged with heat inlet and heat outlet that are connected to circulation pipeline (5). One end of retting pool main structure is set with discharging mouth (1).    USE - Bulk straw organic fertilizer automatic retting pool.    ADVANTAGE - The bulk straw organic fertilizer automatic retting pool is provided with simple operation efficiency, high reliability and low manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bulk straw organic fertilizer automatic retting pool.    Discharging mouth (1)    Sun panel curved roof (2)    Separating mechanism (3)    Circulation pipeline (5)
NOVELTY - Fertilizer comprises 60-70 pts. wt. organic fermentation product, 15-20 pts. wt. fucoidin, 8-12 pts. wt. amino acid chelate manganese, 4-6 pts. wt. zinc sulfate, 12-18 pts. wt. amino acid chelate iron, 12-16 pts. wt. ammonium molybdate, 5-8 pts. wt. selenomethionine, 0.5-1 pts. wt. humic acid, 3-6 pts. wt. copper sulfate, 0.05-0.08 pts. wt. biochemical fulvic acid, 0.02-0.04 pts. wt. amino acid chelate calcium, 4-6 pts. wt. lysine, 0.05-0.08 pts. wt. chitin, 4-6 pts. wt. yeast, 0.2-0.5 pts. wt. mushroom protein polysaccharide and 0.5-1 pts. wt. S-induced resistance factor.    USE - Fertilizer used for planting paddy (claimed).    ADVANTAGE - The fertilizer ensures strong stress resistant, cold resistant, disease resistant, crop water-logging resistant and drought resistant, and regulates plant growth.    DETAILED DESCRIPTION - Fertilizer comprises 60-70 pts. wt. organic fermentation product, 15-20 pts. wt. fucoidin, 8-12 pts. wt. amino acid chelate manganese, 4-6 pts. wt. zinc sulfate, 12-18 pts. wt. amino acid chelate iron, 12-16 pts. wt. ammonium molybdate, 5-8 pts. wt. selenomethionine, 0.5-1 pts. wt. humic acid, 3-6 pts. wt. copper sulfate, 0.05-0.08 pts. wt. biochemical fulvic acid, 0.02-0.04 pts. wt. amino acid chelate calcium, 4-6 pts. wt. lysine, 0.05-0.08 pts. wt. chitin, 4-6 pts. wt. yeast, 0.2-0.5 pts. wt. mushroom protein polysaccharide, 0.5-1 pts. wt. S- induced resistance factor, nitrogen-fixing bacteria, cellulose decomposing fungus and 6-12 pts. wt. Rhizobium bacteria.
NOVELTY - Chinese herbal medicinal fertilizer comprises 15-22 pts. wt. Bacillus subtilis, 11-13 pts. wt. Curcuma zedoaria, 18-25 pts. wt. hyacinth beans, 15-25 pts. wt. Astragalus mongholicus, 10-11 pts. wt. rhizoma arisaematis, 1-3 pts. wt. Eclipta prostrata, 1-4 pts. wt. Zanthoxylum bungeanum, 2-3 pts. wt. Stellera chamaejasme and 3-7 pts. wt. rosin.    USE - Chinese herbal medicinal fertilizer (claimed).    ADVANTAGE - The fertilizers increases yield of cultivated crops, is cost-effective, and effectively prevents soil salinization.
NOVELTY - Tomato plant bioenzymatic organic fertilizer comprises 15-20 pts. wt. cellulase, 35-45 pts. wt. amylase, 8-12 pts. wt. glucanase, 8-12 pts. wt. Bacillus subtilis, 8-12 pts. wt. xylanase, 8-12 pts. wt. chymosin, 2-4 pts. wt. protease, 8-15 pts. wt. ammonium bicarbonate, 8-15 pts. wt. potassium nitrate, and 5-10 pts. wt. copper sulfate.    USE - Tomato plant bioenzymatic organic fertilizer (claimed).    ADVANTAGE - The tomato plant bioenzymatic organic fertilizer achieves ecological agriculture on a large scale.
NOVELTY - An enzyme fertilizer comprises 16-25 pts. wt. dodder seed, 15-13 pts. wt. Chrysanthemum, 20-24 pts. wt. jujube, 16-24 pts. wt. plant soot, 10-15 pts. wt. Gallus gallus, 1 pt. wt. pectin lyase, 1 pt. wt. pectinesterase, 1 pt. wt. subtilisin and 1 pt. wt. cellulase.    USE - Enzyme fertilizer is used for Dolichandra unguis.    ADVANTAGE - The enzyme fertilizer is economical, and prevents soil salination.
NOVELTY - Special Chinese herbal biofertilizer comprises 15-27 pts. wt. radix rehmanniae, 12-13 pts. wt. Ampelopsis japonica, 20-32 pts. wt. herba lycopi, 15-32 pts. wt. gadfly, 10-12 pts. wt. Schizonepeta, 1 pt. wt. pectate lyase, 2 pts. wt. aspartic protease, and 1 pt. wt. pectinase.    USE - The special Chinese herbal biofertilizer is useful for enriching calcium content in vegetables (claimed).    ADVANTAGE - The special Chinese herbal biofertilizer increases crop yield, and controls alkalinity of soil.
NOVELTY - Preparing clopidogrel hydrogen sulfate involves providing 2-bromo-2-chlorophenyl acetic acid methyl ester and 4,5,6,7-tetrahydrothieno(3,2,c) pyridine hydrochloride as raw materials. The appropriate amount of sodium bicarbonate and clopidogrel bisulfate derivative are added in chiral ionic liquid for 1-10 hours at 20-100 degrees C. The reaction solution is cooled to 20-25 degrees C and appropriate amount of methylene chloride is added. The solution is warmed to 60-65 degrees C for 6 hours and then naturally cooled to 20-25 degrees C.    USE - Method for preparing clopidogrel hydrogen sulfate (claimed).    ADVANTAGE - The method enables to prepare clopidogrel hydrogen sulfate that is easy to operate, eco-friendly, cost-effective and has good efficiency.    DETAILED DESCRIPTION - Preparing clopidogrel hydrogen sulfate involves providing 2-bromo-2-chlorophenyl acetic acid methyl ester and 4,5,6,7-tetrahydrothieno(3,2,c) pyridine hydrochloride as raw materials. The appropriate amount of sodium bicarbonate and clopidogrel bisulfate derivative of formula (I) are added in chiral ionic liquid for 1-10 hours at 20-100 degrees C. The reaction solution is cooled to 20-25 degrees C and appropriate amount of methylene chloride is added. The solution is warmed to 60-65 degrees C for 6 hours and then naturally cooled to 20-25 degrees C. The methylene chloride solution is separated and cooled in an ice-salt bath to (-5 degrees C)-0 degrees C. The concentrated sulfuric acid is added drop-wise to the solution. The solution is stirred, filtered and dried to obtain clopidogrel bisulfate product of formula (I).    R=1-10C alkyl group; and    L-=hydroxyl ion.    .
NOVELTY - Complex microbial population comprises 5-7 wt.% nitrifying microorganisms and 10-15 wt.% polyphosphate-accumulating organisms (PAO), where the nitrifying microorganisms are Nitrospirae, and the PAOs are Bacteroidetes, and apparatus for sewage treatment comprises anoxic tank for processing under anoxic environment, anaerobic tank for processing under anaerobic environment, and aerobic tank for processing under aerobic environment.    USE - The complex microbial population is used in sewage disposal method (claimed).    ADVANTAGE - The complex microbial population reduces total phosphorous concentration of sewage water to less than 0.2 mg/l.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage disposal method.
NOVELTY - The utility model is new type supply one A kitchen waste compost, the kitchen waste compost, set with hopper, crushing machine, spiral transport machine, fermentation tank, and oil water separating tank, the lower hopper provided with the crushing machine, in the crushing machine provided with crushing cutter, the spiral transport machine located on the crushing machine downstream, of inclined connected with the fermentation tank for transport pipe, the spiral transport machine below with pipeline connected with the oil water separation tank. When using, the kitchen garbage and solid garbage and generating part of fertilizer in fermentation tank, the may flower cultivating plant vegetable of use, after then kitchen waste and liquid part and carrying out oil water separation, lipid decomposing and deodorizing device through forming lyophilic treatment substance, then with water discharging, using the kitchen waste oil to be the raw material, then air deodorizer and lipid decomposing using the deodorizing device, can make whole machine without ozone sum product and avoids pollute environment.
NOVELTY - The utility model is new type supply A A family kitchen waste composting machine, internal of the compost machine with separated inner container for collecting chamber and mixing chamber of upper part and lower part, the upper part of the mixing chamber provided with garbage entrance, and header using a closeness, lower part of the mixing chamber provided with the inner container, and the inner container bottom and collection chamber connected and provided with leakage mouth, on bottom in the inner container is adhered with heating strip, also provided with temperature sensor inside on box body, also set with one of its bend stick and stirring in the mixing chamber, the stir stick and stirring motor connection. When using, each time the kitchen garbage, at the same time also the wooden meal and soda ash, after stirring uniformly, heating strip and temperature sensor and work, in case the temperature for constant on predetermined value range in, can make garbage generating degradation reaction mixture following at preset temperature, pH, transformation as fertilizer. The utility model is new type product in kitchen garbage and source location for carrying out the purification process, has high social benefit.
NOVELTY - The new type utility claims have one A composting device, especially claims one kind used for compost of household kitchen garbage, belonging to household environment-friendly device design manufacture technology field. A plant can provide effective and shorten the stacking time, obvious reducing environment pollute degree is used for household kitchen waste and compost device. The compost device comprises bracket, for storage and mixing mechanism, storage for the installation on the upper of bracket, wherein the storage of the kitchen garbage storage fermentation by the mixing machine is in the middle of storage for mixing uniformly after, again retting fermentation heap as fertilizer and the storage in fermenter.
NOVELTY - The utility model is new type relates to, claims have A compost device for plant, wherein the compost device comprises vertical cylinder, vertical top part set with sealing cover, upper cover set with hopper for the vertical cylinder set in the whole multi-separating board with vertical distribution and, wherein the discharge door comprises: mounting in compost device and bottom separating board and moving door plate, compost device outside the vertical cylinder set with motor, output shaft on the motor is set with gear, on said moving door plate set and the gear matched with the rack.
NOVELTY - The utility model is new type relates to composting device claims have one kind of vertical multi-layer aerobic biological compost device. The device comprises vertical cylinder, vertical top part set with sealing cover, upper cover set with hopper for the vertical cylinder set in the whole multi-separating board with vertical distribution of the multi-separating board for vertical dividing number is more, the whole of each interlayer plate set with discharging door at the upper vertical set with at the same time through out of the sealing cover and outside end part of rotate shaft, rotate shaft of said multi-separating plate set with one driving motor, rotate shaft with multi-set of stirrer and the multi-number corresponding to the interlayer, one side vertical outside is set with at the same time connected with the multiple layers of the blast pipe, another side set with at the same time connected with the multiple layers of the air pipe. The device capable of regeneration using each series and organic solid waste, reducing occupied square meter of compost device. For ensuring municipal environment, pushing area economic development with the important theory and practice significance.
NOVELTY - The utility model is new type relates to stirring machine, especially relates to one kind compost with stirrer. The stirrer comprises hollow rotating shaft, vertical to the connected hollow rotate shaft is hollow pipe, hollow pipe below connected with hollow harrow teeth, harrow teeth side back hollow formed with out wind hole. The stirrer can give full material oxygenation, fermentation speed increase.
NOVELTY - The new type utility claims have one kind livestock and poultry waste processing device, comprising supporting base, upper supporting base set with the waste fermentation cylinder, inside the waste fermentation cylinder through out of stirring rotating shaft, one end provided with the stirring shaft rotate through the waste fermentation cylinder is connected with drive motor, another end the stirring rotate shaft is connected with supporting sleeve along the axial direction distribution with multiple stirring blade stirring the rotate shaft at the one end the waste fermentation cylinder is set with blower nozzle, another end the waste fermentation cylinder is provided with an air outlet, the air outlet to set with air purifier, the air outlet and the air purifier between set with draught fan, upper part of the waste fermentation cylinder provided with waste feeding port, lower part of the fermentation cylinder is set with fermentation waste discharging mouth, bottom of the waste fermentation cylinder provided with electromagnetic heating pipe. The utility model is new type whole structure design is reasonable, realize effective is good for comprehensively use the waste resource and is suitable for popularization and application.
NOVELTY - Portable hydrogen-rich water rod comprises elongated strip rod body installed with electrolysis apparatus responsible for producing hydrogen-rich water, upper rod (1) with hook, and lower rod (2) set with cavity (14) and female connector. The electrolysis apparatus includes battery, switch device (6) and circuit plate. The circuit plate has charging port, charge management circuit, microcontroller unit (MCU) (10) located at center, and transformer circuit connected to negative and positive electrode. The MCU is connected with switch device, transformer circuit and charge management circuit.    USE - Portable hydrogen-rich water rod.    ADVANTAGE - The portable water rod is convenient and suitable for domestic or household consumers.    DETAILED DESCRIPTION - Portable hydrogen-rich water rod comprises elongated strip rod body installed with electrolysis apparatus responsible for producing hydrogen-rich water, upper rod (1) with hook, and lower rod (2) set with cavity (14) and female connector. The electrolysis apparatus includes battery, switch device (6) and circuit plate. The circuit plate has charging port, charge management circuit, microcontroller unit (MCU) (10) located at center, and transformer circuit connected to negative and positive electrode. The battery and charging port are connected to charge management circuit. The MCU is connected with switch device, transformer circuit and charge management circuit. The charging port and switch device leads to outer rod surface. The positive electrode leads to lower part of inner cavity and connected with multiple holes.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of portable hydrogen-rich water rod.    Upper rod (1)    Lower rod (2)    Switch device (6)    Microcontroller unit (10)    Cavity (14)
NOVELTY - Specialized large-scale integrated pig manure treatment system comprises wastewater inlet (1), sump (2), septic tank (3), sedimentation tank (4), storage tank (5), solid-liquid separator (6), organic fertilizer processing unit (7), waste lift pump (8), high-rate anaerobic reactor tank (9), central inlet pipe (10), gas pipe (11), methane cabinet (12), water-sealed gas purification pressure tank (13), bio-gas power generation device (14), bio-gas transfer duct (15), slurry storage tank (16), and irrigation device (17).    USE - Specialized large-scale integrated system used for treating pig manure.    ADVANTAGE - The system for treating pig manure produces bio-gas and organic fertilizer, avoids secondary pollution of exhaust gases, achieves full and effective waste recycling, and improves integrated utilization.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of specialized large-scale integrated pig manure treatment system.    Wastewater inlet (1)    Sump (2)    Septic tank (3)    Sedimentation tank (4)    Storage tank (5)    Solid-liquid separator (6)    Organic fertilizer processing unit (7)    Waste lift pump (8)    High-rate anaerobic reactor tank (9)    Central inlet pipe (10)    Gas pipe (11)    Methane cabinet (12)    Water-sealed gas purification pressure tank (13)    Bio-gas power generation device (14)    Bio-gas transfer duct (15)    Slurry storage tank (16)    Irrigation device (17)
NOVELTY - Banana seedling matrix based on agricultural waste comprises 20-80 wt.% rice straw compost and 20-80 wt.% mushroom residue.    USE - Banana seedling matrix.    ADVANTAGE - The banana seedling matrix substitutes conventional breeding process of banana with actual nutrients, eliminates need of soil seedling fertilization, and achieves resource utilization of crop straw. It has economic, social, and ecological benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of banana seedling matrix comprising crushing rice straw, adding fermentation liquid while watering to obtain 50-70% water content; fermenting 60% water content crushed rice straw for 2-3 months; drying and crushing into 2-3 mm to obtain rice straw compost product; crushing mushroom residue, adding water to obtain 60-80% water content, fermenting for 1-2 months, and drying and crushing into 1-3 mm to obtain mushroom compost; and mixing rice straw and mushroom compost at 20-80 vol.%:20-80 vol.% ratio.
NOVELTY - Special fertilizer comprises 60-80 pts. wt. cattle manure, 30-40 pts. wt. rice, 20-30 pts. wt. pumpkin vine, 60-70 pts. wt. urea, 50-60 pts. wt. calcium superphosphate, 40-50 pts. wt. potassium chloride, 3-5 pts. wt. copper sulfate, 3-5 pts. wt. zinc sulfate, 3-5 pts. wt. magnesium sulfate, 5-10 pts. wt. lime powder, 10-15 pts. wt. herbal medicine extract, 0.5-0.9 pt. wt. Trichoderma and 0.5-0.9 pt. wt. Bacillus subtilis.    USE - Special fertilizer used for preventing Houttuynia Cordata blight.    ADVANTAGE - The fertilizer reduces pesticide dosage and is suitable for ecological environment.
NOVELTY - Manufacture of Pleurotus citrinopileatus cultivation material comprises taking 58-62 wt.% sawdust, 15-20 wt.% cottonseed hull, 15-17 wt.% soybean cake, 3-4 wt.% mushroom stem, 2 wt.% lime, 1 wt.% gypsum and balance dry matter, soaking mushroom stem in water for 18-24 hours, leaching, adding sawdust, cottonseed hull and soybean cake, stacking, drying, plugging 10-15 cm diameter vertical vent, fermenting, heating at 60 degrees C for 24 hours, turning, adding gypsum and lime, turning for 5-6 days, controlling moisture content at 63-65%, inoculating, cooling and cultivating in dark room.    USE - Method for manufacturing Pleurotus citrinopileatus cultivation material (claimed) used for promoting growth.    ADVANTAGE - The material is environment-friendly, resource-saving and suitable for low-carbon environment.    DETAILED DESCRIPTION - Manufacture of Pleurotus citrinopileatus cultivation material comprises taking 58-62 wt.% sawdust, 15-20 wt.% cottonseed hull, 15-17 wt.% soybean cake, 3-4 wt.% mushroom stem, 2 wt.% lime, 1 wt.% gypsum and balance dry matter, soaking mushroom stem in water for 18-24 hours, leaching, adding sawdust, cottonseed hull and soybean cake, stacking, drying, plugging 10-15 cm diameter vertical vent, fermenting, heating at 60 degrees C for 24 hours, turning, adding gypsum and lime, turning for 5-6 days, controlling moisture content at 63-65%, inoculating, cooling and cultivating in dark room at 18-20 degrees C for 22-24 days. Sawdust is pulverized to 2-3 mm particle size. Each stack has 300-500 kg dry weight.
NOVELTY - Manufacture of Pholiota nameko cultivation material comprises taking 42-48 wt.% corn cob, 27-33 wt.% bagasse, 15-17 wt.% soybean cake, 3-4 wt.% mushroom stem, 4-5 wt.% lime, 1 wt.% gypsum and balance dry matter, soaking mushroom stem in water for 18-24 hours, leaching, adding corn cob, soybean cake and bagasse, stacking, drying, plugging 10-15 cm diameter vertical vent, fermenting, heating at 60 degrees C for 24 hours, turning, adding gypsum and lime, turning for 5-6 days, controlling moisture content at 63-65%, inoculating, cooling and cultivating in dark room at 18-20 degrees C for 22-24 days.    USE - Method for manufacturing Pholiota nameko cultivation material (claimed) used for promoting growth.    ADVANTAGE - The material is environment-friendly, resource-saving and suitable for low-carbon environment.    DETAILED DESCRIPTION - Manufacture of Pholiota nameko cultivation material comprises taking 42-48 wt.% corn cob, 27-33 wt.% bagasse, 15-17 wt.% soybean cake, 3-4 wt.% mushroom stem, 4-5 wt.% lime, 1 wt.% gypsum and balance dry matter, soaking mushroom stem in water for 18-24 hours, leaching, adding corn cob, soybean cake and bagasse, stacking, drying, plugging 10-15 cm diameter vertical vent, fermenting, heating at 60 degrees C for 24 hours, turning, adding gypsum and lime, turning for 5-6 days, controlling moisture content at 63-65%, inoculating, cooling and cultivating in dark room at 18-20 degrees C for 22-24 days. Bagasse and corn cob are pulverized to 2-3 mm particle size. Each stack has 300-500 kg dry weight.
NOVELTY - Biological composite fertilizer comprises household solid waste, orange quince sugar, chili residue, edible mushroom fungus, humus and biological species.    USE - Biological composite fertilizer.    ADVANTAGE - The biological fertilizer provides quality nutrition, prevents soil-borne diseases and rotting of roots. It prevents harmful effect of fertilizer on human body. The precise microbial and raw materials ratio results to increase in production, soil and water conservation, environmental protection, and to create strong green food.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological composite fertilizer comprising mixing raw materials; fermenting at 60-80 degrees C for 15-20 days; drying at 70-90 degrees C and reducing 20-30 wt.% moisture content; sieving at 60-80 mesh screen; and fermenting at 20-30 degrees C for 7-10 or 15-20 days and controlling at 40 wt.% moisture content and pH 6.5-7.5.
NOVELTY - Selenium-rich organic fertilizer comprises sodium selenite, vermicompost and amino acid nutrient solution, where preparation involves mixing livestock manure, mushroom and crushed straw and fermenting; spraying sodium selenite in fermented mixture; and digesting by earthworm and separating earthworm and its manure to get vermicompost; washing earthworm, discharging mud, adding earthworm manure and distilled water, mixing, stirring and reacting to get amino acid nutrient solution; and spraying amino acid nutrient solution in vermicompost, mixing and drying.    USE - Selenium-rich organic fertilizer.    ADVANTAGE - The fertilizer is rich in organic matter, nitrogen, phosphorus, potassium, particulate matter and more than 20 kinds of amino acids. It can change soil structure and improves soil water holding capacity.    DETAILED DESCRIPTION - Selenium-rich organic fertilizer comprises sodium selenite, vermicompost and amino acid nutrient solution, where preparation involves mixing livestock manure, mushroom and crushed straw at mass ratio of 10-15:2-5:1-3 and fermenting; spraying 30-50 mg/kg sodium selenite in fermented mixture at mass ratio of 1:100-150 every 30-45 days; and digesting by earthworm and separating earthworm and its manure to get vermicompost; washing earthworm, discharging mud, adding earthworm manure and distilled water at mass ratio of 1:2-4, mixing at 45-60 degrees C, stirring once every 5-8 hours and reacting for 3-6 days to get amino acid nutrient solution; and spraying amino acid nutrient solution in vermicompost at mass ratio of 1:150-180, mixing and drying to below 20% moisture content.
NOVELTY - Rectification of cyclohexane and isopropyl alcohol mixture includes using dimethyl sulfoxide and N,N-dimethylacetamide as extracting agent, separating mixture first using 15-40 theoretical plates fitted into extractive distillation column having 30-60 theoretical plates, introducing extracting agent, recovering cyclohexane from top of extractive distillation column and isopropyl alcohol from bottom; and separating once more using 10-20 theoretical plates, and recovering isopropyl alcohol from top of solvent recovery column and extracting agent from bottom recovery column.    USE - Method for rectifying cyclohexane and isopropyl alcohol mixture (claimed).    ADVANTAGE - The method has low energy consumption and simple process. It is safe, environmentally friendly, non-polluting, and achieves cleaner production. The product recovery rate is high.    DETAILED DESCRIPTION - Rectification of cyclohexane and isopropyl alcohol mixture involves using dimethyl sulfoxide and N,N-dimethylacetamide as extracting agent, separating cyclohexane and isopropyl alcohol mixture first using 15-40 theoretical plates fitted into extractive distillation column having 30-60 theoretical plates, introducing extracting agent using 6-20 theoretical plates, recovering cyclohexane from top of extractive distillation column and isopropyl alcohol and extracting agent from bottom of extractive distillation column; and separating once more using 10-20 theoretical plates fitted into extraction solvent recovery column having 15-30 theoretical plates, and recovering isopropyl alcohol from top of solvent recovery column and extracting agent from bottom recovery column.
NOVELTY - Rectification of n-hexane and ethyl acetate mixture includes using dimethyl sulfoxide and N,N-dimethylacetamide as extracting agent, separating mixture first using 15-40 theoretical plates fitted into extractive distillation column having 30-60 theoretical plates, introducing extracting agent, recovering n-hexane from top of extractive distillation column and ethyl acetate from bottom of extractive distillation column; and separating once more using 10-20 theoretical plates, and recovering ethyl acetate from top of solvent recovery column and extracting agent from bottom recovery column.    USE - Method for rectifying n-hexane and ethyl acetate mixture (claimed).    ADVANTAGE - The method has low energy consumption and simple process. It is safe, environmentally friendly, non-polluting, and achieves cleaner production. The product purity and yield is high.    DETAILED DESCRIPTION - Rectification of n-hexane and ethyl acetate mixture involves using dimethyl sulfoxide and N,N-dimethylacetamide as extracting agent, separating n-hexane and ethyl acetate mixture first using 15-40 theoretical plates fitted into extractive distillation column having 30-60 theoretical plates, introducing extracting agent using 6-20 theoretical plates, recovering n-hexane from top of extractive distillation column and ethyl acetate and extracting agent from bottom of extractive distillation column; and separating once more using 10-20 theoretical plates fitted into extraction solvent recovery column having 15-30 theoretical plates, and recovering ethyl acetate from top of solvent recovery column and extracting agent from bottom recovery column.
NOVELTY - Rectification of cyclohexane and n-propanol mixture includes using dimethyl sulfoxide and N-methyl-2-pyrrolidone as extracting agent, separating mixture first using 15-40 theoretical plates fitted into extractive distillation column having 30-60 theoretical plates, introducing extracting agent, recovering cyclohexane from top of extractive distillation column and n-propanol from bottom of extractive distillation column; and separating once more using 10-20 theoretical plates, and recovering n-propanol from top of solvent recovery column and extracting agent from bottom recovery column.    USE - Method for rectifying cyclohexane and n-propanol mixture (claimed).    ADVANTAGE - The method has low energy consumption and simple process. It is safe, environmentally friendly, non-polluting, and achieves cleaner production. The product purity and yield is high.    DETAILED DESCRIPTION - Rectification of cyclohexane and n-propanol mixture involves using dimethyl sulfoxide and N-methyl-2-pyrrolidone as extracting agent, separating cyclohexane and n-propanol mixture first using 15-40 theoretical plates fitted into extractive distillation column having 30-60 theoretical plates, introducing extracting agent using 5-20 theoretical plates, recovering cyclohexane from top of extractive distillation column and n-propanol and extracting agent from bottom of extractive distillation column; and separating once more using 10-20 theoretical plates fitted into extraction solvent recovery column having 15-30 theoretical plates, and recovering n-propanol from top of solvent recovery column and extracting agent from bottom recovery column.
NOVELTY - A halogenated alkyl pyrazole compound (I) or (II), is new.    USE - New halogenated alkyl pyrazole compound is used as pesticide (claimed).    ADVANTAGE - The environmentally-friendly halogenated alkyl pyrazole compound having excellent bactericidal activity, is prepared by simple method.    DETAILED DESCRIPTION - A halogenated alkyl pyrazole compound of formula (I) or (II), is new.    R1,R4=fluoro, chloro or bromo;    R2,R5=H, methyl, phenyl, p-fluorophenyl or p-chlorophenyl;and    R3,R6=fluoro, chloro, bromo, methyl, methoxy, 2,4-dichlorophenyl, 2,4,5-trichlorophenyl, 2,4,6-trichlorophenyl, 2,5-dichlorophenyl, 2-methyl-5-chloro, 2,3,4-trichloroethyl or 2-methyl-4,5-dichlorophenyl.    An INDEPENDENT CLAIM is included for preparation of halogenated alkyl pyrazole compound (I) or (II).
NOVELTY - An herbicide isoxaflutole is synthesized by reacting 5-cyclopropyl-4-(2-methylthio-4-(trifluoromethyl)benzoyl) isoxazole with oxidation catalyst, phase transfer catalyst, and inorganic acid at a mass ratio of 10:0.01-0.05:0.01-0.05:0.1-2 to obtain mixed reaction liquid; heating the mixed reaction liquid, dropwise adding hydrogen peroxide, and further reacting at 25-90 degrees C for 3-6 hours to obtain reaction liquid; and standing for separating, washing aqueous layer with brine at 25-30 degrees C, washing organic phase with sodium bisulfite, and concentrating under reduced pressure to give final product.    USE - Method for synthesis of herbicide isoxaflutole (claimed).    ADVANTAGE - The method has mild reaction condition, simple operation, less wastes, controllable reaction, and high product yield which is suitable for green industrial production.
NOVELTY - Cultivating Ganoderma involves taking cottonseed hull (56-64%), sawdust (16-24%), soybean (12-14%), Ganoderma (3-4%), lime (2-3%), and gypsum (1%). Size of sawdust is 3-5 mm, and Ganoderma is 2-3mm. Sawdust and Ganoderma is soaked in water (20-30 times), and fermented for 18h-24 hours. Obtained material is mixed with cottonseed hull, and soybean to obtain a mixture. Obtained mixture (300kg-500kg) is piled in a heap of height 1.0-1.2m, and width 2m-3m. Obtained material is covered with grass at 60 degrees C for 24 hours. Gypsum is added to obtained material.    USE - Method for cultivating Ganoderma (claimed).    ADVANTAGE - The method is cost-effective, and eco-friendly.    DETAILED DESCRIPTION - Cultivating Ganoderma involves taking cottonseed hull (56-64%), sawdust (16-24%), soybean (12-14%), Ganoderma (3-4%), lime (2-3%), and gypsum (1%). Size of sawdust is 3-5 mm, and mushroom is 2-3mm. Sawdust and Ganoderma is soaked in water (20-30 times), and fermented for 18h-24 hours. Obtained material is mixed with cottonseed hull, and soybean to obtain a mixture. Obtained mixture (300kg-500kg) is piled in a heap of height 1.0-1.2m, and width 2m-3m. Obtained material is covered with grass at 60 degrees C for 24 hours. Gypsum is added to obtained material and left for 5-6 days to obtain a product of moisture content (63-65%). Mushroom extract (0.01-0.02g/ml) is added to obtained product for 18-24 hours to obtain final product.
NOVELTY - Cultivating Pleurotus nebrodensis involves taking sawdust (56-60%), corn core (20-24%), soybean cake (11-13%), mushroom (3-4%), lime (3-4%), and gypsum (1%). Size of sawdust, and corn core is 3-5 mm, and mushroom is 2-3mm. Sawdust and mushroom is soaked in water (20-30 times), and fermented for 18h-24 hours. Obtained material is mixed with sawdust, corn core, and soybean cake to obtain a mixture. Obtained mixture (300kg-500kg) is piled in a heap of height 1.0-1.2m, and width 2m-3m. Obtained material is kept at 60 degrees C for 24 hours. Gypsum (3-4 times) is added to obtained material.    USE - Method for cultivating Pleurotus nebrodensis (claimed).    ADVANTAGE - The method is cost-effective, and eco-friendly, and ensures reduced requirement of man-power.    DETAILED DESCRIPTION - Cultivating Pleurotus nebrodensis involves taking sawdust (56-60%), corn core (20-24%), soybean cake (11-13%), mushroom (3-4%), lime (3-4%), and gypsum (1%). Size of sawdust, and corn core is 3-5 mm, and mushroom is 2-3mm. Sawdust and mushroom is soaked in water (20-30 times), and fermented for 18h-24 hours. Obtained material is mixed with sawdust, corn core, and soybean cake to obtain a mixture. Obtained mixture (300kg-500kg) is piled in a heap of height 1.0-1.2m, and width 2m-3m. Obtained material is kept at 60 degrees C for 24 hours. Gypsum (3-4 times) is added to obtained material to obtain a product of moisture content (63-65%). Bed is prepared for sowing Pleurotus nebrodensis by using obtained product, and Pleurotus nebrodensis extract (0.01-0.02 g/ml) is added to prepared bed to obtain final product. Pleurotus nebrodensis extract is prepared by soaking it in water for 18-24 hours at room temperature.
NOVELTY - Processing low energy town garbage involves pre-processing i.e separating broken particles from garbage. Obtained products are piled for aerobic composting to obtain fermented product, and then sorting the fermented product from residue.    USE - Method for processing low energy town garbage used for landscaping, landfilling, and preparing nutrition soil (claimed).    ADVANTAGE - The method is cost-effective.
NOVELTY - Producing microalgae culture medium using anaerobic digestive juice, comprises (a) removing ammonia nitrogen present in anaerobic digestive juice via an ammonia stripping process, (b) demolishing the anaerobic digestive juice using chlorine to remove organic material, color and nitrogen residual, and sterilizing, and (c) dechlorinating the sterilized anaerobic digestive juice to remove chlorine, where the anaerobic digestive juice is formed by anaerobic digesting pig manure containing high concentration of ammonia nitrogen.    USE - The method is useful for producing microalgae culture medium (claimed).    ADVANTAGE - The method removes interfering factor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) culturing microalgae, comprising (i) removing ammonia nitrogen remaining in anaerobic digestive juice via an ammonia stripping process, (ii) demolishing the anaerobic digestive juice using chlorine to remove organic material, color and nitrogen residual, and sterilizing, (iii) dechlorinating the sterilized anaerobic digestive juice to remove chlorine and (iv) contacting microalgae on the anaerobic digestive juice; and    (2) processing pig manure, comprising processing the pig manure with anaerobic microorganisms to obtain anaerobic digestive juice, and performing step of (i), (ii), (iii) and (iv).
NOVELTY - The device has a shell (1) whose upper portion is comprised with a feedstock mouth, and a discharging port which is comprised at lower portion of shell. The inner side of the shell is comprised with an insulating layer (2), and an automatic control device (3) is connected with a ventilating device. A solar energy heat collecting device (5) is connected with a heat exchange device, and the ventilating device is set with inner side of a fermentation cabin (4).    USE - Solar process automation garden waste fermentation device.    ADVANTAGE - The occurrence of pollution is prevented, and improved operation efficiency is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the solar process automation garden waste fermentation device.    Shell (1)    Insulating layer (2)    Automatic control device (3)    Fermentation cabin (4)    Solar energy heat collecting device (5)
NOVELTY - Matrix comprises corn straw compost and mushroom residue in volume ratio of 1:4.    USE - Matrix comprises used for breeding cucumber seedling (claimed).    ADVANTAGE - The matrix ensures low cost, no pollution, obvious economic benefit, social benefit and ecological benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing matrix, which involves:    (A) crushing corn straw;    (B) regulating water content of crushed material to 50-70%;    (C) fermenting crushed corn straw;    (D) drying, crushing and sieving fermented materials; and    (E) mixing corn straw fermented materials with mushroom residue to obtain matrix.
NOVELTY - Cultivation matrix comprises rotten pig manure (50-60 parts), corn cob (20-30 parts), wheat straw (15-20 parts), sawdust (5-8 parts), potassium dihydrogen phosphate (0.02-0.06 parts), quicklime (1.2-1.5 parts), light calcium carbonate (0.08-0.12 parts), and bentonite (0.8-1.2 parts).    USE - Cultivation matrix used for Agaricus bisporus (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing cultivation matrix, which involves:    (A) pulverizing raw materials by 80-120 mesh sieve;    (B) adding water to pulverized material (120-140%); and    (C) fermenting obtained mixture.
NOVELTY - Bio-organic fertilizer comprises 15-20 pts. wt. Lactobacillus, 1-2 pts. wt. solubilizing agent, 2-4 pts. wt. potassium, 10-15 pts. wt. Bacillus subtilis, 8-15 pts. wt. Aspergillus awamori culture, 5-8 pts. wt. polyglutamic acid, 50-100 pts. wt. humic acid, 100-150 pts. wt. organic material, 80-100 pts. wt. chemical fertilizer and 50-80 pts. wt. bentonite.    USE - Bio-organic fertilizer used for preventing soil-borne disease.    ADVANTAGE - The bio-organic fertilizer increases fertilizer utilization rate, crop disease resistance ability, especially composite microorganism, improves soil plate structure, and supplements organic matter to soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) mixing Lactobacillus, phosphorus, potassium solution, Bacillus subtilis and Aspergillus awamori uniformly;    (B) mixing urea, calcium hydrophosphate and potassium sulfate;    (C) mixing seaweed, fish meal and crab shell, and then crushing through 200-300 items sieve to prepare organic material;    (D) mixing all products with remaining components and granulating in a granulator to obtain granules having particle size of 1-2 millimeter; and    (E) adding wet polyglutamic acid in the product and heating at 35-38 degrees C for 1-2 hours.
NOVELTY - Biological organic fertilizer comprise cellulase (15-20 pts. wt.), polygalacturonase (35-45 pts. wt.), serine protease (3-12 pts. wt.), Bacillus subtilis (3-12 pts. wt.), pectin esterase (3-12 pts. wt.), acyl peptide hydrolase (3-12 pts. wt.), protease (2-4 pts. wt.), isooctyl thioglycolate (3-15 pts. wt.), tri-n-hexyl trimellitate (3-15 pts. wt.), and diphenylamine (5-10 pts. wt.).    USE - Biological organic fertilizer used for fennel (claimed).
NOVELTY - Fertilizer comprises 10% livestock manure, 15% dry tea, 15-20% rice bran, 20% humic acid, 25-35% nitrogen, phosphorus and potassium, and 1-3% seaweed extract, 0.5% fermentation strain and balanced amount of trace elements.    USE - Fertilizer used for grapes (claimed).    ADVANTAGE - The fertilizer ensures improved fertility, and has improved amount of nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer used for grapes, which involves:    (A) fermenting livestock manure, tea and rice bran in a fermentation pool in presence of fermentation strain at 55-65 degrees C for 25-35 days;    (B) grinding and granulating the fermented product;    (C) adding remaining raw material to obtained granules to obtain mixture; and    (D) drying, grinding and granulating the obtained mixture to obtain final product.
NOVELTY - Method for synthesizing silver/gold composite nanoparticles, involves culturing Fusarium sp. strain 1281-2 using fermentation culture medium, collecting mycelium, cleaning the mycelium using deionized water, removing residual culture medium, suspending the mycelium in deionized water, performing culturing process, filtering culture liquid, obtaining supernatant comprising the Fusarium sp. strain 1281-2 which is reaction matrix, adding silver nitrate solution and chloroauric acid solution for reduction reaction, and centrifuging mixture.    USE - The method is useful for synthesizing silver/gold composite nanoparticles (claimed).    ADVANTAGE - The method is environmentally-friendly and simple to perform.    DETAILED DESCRIPTION - Method for synthesizing silver/gold composite nanoparticles, involves (a) culturing Fusarium sp. strain 1281-2 using fermentation culture medium, collecting mycelium, cleaning the mycelium using deionized water, removing residual culture medium, suspending the mycelium in deionized water, performing culturing process under sterile conditions, filtering culture liquid for removing mycelium, and collecting supernatant comprising the Fusarium sp. strain 1281-2, and (b) obtaining the supernatant comprising the Fusarium sp. strain 1281-2 as reaction matrix, adding silver nitrate solution and chloroauric acid solution for reduction reaction, and centrifuging mixture to obtain product. The Fusarium sp. strain 1281-2 is Fusarium sp. strain 1281-2 (CCTCC M2014658).
NOVELTY - Fertilizer comprises 30-65 pts. wt. organic fertilizer, 15-25 pts. wt. sulfur, 8-30 pts. wt. trace elements, 0.5-1.5 pts. wt. histidine, 0.5-1.5 pts. wt. cysteine, 0.5-1.5 pts. wt. nicotinamide, 0.5-1.5 pts. wt. citric acid, 0.5-1.5 pts. wt. malic acid, 1-3 pts. wt. surfactant, 1-3 pts. wt. chelating agent, and 80-100 pts. wt. water.    USE - As fertilizer for fruit trees (claimed).    ADVANTAGE - The fertilizer increases iron content and nutritional value of fruit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves fermented manure, and animal and plant residues with straw powder, adjusting moisture content to 40-55%, fermenting the mixture at 45-70 degrees C for 7-10 days, and mixing remaining materials to the mixture.
NOVELTY - Oxidation of alcohol for preparing aldehyde and ketone involves dissolving alcohol in an organic solvent to obtain a homogeneous solution, dissolving hydrogen peroxide, bromine-containing anion reagent and protic acid in an organic solvent to obtain a homogeneous solution, mixing the obtained two homogeneous solution in a micro-mixer, placing in microreactor device for carrying out microreactor reaction and collecting the liquid effluent.    USE - Oxidation of alcohol for preparing aldehyde and ketone (claimed).    ADVANTAGE - The method is environmentally-friendly and enables simple, safe and economical catalytic oxidation of alcohol for preparing aldehyde and ketone without contamination of metals.
NOVELTY - alpha -Carotene is obtained by a rearrangement reaction of 3-methyl-5-(2,6,6-trimethyl-2-cyclohexen-1-yl)-1,4-pentanedienyl phosphonate at - 30 to 3 degrees C under nitrogen protection in organic solvent in the presence of base; and adding decyl dialdehyde to the mixture after rearrangement reaction at 0-3 degrees C for a Wittig-Horner condensation reaction to obtain alpha -carotene.    USE - Method for preparing alpha -carotene (claimed).    ADVANTAGE - The method has simple operation, high yield and low cost. It is green and environment-friendly.
NOVELTY - Preparation of nicotinamide comprises hydrolysis reacting 3-cyanopyridine and water in the presence of small crystal particle NaY zeolite catalyst to obtain the product.    USE - Preparation of nicotinamide (claimed).    ADVANTAGE - The method is simple and green and environment-friendly and has mild reaction condition, high catalytic activity and selectivity, small device corrosion, no environmental pollution, high yield and high purity.
NOVELTY - A sacubitril compound (I) is prepared by reacting (S)-1-( alpha -aminobenzyl)-2-naphthol and (S)-2-methyl-4-oxo-butyric acid, mixing Grignard reagent, reacting, adding (1S,3R,5S)-((3-methyl-5-( beta -biphenyl-4-yl-methyl)-2-pyrrolidone) benzyl)-2-naphthol, performing debenzylation reaction with (3R,5S)-3-methyl-5-(1',1'-biphenyl-4-base-methyl)-2-pyrrolidone, esterifying under acidic catalyst in ethanol solution, and performing amidation with (2R,4S)-2-methyl 4-amino-5-(1,1'-biphenyl-4-yl)-pentanoate and succinic anhydride.    USE - Method for preparing sacubitril compound (claimed).    DETAILED DESCRIPTION - A sacubitril compound of formula (I) is prepared by reacting (S)-1-( alpha -aminobenzyl)-2-naphthol and (S)-2-methyl-4-oxo-butyric acid to obtain (7aR, 9R,12S)-9-methyl-10-oxo-12-phenyl-7a,8,9,10-tetrahydro-12H-naphtho(1,2-e)-pyrrolyl-(2,1-b) (1,3) oxazine, mixing Grignard reagent, reacting, adding (1S,3R,5S)-((3-methyl-5-( beta -biphenyl-4-yl-methyl)-2-pyrrolidone) benzyl)-2-naphthol, performing debenzylation reaction with (3R,5S)-3-methyl-5-(1',1'-biphenyl-4-base-methyl)-2-pyrrolidone, esterifying under acidic catalyst in ethanol solution to obtain (2R,4S)-2-methyl-4-amino-5-(1,1'-biphenyl-4-yl)-pentanoate, and performing amidation with (2R,4S)-2-methyl 4-amino-5-(1,1'-biphenyl-4-yl)-pentanoate and succinic anhydride.
NOVELTY - This new utility model relates to one of positive pressure air-breathing biomass powder coal powder air flow bed gasification furnace and heat coal system, wherein, comprising material storage bin, a gasification furnace and a burner, the bottom storage bin setting material feeding port, wherein feedstock by pneumatic transport pump and gasification furnace of powder coal import connected with, the gasification furnace from the furnace body under gas furnace, and gasification furnace and gasification furnace of furnace body composed of furnace body, wherein the furnace body of gasification furnace and uniform distribution of powder coal multi-import, gasification furnace air import of setting in the furnace body of gasification furnace, diesel oil burner installed on furnace body of the upper gasification furnace, the gasification furnace of the furnace body top part setting fuel gas outlet, gas outlet through pipeline connected with import of fuel gas burner, air import and burner mounted burner fan, installed gas import regulator between the combustion pipe and import in the burner, air import regulator installed between air import and burner blower in the burner. The utility model can realize new combustion fire and adjust to ensure combustion effect.
NOVELTY - The reactor has an ash collection container provided with a bottom arranged at a level below a grid. A passage is determined between a contour of a grid and sides of the container for driving ashes that are emptied from the grid to the bottom of the container. A scraping arm (5) includes a leading section (5a) in a shape of a spiral with center in an axis of rotation generating lateral movement of an ash built up on the grid beyond the contour to be emptied into the bottom of the container by gravity as the container moves with respect to the grid.    USE - Gasification reactor for solid fuels e.g. household waste, industrial waste, and agricultural waste such as corncob.    ADVANTAGE - The reactor transmits torque to the scraping arm for cutting and removing possible solidified ash portion. The reactor allows a gasification chamber to reduce manufacturing costs compared to costs associated with a cylindrical gasification chamber while allowing systems with reliable construction and final quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gasification reactor.    Scraping arm (5)    Leading section (5a)    Trailing section (5b)    Perforated plate (9)    Cooling unit (10)
NOVELTY - Method for preparing pineapple leaf-and-stem fertilizer involves harvesting and crushing pineapple leaf-and-stem grown in pineapple field, accommodating crushed pineapple leaf-and-stem under aerobic fermentation environment, performing fermentation process, accommodating crushed pineapple leaf-and-stem in pool for fermentation, again performing fermentation under aerobic condition at room temperature, and continuously performing fermentation process.    USE - The method is useful for preparing pineapple leaf-and-stem fertilizer (claimed).    ADVANTAGE - The method enables to prepare product without reducing nutritional content of pineapple.    DETAILED DESCRIPTION - Method for preparing pineapple leaf-and-stem fertilizer involves harvesting and crushing pineapple leaf-and-stem grown in pineapple field, accommodating crushed pineapple leaf-and-stem under aerobic fermentation environment, performing fermentation process, accommodating crushed pineapple leaf-and-stem in pool for fermentation, again performing fermentation under aerobic condition at room temperature, where the crushed pineapple leaf-and-stem is dried before fermentation process, and comprises crushed layer, the dried pineapple leaf-and-stem comprising crushed layer is made to absorb moisture arises from a pineapple leaf-and-stem crushed layer which is used for fermentation process, and continuously performing fermentation process.
NOVELTY - Separation of bio-oil involves contacting a bio-oil produced from biomass by a thermochemical process with a supercritical alkane to dissolve non-polar compounds of the bio-oil in the supercritical alkane and removing the non-polar compounds from the bio-oil. The obtained fractionated bio-oil contains polar compounds.    USE - Separation of bio-oil used as alternate fuel for petroleum.    ADVANTAGE - The method is economical and energy efficient. The method uses biomass which improves the yield of bio-oil with low ash content and high lipid content. The method increases the thermal stability of bio-oils for transport and storage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system used to separate bio-oils using a supercritical alkane.    System (2)    Extractor (8)    Pump (10)    Separators (12,12',12")
NOVELTY - Composition comprises a Trichoderma virens component comprising Trichoderma virens G1-3 or Trichoderma virens G1-21, a Bacillus amyloliquefaciens component, a mycorrhizal fungus or mycorrhizal fungi component, and a phytate or phytic acid component.    USE - The composition is useful for: creating an effective association of mycorrhizal fungi with the root of host plant in phosphorus rich environment; germination of mycorrhizae propagules and subsequent root colonization triggered by signal molecule; producing phytase enzyme in high phosphorus environment because of the presence of the phytochrome C gene; producing phosphatase enzymes that can break the bonds on stable compounds comprising tricalcium phosphate and release calcium ions; increasing the yield of plants or seed; improving soil aggregation and soil quality; and growing of most agriculturally important crops including alfalfa, barley, beans (all), maiz, cotton, millet, rice, sorghum, soybeans, sunflower and wheat. Test details are described but no results given.    ADVANTAGE - The composition: exhibits synergistic effect and allows mycorrhizal fungi to colonize the root in the presence of plant available nutrients and increases plant yield of seed yield; and increases the germination and colonization of mycorrhizal fungi, which allows farmers to reduce input costs and obtain greater yields by utilizing nutrients already present in the soil while still maintaining adequate inorganic nutrient fertilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method comprising applying the composition to a soil.
NOVELTY - Filtration equipment comprises a closed reactor (20) connected with supply flow passage (10) connected with hopper (11) which introduces fuel on one side, a first pump located at one side of supply flow passage, connected with hopper, a three-way valve (13) located at other side of supply flow passage, and connected with closed reactor. The closed reactor generates vapor pressure by heating to hydrothermal carbonize raw materials, and injects carbonized material via a spraying nozzle (31), and performs solid-liquid separation by bumping carbonized material in a multilayer mesh assembly.    USE - The filtration equipment is useful in hydrothermal carbonization reactor (claimed).    ADVANTAGE - The equipment improves workability and shortens filtration and production times, and is easy to operate.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the filtration equipment for hydrothermal carbonization reactor.    Supply flow passage (10)    Hopper (11)    Three-way valve (13)    Closed reactor (20)    Spray nozzle (31)
NOVELTY - A nail polish contains 20-30 pts. wt. glycerol, 6-12 pts. wt. butyl acetate, 2-8 pts. wt. Cordyceps extract, 1-3 pts. wt. n-butane, 12-24 pts. wt. corn extract, 4-9 pts. wt. collagen protein, 18-24 pts. wt vitamin B and 12-16 pts. wt. deionized water.    USE - Nail polish (claimed).    ADVANTAGE - The nail polish can be prepared in a simple, easy and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of nail polish.
NOVELTY - The system (1) has first supply line (12) for supplying reformed gas generated from hydrocarbon fuel, and second supply line (13) for supplying pure hydrogen. Cell stacks (20a-20d) produce electric power using the first supply line or second supply line and supplies the power to a load (30). Valves (12a-12d, 13a-13d) are provided in the first supply line or second supply line, where opening and closing of the valves is controlled according to variation of the load. A control apparatus (40) selects/drives the stacks generating the power by using the gas and pure hydrogen.    USE - Fuel cell system e.g. electric power generating apparatus system, polymer electrolyte fuel cell (PEFC) system and solid oxide fuel cell (SOFC) system.    ADVANTAGE - The control apparatus selects/drives the stacks generating the electric power by using the reformed gas and the pure hydrogen, thus improving trackability of the load with reduced fuel cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electric power generation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system. '(Drawing includes non-English language text)'    Fuel cell system (1)    Supply lines (12, 13)    Valves (12a-12d, 13a-13d)    Cell stacks (20a-20d)    Load (30)    Control apparatus (40)
NOVELTY - This utility model claims a biomass fuel gas carbonizing device, comprising gasification furnace, gas filtering device and fuel gas furnace end, gasification furnace can make biomass fuel burning is combustible gas, fuel gas filtering device for gasification furnace generating flammable gas for the second time filtering, for effective in combustible gas containing the harmful gas and dust removing completely, increase the purity of gas, purified gas entering through the second time filter fuel gas furnace head in the combustion process, wherein in the combustion process, fuel gas furnace head is set with filter screen, and has isolation effect, can effective prevent backfire phenomenon happen, which is good for increase the safety. This new utility model claims biomass fuel gas and carbonizing device, structure is simple, can effective using agriculture and forestry waste with combustible gas, energy conversion rate high, for no pollute environment, the combustible gas with high purity.
NOVELTY - The solid fuel production equipment has heat feeding unit (600) which is provided to collect the waste heat generated in generation unit (4). A drying unit (400) is configured to dry the digested sludge passing through the mixing preheating unit (200) at predetermined temperature. A biogas production unit (100) is installed among supply path in which sludge is supplied to generation unit. A waste heat supply unit (10) is provided to refurnish the waste heat collected in drying unit to anaerobic digestion tub (110) so as to control the reaction temperature.    USE - Solid fuel production equipment using sludge, installed in sewage disposal plant, waste water disposal plant, and food waste treating plant.    ADVANTAGE - The digested sludge remained in the moisture is removed, so that the calorific value of the sludge is improved. The sewage sludge is recycled efficiently. The solid fuel is produced efficiently. The operation efficiency of the generation unit is improved. The usage of the fuel production equipment is increased. The combustibility of the fuel production equipment is improved. The cost of the equipment is reduced. The temperature of the mixing preheating unit is maintained regularly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid fuel production equipment. (Drawing includes non-English language text)    Generation unit (4)    Waste heat supply unit (10)    Biogas production unit (100)    Anaerobic digestion tub (110)    Mixing preheating unit (200)    Drying unit (400)    Heat feeding unit (600)
NOVELTY - The system (100) has a housing (102) with an interior volume (104) in which an electrolyte (106) is exposed to a first electrode (108) comprising an aluminum-based electrode active material and a second electrode (110). The interior volume is provided with an outlet (112). A hydrogen-permeable medium (114) that is not permeable to the electrolyte is associated with the outlet and defining an interface between the interior volume of the housing and an environment (116) external to the interior volume.    USE - Electrochemical system.    ADVANTAGE - The hydrogen accumulation within electrochemical system is mitigated. The electrochemical system allows for the selective reduction in the concentration of hydrogen gas even when the electrolyte of the electrochemical cell is highly reactive. The hydrogen gas concentration is reduced while retaining electrolyte. The hydrogen gas is continually removed from the electrochemical system to prevent pressure build-up that ruptures the cell. The hydrogen buildup is mitigated while preventing leaking of other compounds inside the cell, such as liquid electrolytes. The concentration of hydrogen byproduct within the electrochemical system is reduced by venting and/or reacting the hydrogen byproduct.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an apparatus for transporting water into an electrochemical cell; and    (2) a method for operating an electrochemical cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the electrochemical system comprising a hydrogen-permeable membrane.    Electrochemical system (100)    Housing (102)    Interior volume (104)    Electrolyte (106)    Electrodes (108,110)    Outlet (112)    Hydrogen-permeable medium (114)    Environment (116)
NOVELTY - A methanol gasoline additive comprises 10-15 parts of isopropanol, 5-9 pts. wt. polyisobutylene amine, 2-4 pts. wt. benzyl alcohol, 2-5 pts. wt. ethanol, 12-15 pts. wt. butylated hydroxytoluene, 8-11 pts. wt. monoalkenyl succinimide, 0.5-1 pts. wt. copper sulfate, 4-6 pts. wt. isobutanol, 5-8 pts. wt. ferrocene, 1-4 pts. wt. barium titanate, 8-10 pts. wt. diethyl dithiocarbamate, 7-9 pts. wt. disodium ethylenediaminetetraacetate, 6-13 pts. wt. lauryl methacrylate and 0.2-0.7 pts. wt. lubricant.    USE - Methanol gasoline additive (claimed).    ADVANTAGE - The additive effectively increases combustion rate of methanol gasoline and reduces generation of waste during combustion. The engine using the additive has suppressed damage.
NOVELTY - Method for preparing gamma -form crystal of silodosin involves (a) dissolving silodosin in alcohol solvent to obtain a solution, (b) precipitating the solution in a seeding chamber, and (c) filtering and drying the precipitated crystals.    USE - The method is useful for preparing gamma -form crystal of silodosin (claimed).    ADVANTAGE - The method is suitable for large-scale production of silodosin and environmentally-friendly since the amount of alcohol used in production is relatively small, and produces a product with uniform quality and homogeneous crystal. The gamma -form crystal of silodosin is safe as it does not contain toluene which is harmful to the human body.
NOVELTY - Method for marking a petroleum hydrocarbon or a liquid biologically-derived fuel involves adding 0.01-20 ppm tetraphenyl compound (I) to petroleum hydrocarbon or liquid biologically derived fuel.    USE - Method for marking petroleum hydrocarbon and liquid biologically-derived fuel used for identifying origin and characteristics of petroleum hydrocarbon and liquid biologically-derived fuel. Uses include but are not limited to biodiesel fuel, ethanol fuel, crude oil, gasoline, diesel fuel, kerosene, jet fuel, and heating oil.    DETAILED DESCRIPTION - Method for marking a petroleum hydrocarbon or a liquid biologically-derived fuel involves adding 0.01-20 ppm tetraphenyl compound of formula: C(Ph(R1)i(OR2)j)2(Ph(R3)m(OR4)n)(Ph(R5)o(OR6)p) (I) to petroleum hydrocarbon or liquid biologically derived fuel.    Ph=phenyl;    R1-R6=1-18C alkyl or 4-18C heteroalkyl;and    i,j,m,n,o,p=0-2.    (i) At least one of i and j is not zero; and (ii) At least one of m and n, and at least one of o and p are not zero.
NOVELTY - The system has a gas price (GP) administration unit for transmitting first information in response to an external request. A TSP administration unit stores second information related to tentative sale unit cost based on transformation information of the first information. The TSP administration unit transmits the second information to a server of a developmental history and a financial facility server to purchase a final neogenesis energizing certificate (FREC). A FSP administration unit transmits third information in response to the external request.    USE - System for performing risk hedge about fuel cell generation business based on gas price increase at a financial facility.    ADVANTAGE - The TSP administration unit transmits the second information to the server of the developmental history and the financial facility server to purchase the FREC so as to effectively perform the risk hedge about the fuel cell generation business without causing risk to restricted cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a system for performing risk hedge about fuel cell generation business based on gas price increase. '(Drawing includes non-English language text)'
NOVELTY - The apparatus has diffusion gas that is collected from soil through a bottom face portion by which a lower portion of measurement chamber (1) is released. A gas concentration detection unit (3) is positioned inside the chamber and the gas concentration of a detection target is measured in two types of operation mode. The gas concentration detection unit measures a gas flux from the calculation value of initial stage gas concentration time gradient of measurement chamber in circulation mode, and measures the gas concentration in the air in ventilation mode by turns.    USE - Gas monitoring apparatus installed in thermal power station, iron mill, petroleum refinery, petroleum and natural gas mining areas and their transport areas, and agricultural zone, for monitoring levels of carbon dioxide and methane gas emission.    ADVANTAGE - The long-term measurement of the gas concentration in the gas flux diffused from soil or the rock layer surface and surrounding surface layer air are continuously carried out by turns by the time cycle for about 30 second or more.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of showing measuring situation of gas flux from the soil in internal circulation mode in chamber. (Drawing includes non-English language text)    Measurement chamber (1)    Gas concentration detection unit (3)    Air intake pipe (10)    Top defense pipe (13)    External air opening portion (15a,15b)
NOVELTY - Apparatus comprises a hopper (100) for storing the polyurathane, a molding machine (200) coupled to the hopper, and a mold collector (400) coupled to the molding machine. The molding machine is provided with a driving unit, a deceleration unit (260) coupled to the driving unit, a pressure roller to transfer power from the deceleration unit, and a ring die located inside the pressure roller. An upper surface of the ring die is provided with multiple through holes. The thickness of ring die is 40-55 mm corresponding to interval between one side end and other side end of the through holes.    USE - The apparatus is useful for solidifying polyurethane (claimed) in form of fuel.    ADVANTAGE - The apparatus provides adequate strength to waste solidified polyurathane, consumes less energy, and reduces risk of explosion, and is environmental friendly.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the apparatus for solidifying polyurethane (Drawing includes non-English language text).    Hopper (100)    Molding machine (200)    Deceleration unit (260)    Separator (300)    Mold collector (400)
NOVELTY - The anode plate is formed in oxygen generating room. A negative plate is formed in hydrogen generation room. A nozzle is provided for spraying the raw water and hydrogen from the hydrogen generation room of the electric decomposition unit (200) which performs the electrolysis by the electric power supply. The fluid pump (300) sprays the raw water and hydrogen from the fluid pump. The hydrogen in the raw water is dissolved and the fluid pump is driven according to detect water supply of hydrogen water. A flux detection sensor (500) supplies power to electric decomposition unit.    USE - Hydrogen water manufacturing system.    ADVANTAGE - The durability of composition portion is extended since the water pressure of the feedwater pipe does not work within the hydrogen water manufacturing system. The hydrogen dissolved amount about the hydrogen water through the dissolution of hydrogen is enhanced. The damage of the component generated in the abort of the inevitable source water supply is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen water manufacturing system.    Hydrostatic maintenance unit (100)    Electric decomposition unit (200)    Fluid pump (300)    Flux detection sensor (500)    Valve (600)
NOVELTY - An environmentally-friendly biofuel comprises 50-70 pts. wt. blue-green algae extract oil, 2-4 pts. wt. cumene sulfonate, 5-10 pts. wt. water, 15-25 pts. wt. diesel oil, 2-6 pts. wt. oleic acid, 2-6 pts. wt. ethanol, 1-8 pts. wt. modifier, and 0.1-2 pts. wt. cyclopentadienyl manganese tricarbonyl.    USE - Environmentally-friendly biofuel (claimed).    ADVANTAGE - The environmentally-friendly biofuel has high calorific value, can replace diesel oil, and is energy efficient. The environmentally-friendly biofuel is prepared by a method which is simple, economical, and can be industrialized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environmentally-friendly biofuel, which involves mixing blue-green algae extract oil, cumene sulfonate and water to obtain component (A), mixing diesel oil, oleic acid, ethanol, modifiers and cyclopentadienyl manganese tricarbonyl to obtain component (B), adding the component (B) to component (A), and mixing.
NOVELTY - Complex method biomass fuel processing machine, belonging to biomass fuel processing machine, wherein on machine frame, to side part of the extruder housing is assembled mixing stirrer shell and speed reducing motor, mixing stirring shaft assembly installed in mixing stirrer inside shell, and speed reducing motor and connected with the hopper for discharge port and is set with in mixing stirrer shell of the mixing stirrer shell on lower side part of the extruder inlet housing upper part position is provided, wherein on machine frame, between the blanking part and extruder feeding port upper shell installed with feeding impeller and impeller shaft, driven gear and driving gear respectively fixed on impeller shaft and main shaft of extrusion, and mesh mutually, the machine can produce from biomass, coal, combustion improver composed of prescription of biomass fuel, structure is novel, reasonable, whole size compact, the processing quality is good, the production efficiency high, using reliability, using life long.
NOVELTY - System has packed bed solid state fermentation bioreactor, where the bioreactor is adapted to contain and to operate using organic waste as fermentation substrate, and is provided with e.g. spray nozzle for controlling moisture content of the fermentation substrate, unit for supplying air to pass through packed bed of the fermentation substrate in the bioreactor, unit for analyzing gas content in the bioreactor, and unit for monitoring temperature in the bioreactor.    USE - The system is useful for producing glucoamylases and/or proteases (claimed).    ADVANTAGE - The system sterilizes waste by bleach before discharging to environment to prevent contamination, maintains optimal moisture content, and converts organic wastes, preferably food wastes into valuable protease and/or glucoamylase.    DETAILED DESCRIPTION - System has packed bed solid state fermentation bioreactor, where the bioreactor is adapted to contain and to operate using organic waste as fermentation substrate, and is provided with spray nozzle for controlling moisture content of the fermentation substrate, unit for supplying air to pass through packed bed of the fermentation substrate in the bioreactor, unit for analyzing gas content in the bioreactor, unit for monitoring temperature in the bioreactor, unit for controlling temperature of the bioreactor, and port through which a sample in the bioreactor is obtainable; and unit for harvesting enzymatic solution from the bioreactor, where the enzymatic solution comprises glucoamylases and/or proteases. An INDEPENDENT CLAIM is included for method of producing glucoamylases and/or proteases.
NOVELTY - The system has a catalytic material comprising oxygen and metal atoms, a bulk portion and a surface portion, where the surface portion forms a non-stoichiometric region under set conditions in contact with water. An electrode is in electronic communication with the catalytic material. The catalytic material comprises a perovskite structure, where the surface portion of the catalytic material comprises an overlayer and a sub-layer. The surface of the catalytic material oxidizes the water at a lower barrier than a bulk termination.    USE - Photoelectrolysis system for performing water-splitting used in a vehicle.    ADVANTAGE - The system provides electrical potential by illuminating a photoactive material in electronic communication with the catalytic material such that the illumination gives rise to an electronic potential applied to the catalytic material in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for performing water-splitting.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a photoelectrolysis system.
NOVELTY - Generating biogas from organic biomass e.g. energy crops, manure, solid manure and organic waste in a biogas plant having at least one fermentation vessel and a hydrolysis reactor, comprises pre-fermenting biomass to form a digestate in the fermentation vessel, hydrolyzing at least one portion of the digestate in the hydrolysis reactor, and post-fermenting the hydrolyzed digestate. The pre-fermented digestate is chemically hydrolyzed.    USE - The method and the biogas plant are useful for generating biogas from organic biomass e.g. energy crops, manure, solid manure and organic waste in a biogas plant (all claimed).    ADVANTAGE - The method and the biogas plant are economical and space saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant (100) for generating biogas from organic biomass e.g. energy crops, manure, solid manure or organic waste, comprising the fermentation vessel (1) in which the biomass to be fermented or digestate to be fermented is introduced and biogas and fermented digestate are removed, and the hydrolysis reactor (4) for receiving the fermented digestate from the fermentation tank, connected to the fermentation vessel, where at least one dosing device (8) is connected with a chemical storage and the hydrolysis reactor, for supplying a defined amount of a chemical to the hydrolysis reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biogas plant (Drawing includes non-English language text).    Fermentation vessel (1)    Hydrolysis reactor (4)    Gas scrubber (6)    Dosing device (8)    Biogas plant (100)
NOVELTY - Highly-clean methanol gasoline M85 comprises 84-86 vol.% methanol, 12-15 vol.% gasoline, and 1-3 vol.% M85 special modifying additive. The M85 special modifying additive is obtained by stir-mixing 20-30 vol.% t-butanol, 10-15 vol.% diisooctyl phthalate, 6-8 vol.% sec-butyl acetate, 8-10 vol.% N,N'-disalicylidene-1,2-propanediamine, 20-25 vol.% fatty acid diethanolamide, 4-8 vol.% dimethoxymethane, 3-7 vol.% hydrogen peroxide, 3-5 vol.% 1-n-propyl-2-pyrrolidone, 5-8 vol.% 1:1 n-octanol and dodecanol complex co-solvent, and 2-3 vol.% dehydrating agent.    USE - Highly-clean methanol gasoline M85 is used for vehicles.    ADVANTAGE - The highly-clean methanol gasoline M85 has excellent low-temperature cold stability, long-term storage stability, and combustion efficiency, enables easy separation of water phase, and does not cause metal corrosion and rubber swelling, all due to the presence of M85 additive. The fuel can be directly filled in existing vehicle engines without requiring engine modification.
NOVELTY - Removal of odor from biodiesel oil, involves adding and mixing water with biodiesel oil in a weight ratio of 0.01-1:1, preferably 0.03-0.3:1.    USE - Removal of odor from biodiesel oil (claimed).    ADVANTAGE - The method is simple, effective and convenient.
NOVELTY - The system (21) has a reforming furnace (25) which modifies a carbon containing non-gas component in pyrolysis gas. A boiler facilities (26) recovers a heat of the reformed gas discharged from the reforming furnace and generates a steam. A hydrogen peroxide is supplied with the steam which generates with water and/or the boiler facilities to carry out the partial combustion of the carbon containing non-gas component to supply an oxygen or air.    USE - Gasification processing system for thermal decomposition of biomass resources, such as general waste is supplied to gas engine as fuel and obtains reformed gas.    ADVANTAGE - Even if the temperature in a reforming furnace is lower than before, the tar discharges concentration from a reforming furnace is reduced. The tar removal rate of the reformation in high temperature and a same degree is acquired. The tar removal rate is improved, by adding hydrogen peroxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the gasification processing system. (Drawing includes non-English language text)    Gasification processing system (21)    Reforming furnace (25)    Boiler facilities (26)    Waste gas processing facility (27)    Gas engine (28)
NOVELTY - The system (21) has a gasifier (24) which thermally decomposes and gasifies biomass resources (22) and generates pyrolysis gas. A reforming furnace (25) reforms the carbon containing non-gas component. The boiler facilities (26) collect the heat of the reformed gas discharged from the reforming furnace and generate a vapor. A waste gas processing facility (27) for processing the waste gas discharged from boiler facilities. The carbon containing non-gas component is a wet dust precipitator using water washing and are collected by water washing is supplied to the reforming furnace.    USE - Gasification processing system used for thermally decomposing biomass resources e.g. general waste and obtain reformed gas.    ADVANTAGE - The energy loss of the gasification processing system is reduced by reducing supply to the vapor reforming furnace obtained by heat exchange with reformed gas by providing gasification processing system. The quantity supplied to the vapor reforming furnace which arose by heat exchange with reformed gas is reduced by the waste water containing the carbon containing non-gas component collected by the wet dust precipitator being supplied to a reforming furnace. The waste water originally discharged to the wastewater treatment system is weight-reduced and the amount of wastewater treatment is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the gasification processing system. (Drawing includes non-English language text)    Gasification processing system (21)    Biomass resources (22)    Gasifier (24)    Reforming furnace (25)    Boiler facilities (26)    Waste gas processing facility (27)
NOVELTY - The method involves modifying degradation product (4) which arises in the case of dry distillation by steam reforming reaction to produce carbon monoxide (CO) (5) and hydrogen (H2) (6). The hydrogen is utilized by a biomass charcoal (11) and carbon monoxide as an energy source (101).    USE - Utilization method of biomass used in factory.    ADVANTAGE - The biomass can be efficiently utilized as the energy source. The global warming is prevented and the manufacturing biomass charcoal can be easily modified. The usage-amount of expensive cokes and the discharge amount of carbon dioxide (CO2) derived from the cokes which are not carbon-free can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory diagram illustrating the utilization method of biomass.    Degradation product (4)    CO (5)    H2 (6)    Biomass charcoal (11)    Energy source (101)
NOVELTY - The substratum has cell culturing rooms (1,2) which are separated by partition (4). The patterns of cell-adhesion area (6) and cell non-bonded area (7) are formed in bottom portion of cells culturing room. The largest length of surface demarcated by outer edge of through-hole of partition is less than 1/2 of minimum length of surface demarcated by outer edge of cell adhesion area in patterns. The area of cell-adhesion area in pattern is smaller than area of cell-adhesion area in another pattern. The shape of pattern is different from shape of another pattern.    USE - Substratum for cell culture used in cytobiology research, medical study, and clinical laboratory testing field.    ADVANTAGE - The size of the cell assembly is controlled efficiently to generate and culture the cell. The target size and shape of the cell is collected selectively at the time of culture of cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing cell culture substratum.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cell culture substratum.    Cell culturing rooms (1,2)    Partition (4)    Cell-adhesion area (6)    Cell non-bonded area (7)    Cell sheet (8)
NOVELTY - The installation has a heat-resistant housing (3) including a first chamber (5) for gasification of liquid fuels and liquefied waste. The first chamber is connected with a second chamber (6) through a bath unit (7). The second chamber is connected to a gas flow channel (P) through a primary combustion chamber (10) and a secondary combustion chamber (11). A gas channel is connected to a combustion chamber (12) that is integrated with a cyclone part (13). The second gasification chamber is connected to an outlet channel of a receiver of synthesis gas (S).    USE - Installation for thermal treatment of municipal or industrial solid and liquefied waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an installation for thermal treatment of municipal or industrial solid and liquefied waste.    Gas flow channel (P)    Synthesis gas (S)    Heat-resistant housing (3)    Chambers (5, 6)    Bath unit (7)    Primary combustion chamber (10)    Secondary combustion chamber (11)    Combustion chamber (12)    Cyclone part (13)
NOVELTY - The utility model provides a biomass effecitvely using distributive energy system based on fuel gas internal combustion engine. The energy system comprises carbonization furance, purification system, fuel gas internal combustion engine power generation unit and smoke recycling system, carbonization furnace and gas discharge pipe through gas pipe and gas internal combustion engine power generation unit and gas import connected, the purification system includes in turn mounted on fuel gas pipeline of the first cyclone separator, liquid separator, wood tar separator, the first filter component, active coal, the second filter component and fuel gas cooling device, the recycling system comprises smoke waste heat recovery boiler and absorb type refrigerator, a fuel gas internal combustion engine power generation unit and engine smoke gas discharge tube separately recovery boiler and heating chamber and absorb type refrigeration machine connected and waste heat, waste heat recovery boiler smoke gas discharge pipe and the furnace heating chamber connect. This new utility model can be the same when generating charcoal, gas, wood tar and electric power, steam and low temperature water equal, biomass energy use ratio can reach 90%.
NOVELTY - Netupitant or its pharmaceutically acceptable salt is synthesized by reducing ethyl(6-(4-methylpiperazin-1-yl)-4-(o-tolyl)pyridine-3-yl)carbamate and subsequently coupling resulting compound with 2-(3,5-bis(trifluoromethyl)phenyl)-2-methylpropanoyl chloride.    USE - Synthesis of netupitant or its pharmaceutically acceptable salt.    ADVANTAGE - The process has shorter reaction time and is environment-friendly, economical, and free from hazardous reagents and extremely difficult reaction conditions.    DETAILED DESCRIPTION - Netupitant or its pharmaceutically acceptable salt is synthesized by reducing ethyl(6-(4-methylpiperazin-1-yl)-4-(o-tolyl)pyridine-3-yl)carbamate of formula (3H) and subsequently coupling resulting compound with 2-(3,5-bis(trifluoromethyl)phenyl)-2-methylpropanoyl chloride of formula (T). INDEPENDENT CLAIMS are included for:    (1) ethyl(6-(4-methylpiperazin-1-yl)-4-(o-tolyl)pyridine-3-yl)carbamate of formula (3H);    (2) synthesis of netupitant and its pharmaceutically acceptable salts which involves coupling compound of formula (2J) with o-tolyl boronic acid;    (3) synthesis of netupitant and its pharmaceutically acceptable salts which involves coupling of compound of formula (2H) with 2-halo substituted toluene;    (4) compound of formula (2J);    (5) preparation of compound of formula (2J) which involves condensing 4-chloro-6-(4-methylpiperazin-1-yl)pyridin-3-amine with 2-(3,5-bis(trifluoromethyl)phenyl)2-methylpropanoyl chloride in the presence of an organic base;    (6) compound of formula (2H); and    (7) an amorphous netupitant.    X=alcohol-protecting group, e.g. Cl, Br, OCH3, OTf, OBz, or o-pivaloyl.
NOVELTY - A transformed oleaginous cell, comprising a first genetic modification, where the first genetic modification increases the activity of a native diacylglycerol acyltransferase (DGAT), or encodes a copy of a DGAT gene native to the oleaginous cell or from a different species; and a second genetic modification, where the second genetic modification decreases the activity of a triacylglycerol lipase (TGL) in the oleaginous cell, is new.    USE - The transformed oleaginous cell is useful for producing lipids. The lipids are used in multiple industrial applications, including in the cosmetic and food industries, as well as precursors for biodiesel and biochemical production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of increasing the lipid content of a cell by transforming a parent cell with a first nucleic acid and a second nucleic acid; where the first nucleic acid increases the activity of a native DGAT or comprises a DGAT gene; and the second nucleic acid decreases the activity of a TGL.
NOVELTY - Catalyst (C1) comprises a mixed oxide base material comprising erbium and at least one further lanthanide element.    USE - The catalyst is useful as a nanowires catalyst, and for conversion of methane to more than 2C hydrocarbons (all claimed).    ADVANTAGE - The catalyst exhibits a more than 2C selectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at less than or equal to 750 degrees C (claimed), thus improving the yield, selectivity and conversion of methane to more than 2C hydrocarbons.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a catalyst (C2) comprising a mixed oxide base material that comprises two different lanthanide elements, where one of the lanthanide elements is not lanthanum when the other lanthanide element is neodymium;    (2) a catalyst (C3) comprising a mixed oxide base material comprising three different lanthanide elements;    (3) a catalyst (C4) comprising a base material comprising an oxide of at least one lanthanide element and a dopant combination comprising strontium/samarium, strontium/gadolinium, strontium/dysprosium, strontium/erbium, strontium/lutetium, strontium/barium/boron, barium/boron, barium/strontium, erbium/tungsten, strontium/potassium, barium/cerium, barium/hafnium, gallium/magnesium, magnesium/erbium, yttrium/barium, strontium/gallium/magnesium, strontium/yttrium, strontium/boron/yttrium, calcium/boron, strontium/aluminum, barium/tungsten, boron/tungsten, strontium/barium/tungsten, strontium/tungsten/boron, barium/tungsten/boron or strontium/barium/tungsten/boron;    (4) a catalyst (C5) comprising a group 4 or lanthanide oxide in combination with an alkaline earth metal dopant; and    (5) conversion of methane to more than 2C hydrocarbons, comprising contacting the catalyst (C1) with methane and an oxidant source.
NOVELTY - The method involves periodically delivering a cleaning gas comprising oxygen from a cleaning gas source into a reaction tube (103) without stopping propagation of microwave energy into the reaction tube. Plasma is formed in the reaction tube from the cleaning gas in the presence of the microwave energy such that the plasma causes burning off of a carbon residue film from the reaction tube. The cleaning gas is extracted from the product stream. The extracted cleaning gas is delivered to the cleaning gas source.    USE - Method for processing hydrocarbon material e.g. fossil hydrocarbons and biomass coal, using microwave energy. Can also be used for processing bitumen, oil, sand, tar sands, oil shale, petroleum residue, asphaltenes, pre-asphaltenes or vitrinite and kerogen-containing materials, municipal waste, sludge, and carbon-rich materials.    ADVANTAGE - The method enables using microwave energy to induce electric discharges in ionized gas that rapidly and locally heat surrounding gas and hydrocarbon feedstocks, thus converting or upgrading the feedstock for delivery into a product storage facility, and hence maximizing production by providing the flow of feedstock and process gas on a continuous basis. The method enables removing the films without a need to take a unit offline for maintenance and a need for vacuuming to remove carbon deposits so as to ensure minimum disruption to operation.    DETAILED DESCRIPTION - The cleaning gas comprises argon and steam.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for processing hydrocarbons.    Reaction tube (103)    Hydrocarbon feedstock sources (105)    Process gas source (107)    Product storage vessels (109)    Microwave generator (111)    Waveguide (113)
NOVELTY - A Kluyveromyces marxianus strain No. 21 (NITE BP-01739) or its mutant strain having xylose assimilating ability and ethanol producing ability when cultured at 30 degrees C under aerobic conditions from a culture medium containing xylose as a sugar source, is new.    USE - The K.marxianus strain No. 21 or its mutant strain is useful for assimilating xylose and producing ethanol (all claimed) which is used as biofuel.    ADVANTAGE - The K.marxianus strain No. 21 or its mutant strain produces ethanol cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing ethanol, which involves culturing the K.marxianus or its mutant strain in a culture medium containing xylose as a sugar source, under aerobic condition.
NOVELTY - Method for applying reducible fertilizer, involves applying the reducible fertilizer obtained by hydrothermal reaction of mixture of yeast or yeast component and phosphoric acid and/or potassium to plant to leaf surfaces of the plant from beginning of physiological fruit drop until harvesting of fruit.    USE - The method and medicinal agent are useful for suppressing leaf fall after harvesting deciduous fruit tree chosen from apple, pear, cherry, peach, plum, apricot, loquat, grape, and prune by increasing storage nutrient of the deciduous leaves fruit tree (all claimed) and preventing fruit drop before harvesting fruit.    ADVANTAGE - The method improves weight of the fruit, and is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for medicinal, which is prepared by performing hydrothermal reaction of mixture of component of yeast or yeast, and phosphoric acid and/or potassium.
NOVELTY - Preparation of bispyrazole compound (II) involves reacting bromobenzene derivative (I) with hydrazine. The molar ratio of compound (I) and hydrazine is 1.0:5.2-1.0:11.7.    USE - Preparation of bispyrazole compound. Uses include but are not limited to pharmaceutical and agrochemical material, analytical reagent, dye, pigment, optical material and electronic material.    ADVANTAGE - The method provides bispyrazole compound with high purity, by safe process without requiring purification process. The generation of side reaction is prevented.    DETAILED DESCRIPTION - Preparation of bispyrazole compound of formula (II) involves reacting bromobenzene derivative of formula (I) with hydrazine. The molar ratio of compound (I) and hydrazine is 1.0:5.2-1.0:11.7.    R1,R2=optionally substituted aryl.
NOVELTY - Method for preparing a sugar product from lignocellulosic material, involves (a) optionally, pretreating lignocellulosic material, (b) optionally, washing pretreated lignocellulosic material, (c) performing enzymatic hydrolysis of optionally washed and/or optionally pretreated lignocellulosic material using an enzyme composition comprising at least two cellulases and a laccase, and (d) optionally, recovering a glucose-containing composition.    USE - The method is useful for preparing a sugar product from lignocellulosic material. The method is useful for preparing a fermented material from the lignocellulosic material (all claimed).    ADVANTAGE - The method prepares product simply, cost-effectively and rapidly with reduced dosage of enzymes.    DETAILED DESCRIPTION - Method for preparing a sugar product from lignocellulosic material, involves (a) optionally, pretreating lignocellulosic material, (b) optionally, washing pretreated lignocellulosic material, (c) performing enzymatic hydrolysis of optionally washed and/or optionally pretreated lignocellulosic material using an enzyme composition comprising at least two cellulases and a laccase, where the enzyme composition comprises lytic polysaccharide monooxygenases (LPMO), and (d) optionally, recovering a glucose-containing composition, where after the pretreatment and before and/or during the enzymatic hydrolysis oxygen is added to the lignocellulosic material. An INDEPENDENT CLAIM is included for method for preparing a fermentation product from lignocellulosic material, which involves performing the above-mentioned steps (a)-(c), and then optionally purifying the hydrolysed lignocellulosic material, fermenting the hydrolysed lignocellulosic material to produce a fermentation product, and recovering fermentation product.
NOVELTY - A reaction tube for the steam-reforming of at least one C2+ hydrocarbon and/or a C2+ alcohol and water vapor, comprises: an entrance area for supplying the reagents, a catalyst zone where the reaction occurs and catalyst is deposited; and an area of generation and/or gas outlet which is refurbished because the inlet zone and catalytic zone of the tube is formed by a metallic stainless steel alloy containing no nickel or a stainless steel alloy coated by a nickel-free material.    USE - The reaction tube is useful for the steam-reforming of at least one C2+ hydrocarbon and/or a C2+ alcohol and water vapor (claimed).    ADVANTAGE - The reaction tube allows for efficient and effective reforming of hydrocarbons and alcohols for the production of hydrogen then used to produce electrical energy using fuel cells. Also, the reaction tube avoids the formation of coke, thus preventing clogging of the tubes and/or increasing pressure drop and consequent loss of catalyst efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a reformer for a steam reforming system water comprising at least one reaction tube.
NOVELTY - The method of improving oxidation stability of biodiesel involves placing biodiesel and methyl isostearate according to specific proportion into reaction kettle, blending biodiesel higher than the solidification point of 5 degrees C, and stirring under atmospheric pressure for 0.5 hour.    USE - The method is useful for improving oxidation stability of biodiesel (claimed).    ADVANTAGE - The method improves oxidation stability of biodiesel in a simple and safe manner.
NOVELTY - This new utility model claims the cooling device and one of a kind of biomass carbonizing furnace, comprising cooling room in the biomass carbonizing furnace in the furnace lower part in the biomass carbonizing furnace after carbonizing furnace and high temperature biological carbon from cooling chamber top and wherein feedstock entering into cool indoor, set up with discharging port on bottom cooling chamber, with mobile furnace grate to set in feedstock wherein the cooling chamber and feedstock port from entering into the high temperature biological carbon can stack up on mobile furnace grate, and dropping to cool in room through gap of the mobile furnace grate, set up with discharge port and mutually connect the hopper, hopper outlet valve and connected with bottom in cooling room, set up and cooling chamber communicated with the way of hole on hopper side wall, cooling gas can pass way hole entering into indoor cooling. This new utility model is advantages as: can uniformly, full cooling high temperature biological carbon, show the biological carbon and air input contact and then the oxidation.
NOVELTY - This new utility model claims of one of a kind of biomass carbonizing furnace and continuous feedstock transport device, comprising furnace body with the inner cavity, a furnace body inner cavity from upper to lower in turn set up with drying room, carbonization chamber, high temperature chamber and cooling chamber of four chamber, each adjacent chamber respectively separated by mobile furnace grate, wherein the feedstock drying room top part and the furnace body top phase connect, has set up for hopper in the furnace top, wherein the feedstock discharge port and furnace top hopper for the mutually connected, also set with feedstock, feedstock control device can prevent the gas of the furnace body inner cavity from feedstock the hopper mouth to leak out between feedstock wherein at the discharge port of the hopper and the furnace body for top. This new utility model is advantages as: can realize continuous production, and the furnace material is heated evenly in full.
NOVELTY - This new utility model relates to one used for a kind of the biomass feedstock pressurizing device, comprising storage unit, stirring unit, spiral element and pneumatic transport unit. Through setting sealing device, using feedstock device stable feedstock under at 0-1.0MPa pressure condition. Using rotary blade of the snail rod extrusion, loose air blowing and vibrator vibration, biomass material by spiral and is sent in, by gas force transport enter into reactor. Through balance pipeline regulating cabin pressure to prevent the material gas pipeline in pressure difference and cause excessive feedstock not smooth, problem of low density, poor in flowability and biomass to show bridging, channelling, agglomeration and blockage and in transport course equal problem, using biomass can continue, stable feedstock at low pressure condition. The device operation flexible, can the pressurizing operation, wherein screw rotation and at the same time the feeding the feedstock seal device, system pressure, influence the air quantity small, is suitable for variety, device occupying small area, has the good engineering practicability.
NOVELTY - This new utility model claims of a kind of one tower type biomass continuous carbonization furnace, comprising furnace body and installation base, a furnace body inner cavity from upper to lower in turn provided with drying room, carbonization chamber, high temperature chamber and cooling chamber, each adjacent chamber respectively through mobile furnace grate; equipped with combustion chamber at high temperature of room side wall, provided with the first upper belt in the furnace body side wall, and the second air inlet nozzel, nozzel head extends in the combustion chamber, the second air inlet and a draught fan with burner is connected with the hopper by feedstock for control device and the furnace body inner cavity mutually connected, with hopper is set with ash discharging valve on the furnace body bottom, and drying chamber mutually connected equipped with the gas channel, the gas channel and gas purification cooling system mutually connected on the furnace body top, outlet of gas purification cooling system through transporting pipeline respectively and the way of the second air inlet nozzel hole and hopper and connected mutually, the first fan equipped with on of transporting pipeline. The advantages is: can realize continuous production, low energy consumption, biological coal high yield, good quality and stable quality.
NOVELTY - This utility model new one of biomass fuel gas use and remove coke, wherein remove coke (4) is drawer-type filter, remove the coke tank (4) equipped with middle part clapboard (48) will remove the coke tank (4) divided and lay out , and lay out on remove coke tank (4) bottom connect mutually, and lay out top separately provided with air inlet pipe (41) and air outlet pipe (42), remove the coke tank (4) top and bottom set with cover plate (46) and bottom plate (45), wherein the bottom plate (45) is set with lower bracket (47), remove the coke tank (4) provided with can extract out of the box (43), box (43) set with upper remove coke silk net (44). This utility model new one of biomass fuel gas use and remove coke, biomass fuel combustion full use, increase of heat efficiency high, saves energy, without smoke and dust discharge, effective environmental protection.
NOVELTY - Of the new utility model claims of one with nitrogen alkyl cooling function of the separated methane gas device, it comprises heat exchanger (1), a rectifying tower (2) and product channel set up in heat exchanger (1) in the (3), a tail gas channel (4), a methane-rich gas channel (5), flow nitrogen methane passage I (6), flow nitrogen methane channel II (7), a nitrogen methane passage (8) and alkyl nitrogen cooling channel (9), a nitrogen methane expand compressor (12) is connected with nitrogen methane expansion machine (14), flow nitrogen methane passage II (7) is outlet end D too nitrogen and methane circulation compressor (10) connected with. The utility model is new beneficial effect is: it saves production cost, can reduce investment and energy consumption and operation complexity of separating device, and can increase benefit and competitive power of liquid.
NOVELTY - This new utility model claims of one use of liquefied natural gas washing rich methane gas and nitrogen gas and device of carbon monoxide, it comprises washing tower (1), a rectifying tower (3) and product cooler (4), a washing tower (1) is outlet end C and rectifying column (3) entrance end F is connected with the rectifying tower (3) and outlet terminal E orderly connected rectifying tower with tower top cooling device (7) and tower top rectifying tower relux tank (8), a rectifying tower (3) is outlet end D and product cooler (4) and entrance end connected with, product cooler (4) outlet end and the relux pump (2) and entrance end connected with the relux pump (2) outlet end and the washing tower (1) and entrance end N connected with the rectifying tower (3) is internal and the rectifying tower (3) bottom is set with bottom tower boiling heat device (9). This new utility model the beneficial effect is: structure is compact, placing the purifying device can follow-up rich hydrogen reducing, washing rich methane gas and nitrogen gas and carbon monoxide and high efficiency.
NOVELTY - The installation has an electrolytic cell provided with a decontamination chamber (1) and a neutralization chamber (21) that are separated by a cation-active or anion-active membrane (15). The decontamination chamber comprises an anode (4), a cathode (5) and a protective iron electrode (7). A 3D electrode bed (6) is arranged between anode and cathode systems. The neutralization chamber comprises an auxiliary cathode (8). Electrodes are electrochemically decomposed with hydrogen and oxygen. A catalyst is arranged in the 3D electrode.    USE - Wastewater treatment installation.    DETAILED DESCRIPTION - The 3D electrode bed is provided with catalyst particles that are selected from a group consisting of metallic palladium on activated charcoal, metallic palladium on titanium oxide, metallic palladium, alumina and gold.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a wastewater treatment installation. '(Drawing includes non-English language text)'    Decontamination chamber (1)    Anode (4)    Cathode (5)    3D electrode bed (6)    Protective iron electrode (7)    Auxiliary cathode (8)    Cation-active or anion-active membrane (15)    Neutralization chamber (21)
NOVELTY - Culture medium comprises (a) one or more ammonium salt chosen from ammonium sulfate, ammonium nitrate, ammonium chloride and ammonium carbonate, (b) one or more inorganic acids comprising phosphoric acid and/or its metal salt, and (c) one or more sodium salts chosen from sodium chloride, sodium sulfate and sodium hydrogen sulfate. The cell cultured in the culture medium is modified. The concentration of the inorganic acid in the culture medium is 0.5 mu mol -1 mM. The pH of the culture medium is 1-3.    USE - The culture medium in form of liquid or powder is useful for culturing red algae, preferably Cyanidium at 40 degrees C or more and producing lipid (all claimed) which is used as raw material of biofuel.    ADVANTAGE - The culture medium enables to produce in lipids cost-effectively in larger-quantities by maintaining proliferation of the red algae and reduces risk of contamination by other microorganism even when used in open culture system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing lipid, which involves taking the culture medium, culturing the red algae, preferably Cyanidium in the culture medium, and recovering lipids derived from culture.
NOVELTY - Method for preparing organic fertilizer involves (a) packing root and leaf vegetables using adhesive tape, and burying packed vegetables in a pit for 10-20 days, (b) drying rapeseed and rice straw, feeding dried rapeseed and rice straw to sheep, collecting sheep manure after excretion, mixing sheep manure and chicken manure in a weight ratio of 1:10, and adding mixture into fermentation tank, (c) adding buried vegetables into fermentation tank, and mixing mixture, (d) covering mixture with water, and fermenting mixture at 35-40 degrees C for 45 days.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to improve soil fertility, loosen soil, improve soil aggregate structure, increase water retention capacity and soil organic matter, and activate soil, which improves crop growth, crop vitality, and immunity.
NOVELTY - Water is electrolyzed and oxygen is produced. The oxygen produced and hydrogen are reacted with natural gas containing carbon monoxide and hydrogen. Synthesis gas produced is reacted, and natural gas processed material is obtained.    USE - Manufacture of natural gas processed material e.g. methanol, gas-to-liquid oil and dimethyl ether (all claimed).    ADVANTAGE - The method enables energy effective synthesis of the processed material using a compact installation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for natural gas process plant (10), which is used for manufacturing natural gas processed material and contains electrolyzer, synthesis gas production apparatus (15), and natural gas processed material manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the natural gas process plant. (Drawing includes non-English language text)    Natural gas process plant (10)    Solar fuel installation (11)    Electric power generating apparatus (12)    Seawater desalination installation (13)    Carbon dioxide separation apparatus (14)    Synthesized gas production apparatus (15)    Methanol purifier (17)    Hydrogenation installation (18)
NOVELTY - This new utility model claims of one of biomass coal, gas, wood tar and pyroligneous cogeneration system, comprising biomass dry distillation kettle, heating furnace, cooling tank, water cool device, washing device and water storage tank, a cooling tank through output port of the first pipe and biomass dry distillation kettle connected with the cooling tank through the second pipe and cold water and part of water cool device before mixed gas import connected, water cold water cold device and after mixed gas outlet through the third pipeline and water washing device is water washing before mixed gas import connected, water washing device and water back washing gas mixture outlet via the fourth pipeline and , cooling tank through connected pipe connected with liquid level control tank, liquid level control tank through the fifth pipeline connected with mixed liquid storage tank, the fifth pipe mounted above the first transporting pump, water cool water cool device after mixing liquid outlet through the sixth pipeline and liquid level control tank connect. The cogeneration system can reducing water cold device is arranged, saving of production cost, increase of cooling effect and gas liquid separation effect.
NOVELTY - This new utility model claims of one three-dimensional box type heat source of biomass grain, it includes from up to down in turn install the spiral transporting burdening device, a furnace body, a air patenting device, water cool device and upper bin, the spiral transporting device installed with burdening bin, the furnace body hearth by inner clapboard divide preheat zone, a carbonization zone, cooling zone, the preheat zone furnace body installed with mixing gas recycling pipe, the carbonization zone mounted with carbonization furnace body recycling pipe, the cooling area furnace body installed with cooling mixed gas recycling pipe, the air patenting device two side respectively set with air inlet and air outlet, the water cold device two side respectively set with water inlet and water outlet, the two side cabin installed with spraying device, the bottom mounted with spiral input device, using biomass grain in put in the device, from up to down in turn through each device, complete carbonization of biomass. The product effective processing waste biomass, using regeneration resource recovery, implement waste use, energy saving and environmental protection.
NOVELTY - This new utility model provide a kind of one container modularized distributed type biomass energy for more efficient cogeneration system. The cogeneration system includes, multi-purification system, fuel gas internal combustion engine power generation unit and smoke recycling system, carbonization furnace and gas discharge pipe through gas pipe and gas internal combustion engine power generation unit and gas import connected, the purification system includes in turn mounted on fuel gas pipeline of the first cyclone separator, liquid separator, wood tar separator, the first filter component, active coal, the second filter component and fuel gas cooling device, the recycling system comprises smoke waste heat recovery boiler and absorb type refrigerator, a fuel gas internal combustion engine power generation unit and engine smoke gas discharge tube separately recovery boiler and heating chamber and absorb type refrigeration machine connected and waste heat, waste heat recovery boiler smoke gas discharge pipe and the furnace heating chamber connect. This new utility model can be the same when generating charcoal, gas, wood tar and electric power, steam and low temperature water equal, biomass energy use ratio can reach 90%.
NOVELTY - A soil improvement preparation comprises 40-50 pts. wt. silicate, 10-20 pts. wt. activated charcoal, 10-20 pts. wt. alum, 10-20 pts. wt. Bacillus subtilis powder, 10-20 pts. wt. nitrogen-fixing bacteria powder, 25-35 pts. wt. fulvic acid, 15-25 pts. wt. chlorogenic acid, 15-25 pts. wt. amino acid, 20-30 pts. wt. straw rotten agent and 10-20 pts. wt. slag.    USE - The soil improvement preparation is useful for seedling plant, agricultural areas and for eliminating organic substances, harmful microorganism and heavy metal in water.    ADVANTAGE - The soil improvement preparation: can be prepared using cheap abundant raw material in a simple and safe manner; and can quickly and thoroughly eliminates heavy metals and harmful microorganisms in water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of soil improvement preparation.
NOVELTY - An iodobenzamide derivative (I) is new.    USE - New iodobenzamide derivative used as catalyst for oxidizing alcohol (claimed) to produce ketone and carboxylic acid used in manufacture of fine chemicals, pharmaceuticals and agrochemicals.    ADVANTAGE - The iodobenzamide derivative is environmentally-friendly, and can be manufactured even under low-temperature conditions.    DETAILED DESCRIPTION - An iodobenzamide derivative of formula (I) is new.    R1=H, halo, alkyl, alkoxy, acyl, acyloxy or nitro;and    R2,R3=H, cycloalkyl, alkylsulfonyl, arylsulfonyl, or alkylene or alkyl (both optionally substituted).    An INDEPENDENT CLAIM is included for oxidation of alcohol, which involves using iodobenzamide derivative (I) as catalyst and co-oxidation agent.
NOVELTY - Recovery of methane from a gas stream (1) containing methane and ethylene, involves contacting the gas stream with a sorption agent which has a lower affinity for methane than ethylene, resulting in sorption of ethylene and 0-90% methane by the sorption agent and in a gas stream containing 10-100% methane, and desorbing sorbed ethylene and optionally sorbed methane resulting in a gas stream comprising ethylene and optionally methane.    USE - Recovery of methane from gas stream containing methane and ethylene (claimed).    ADVANTAGE - The process enables economical and efficient separation of methane from a gas stream comprising methane and ethylene at a relatively low pressure (e.g. at most 15 bar) and at a non-cryogenic temperature (e.g. 0-100 degrees C), with reduced energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a process involving sorption, desorption and distillation of a gas stream.    Gas streams (1,2,3)    Top stream (4)    Bottom stream (5)    Single stream (6)
NOVELTY - A tertiary diamine (I), is new.    USE - New tertiary diamine is used for removal of acid component e.g. hydrogen sulfide from gas effluent e.g. natural gas, synthesis gas, flue gas, refinery gas and gas generated from amine unit, Claus process, fermentation of biomass, cement factory and incinerator (all claimed).    ADVANTAGE - The tertiary diamine compound enables removal of acid component from gas effluent with high selectivity and yield, by economical process, with reduced energy consumption, within short period of time.    DETAILED DESCRIPTION - A tertiary diamine of formula (I), is new.    R1=methyl or ethyl;and    R2-R5=H or 1-6C alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of compound (I); and    (2) method for removal of acid component from gas effluent, which involves contacting gas effluent comprising acid compound with absorbing solution comprising water and compound (I).
NOVELTY - Improving fuel value of organic wastewater biotransformed alcohol-based fuel comprises adding 1-4% diethyl ether and dicyclopentadienyl iron into organic wastewater biotransformed alcohol-based fuel and stirring.    USE - The method is useful for improving fuel value of organic wastewater biotransformed alcohol-based fuel (claimed).    ADVANTAGE - The biological fuel: ensures complete combustion in a boiler.
NOVELTY - Preparing benzoic acid esters (I), comprises adding benzonitrile compound, an alcohol or phenol compound, a copper catalyst and an organic solvent into a reaction vessel, mixing, and reacting by stirring at 80-120 degrees C for 20-30 hours under oxygen atmosphere, then cooling to room temperature, washing with saturated ammonium chloride solution, extracting with an organic solvent, drying, distilling under reduced pressure to remove the solvent, and purifying obtained crude product by column chromatography.    USE - The method is useful for preparing benzoic acid esters (claimed).    ADVANTAGE - The method: utilizes cheap and easily available raw materials and copper catalyst; has mild reaction conditions, high product yield and high conversion rate; and is environment-friendly.    DETAILED DESCRIPTION - Preparing benzoic acid esters of formula (I), comprises adding benzonitrile compound, an alcohol or phenol compound, a copper catalyst and an organic solvent into a reaction vessel, mixing, and reacting by stirring at 80-120 degrees C for 20-30 hours under oxygen atmosphere, then cooling to room temperature, washing with saturated ammonium chloride solution, extracting with an organic solvent, drying, distilling under reduced pressure to remove the solvent, and purifying obtained crude product by column chromatography.    R = H, Cl, Br, methyl, nitro, methoxy or trifluoromethyl; and    R1 = 2-8C alkyl, benzyl, p-methoxybenzyl, p-nitrobenzyl, p-(trifluoromethyl)benzyl, 1-phenylethyl, 1-naphthylmethyl, 2-naphthylmethyl, 3-furylmethyl, 3-thiophenylmethyl, phenyl, p-methylphenyl, p-nitrophenyl, m-nitrophenyl, m-methoxyphenyl, o-bromophenyl or 2-naphthyl.
NOVELTY - Synthesis of caffeine involves carrying out methylation of theophylline or its sodium salt in presence of phase transfer catalyst using dimethyl carbonate as methylation reagent.    USE - Synthesis of caffeine (clamed).    ADVANTAGE - The method enables simple, economical and environmentally-friendly synthesis of high-purity caffeine with high yield and without waste generation.
NOVELTY - A rare-earth praseodymium(III)-tricarboxylic acid complex (I) having porous structure, is new.    USE - New rare-earth praseodymium(III)-tricarboxylic acid complex is used in adsorption of energy gases e.g. carbon monoxide, carbon dioxide, methane, hydrogen sulfide and hydrogen, preferably hydrogen gas (all claimed).    DETAILED DESCRIPTION - A rare-earth Praseodymium(III)-tricarboxylic acid complex having porous structure of formula: (Pr(L)(H2O)(DMF)), is new.    L=5-(4-(4-carboxyphenyl)phenyl)benzene-1,3-dicarboxylic Acid of formula (I).    An INDEPENDENT CLAIM is included for preparation of rare-earth praseodymium(III)-tricarboxylic acid complex, which involves dissolving 106.84 mg (0.03 mmol) praseodymium perchlorate in 5 mL water, dissolving 5-(4-(4-carboxyphenyl)phenyl)benzene-1,3-dicarboxylic acid as ligand in 5 mL water and 5 mL dimethylformamide, mixing the obtained solutions, adding 15 mL water to the mixed solution, placing in autoclave at 120 degrees C for 3 days and cooling to obtain a colorless transparent crystal.
NOVELTY - This new utility model claims of one of internal combustion type biomass particle material drying, carbonizing, activate integrated furnace, comprising the furnace body, the furnace body from above downward in turn provided with drying section, sealing section material, a carbonization section, activate segment, steam generating section and cooling section, the side wall of the drying section connected the inner cavity provided with the wet smoke gas outlet pipe, and carbonizing section equipped with upper tube tank, and activate section provided with , of part connected with the lower pipe box, the pipe box and the following upper tube box through connected between, the upper pipe box by rising smoke material sealing section is connected through wet smoke gas outlet pipe, the sleeve and extending to outside of the furnace body connected, outside end of the sleeve set with connected air import pipe and coal combustion tube of combustion nozzle, and the steam generating section bottom is equipped with cold water chamber and water-spraying hole plate, the cooling section outside wall set with coil, the water cool chamber by water cold pipe coil connected.
NOVELTY - This new utility model claims a novel energy saving sewage purification device, a water electrolytic system, a combustion chamber, a condenser, oxygen transporting pipe, hydrogen transporting pipeline, steam transporting pipe, oxygen storage tank and hydrogen storage tank, a heat transporting pipeline. Electrolytic water system in the anode pool through oxygen transport pipeline connected with oxygen storage tank and combustion chamber, a cathode hydrogen transporting pipeline by a hydrogen storage tank and a combustion chamber. Outside the electrolytic water system is covered with a jacket, electrolytic pool electrolytic jacket by hot air transporting pipe connected with the combustion chamber the combustion chamber jacket. Outside combustion chamber installed with external combustion engine and generator, the external combustion engine further a combustion indoor heat drive the electric generator generate electricity, a combustion chamber connected with the condenser. The condenser setting at the combustion chamber the upper part, a condenser and the lower part connected with water storage tank. This new utility model effectively increase energy use ratio, reducing energy consume, water purification degree high, can directly.
NOVELTY - A kind of a biomass grain fuel production line, a material pulverizer, the raw material conveying belt, a mixer, a mixing belt, a stirrer, a magnetic, forming raw material conveying belt, a pressing block forming machine, blank conveying belt, drying workshop, composed of packing machine. Mixer through full mixing the biomass particle fuel and raw material, a mixed material conveying belt transporting a stirrer in full stirring, again forming a raw material conveying belt transporting a block forming machine in a pressing process to make blank, again a blank conveyor for transporting a blank drying workshop, carrying out drying treatment, through drying processing the blank to obtain the biomass particle fuel and biomass particle fuel through a packaging machine, a package as a commodity sale or use. And the existing technology, this utility new type machine with a stable, work efficiency high, using a suitable positive effect.
NOVELTY - Fertilizer composition comprises 40-44 pts. wt. coal, 42-46 pts. wt. urea, 5-8 pts. wt. monoammonium phosphate, and 1-2 pts. wt. Bacillus subtilis, prepared by mixing components, crushing, stirring, pelletizing, drying, sieving, and packaging.    USE - The fertilizer composition is used for corn planting (claimed).    ADVANTAGE - The fertilizer composition is rich in nutrient, uses less auxiliary component, and has good physical and chemical properties.
NOVELTY - The device has an esterification reaction tower (30) which is provided with tower main portion (32), reboiler (34) and glycol circulation pump (36). One end of reboiler is connected to bottom of tower and another end is connected to reboiler temperature section. One end of circulation acid pump is connected to extract device and another end is connected to pre-heater (20) that is fixed to distributor (324). One end of esterification lipid pump (40) is connected to bottom of tower main portion and another end is connected to ester exchange reactor (50) through pre- heater.    USE - Device for preparing biologic diesel oil.    ADVANTAGE - The conversion rate and yield are high.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing biologic diesel oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of device for preparing biologic diesel oil. (Drawing includes non-English language text)    Pre-heater (20)    Esterification reaction tower (30)    Tower main portion (32)    Reboiler (34)    Glycol circulation pump (36)    Esterification lipid pump (40)    Ester exchange reactor (50)    Distributor (324)
NOVELTY - The method involves converting the tetrahydronaphthalene (5) to biofuel material. The conversion reactor is preheated to a specified temperature. The lignocellulosic biomass feedstock is added to a screw feeder funnel. The first reactor is purged with an inert gas, before discharge reaction, and tetralin is added with a peristaltic pump (6). Mixed gas of gas and water vapor are added together in the reactor. The micro-streamer discharge control system is turned-off, when the shock excitation voltage is adjusted and the discharging reaction is started.    USE - Method for preparing plasma discharge circuit conversion straw biological fuel.    ADVANTAGE - The preparation process is environment-friendly, increased quality, effective conversion rate and improved production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of preparation process of plasma discharge circuit conversion straw biological fuel.    Tetrahydronaphthalene (5)    Peristaltic pump (6)    Mixing machine (7)    Plasma conversion reactor (8)    Medium (9)
NOVELTY - Treatment of an aqueous mixture involves introducing an aqueous mixture comprising at least one kinetic hydrate inhibitor (KHI) and hydrolyzed polyacrylamide (HPAM) to a treatment vessel, subjecting the aqueous mixture to superatmospheric pressure and elevated temperature in or upstream of vessel, contacting catalyst with the aqueous mixture for specific period of time to disrupt chemicals bonds, and separating the disrupted portion of KHI or HPAM for producing treated aqueous mixture having a residual level of KHI or HPAM below predetermined threshold.    USE - Treatment of aqueous mixture e.g. produced water or derived from produced water formed by enhanced oil recovery process for producing methane (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a treating system.    Storage tank (10)    High pressure pump (14)    Heat exchanger (20)    Reactor vessel (24)    Separator vessel (32)
NOVELTY - The utility model claims a.... a collsion catalyze double catalyze water fuel system for preparing, preparing mineral or biomass water belongs to catalyze fuel processing technology area. Wherein it is made of solid material gasification generator and liquid or gas material high temperature steam generator and dual-rotary flow slow speed a water film desulfurization dust remover and a gas cabinet, a water-gas separator, a pressurizing pump, or using a power generation fuel gas apparatus dual channel,.... collsion catalyze to prepare water catalyze fuel system. The innovation wherein: eliminating a manufacture method of single charging smoke fire burn in existing technology, preparing the catalyze water fuel, material use efficiency is high, no combustion waste gas, comprising a tar content almost is zero, a desulphurization and dust removal aspect, implementation of a certain volume in a tank as dozens of time and reduce smoke gas flow speed and, at the same time a.... increased pollutant capturing several time more than a contact area of air, providing a technology guarantee for production mineral or biomass. catalyze fuel.
NOVELTY - The utility model claims a new microorganism flora culture equipment technology area, specifically claims a device used for sewage treating photosynthetic flora expanding culture, comprising culturing container, stirring component and used for providing light source of fluorescent lamp module, said stirring component comprises set on the stirring shaft in the culture container, the agitator blade on the stirring shaft and used for driving the stirring shaft rotate and drive group s part, this utility new type culture device and greatly reducing of work intensity, increase of production efficiency, no influence by the sunlight condition, especially suitable for batch production of photosynthetic flora.
NOVELTY - The utility model claims a top slag cursher of anaerobic reactor, comprising feed manifol, diverter, distributing branch pipe and distributing head, discharging port of the feed manifold is connected to upper end of the diverter, side face of the diverter is uniformly installed with distributing branch pipes, the distributing branch pipe along clockwise or anticlockwise direction is gradually lengthened, tail end of distributing branch pipe is installed with distributing head, included angle of the distributing head and the horizontal line is inwards 45 degrees, and included angel of distributing head and distributing branch pipe is outwards 135 degrees, distributing head is gradually enlarged or gradually flattened structure. Scum the utility new type can solve excrement equal marsh gas raw material in existing in Anaerobic fermentation process of large quantity, compact and affect gas generating effect, cause discharge pipe blockage problem equal, has simple manufacture, suitable mounting, crushing good effect equal.
NOVELTY - Steam exploded straw and cow dung mixed anaerobic fermentative production of biogas comprises carrying out steam fermentation of steam exploded straw and cow dung to obtain organic acids, and then preparing biogas by using organic acids.    USE - The method is useful for preparing steam exploded straw and cow dung mixed anaerobic fermentative production of biogas (claimed).    ADVANTAGE - The method has fast starting fermentation with short period, and high production rate of gas.
NOVELTY - Culture material comprises 50-70% biogas residue, 5-40% corn cob, 13% wheat bran, 5% corn powder, and 2% gypsum.    USE - As culture material for Coprinus comatus (claimed).    ADVANTAGE - The culture material reduces cost of raw materials of C.comatus production, and shortens C.comatus production cycle.
NOVELTY - A banana pseudostem biochar is prepared by naturally drying chopped banana pseudostem to moisture content of 15% or less, igniting to moisture content of less than 8%, air-drying, pulverizing banana pseudostem into particles having diameter of 2-10 mm, and processing.    USE - Banana pseudostem biochar is used in preparation of banana tissue culture substrate (all claimed) used in cultivation of banana and other plants.    ADVANTAGE - The banana pseudostem biochar improves soil fertility and significantly promotes growth of banana plantlets.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) banana tissue culture substrate, which comprises 1-3 %mass banana pseudostem biochar, and remainder of nutritional soil, with respect to 100 %mass substrate; and    (2) preparation of banana tissue culture substrate.
NOVELTY - Extracting green walnut extract epicarp, comprises peeling green walnut epicarp, washing with water, drying at 60-80 degrees C to constant weight, pulverizing and passing through a 80-120 mesh screen, adding green walnut epicarp powder into water, reflux boiling twice at 80-90 degrees C, filtering the decoction, vacuum concentrating at 60-70 degrees C, concentrating to thick paste.    USE - The green walnut epicarp extract is used as antibacterial agent for controlling leaf blight plant disease caused by Exserohilum rostratum.    ADVANTAGE - The method does not use any organic solvents and other chemical reagents. The green walnut epicarp extract does not cause pollution in ecological environment, ecological problems, generation of pesticide residues and other livestock poisoning.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) green walnut epicarp extract; and    (2) preparing the green walnut epicarp extract seed coating agent, comprising directly drying 100 pts. green walnut epicarp extract powder, preparing with 45% ethanol solution, adding 100 pts. (3%) hydroxypropylmethylcellulose (HPMC), 80 pts. polysorbate, 1 pt. edible rapeseed oil and 1 pt. polyethylene glycol 400 (PEG400), and mixing to prepare corn seed coating material.
NOVELTY - Processing quail farming waste, comprises, in quail breeding process, feeding 2asterisk108-4asterisk108 colony forming unit (cfu)/ml of effective microorganisms probiotics aqueous solution as quail drinking water, filling quail excrement into fementation tank, adding husk, controlling moisture content to less than 60%, stirring uniformly, adding 0.01- 0.1 wt.% quail feces, viable cell concentration of 2asterisk107-9asterisk107 cfu/ml of organic fertilizer special fermentation agents, step on solid object, covering with plastic sheeting, pressing, ensuring anaerobic fermentation environment for 10-15 days.    USE - The method is useful for processing quail farming waste (claimed).
NOVELTY - Preparing organic fertilizer by Hermetia illucens processed dairy manure comprises e.g. taking dairy manure, adding in dehydrating machine for dehydration, spreading out on ground, obtaining dehydrated dairy manure, adding swill or kitchen waste in dehydrated manure, preparing culture material, adding lactic acid bacterial dry powder, mixing evenly, fermenting and processing, paving cow dung cultured material, adding Hermetia illucens larvae in cow dung cultured material, culturing, separating out mature larva and aging to obtain organic fertilizer.    USE - The method is useful for preparing organic fertilizer by Hermetia illucens processed dairy manure (claimed).    ADVANTAGE - The method has strong process ability, short period treatment process, reduces energy consumption, can convert waste into useful product, improves palatability and fly feeding rate and yield of larva is increased to more than 50%, and improves environmental hygiene.    DETAILED DESCRIPTION - Preparing organic fertilizer by Hermetia illucens processed dairy manure comprises (i) taking dairy manure, adding in dehydrating machine for dehydration, spreading out on ground, obtaining dehydrated dairy manure, (ii) adding 10-15% swill or kitchen waste in dehydrated manure, preparing culture material, adding culture material with 0.1% lactic acid bacterial dry powder, mixing evenly, fermenting and processing for 1-2 days, and (iii) after fermentation, paving cow dung cultured material of 5-7 cm thick, adding 25% 3-4 Hermetia illucens larvae in cow dung cultured material, at 30-35 degrees C, and air humidity of 75-85%, culturing for 5-6 days, separating out mature larva and aging to obtain organic fertilizer.
NOVELTY - Selenium-containing organic fertilizer comprises 30-40% edible fungus residue, 15-20% chicken manure, 8-10% rice bran, 2-5% cellulase, 5-8% neutral protease, 1-2% yeast, 4-6% selenium yeast, 2-5% ammonium molybdate, 8-15% magnesium sulfate, 8-15% potassium nitrate, 5-6% sodium fluorosilicate and 8-10% calcium citrate.    USE - The method is useful for preparing selenium-containing organic fertilizer (claimed).    ADVANTAGE - The selenium-containing organic fertilizer is prepared by economical, simple, convenient and natural method, and is safe and reliable, .    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing selenium containing organic fertilizer, which involves (a) mixing edible fungus residue, chicken manure and rice bran and crushing mixture, (b) adding cellulase and neutral protease to mixed product obtained in step (a), where mixture has moisture content of 30-45% and pH of 6.8-7.2, and performing enzymatic degradation at 35-37 degrees C for 72 hours, (c) adding yeast and selenium yeast to product obtained in step (b) maintaining moisture content of mixture at 55-60% and fermenting mixture at 40 degrees C for 8-15 days, and (d) mixing fermented product with ammonium molybdate, magnesium sulfate, potassium nitrate, sodium fluorosilicate and calcium citrate; and    (2) application method of selenium-containing organic fertilizer, which involves applying at a rate of 20-30 kg/acre, before planting rice into soil, filling paddy field with 2-3 cm water and plowing soil evenly.
NOVELTY - This new utility model relates to a four bit integrated marsh gas fermentation device, it comprises one grade dry fermentation machine, second level wet fermentation machine, folding the air pocket, room temperature and solar energy water heater, one grade dry ferment machine comprises filling with material liquid and is set with the ring shape in daylight room temperature in dry fermentation tank, filling material and soaking with the cage in material liquid in, and sealing is set with water seal cover on the box top part, second level wet fermentation machine and dry fermentation tank comprises mutually connected the wet fermentation tank, wherein the heat exchanger is set with wet in fermentation tank, and biological film fixed on wet fermentation tank is in the top part of the wet fermentation tank with gas-guide tube is set with the folding storage air pocket formed on top of wet fermentation tank and gas-guide tube and mutually connected, solar energy water heater is set with top of sunlight at room temperature and for providing circulation hot water heat exchanger. This new utility model solves of sludge pump is easy to be blocked problem, using combination of solar energy and fluorescent kl, saving of energy, shortens the degradation time of the fiber material, increase of use rate of fermentation raw material, increase of the amount of methane gas, increase of comprehensive use ratio of biogas.
NOVELTY - This new utility model claims agricultural convenient marsh gas pool, comprising pool body and air pipe, the pool body divide the marsh gas layer, clean water layer, layer and biogas slag layer, the pool body top end is set with pool body with cover, the pool body is set with bottom with slope, the pool body one side is set with a feeding port, the pool body with the other side set up with discharging port, feedstock port connected with the material groove, the discharging port connected with chute, the upper pool body cover connected with gas pipe, the gas pipe is set with upper with control valve, a water-gas separator, gas storage bag, evolution controller and air pressure regulator, the air pipe the other end set with marsh gas stove. The agricultural convenient marsh gas pool manual work for the suitable process, using marsh gas dry is ignition to prevent air pressure to make high in marsh gas pool of raw material and be discharged, pollute environment, make methane with pool body in the piercing nose smell to for one character, when time for preventing flame would appear large and small, has simple structure, reasonable design.
NOVELTY - The utility model provides a marsh gas system, comprising section for marsh gas pool is pot shape, inside of said marsh gas pool is embedded in high-order side of step-shaped floor, a kettle mouth of the marsh gas pool set with one buffer in the feedstock and the buffering cavity end and discharging end and one packing auger extrusion device connected with the feedstock and the packing auger device is set with mouth with one groove, located in the marsh gas pool set with one discharging pipeline, the discharging pipeline comprises one trumpet suction mouth slag, wherein the trumpet suction slag close to the bottom of the marsh gas pool, a slag outlet of the slag discharging pipeline extending to one slag containing groove in the inside of the slag containing groove embedded in the low level side of the step-shaped floor, the marsh gas pool side of wall is also set with one arrange liquid pipeline, top part of marsh gas pool set with discharge pipeline, the discharge pipeline through all valve and one three-way pipe connection. This new utility model can make dejecta, sewage, garbage collective get in marsh gas pool, carrying out to manufacture marsh gas, and discharging the liquid can used for cultivating fish or irrigation.
NOVELTY - Rapid increasing soil fertility, comprises applying composite conditioning agent and the releasing earthworms to the soil, where in before releasing earthworms to the soil, the soil needs to meet the following conditions: moisture content of soil is 30-50% and soluble salt content of soil is 4. The amount of adding composite conditioning agent is 300-500 kg/acre and amount of releasing earthworms is 30-50 kg/acre.    USE - The rapid increasing organic agriculture soil fertility is useful in organic agriculture production fields (claimed).    ADVANTAGE - The method: increases activity of earthworm in farmland, soil microbial diversity environment; accelerates the rate of soil fertility and rejuvenation; improves soil quality, crop quality and yield, thus achieves sustainable development of organic agriculture.
NOVELTY - Finishing gas aquo-complex reversible gas storage using hydrogel, using polymethacrylate hydrogel as gas storage medium comprises e.g. swelling polymethacrylate hydrogel to reach equilibrium, adding in high pressure reaction kettle, sealing, opening gas valve, inflating reaction kettle, adjusting the autoclave pressure and temperature to reach specified temperature and pressure, generating gas aquo complex, obtaining gas aquo-complex polymethacrylate hydrogel, decomposing gas aquo-complex polymethacrylate hydrogel, after re-stabilizing temperature and pressure, decomposing.    USE - The method is useful for finishing gas aquo-complex reversible gas storage using hydrogel (claimed).    ADVANTAGE - The method realizes high storage gas quantity and reversible storage effect, has simple process, and achieves good stability.    DETAILED DESCRIPTION - Finishing gas aquo-complex reversible gas storage using hydrogel, using polymethacrylate hydrogel as gas storage medium, comprises (i) swelling polymethacrylate hydrogel to reach equilibrium, adding in a high pressure reaction kettle, sealing, opening gas valve, inflating reaction kettle, (ii) carrying out gas storage process: adjusting the autoclave pressure and temperature to reach specified temperature and pressure, generating gas aquo complex, when the temperature and pressure changes do not occur, obtaining gas aquo-complex polymethacrylate hydrogel, and (iii) decomposing: taking obtained gas aquo-complex polymethacrylate hydrogel, raising temperature, decomposing, after re-stabilizing the temperature and pressure, decomposing.
NOVELTY - Preparing 2-chloro-4-formyl pentanenitrile, comprises (i) adding organic medium A and catalyst A into a reaction kettle, introducing nitrogen, adding propionaldehyde dropwise in presence of chlorine gas, and incubating; (ii) adding a solvent, recovering solvent, and carrying out vacuum distillation of residue in reaction kettle, to obtain 2-chloropropionaldehyde; (iii) adding organic medium B, 2-chloropropionaldehyde, acrylonitrile, catalyst B and ligand into the reaction kettle, stirring while reacting; and (iv) recycling organic medium B.    USE - The method is useful for preparing 2-chloro-4-formyl pentanenitrile (claimed).    ADVANTAGE - The method replaces chlorine; is simple, economical, and suitable for industrial production; has low device investment; and utilizes raw material which can be recycled.
NOVELTY - Extracting fulvic acid, comprises mixing coal powder and water, adding hydrogen peroxide, reacting at 30-70 degrees C, balancing reaction, adjusting pH to 9-10, stirring, dropwise adding hydrogen peroxide at 30-70 degrees C, reacting, adjusting pH rate reduction to 0.005-0.02/minute, stopping adding hydrogen peroxide, where the determination of reaction equilibrium is based on pH stable system, does not raise the temperature, the dropwise rate of hydrogen peroxide per minute is 0.0001-0.001 times to mass of the coal powder.    USE - The method is useful for extracting fulvic acid (claimed).    ADVANTAGE - The method is simple, utilizes low device requirements and is environmentally friendly.
NOVELTY - Method for obtaining feed, involves under aerobic conditions, culturing Gluconacetobacter sucrofermentans strain H-110 using distiller's dried grains with solubles (DDGS) having pH of 3.9-4.4 at neutral pH for 2 days to obtain proteinaceous biomass and bacterial cellulose.    USE - The method is used for obtaining feed (claimed).
NOVELTY - Microwave decomposition dry process rapid extraction of fluorine resources from defluorination slag comprises taking defluorination slag and concentrated sulfuric acid in a microwave reactor, purifying the generated gas, condensing, rectifying to obtain anhydrous hydrogen fluoride, or purifying, absorbing with hydrofluoric acid, or recycling into other fluoride products, discharging the solid slag and using for fertilizer production, where the fluorine content in slag in the form of calcium fluoride is 10-40%, the slag has free water content of 0-10% and concentrated sulfuric acid of 93-100%.    USE - The method is useful for microwave decomposition dry process rapid extraction of fluorine resources from defluorination slag (claimed).    ADVANTAGE - The method: is simple, and fast; ensures quick fluorine resource recovery rate; has low equipment investment; is easy for industrial production; and has economic benefits.    DETAILED DESCRIPTION - Microwave decomposition dry process rapid extraction of fluorine resources from defluorination slag comprises taking defluorination slag and concentrated sulfuric acid in a microwave reactor at a frequency of 915 MHz to 2.45 GHz, controlling reaction process and slag and sulfuric acid in a solid state, purifying the generated gas, condensing, rectifying to obtain anhydrous hydrogen fluoride, or purifying, absorbing with hydrofluoric acid, or recycling into other fluoride products, discharging the solid slag and using for fertilizer production, where the fluorine content in the slag in the form of calcium fluoride is 10-40%, the slag has free water content of 0-10%, concentrated sulfuric acid of 93-100%, the mass ratio of slag and concentrated sulfuric acid is 1:0.4-1, reacting in a microwave reactor at 110-250 degrees C for 4-40 minutes.
NOVELTY - Ecological treatment pigeon house dirt comprises pouring the pigeon dropping into pretreatment pool to form a complex, drying, separating water from rushing ring, pouring solid into biogas fermentation tank, mixing biogas residue and dried pigeon dung to obtain fertilizer.    USE - The method is useful for ecological treatment pigeon house dirt (claimed).    ADVANTAGE - The method ensures environmental hygiene. The fertilizer can be used for crop and is eco-organic.
NOVELTY - Preparing compost involves mixing livestock excrement, straw and straw biological coal mixture in mass ratio of 1:0.2:0.1-0.3. The mixture is composting for14-20 days with ventilating speed of 0.01-0.05 m3 per hour.    USE - Method for preparing compost used for crop (claimed).    ADVANTAGE - The method enables to prepare compost ensures quick effect, is applicable in agriculture, and has increased amount of total nitrogen and phosphorus.
NOVELTY - Iodine rich fertilizer comprises 30-50 parts rotten chicken manure, 30-40 parts plant ash, 2-4 parts borax, 8-10 parts ferrous sulfate, 20-40 parts more than five year old canal mud, 8-10 parts Chile saltpeter, 20-25 parts kelp, 10-20 parts Porphyra, 15-20 parts citric acid residue, 16-20 parts ammonium phosphate, 10-25 parts urea, 20-25 parts peanut shell and 1-1.5 parts water-retaining agent.    USE - Iodine rich fertilizer used for tea (claimed).    ADVANTAGE - The iodine rich fertilizer ensures 4.32 plus minus 0.4 mg iodine in per kilogram dry tea leaf, and enhances growth and yield of tea.
NOVELTY - A natural gas and argon gas extracting method involves cooling helium gas and compressing, pre-cooling and purifying natural gas. The cooled helium gas is transferred to a main heat exchanger to obtain condensed liquid. The condensed liquid is decompressed to discharge nitrogen. The discharged nitrogen is entered into a nitrogen circulation system to obtain nitrogen gas. The nitrogen gas is mixed with methane. The methane is removed from a refined argon tower. The refined argon tower bottom is performed with a micro-nitrogen component separation process to obtain pure liquid argon.    USE - Method for extracting natural gas and argon gas.    ADVANTAGE - The method enables extracting natural gas and argon gas with high purity, anti-radiation effect and continuous operation time.    DETAILED DESCRIPTION - An INDEPENDEDNT CLAIM is also included for a natural gas and argon gas extracting device.
NOVELTY - The device has a sample and liquid treatment unit provided with an imaging element and connected with a control system. An imaging unit is fixed with a biological chip and connected with the liquid treatment unit. An optical biological sensing device is connected with the control system and a data collection processing unit. The optical biological sensor device performs automatic operation and generates a filtering signal. A monochromatic light generator (1) is fixed with a reflection lens and connected with a beam expander (3). A platform (20) is formed with a fluid cavity (19).    USE - Fully automatic high flux optical biological sensor device.    ADVANTAGE - The device has high efficiency, environmental safety and drug screening throughput, and wide range of applications.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fully automatic high flux optical biological sensor device.    Monochromatic light generator (1)    Beam expander (3)    Photoelectric detector (12)    Fluid cavity (19)    Platform (20)
NOVELTY - A. the utility model claims... a sewage biochemical treatment device, it comprises a pool body and a gas supply tube, a a a a a a wall formed with a sewage import, a shape of the other side wall is set with a with a sewage outlet, an air supply pipe is set with a horizontal through one side wall a shape of, a gas supply pipe and a pool body and the air outlet and a air blower and connected, the other end air supply pipe of the pool body, the other end a supply air tube is closed, the part is in a shape of air supply pipe set with a number of air outlet hole, an air supply pipe and a body located outside is wound with the electric heating silk, the air supply pipe is aluminum pipe, the pool body is set with upper part has a fan, fan is positive downward. This new utility model a sewage temperature is more suitable, and a microorganism activity.
NOVELTY - The utility model claims a... strain circle has a function of high efficient sewage treatment pool, comprising a water pipe, a water groove, a relux, relux valve, transporting belt, an aeration pipe, a clapboard and a pool, the bottom of the reaction pool in turn provided with aeration pipe and transporting belt, an aeration pipe connected with air pump, an aeration pipe water inlet end of a pool, then a pool is provided with multiple alternately arranged in the upper clapboard and lower clapboard, to steady flow direction of sewage, the transporting belt is set with incline. A aeration pipe is set with a water inlet end of a pool, a sludge and the sewage containing fungus full mixing, matched transport belt will precipitate a deposited strain sludge conveying to the water inlet end of a pool, the utility model is a new type continuous adequate reaction treatment of sewage, wherein a reaction pool is set with a upper clapboard, lower clapboard sewage is stable, the internal flow speed not to a response of a not full and a slow and.
NOVELTY - This new utility model claims ceramic membrane integrated device system used for sewage treatment, it includes sewage material liquid storage tank, through pipeline circulation groove is connected with the sewage material liquid storage tank via pipeline and circulation groove mutually connected filtering device and the clean liquid groove is connected with the filtering device, the filtering device comprises primary filter and ceramic membrane filter, the entrance of the primary filter connected to circle groove, the ceramic membrane filter outlet connected to cleaning liquid groove, said ceramic membrane filter comprises collecting tank, the collecting tank set with material of liquid entrance and liquid exit material, the material to liquid outlet is equipped with spherical surface distribution of porous ceramic filtering film within in the collection tank, the material to liquid entrance equipped with material liquid sprayer in the internal collection tank. This new utility model provided waste water processing system device is simple, not need regulating groove, a floatation, biochemical reactor equal a kind of multi-processing device, and sewage processing amount large, treatment period short, the water outlet water quality is clear and stable.
NOVELTY - This utility model claims a precision filtration membrane treatment device system, it includes sewage material liquid storage tank, through pipeline circulation groove is connected with the sewage material liquid storage tank via pipeline and circulation groove mutually connected filtering device and the clean liquid groove is connected with the filtering device, the filtering device comprises primary filter and ceramic membrane filter, the entrance of the primary filter connected to circle groove, the ceramic membrane filter outlet connected to cleaning liquid groove, said ceramic membrane filter comprises collecting tank, the collecting tank on the upper part and provided with primary filter liquor entrance, provided with clear liquid outlet at top end of gathering tank, provided with several parallel arranged of porous aluminium oxide ceramic film tube in in the collecting tank. This new utility model providing is one of waste water processing system device is simple, not need regulating groove, a floatation, biochemical reactor equal a kind of multi-processing device, and sewage processing amount large, treatment period short, the water outlet water quality is clear and stable.
NOVELTY - The utility model claims a new kind of flow type sediment hydrolysis and a grade AO biochemical treatment system, comprising a flow type sediment hydrolysis pool, an anoxic grid, an aerobic grid, transition grid, the up flow type sediment hydrolysis pool through a water pipe connected with the anoxic grid, a flow type sediment center and hydrolysis pool is set with a guide cylinder, the guide cylinder in the opening up of a water inlet pipe, a guide cylinder connected with a reflection plate, the up flow type sediment center and hydrolysis pool is set with vertical stirrer rotate shaft is vertical stirrer through a reflection plate guide cylinder, stirring blades and vertical stirring the reflection plate, the up flow type sediment bottom hydrolyzing a part formed with a slope is a centre, forming bucket, bucket bottom mud suction by connecting with sand washing machine, washing by fermentation liquid relux pipe and pump connected with a water inlet pipe. The utility model claims a new upper flow type sediment hydrolysis.. type sludge hopper deep, the layer thickness, the can bottom a high concentration sludge for fermentation, production of VFA, strengthening Anaerobic release P of effect.
NOVELTY - The utility model claims a new HVC a biological strengthened undercurrent artificial wetland module, the technology point is: a left and a right two side one side of wetland is water channel, the other side is a water well the whole wetland according to front and rear direction dividing several lengthways arranged and constructed wetland.... In each of wetland pool is set with a sewage pipe and a drain pipe, sewage pipe from a water well, bc pebble to a sewage water outlet pipe between a wetland bottom.... microorganism solidify filler in cobble beside the main pipe of flora adjusting device is a microorganism curing agent filler of the drain pipe is bent pipe, a vertical pipe of a horizontal tube and to pipe, horizontal pipe and bent pipe extends into the marsh pool, turning part and the vertical pipe is set with a water channel, and is set with lengthways arranged a plurality of drainage hole on pipe wall of the vertical pipe.
NOVELTY - Organic fertilizer comprises 40-50 pts. wt. enzyme fermentation residue, 10-20 pts. wt. sheep manure, 20-25 pts. wt. water hyacinth, 10-15 pts. wt. biogas residues, 10-15 pts. wt. wood pieces, 2-3 pts. wt. purslane and 5-8 pts. wt. kaolin.    USE - Used as an organic fertilizer.    ADVANTAGE - The organic fertilizer is economical; can effectively change the microenvironment of the soils; utilizes raw material of batch fermentation, where fermented materials utilized are optimized; and has high utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer, comprising uniformly stirring enzyme fermentation slag and wood pieces by adding kaolin, and carrying out fermentation by add photosynthetic bacteria, Actinomycetes and Trichoderma, preferably Trichoderma strain T39 for 2-3 months at 25-30 degrees C environment.
NOVELTY - Environment-friendly alcohol oil biofuel comprises 50-60 wt.% methanol/ethanol, 5-8 wt.% biological oil, 5-8 wt.% t-butanol, 5-10 wt.% dimethoxy methane, 0.02-0.03 wt.% Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate), 0.02-0.03 wt.% Span 20 (RTM: sorbitan monolaurate) and 5-15 wt.% biphenyl structure high-energy fuel.    USE - Environment-friendly alcohol oil biofuel.    ADVANTAGE - The biofuel is energy-saving, inexpensive and has increased fuel use ratio.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of environment-friendly alcohol oil biofuel comprising mixing raw materials.
NOVELTY - Biomass fuel comprises 50-60 pts. wt. biomass coal powder, 10-20 pts. wt. coal powder and 5-10 pts. wt. combustion promoter. The biomass coal powder is prepared by taking 60-70 wt.% wood material and 30-40 wt.% crop straw, drying, crushing, mixing, pressing and forming. The outer surface of the biomass fuel is wrapped with a layer of biomass resource polyester. The main repeating unit of polyester is dicarboxylic acid unit and diol unit. The combustion promoter comprises 30-40 wt.% talc, 30-50 wt.% sulfuric acid residue, 15-20 wt.% magnesium chloride salt block, and 3-5 wt.% sodium nitrate.    USE - Used as biomass fuel.    ADVANTAGE - The fuel has good adhesion, high burning value, produces less pollution, does not generate sulfur dioxide and fly ash, and facilitates construction of ecological environment.
NOVELTY - Lipids or oils production involves using natural sources of starchy materials and processing by-products of the materials, preferably cassava and sweet potatoes.    USE - Method for producing lipids or oils for producing biodiesel or fuel oil.    ADVANTAGE - The method produces high performance biodiesel or fuel oil for direct use in engines and power generation in a simple, cost-effective and eco-friendly manner. The produced biodiesel is flammable and better than fuel mineral diesel in terms of sulfur content, flash point, aromatic hydrocarbon content and biodegradability, offers same performance and diesel engine durability, and reduces emissions of exhaust gases, visible smoke and noxious gases and odors.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the oilseed microbial biomass production stage. (Drawing includes non-English language text).
NOVELTY - Preparation of divalproex sodium comprises condensation of alkyl cyanoacetate with n-propyl bromide in presence of sodium in an alcoholic solvent to give alkyl-di-n-propyl cyanoacetate followed by saponification using aqueous base at an ambient temperature in presence of phase transfer catalyst (PTC) to prepare di-n propyl cyanoacetic acid; one step conversion of di-n-propyl cyanoacetic acid to valproic acid in presence of an acid and PTC at an ambient temperature, optionally isolating di-n-propyl acetonitrile and di-n-propyl acetamide; and reaction of valproic acid with sodium salt or base.    USE - The process is for preparation of divalproex sodium (I) (claimed) used for treatment of manic episodes of bipolar disorder, major depressive disorder, depressive phases of bipolar disorder, epilepsy, certain side effects of autism, chronic pain associated with neuropathy, and migraine headaches.    ADVANTAGE - The process provides simpler (i.e. uses non-hazardous reactants and better scalability at plant level), cost effective, environment friendly and less energy intensive process to produce valproic acid and produces divalproex sodium of International Committee on Harmonization purity in shorter time and better yields.    DETAILED DESCRIPTION - Preparation of divalproex sodium of formula (I) comprises:    (A) condensation of alkyl cyanoacetate with n-propyl bromide in presence of sodium in an alcoholic solvent to give alkyl-di-n-propyl cyanoacetate followed by saponification using aqueous base at an ambient temperature in presence of phase transfer catalyst (PTC) to prepare di-n propyl cyanoacetic acid;    (B) one step conversion of di-n-propyl cyanoacetic acid to valproic acid in presence of an acid and PTC at an ambient temperature, optionally isolating di-n-propyl acetonitrile and di-n-propyl acetamide; and    (C) reaction of valproic acid with sodium salt or sodium base in an organic solvent at an ambient temperature to produce (I).
NOVELTY - Grape fertilizer comprises 35-40 pts. biogas fertilizer, 35-40 pts. potassium dihydrogen phosphate, 12-15 pts. yeast selenium, 5-8 pts. ferrous sulfate, 5-8 pts. zinc sulfate, 30-40 pts. peat, 20-25 pts. seaweed, 3-5 pts. EM microbial inoculum, 10-15 pts. earthworm, 10-15 pts. Astragalus membranaceus, 15-20 pts. Chinese yam, and 30-35 pts. sawdust.    USE - Used as grape fertilizer.    ADVANTAGE - The fertilizer has steady performance, low cost, no toxicity and side effects, increases yield and quality of grapes, is pure natural and organic substance, cultivates pest-free grapes, is harmless to public, and does not generate pesticide residues.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the grape fertilizer, comprising (i) drying seaweed, earthworm, Astragalus membranaceus and Chinese yam, and grinding into 80-100 meshes particle; (ii) mixing the sawdust, peat and grinded powder of step (i), adding EM microbial inoculum and water, sealing and fermenting for 5-7 days, stirring once every other day, to obtain fermented material; and (iii) mixing the fermented material with biogas fertilizer, potassium dihydrogen phosphate, yeast selenium, ferrous sulfate and zinc sulfate, and dry granulating.
NOVELTY - A tank shoal artificial wetland comprises tank, shoal, S-type water impermeable wall (3) located between tank and shoal, and hard substrate, large particle diameter and large hole rate biological porcelain granule matrix (2).    USE - Tank shoal artificial wetland.    ADVANTAGE - The method reduces operation cost, increases efficiency and effectiveness, realizes organic unity of aerobic treatment and zoology treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for aerobic treatment method of active sludge wastewater comprising falling utilized wastewater, oxygenating, re-oxygenating by performing potential energy into kinetic energy, aerobic degrading though microorganism growth environment of tank bottom layer matrix, and absorbing and removing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of tank shoal artificial wetland.    Biological porcelain granule matrix (2)    S-type water impermeable wall (3)
NOVELTY - Treating organic sewage involves using Aeromonas salmonicida into organic sewage.    USE - Method for treating organic sewage (claimed).    ADVANTAGE - The method enables to treat organic sewage in simple and eco-friendly manner.
NOVELTY - The method involves using municipal sludge and solid organic waste and adding to feeding port (9) of compost device. The feeding port is closed. An electric control stop valve (14) is opened. A vacuum pump (22) is started. The negative pressure of fermentation chamber (6) is 10-20KPa. The stop valve is closed. A variable frequency motor is driven to rotate stirring roller (21). The products are heated at 40-60 degrees C temperature and hydrogen peroxide solution is added and stirred for 20-28 hours. The temperature is maintained to 70 degrees C for 1-2 days at low temperature to complete process.    USE - Organic garbage compost treatment method using organic garbage composting device.    ADVANTAGE - The treatment time is shortened. The processing efficiency is increased. The process cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic garbage composting device.    Fermentation chamber (6)    Feeding port (9)    Electric control stop valve (14)    Stirring roller (21)    Vacuum pump (22)
NOVELTY - Method for preparing fertilizer by solid-state fermentation, involves (a) activating Bacillus licheniformis strain FA08 by culturing the B.licheniformis strain FA08 using Luria-Bertani (LB) culture medium, inoculating culture into LB culture medium, performing culturing process to obtain seed liquid, inoculating seed liquid into LB culture medium, and performing culturing process, and (b) adding culture obtained in step (a) to seaweed residue, performing solid-state fermentation, and blast drying, cooling and packaging product.    USE - The method is useful for preparing fertilizer by solid-state fermentation (claimed).    ADVANTAGE - The method is environmentally-friendly, and simple to performs, avoids wastage of resources, and improves yield of crops.    DETAILED DESCRIPTION - Method for preparing fertilizer by solid-state fermentation, involves (a) activating Bacillus licheniformis strain FA08 by inoculating the B.licheniformis strain FA08 into 10 ml Luria-Bertani (LB) culture medium, performing culturing process at 30-40 degrees C and 150-200 revolutions/minute (rpm) for 8-10 hours, inoculating 1-10 vol.% culture into LB culture medium contained in an Erlenmeyer flask, performing culturing process at 30-40 degrees C and 150-200 rpm for 10-24 hours to obtain seed liquid, inoculating 1-5 vol.% seed liquid into LB culture medium contained in fermenter, and performing culturing process at 30-40 degrees C, pH of 6.8-7.4 and 500-1000 rpm for 24-48 hours, and (b) adding 1-10 vol.% culture obtained in step (a) to seaweed residue, performing solid-state fermentation for 10-15 days, stirring mixture during fermentation, blast drying fermented product at 30-45 degrees C until moisture content of the product reaches 10-15%, cooling the product, and packaging the product.
NOVELTY - Preparing acetylsalicylic acid involves mixing salicylic acid, acetic anhydride and citric acid on water bath at 70 degrees C for 40 minutes and then washing mixed material reaction vessel with cold water after formation of crystals. The washed material is added with water and then the obtained material is filtered, dried and cooled on ice bath for 30 minutes to obtain the desired product.    USE - Method for preparing acetylsalicylic acid (claimed).    ADVANTAGE - The method enables to prepare acetylsalicylic acid in simple, environment-friendly and cost-effective manner, and with high yield.
NOVELTY - The method involves flowing a fermentation raw material into a U-type fermentation chamber. The biogas is produced by fermentation in the upper portion of the fermentation chamber and discharged into the air through an air inlet (320). An air piston (340) of a piston connecting rod (350) is connected with an air inlet passage (360). The gas is entered into the air bag through a gas pump. The elastic potential energy of an air spring (390) is released, when the pressure drop of the gas pump is carried out. The piston is moved downward into an annular air guide groove (370) and an air bag.    USE - Method of collecting gas from gas collecting device.    ADVANTAGE - The blocking of the gas collecting device is complete avoided, the fermentation raw material is uniformly distributed, and the residue is eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the gas collecting device.    Air inlet (320)    Air piston (340)    Piston connecting rod (350)    Air inlet passage (360)    Air guide groove (370)    Air spring (390)
NOVELTY - New Leptolyngbya species scsio T-2 strain with the preservation number CCTCC NO: M 2015061, is new.    USE - The strain is useful in preparing fertilizer for prompting nitrogen fixing in bacteria and in preparing indole-3-acetic acid (all claimed).
NOVELTY - Bacillus mucilaginosus (AMCC100035) strain, comprising a preservation number CGMCC NO.6766, is new.    USE - Bacillus mucilaginosus is useful in potato bio-organic slow-release fertilizer (claimed).    ADVANTAGE - The fertilizer: meets different nutritional elements for growth development of potato; increases potato yield; prevents potato diseases; and improves soil texture.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) potato bio-organic slow-release fertilizer, comprising Bacillus mucilaginosus (AMCC100035), and fertilizer comprising 42-50% bioorganic fertilizer, 11-14% resin coated urea, 6-9% urea, 11-13% diammonium phosphate and 20-22% potassium sulfate; and (2) preparing the fertilizer, comprising mixing bioorganic fertilizer, resin coated urea, urea, diammonium phosphate and potassium sulfate in a blender, stirring for 10 minutes, measuring, and packaging.
NOVELTY - Planting strawberries involves adding fine river sand (120-150kg), rotten chicken manure (1000-1200kg), compound fertilizer (80-100kg), light rare earth fertilizer (3-5 kg), and green Asparagus powder (40%) to soil. Soil is plowed to make ridges having depth of 30-40cm, height of 20-30cm, width of 30-35cm, and length of 25-30m. Strawberries are planted in August-September, and nutrient solution (50g) is sprayed on soil. Ratio of nitrogen, phosphorus and potassium in nutrient solution is 2:1:1.    USE - Method for planting strawberries (claimed).    ADVANTAGE - The method is good color, taste shape and yield of strawberries.    DETAILED DESCRIPTION - Planting strawberries involves adding fine river sand (120-150kg), rotten chicken manure (1000-1200kg), compound fertilizer (80-100kg), light rare earth fertilizer (3-5 kg), and green Asparagus powder (40%) to soil. Soil is plowed to make ridges having depth of 30-40cm, height of 20-30cm, width of 30-35cm, and length of 25-30m. Strawberries are planted in August-September, and nutrient solution (50g) is sprayed on soil. Ratio of nitrogen, phosphorus and potassium in nutrient solution is 2:1:1. Nutrient solution (having nitrogen, phosphorus and potassium in ratio of 2:2:1) is sprayed after every 15 days. Nutrient solution (having nitrogen, phosphorus and potassium in ratio of 3:2:2) is sprayed in flowering period. Weeds and diseased leaves are removed. Carbendazim (25%) is sprayed for preventing Botrytis cinerea. Rare earth fertilizer and ash are added in soil.
NOVELTY - Cultivating Yucca gloriosa variegata involves selecting soil in February or march. Fertilizer (800-1000 kg/acre) is added to it. Soil is plowed (15-20 cm), and Yucca gloriosa variegata is planted in soil at a gap of 1.5-2.5 meter for 20-25 days to obtain seedlings. Seedlings are planted into planting hole. Planted seedlings are left for June to July. Fertilizer (500-700 kg/acre) is applied in September to October, another fertilizer (600-700 kg/acre) is applied in autumn. Manure is applied in November, and permeability enhancer is applied in July to September after 3-4 days.    USE - Method for cultivating Yucca gloriosa variegata (claimed).    ADVANTAGE - The method is eco-friendly.
NOVELTY - Cultivating white fungus involves pulverizing corn cob (68-74%) to obtain particles having diameter of 3-5mm. Mushroom is pulverized to obtain particles having diameter of 2-3mm. Pulverized mushroom is soaked in water (20-30 times the quantity of mushroom) for 18-24 hours. Obtained mushroom product is mixed with corn cob. Obtained mixture (300-500kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical vent is made in heap by stick having diameter of 10-15cm. Heap is covered with grass, fermented naturally at 60 degrees C, and turned periodically.    USE - Method for cultivating white fungus (claimed).    ADVANTAGE - The method is eco-friendly and saves labor. The method ensures increased breeding of beneficial microorganisms, and high content of active metabolites.    DETAILED DESCRIPTION - Cultivating white fungus involves pulverizing corn cob (68-74%) to obtain particles having diameter of 3-5mm. Mushroom is pulverized to obtain particles having diameter of 2-3mm. Pulverized mushroom is soaked in water (20-30 times the quantity of mushroom) for 18-24 hours. Obtained mushroom product is mixed with corn cob. Obtained mixture (300-500kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical vent is made in heap by stick having diameter of 10-15cm. Heap is covered with grass, fermented naturally at 60 degrees C, and turned periodically. Gypsum is added, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is cooled, and inoculated with fungus. Mushroom extract (0.01-0.02 g/ml) is sprayed on obtained material in a dose of 4-6 kg/m2.
NOVELTY - Solid fermented product is prepared by using buckwheat as culture substrate and performing solid fermentation using mixture of Cordyceps sinensis and C.militaris.    USE - As solid fermented product.    ADVANTAGE - The solid fermented product provides excellent healthcare effect.
NOVELTY - Agaricus granules comprise dry material (40-50%) and water. Dry material comprises chaff (3-5%), quicklime (1-3%), gypsum (0.5-1.5%), river mud (20-30%), and wheat or barley (60-70%).    USE - Agaricus granules.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing Agaricus granules, which involves:    (A) drying dairy manure or pig manure in sun;    (B) composting dried product at 60-70 degrees C;    (C) adding lime water to obtained product to maintain pH at 8-8.5;    (D) pulverizing chaff, bran and river mud;    (E) wetting obtained mixture with water for 10-15 hours;    (F) adding soaked wheat or barley kernels to obtained mixture to obtain auxiliary material;    (G) mixing auxiliary material and obtained compost;    (H) adding quicklime and plaster to obtained mixture to obtain product having water content of 50-60% and pH of 8.5-9;    (I) filling obtained product in bottles;    (J) sterilizing bottles under high pressure; and    (K) inoculating Agaricus.
NOVELTY - An impurity adsorption-type purification column consists of column pipe from the top down sequentially disposed within the vial on the sieve, and blended mixture containing a C18 packing and N-propyl ethylene diamine in the mass ratio of 1:1-2 as filler.    USE - Impurity adsorption-type purification column for pre-treatment of detection of clenbuterol residue in animal urine (claimed).    ADVANTAGE - The column has convenient manufacture, simple operation, low cost, rapid purification, environment-friendliness and wide range of application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a use of impurity adsorption-type purification column for pre-treatment of detection of clenbuterol residue in animal urine.
NOVELTY - Preparing gas adsorbent i.e. terephthalic acid salt (I) involves dissolving terephthalic acid in ammonia, and adding salt solution to adjust pH to 8 at 10-50 degrees C for 1-15 hours. The terephthalic acid and salt solution are mixed in ratio of 1:1-2.5. The obtained precipitate is filtered and washed with aqueous ammonia. The obtained precipitate is dried to obtain terephthalic acid salt.    USE - Method for preparing gas adsorbent i.e. terephthalic acid salt for adsorbing nitrogen, carbon-dioxide or methane gases (claimed).    ADVANTAGE - The method enables to prepare gas adsorbent i.e. terephthalic acid salt that has high selectivity and adsorption capacity in simple manner under mild conditions.    DETAILED DESCRIPTION - Preparing gas adsorbent i.e. terephthalic acid salt of formula C8H4O4(Rx) (I) involves dissolving terephthalic acid in ammonia, and adding salt solution containing R to adjust pH to 8 at 10-50 degrees C for 1-15 hours. The terephthalic acid and salt solution containing R are mixed in ratio of 1:1-2.5. The obtained precipitate is filtered and washed with aqueous ammonia. The obtained precipitate is dried to obtain terephthalic acid salt.    R=lithium, sodium, rubidium, cesium, magnesium, calcium, barium and zinc; and    x=1-2.
NOVELTY - A biomass fuel gas methanation catalyst comprises 10-45 wt.% nickel oxide as active component, 3-15 wt.% copper, iron, manganese or molybdenum metal oxide as additive, and balance magnesium and zinc comodified gamma -aluminum oxide as carrier.    USE - Biomass fuel gas methanation catalyst.    ADVANTAGE - The catalyst has high activity and methane selectivity. The method is simple, and has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass fuel gas methanation catalyst comprising dissolving magnesium and zinc soluble salts into deionized water, soaking gamma -aluminum oxide into soluble salt solution, drying, heat treating to obtain magnesium-zinc comodified gamma -aluminum oxide carrier, dissolving catalyst active component nickel and additive copper, iron, manganese or molybdenum into deionized water, immersing magnesium-zinc comodified gamma -aluminum oxide carrier, drying, and heating.
NOVELTY - Synthesizing pig bone biodiesel oil catalyst comprises taking pig bone, washing with distilled water to remove surface soluble impurity, removing water into blast drying box, placing into muffle furnace, sintering at 800-1000 degrees C for 3-5 hours, getting white strip and block-shaped solid, crushing, sieving through 160-180 mesh to obtain white powder shape solid, adding potassium carbonate solution, stirring to obtain suspension, drying to obtain powder shape solid, and sintering into muffle furnace. The ratio of white powder shape solid and potassium carbonate solution is 7:3-9:1.    USE - Method for synthesizing pig bone biodiesel oil catalyst (claimed).    ADVANTAGE - The catalyst has oil yield reaching more than 90% and fatty acid conversion rate reaching to more than 85%, and can be utilized for 8 times.
NOVELTY - Two side separator insert the new utility model claims of disordered biogas slurry mixed convection type and high efficient stirring marsh gas ferment device, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipe and a discharge pipe respectively feedstock and the vertical, feedstock pipe and side wall of discharging pipe extending to annular pipe of biogas fermentation liquid face below seat, set with at least one plate of annular pipe in fermentation, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve with the fermentation system also comprises cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure in connecting, bacteria distributing pipe is circular pipe fixed on annular ferment bacteria distributing pipe in side wall, Brucella and pipe shape is annular pipeline phase, ferment bacteria distributing pipe set with multiple of one vertical direction of the cloth fungus through hole.
NOVELTY - This new utility model claims one kind of solar energy heating marsh gas tank, the round fermentation tank body and support frame welding fixed connection, said solar energy solar panels cover on surface of round fermentation tank body, the moving cover is set with round fermentation tank body at the top part, the guide gas tube passes through the bottom round fermentation tank body, the gas-guide tube through moving the top cover top, the water storage ring is set with in connected with the gas guide pipe and round tank body to ferment, the feedstock pipe is set with round fermentation tank body on the left side middle part, the hopper and top for the feedstock pipe connected with, in the water press is set with round fermentation tank body on the right side upper part, heating component is set with on the inner right side wall of round fermentation tank body lower part of the waste outlet on bottom is set with the round fermentation tank body, the photovoltaic inverter set at bottom left end of supporting frame, the storage battery is set with on the supporting frame bottom right end. The solar energy heating marsh gas tank structure is simple, the floor space is small area, suitable operation, energy saving environmental protection.
NOVELTY - External ointment comprises 15-20 pts. wt. Notopterygium root, 15-25 pts. wt. Euodia fruit, 10-20 pts. wt. herba siegesbeckiae, 20-40 pts. wt. Chinese Angelica, 5-15 pts. wt. Rhodobryum roseum, 10-20 pts. wt. Rhododendron molle, 10-20 pts. wt. herba solidaginis, 5-15 pts. wt. Trogopterus dung, 5-15 pts. wt. pepper, 10-20 pts. wt. green ormer, 10-20 pts. wt. caltrop, 5-10 pts. wt. borneol and 5-10 pts. wt. licorice.    USE - The external ointment is useful in acupuncture therapy, for treating anorectal disease and headache (claimed), such as migraine and nervous headache, activating blood and dissolving stasis, eliminating stasis, soothing nerve, expelling wind and activating collaterals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of external ointment, which involves (a) taking borneol and green ormer, and grinding through 120 mesh sieve to obtain fine powder, (b) adding 8-15 times water to herba siegesbeckiae, Chinese Angelica, R. roseum and R. molle, decocting 2-3 times (each time for 1.5-2 hours), combining decoctions, filtering and concentrating the filtrate to a relative density of 1.15-1.25 at 80 degrees C to obtain extract (E1), (c) adding 8-15 times 85% ethanol to Notopterygium root, Euodia fruit, Trogopterus dung, pepper and green ormer, extracting 2-3 times (each time for 2-3 hours), filtering, combining the filtrates, recovering ethanol for 24 hours, concentrating the filtrates to a relative density of 1.15-1.25 at 60 degrees C to obtain extract (E2), and (d) mixing the extracts obtained in steps (b) and (c) with fine powder obtained in step (a), and stirring uniformly to obtain finished product.
NOVELTY - Modified manganese dioxide electrocatalyst comprises using doped with calcium element or silver element or calcium.    USE - Modified manganese dioxide electrocatalyst used for electrolysis of catalytic alkaline water (claimed).    ADVANTAGE - The product has increased electrocatalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of electrocatalyst comprising taking manganese source and inorganic ammonium salt and dissolving in solvent; hydrothermally processing; separating solids, washing, and drying; dissolving inorganic calcium and inorganic silver in solvent; and mixing with third step product, stirring, standing, roasting, and doping with calcium element or calcium or silver element.
NOVELTY - Removal of sewage synthetic musk comprises introducing sewage containing synthetic musk into aerobic treatment device containing microorganism pellets for adsorption of synthetic musk, contacting sewage and microorganism pellets, conducting degradation treatment, introducing into sedimentation device for sludge sediment processing, and discharging the supernatant. Each microorganism pellet comprises Bacillus subtilis and curing agent.    USE - Removal of sewage synthetic musk (claimed).    ADVANTAGE - The method achieves high synthetic musk removal rate.
NOVELTY - Karst rock contaminated water repairing device comprises floating device (1), solar energy battery (3), air pump (2), air conduit (5), microbial community pipe (6), rope (7) and jin pendant (8). The air pump and solar energy battery are directly connected to the floating device. The microbial community pipe comprises main pipe having radial shape center and microbial community module.    USE - Device used for karst rock contaminated water repairing process (claimed).    ADVANTAGE - The device has simple design, is convenient to disassemble and transport and more suitable for energy deficient and complicated geographical environment, and achieves good processing water quality and denitrification and organic pollutant removal effects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for karst rock contaminated water repairing process using karst rock contaminated water repairing device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of karst rock contaminated water repairing device.    Floating device (1)    Air pump (2)    Solar energy battery (3)    Air conduit (5)    Microbial community pipe (6)    Rope (7)    Jin pendant (8)
NOVELTY - Microbial pellet comprises curable embedding agent for adsorbing synthetic musk in sewage, Bacillus subtilis for degrading the adsorbed synthetic musk, and additive for supporting the microbial pellet structure. The curing agent comprises activated sludge and activated carbon.    USE - The microbial pellet is useful for removing synthetic musk in sewage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of microbial pellet for removing synthetic musk in sewage, which involves (a) inoculating B. subtilis strain in a solid culture medium and expanding the culture, (b) centrifuging the expanded culture to obtain wet bacterial cells, (c) adding additive to the wet bacterial cells and uniformly stirring the mixture to obtain suspension, (d) adding curable embedding agent to suspension and uniformly stirring the mixture to obtain mixed raw material, and (e) forming mixed raw material into spherical microbial pellet, fermenting microbial pellet under dark conditions and generating white mycelium on the surface of microbial pellet.
NOVELTY - A municipal sludge dewatering performance is improved under cryogenic conditions by repeatedly using microorganism after cold acclimation complex at 10-15 degrees C.    USE - Method for improving municipal sludge dewatering performance (claimed).
NOVELTY - A manure is treated with Hermetia illucens by mixing raw yeast agents and antidegradants at weight ratio of 1:1, adding 0.02-0.04 wt.% manure agents, and 3-5 wt.% sugar containing coarse powder, adding manure, mixing, sealing for 12-24 hours, inoculating larvae, hatching eggs for 10-20 days, feeding with sawdust and/or and bran flour, and stirring under 20-50% relative humidity.    USE - Method for treating manure using Hermetia illucens (claimed).    ADVANTAGE - The method is environment-friendly, has high yield, and reduces cost, and pollution.
NOVELTY - A biological organic fertilizer is prepared by mixing photosynthetic bacteria, mold spores, thermophilic Actinomycetes, and fermented chicken manure to obtain fermented material, adding Bacillus megaterium, Bacillus subtilis, and corn straw and wheat straw fermented material, mixing, adding yeast, fermenting, adding effective microbial agents, fermenting, drying, crushing, and packaging.    USE - Method for preparing biological organic fertilizer used for potato (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of fermented chicken manure comprising taking fresh chicken manure, spraying photosynthetic bacteria, and fermenting for 15-20 hours under light intensity of 10000 lux; and (2) preparation of corn straw and wheat straw fermented material comprising drying, crushing to particle size of 40 mesh, adjusting carbon-to-nitrogen ratio to 25:1, and moisture content to 65%, and inoculating Bacillus megaterium and Bacillus subtilis at 55-58 degrees C for 14-15 days.
NOVELTY - Bioorganic fertilizer comprises 30-64 wt.% sugarcane filter mud, 2-4.7 wt.% bagasse, 6-12 wt.% ash and/or pulverized coal, 5-14.5 wt.% sheep manure, 7-11 wt.% cow dung, 5.5-9 wt.% chicken manure, 1.2-4.6 wt.% tobacco stalk and/or tobacco, 1-6.5 wt.% coffee grounds, 0.9-12 wt.% peat soil, 0-1 wt.% urea, 0.1-1.2 wt.% magnesium sulfate, 0-0.8 wt.% boron powder, 0.7-4 wt.% humic acid and 0.1-3 wt.% effective microorganisms.    USE - Bioorganic fertilizer.    ADVANTAGE - The product is low-cost and increases production yield and quality of vegetables and fruit trees. The method is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bioorganic fertilizer comprising mixing sugarcane filter mud, bagasse, ash and/or pulverized coal, sheep manure, cow dung, tobacco stalk and/or tobacco stem and coffee grounds to obtain premix material, mixing peat soil, urea, magnesium sulfate, boron powder, humic acid and effective microorganisms, adding to premix material, fermenting for 5-7 days to obtain fermented material, turning for 2 times, raising fermentation temperature at 60 degrees C when surface of the pile reaches 20 cm, fermenting at 55 degrees C when surface pile reaches to more than 20 cm, turning, setting fermentation temperature at 60 degrees C for 2-3 days when surface of the pile reaches 20 cm, cooling to 50 degrees C, carrying out second stage fermentation for 28-35 days to obtain secondary fermentation materials and packaging.
NOVELTY - Panax notoginseng saponin i.e. (1S,2R,3S,4R)-4-((3S,5R,8R,9R,10R,12R,13R,14R,17S)-12-hydroxy-17-((Z)-1-hydroxyprop-1-en-2-yl)-4,4,8,10,14-pentamethylhexadecahydro-1H-cyclopenta(a)phenanthren-3-yloxy)-6-(hydroxymethyl)cyclohexane-1,2,3-triol (I) is new.    USE - (I) is useful for treating cancer including liver cancer (claimed).    DETAILED DESCRIPTION - Panax notoginseng saponin i.e. (1S,2R,3S,4R)-4-((3S,5R,8R,9R,10R,12R,13R,14R,17S)-12-hydroxy-17-((Z)-1-hydroxyprop-1-en-2-yl)-4,4,8,10,14-pentamethylhexadecahydro-1H-cyclopenta(a)phenanthren-3-yloxy)-6-(hydroxymethyl)cyclohexane-1,2,3-triol of formula (I) is new. An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - The utility model claims a landfill garbage sorting machine process resource use device, including transport to a get in engine (20) of a landfill waste sorting landfill garbage and combustible garbage first sorting device (10); a landfill waste separation and separating a separating soil sand kind waste separating soil and sand separating device (60), wherein for the separating soil sand separating device (60) selecting and separating sand kind waste and humus soil, lime, saw dust, microorganism equal mixture again a manufacturing separating soil sand and organic fertilizer again using device (100), and wherein for the landfill garbage first sorting device (10) selecting the combustible garbage. do combustible garbage and a regeneration fuel again using device (200). The utility model is a garbage sorting machine process a resource use device a processing landfill waste a large, distinguish a kind garbage waste and recycling use, soil sand again a manufacturing organic fertilizer, a. processing is again use is made of fuel, realize full garbage waste energy, saving resource, use.
NOVELTY - Anti-aging moisturizing and whitening cosmetic comprises 0.5-5 wt.% radix glycyrrhizae, 0.5-5 wt.% large-headed atractylodes rhizome, 2-15 wt.% Bletilla striata, 0.5-5 wt.% Ginkgo, 1-10 wt.% American ginseng, 10-20 wt.% Salvia, 10-25 wt.% ginger, 1.8-2.2 wt.% 10% titanium dioxide colloid, 7-9 wt.% glycerin, 10-14 wt.% ethanol, 0.08-0.12 wt.% methyl parahydroxybenzoate, and balance deionized water.    USE - Anti-aging moisturizing and whitening cosmetic.    ADVANTAGE - The cosmetic is easy to produce, and has simple preparation, and low cost.    DETAILED DESCRIPTION - Anti-aging moisturizing and whitening cosmetic comprises 0.5-5 wt.% radix glycyrrhizae, 0.5-5 wt.% large-headed atractylodes rhizome, 2-15 wt.% Bletilla striata, 0.5-5 wt.% Ginkgo, 1-10 wt.% American ginseng, 10-20 wt.% Salvia, 10-25 wt.% ginger, 1.8-2.2 wt.% 10% titanium dioxide colloid, 7-9 wt.% glycerin, 10-14 wt.% ethanol, 0.08-0.12 wt.% methyl parahydroxybenzoate, and balance deionized water; prepared by soaking licorice, large-headed atractylodes rhizome, Bletilla striata, Ginkgo, ginseng, Salvia, and ginger in distilled water for 30-60 minutes, boiling at low heat for 20-30 minutes, filtering to obtain first filtered liquid, soaking medicine dregs in water, boiling at low heat for 20-30 minutes, filtering to obtain second filtered liquid, combining filter liquids, adding 90% ethanol at volume ratio of 1:1, standing at 4 degrees C for 24 hours, collecting supernatant, filtering, recycling ethanol, pre-freezing at - 80 degrees C, and vacuum freeze-drying.
NOVELTY - A traditional Chinese medicine composition comprises 50-200 pts. wt. epigallocatechin gallate, 30-80 pts. wt. lecithin, and 5-50 pts. wt. glabridin.    USE - Traditional Chinese medicine composition used for improving memory (claimed).    ADVANTAGE - The medicine composition can be prepared into a variety of dosage forms, meets urgent needs of elderly, and has easy administration, better improving memory effect, less dosage, small adverse reactions, simple preparation method, low cost and no environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of medicine composition comprising mixing epigallocatechin gallate, lecithin and glabridin, and sieving through 100 meshes sieve.
NOVELTY - Treatment of cypermethrin-containing wastewater involves adjusting pH of to-be-treated wastewater to 2-3 using sulfuric acid or hydrochloric acid, adding 10-40 wt.% sodium chlorite solution at 10-100 degrees C, oxidizing for 0.5-10 hours, adjusting pH of resultant water to 9-13 using sodium hydroxide, calcium hydroxide or calcium oxide, adding 2-10 kg chlorine dioxide, oxidizing for 0.5-6 hours, adjusting pH of resultant water to 9-14 using sodium hydroxide, calcium hydroxide or calcium oxide, introducing 50-1000 L ozone and oxidizing for 0.5-9 hours.    USE - Treatment of cypermethrin-containing wastewater (claimed).    ADVANTAGE - The method enables treatment of cypermethrin-containing wastewater by simple, economical and environmentally-friendly process with chemical oxygen demand removal rate of 90%. The content of total cyanide compound and ratio of biological oxygen demand and chemical oxygen demand of the treated water provided by the water is 0.5 mg/L or less and 0.06-0.38, respectively.
NOVELTY - Recovering 3-isobutyl glutaric acid monoamide from pregabalin intermediate mother liquor involves concentrating mother liquor to dryness and then adding water to the system. The liquid caustic soda is added to adjust temperature and pH of system. The solution is cooled and hydrochloric acid is added to adjust pH. The solution is cooled, filtered and dried. The solvent is filtered and dried to obtain final product. The ammonia is added to mother liquor 3-isobutyl glutaric anhydride. The product is extracted with ethyl acetate and then concentrated, cooled and filtered.    USE - Method for recovering 3-isobutyl glutaric acid monoamide from pregabalin intermediate mother liquor (claimed).    ADVANTAGE - The method enables to recover 3-isobutyl glutaric acid monoamide from pregabalin intermediate mother liquor in eco-friendly and simple manner.
NOVELTY - Preparation of R-3-isobutyl-glutarate monoamide involves adding chloroform and alcohol solvent to 3-isobutyl-glutarate monoamide, heating to 40-50 degrees C, dripping R-phenethylamine, heat-preserving, cooling to 20-30 degrees C, crystallizing, filtering, adding water to filter cake, adjusting pH of aqueous layer to 1-4 using acid, cooling to 0-5 degrees C, crystallizing, filtering and drying. The alcohol solvent is methanol or ethanol.    USE - Preparation of R-3-isobutyl-glutarate monoamide used as pregabalin intermediate.    ADVANTAGE - The method enables preparation of R-3-isobutyl-glutarate monoamide with high yield, within short period of time, by environmentally-friendly process.
NOVELTY - Wood raw material is continuously injected at predetermined speed from top to bottom of gravity moving bed, and solid carbon which is not gasified is continuously discharged at predetermined speed from bottom of gravity moving bed. At top of gravity moving bed, controlled amount of air is introduced into dispersion, and particulate material and high-temperature gas generated in bed flow downstream, lower-solid-separated, continuously-drawn, compressed by high-temperature induced draft fan and fed back to burner. Thus, the carbonization and gasification of wood is carried out.    USE - Carbonization and gasification of wood (claimed).    ADVANTAGE - The method is economical and environmentally-friendly, and provides carbonized and gasified wood, by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for carbonization and gasification of wood.
NOVELTY - Preparation of pure lamivudine (I) involves treating lamivudine using hydrochloric acid, obtaining lamivudine hydrochloride salt (II), isolating lamivudine hydrochloride salt, desalifying lamivudine hydrochloride salt, and obtaining pure lamivudine.    USE - Preparation of pure lamivudine used for treating retroviral infections.    ADVANTAGE - The improved method enables stereo-selective preparation of pure lamivudine with high productivity and reduced generation of effluents, by economical process.    DETAILED DESCRIPTION - Preparation of pure lamivudine of formula (I) involves treating lamivudine using hydrochloric acid, obtaining lamivudine hydrochloride salt of formula (II), isolating lamivudine hydrochloride salt, desalifying lamivudine hydrochloride salt, and obtaining pure lamivudine.
NOVELTY - 850 %Mass waste animal and vegetable oil is boiled, filtered, agitated, and concentrated sulfuric acid or concentrated phosphoric acid is added until the pH is adjusted to 3-4. Oil is then heated, stirred continuously, and left still. Stratified acid residue is then removed from the stirring tank, and oil is retained. Methanol and catalyst are sequentially added, constantly stirred, heated and esterified. Resultant material is refluxed, and residual methanol is distilled. Heating process is terminated, and aqueous phase material, glycerin and catalyst are removed to obtain biodiesel.    USE - Production of biodiesel using waste animal and vegetable oil (claimed).    ADVANTAGE - The method efficiently provides biodiesel having stable combustion efficiency with reduced combustion exhaust emission.    DETAILED DESCRIPTION - 850 %Mass waste animal and vegetable oil is added to a tank, boiled for 30 minutes, and filtered after completely evaporating water. The resultant oil is added to a stirring tank, agitated, and concentrated sulfuric acid or concentrated phosphoric acid is added until the pH is adjusted to 3-4. Oil is then heated at 40 degrees C in an autoclave, stirred continuously for 30 minutes, and left still for 30 minutes. Stratified acid residue is then removed from the stirring tank, and oil is retained. 120 %Mass methanol and 2.55 %mass catalyst containing 2 %mass zinc sulfate, 0.5 %mass aluminum sulfate, 1 %mass tetraamminecopper sulfate complex, 0.15 %mass chromium oxide and 0.35 %mass aluminum sulfide are sequentially added to the stirring tank, constantly stirred, heated and esterified for 3 hours. The resultant material is refluxed for one hour by continuously heated at 70 degrees C, and residual methanol is distilled. The heating process is then terminated, maintained for 40 minutes and aqueous phase material, glycerin and catalyst are removed from the bottom of the stirring tank to obtain biodiesel.
NOVELTY - Preparation of fuel oil involves uniformly mixing 15-20 pts. wt. straight-run heavy oil, 35-45 pts. wt. biodiesel and 50-75 pts. wt. coal tar into a reactor to obtain component (A), adding 0.0148-0.018 pt. wt. ferrocene, 0.5-1.5 pt. wt. sodium hydride and 0.05-0.1 pt. wt. sulfite to component (A), stirring to obtain component (B), adding 0.03-0.05 pt. wt. dispersant and 3-5 pts. wt. photocatalyst to component (B), stirring to obtain component (C), adding 3-4 pts. wt. toluene to component (C), uniformly mixing, filtering using 100 mesh screen and precipitating in clarification tower.    USE - Preparation of fuel oil (claimed).    ADVANTAGE - The method enables economical preparation of fuel oil which has excellent storage stability and long-term usability, reduces sulfur dioxide, nitrogen dioxide and carbon monoxide emissions, and does not generate smoke or carbon deposition during combustion.
NOVELTY - Organic fertilizer is produced by weighing 8 pts. wt. microorganism, 50 pts. wt. plant ash, 20 pts. wt. peanut shell powder, 32.5 pts. wt. wheat bran, 34 pts. wt. humic acid and 55 pts. wt. water, mixing the weighed materials, fermenting the mixture at 50 degrees C for 50-80 days, drying the fermented product at 70 degrees C, and pelletizing the dried product using pelletizer.    USE - As organic fertilizer in a form of pellet for crop (claimed).    ADVANTAGE - The organic fertilizer is environmentally-friendly.
NOVELTY - Method for producing organic fertilizer, involves weighing 9.5 pts. wt. effective microorganism, 23 pts. wt. citric acid residue, 40 pts. wt. peanut shell powder, 50 pts. wt. kitchen waste, 27 pts. wt. vinegar and 65 pts. wt. water, mixing the weighed materials, fermenting the mixture at 50 degrees C for 50-80 days, drying the fermented product at 70 degrees C, and pelletizing using pelletizer.    USE - The method is used for producing organic fertilizer for crops (claimed).
NOVELTY - Organic fertilizer is produced by weighing 13 pts. wt. effective microorganism, 43 pts. wt. cassava residue, 28 pts. wt. passion fruit cuticle, 24 pts. wt. humic acid, 37 pts. wt. cottonseed meal and 53 pts. wt. water, mixing the weighed materials, fermenting the mixture at 50 degrees C for 50-80 days, drying the fermented product at 70 degrees C, granulating the dried product using granulator, and packaging the granules.    USE - As organic fertilizer in a form of granule for crops (claimed).    ADVANTAGE - The organic fertilizer is environmentally-friendly.
NOVELTY - Preparing alkali-soil fruit tree organic nutrient solution comprises: (i) crushing 100 kg waste animal hair into 80-300 meshes, adding sulfuric acid, hydrolyzing by stirring to obtain a hydrolyzate; (ii) cooling the hydrolyzate, adding scrap iron wire into hydrolyzate, stirring for 22-25 hours, purifying to remove residue; (iii) adding ultra-fine phosphate rock powder into the reaction mixture under stirring condition, then adjusting the pH of mixture to 6.5-7.5; and (iv) adding 1000-2000 kg sheep manure or cow dung and 1 kg mixed fermentation bacteria into the mixture, fermenting.    USE - The method is useful for preparing alkali-soil fruit tree organic nutrient solution (claimed).    ADVANTAGE - The nutrient solution supply crop nutrients, improves the soil fertility, provides lasting fertilizer efficiency and suitable for alkaline-soil and infertile soil fruit trees.    DETAILED DESCRIPTION - Preparing alkali-soil fruit tree organic nutrient solution comprises: (i) crushing 100 kg waste animal hair into 80-300 meshes, adding sulfuric acid (25-30% to 0.2 cm2 raw material), hydrolyzing at 130-160 degrees C for 7-10 hours by stirring to obtain a hydrolyzate; (ii) cooling the hydrolyzate to 30-60 degrees C, adding 3-5 kg scrap iron wire or scrap iron into hydrolyzate, stirring for 22-25 hours, where the amino acid complexes in the hydrolyzate, purifying to remove residue; (iii) adding 300-500 kg ultra-fine phosphate rock powder into the reaction mixture under stirring condition, then adjusting the pH of mixture to 6.5-7.5; and (iv) adding 1000-2000 kg sheep manure or cow dung (moisture content of 20-30%) and 1 kg mixed fermentation bacteria into the mixture, fermenting at 30-60 degrees C for 25-30 days by turning the compost 2 or 3 times.
NOVELTY - A fipronil and/or ethiprole contaminated sediment repairing method involves preparing biochar from Michelia alba wood and carrying out repairing process of the fipronil and/or ethiprole contaminated sediment.    USE - Method for repairing fipronil and/or ethiprole contaminated sediment by using biochar.    ADVANTAGE - The method enables repairing the fipronil and/or ethiprole contaminated sediment with high practical application value, accurate determination of concentration of fipronil and/or ethiprole, better efficiency, and better utilization of biochar prepared from the Michelia alba wood having large specific surface area and strong adsorption ability, in a simple, cost effective and environment friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for detecting concentration of free-dissolved fipronil and/or ethiprole in the sediments after repairing, which involves determining concentration of free-dissolved fipronil and/or ethiprole in the sediments after repairing, by using polyformaldehyde resin.
NOVELTY - Preparing organic and inorganic compound fertilizer involves mixing lignite and tobacco in ratio of 5-8:2-5 to obtain a former mixture. Ammonium carbonate is mixed with the former mixture in ratio of 3-8:1-3 to obtain later mixture. Molasses powder, yellow potassium humate, amino acid or bean pulp are mixed with water and heated at 50-100 degrees C to prepare saturated nutrient liquid. Saturated nutrient liquid is mixed with later mixture in ratio of 85-75:15-25 and stirred uniformly to obtain tertiary mixture.    USE - Method for preparing organic and inorganic compound fertilizer used for controlling insect pests on plant (claimed).    ADVANTAGE - The method enables to prepare quick-acting nutrient organic and inorganic compound has soil improvement function.    DETAILED DESCRIPTION - Preparing organic and inorganic compound fertilizer involves mixing lignite and tobacco in ratio of 5-8:2-5 to obtain a former mixture. Ammonium carbonate is mixed with the former mixture in ratio of 3-8:1-3 to obtain later mixture. Molasses powder, yellow potassium humate, amino acid or bean pulp are mixed with water and heated at 50-100 degrees C to prepare saturated nutrient liquid. Saturated nutrient liquid is mixed with later mixture in ratio of 85-75:15-25 and stirred uniformly to obtain tertiary mixture. Bacillus strain and potassium dihydrogen phosphate are mixed in ratio of 1000:1-2 and stirred uniformly and fermented for 15-60 days to obtain fermented product. Polyacrylamide, chitosan, modified attapulgite and polymerized aluminum chloride are ground through 80 meshes in ratio of 5-20:5-10:40-80:20-30 to obtain mixture. All products are combined, and then granulated by using a rotary drum granulator.
NOVELTY - 4-Fluorobenzonitrile or 4-fluoro-phthalonitrile as raw material, and nitrogen-containing heterocyclic compound are heated in presence of base and solvent, reacted at 60-120 degrees C for 5-10 hours to obtain heterocyclic group-containing benzonitrile or phthalonitrile compound.    USE - Synthesis of heterocyclic group-containing benzonitrile or phthalonitrile compound (claimed).    ADVANTAGE - The method efficiently and economically provides high yield of heterocyclic group-containing benzonitrile or phthalonitrile compound with high productivity, by simple method in mild reaction condition without affecting the environment.
NOVELTY - An organic fruiting time fertilizer comprises potassium, carbon, nitrogen, phosphorus, microbial inoculant, and nitrogen-fixing bacteria. The microbial inoculant comprises lactobacilli, photosynthetic bacteria and other bacteria of bacilli group which decompose plant waste in soil and convert it into organic material. The nitrogen-fixing bacteria comprise Azospirillum, Azotobacter, or Clostridium that deposits near rhizosphere and fixes nitrogen.    USE - Organic fruiting time fertilizer.    ADVANTAGE - The fertilizer has very high potassium content and provides required quantity of potassium to the plants at fruiting time, thus improving yield; has very low heavy metal content; and does not contain pathogen. The microbial inoculant induces plant systemic responses to foliar fungal diseases and improves plant responses to problems caused by soilborne pathogens.
NOVELTY - Organic fertilizer comprises necessary nutrient that are required for plant in suitable quantity, is claimed.    USE - As organic fertilizer.    ADVANTAGE - The fertilizer is purely organic, completely free from chemical, and pathogen, and increases yields, and enables to maintain physical property, water balance and nutrients of soil.
NOVELTY - Sewage irrigation with zero value iron or microorganism composite water percolation wall purification system comprises slope systems set with multiple sewage disposal units. The sewage disposal units include anaerobic fermentation tank (2), biological filter percolation pool and zero value iron wall (4). Domestic sewage were collected through water transmission pipeline system for treatment at disposal units, discharged into waterfront vegetation zone (10) for further purification process, and discharged into river.    USE - Method for irrigating sewage with zero value iron or microorganism composite water percolation wall purification system used for increasing treatment efficiency and strengthening water quality without peculiar smell.    ADVANTAGE - The method has synergistic effect, convenient management and maintenance, and low cost. The use of gullies in sewage effluent disposal unit improves water level and creates anaerobic environment more conducive to removal of ammonia.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of zeolite coated-zero value iron comprising soaking zeolite in ferrous sulfate or ferrous chloride solution under nitrogen gas protection, uniformly stirring, gradually adding sodium borohydride or potassium borohydride solution as reducing agent under alkaline conditions, and reacting for 0.5-3 hours.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage irrigation system.    Sewage collecting pipe (1)    Anaerobic fermentation tank (2)    Circular gravel biological filter percolation pool (3)    Zero value iron water filter wall (4)    Waterfront vegetation zone (10)
NOVELTY - Processing anaerobic treatment of animal manure comprises diluting manure into hot hydrolysis tank, reacting at 70 plus minus 5 degrees C, carrying out solid retention for 1-3 days; drying at low temperature, diluting to solid content of 12-15%; mixing into anaerobic tank at 35 plus minus 5 degrees C or 55 plus minus degrees C, carrying out solid retention for anaerobic digestion for 14-20 days; and collecting and utilizing biogas.    USE - Method for processing anaerobic treatment of animal manure used for increasing biogas yield to 60%.    ADVANTAGE - The method saves energy consumption and reduces health risk biogas residue and agricultural slurry which meets United States Environmental Protection Agency on pasteurized biosolids.    DESCRIPTION OF DRAWING(S) - The drawing shows process flow diagram of anaerobic treatment of animal manure (Drawing includes non-English language text).
NOVELTY - An S-carbinoxamine is synthesized by reacting 2-pyridine formaldehyde and chlorophenyl boric acid in the presence of rhodium carbene catalyst, performing condensation reaction to obtain (S)-(4-chlorophenyl)-2-pyridine methanol, and conducting Williamson etherification by reacting with 2-chloro-N,N- dimethyl-ethanamine.    USE - Method for asymmetric synthesis of S-carbinoxamine (claimed).    ADVANTAGE - The method has short process, mild reaction condition, simple operation, and high efficiency. It is environment-friendly, suitable for industrial production.
NOVELTY - Cultivating Agrocybe aegerita involves crushing 46-54% cottonseed hull, 28-36% sawdust, 10-12% tea seed cake, 3-4% mushroom, 2-3% lime and 1% precipitated calcium carbonate into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) at low temperature for 18-24 hours, and then performed piling of product with height of 1.0-1.2m and width 2-3m to obtain stack (300-500kg), covered it with tarpaulin, and then carried out natural fermentation at 60 degrees C for 24 hours. Calcium carbonate is mixed with fermented product and covered with material.    USE - Method for cultivating Agrocybe aegerita (claimed).    ADVANTAGE - The method is eco-friendly and save labor cost, and enables to promote mycelial growth of Agrocybe aegerita.    DETAILED DESCRIPTION - Cultivating Agrocybe aegerita involves crushing 46-54% cottonseed hull, 28-36% sawdust, 10-12% tea seed cake, 3-4% mushroom, 2-3% lime and 1% precipitated calcium carbonate into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) at low temperature for 18-24 hours, and then performed piling of product with height of 1.0-1.2m and width 2-3m to obtain stack (300-500kg), covered it with tarpaulin, and then carried out natural fermentation at 60 degrees C for 24 hours. Calcium carbonate is mixed with fermented product and covered with material with thickness of 1-2 cm to obtain seeding bed. Agrocybe aegerita is placed into seeding bed to carry out fruiting, and then lixiviums (0.01-0.02g/ml) and mixture (4-6kg) are sprayed. The seeding bed is soaked in water (20 times) for 18-24 hours, and filter residue is removed.
NOVELTY - Wheat seed treating agent comprises 1-30 wt.% silthiofam, 0.1-10 wt.% prochloraz or its manganese salt, 1-20 wt.% fipronil and subsidiary component.    USE - Wheat seed treating agent used for preventing and treating wheat root rots and controlling wireworms (claimed).    ADVANTAGE - The wheat seed treating agent reduces labor intensity and energy consumption.
NOVELTY - Purification apparatus comprises (a) ozone generator supplying 25-50 parts per million (ppm) dissolved ozone to the organic wastewater, (b) dissolver equipped with oxygen generator for supplying 25-50 ppm oxygen to wastewater, (c) preprocessing tank for circulating wastewater, and (d) post-treatment tank for purifying wastewater. The post-treatment tank comprises first reaction tank which is filled with Cryptomeria japonica chips, and second reaction tank which is filled with activated charcoal.    USE - The apparatus or method is useful for purification of organic wastewater at high concentration (all claimed).    ADVANTAGE - The apparatus purifies water, and provides harmless water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for purifying organic wastewater at high concentration.    DESCRIPTION OF DRAWING(S) - The drawing shows block view of purification apparatus.    Ozone generator (10)    Oxygen generator (20)    Dissolver (30)    Preprocessing tank (40)    First reaction tank (60)    Second reaction tank (70)
NOVELTY - The device has a material feeder that supplies the pre-processed biomass. The simultaneous saccharification or the diastatic fermentation is performed. A mixer (10) is provided with a shaft (11) and impeller (12). The board-shaped impeller is provided with the flat plane (a) which is inclined to the predetermined angle from the longitudinal direction and the parallel reference surface (b) of the shaft is inclined to predetermine angle.    USE - Device for producing high concentration fermentable sugar.    ADVANTAGE - The cellulosic biomass reduces the cost of the raw material. The speed of the saccharification or simultaneous saccharification and fermentation is increased. The operation cost of the purification process is reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing high concentration fermentable sugar; and    (2) biochemical material.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the mixer.    Mixer (10)    Shaft (11)    Impeller (12)    Flat plane (a)    Parallel reference surface (b)
NOVELTY - The apparatus has a reduction unit (300) which is connected to remnant treatment unit (400) installed inside case (410) for processing the remaining food wastes. A dryer unit (500) dries food waste which is provided through reduction unit and recycles food waste as fertilizer or fodder. A sludge recovery unit (420) has a dehydrating hole (421) or mesh network. The reduction unit compresses the moisture contained in the food waste dropped down from the breaking unit (200). The breaking unit connects to main portion (100) in which food waste is filled and crushes the food waste.    USE - Food garbage treating apparatus.    ADVANTAGE - The reduction unit compresses the moisture contained in the food waste dropped down from the breaking unit, so that the capacity is increased and the microorganism decomposition treatment time is increased. The remnant of the kneading is easily processed and process efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of food garbage treating apparatus.    Main portion (100)    Breaking unit (200)    Reduction unit (300)    Remnant treatment unit (400)    Case (410)    Sludge recovery unit (420)    Dehydrating hole (421)    Dryer unit (500)
NOVELTY - Waste is pre-treated by crushing solid waste with crushing device, and solid, liquid and gaseous wastes are pumped alone or mixed and pumped into absorbing tube, and transmitted to microwave absorber tube by magnetron. Pyrolysis wastes, organic waste cleavage solid carbon and carbon monoxide gas, hydrogen, methane and other combustible gases and inorganic waste cleavage glassy mixture are separated with microwave energy. Pyrolysis gases generated by secondary processing unit are processed, to obtain carbon dioxide gas and steam.    USE - Heat-accumulating-type microwave processing of waste (claimed).    ADVANTAGE - The method enables environmentally-friendly heat-accumulating-type microwave processing of waste, by simple method.
NOVELTY - Processing device comprises livestock and poultry processing tank (10) that is provided with cleaning hole (101) and discharge port (102). The discharge port is connected with digester. The livestock and poultry processing tank is located at the top of feed and exhaust port (104). The exhaust port is connected to sterilization unit and ultraviolet sterilizing device through pipe. The feeding mouth is connected to feed mechanism (20).    USE - Processing device used for cleaning biodegradable dead and diseased livestock and poultry (claimed).    ADVANTAGE - The processing device ensures no smell, body decay, no epidemic disease spreading, safety, no human and animal toxicity and no environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a processing device.    Livestock and poultry processing tank (10)    Feed mechanism (20)    Cleaning hole (101)    Discharge port (102)    Exhaust port (104)
NOVELTY - Chicken manure turning and rotating machine comprises roller body (1), rake (2) and roller end provided with connecting shaft (3). The rake comprises polishing blade, block and connecting arc plate that is connected with inner side plate, which is connected with roller body. The inner side plate is provided with upper connecting hole, and connected with block. The polishing blade, roller body and rake surface are set with uniform corrosion resistant layer (8).    USE - Chicken manure turning and rotating machine.    ADVANTAGE - The chicken manure turning and rotating machine ensures high polishing efficiency, low maintenance cost, good quality organic fertilizer production and durability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a chicken manure turning and rotating machine.    Roller body (1)    Rake (2)    Connecting shaft (3)    Corrosion resistant layer (8)
NOVELTY - Preparing bio-fertilizer involves ventilating vegetable waste in flat space on ground, and removing impurity. Vegetable waste comprises microorganism itself, which is utilized to carry out natural fermentation at 60-75 degrees C for 30-45 days, where vegetable waste water content reduce to 40-60%. Earthworm is inoculated in fermented product, and then earthworm is taken out.    USE - Method for preparing bio-fertilizer (claimed) used for promoting crop growth, especially high plant.    ADVANTAGE - The method is eco-friendly, and enables to prepare bio-fertilizer that increases compost product and nutrient element content.
NOVELTY - Organic fertilizer comprises 17-20 pts. wt. cellulase, 37-47 pts. wt. pectin, 5-12 pts. wt. glucanase, 5-12 pts. wt. pectin esterase, 5-12 pts. wt. xylanase, 5-12 pts. wt. lipopeptide, 2-4 pts. wt. thiol protease, 5-17 pts. wt. urea, 5-17 pts. wt. naphthyl isocyanate and 7-10 pts. wt. diisooctyl adipate.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is eco-friendly.
NOVELTY - Microbial fertilizer comprises not less than 40% organic matter content, photosynthetic bacteria, nitrogen-fixing bacteria, phosphorus bacteria, colloidal Bacillus, Paecilomyces and Penicillium.    USE - Microbial fertilizer.    ADVANTAGE - The microbial fertilizer ensures soil improvement effect, and relieves crop plant nematode, cyst, dangerous disease and continuous cropping obstacle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial fertilizer, which involves:    (A) inoculating Paecilomyces lilacinus in culture medium;    (B) oscillating culture medium with water;    (C) sterilizing obtained culture medium;    (D) fermenting obtained material with remaining materials at 40 degrees C; and    (E) fermenting obtained material for second time at 30-35 degrees C for 3-5 days to obtain product.
NOVELTY - Preparing high-fertility soil matrix involves mixing manure, corn straw and pine needle. Ratio of carbon and nitrogen content is regulated to 30:40. Obtained mixture is mixed with lignin, fiber and cellulose in ratio of 25-30:20-25:10-15. Obtained mixture is inoculated with microbial inoculum, and then covered by black plastic film and sealed. Obtained product is fermented at 50-60 degrees C for 25-30 days. Temperature is reduced to 25-30 degrees C, and zeolite powder (5-7%) and biochar (5-7%) is added to fermented product. Obtained product is pulverized to obtain the final product.    USE - Method for preparing high-fertility soil matrix (claimed).
NOVELTY - The system has a main portion that is comprised with a strip-shaped discharging pool that is provided with a lengthways track, and a traveling crane which is provided along the lengthways track of the strip-shaped discharging pool. The upper shift portion of the traveling crane is set with a self-motion feedstock unit. One end of the transverse channel is set with a buffer bin, and the other end of the transverse channel is set with a material transport mechanism. A programmable logic controller is connected with the system main portion.    USE - Automatic sludge processing system.    ADVANTAGE - Low energy consumption, increased production and environmentally-friendly effect is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an automatic sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the automatic sludge processing system. (Drawing includes non-English language text)    Long fermentation pool (1)    Strip-shaped discharging pool (2)    Lengthways track (3)    Lateral channel (4)    Traveling crane (6)
NOVELTY - Preparing cultivation material and cultivating Hypsizygus marmoreus involves crushing 48-52% cottonseed hull, 28-32% bagasse, 12-14% bean cake, 3-4% mushroom, 2-3% lime and 1% calcium carbonate to obtain powder with particle diameter of 3-5mm. Powder is soaked with clean water (20-30 times) for 18-24 hours and then piling to obtain stack of culture material (300-500kg). Culture material is subjected to natural fermentation at 60 degrees C for 24 hours, and then calcium carbonate (3-4 times) is mixed to reduce water content to 63-65%. Product is packaged in polypropylene plastic bag.    USE - Method for preparing cultivation material and cultivating Hypsizygus marmoreus (claimed).    ADVANTAGE - The method enables to prepare cultivation material and cultivate Hypsizygus marmoreus in eco-friendly manner, and promotes beneficial microorganism breeding and fruiting of Hypsizygus marmoreus.    DETAILED DESCRIPTION - Preparing cultivation material and cultivating Hypsizygus marmoreus involves crushing 48-52% cottonseed hull, 28-32% bagasse, 12-14% bean cake, 3-4% mushroom, 2-3% lime and 1% calcium carbonate to obtain powder with particle diameter of 3-5mm. Powder is soaked with clean water (20-30 times) for 18-24 hours and then piling to obtain stack of culture material (300-500kg). Culture material is subjected to natural fermentation at 60 degrees C for 24 hours, and then calcium carbonate (3-4 times) is mixed to reduce water content to 63-65%. Product is packaged in polypropylene plastic bag, and then Hypsizygus marmoreus is transferred in bag. Polypropylene plastic bag is placed in dark cultivating bacterium room at 18-20 degrees C and humidity 60-75% for 22-24 days.
NOVELTY - Preparing cultivation material involves pulverizing wood powder (52-58%), corn cob (20-24%), soybean (15-17%), mushroom (3-4%), lime (2.5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn cob and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin.    USE - Method for preparing cultivation material used for Pleurotus citrinopileatus (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of Pleurotus eryngii.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (52-58%), corn cob (20-24%), soybean (15-17%), mushroom (3-4%), lime (2.5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn cob and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Lime and gypsum are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Bio-fertilizer comprises 15-22 pts. wt. Bacillus subtilis, 11-13 pts. wt. Curcuma zedoaria, 18-25 pts. wt. hyacinth bean, 15-25 pts. wt. Astragalus mongholicus, 10-11 pts. wt. rhizoma arisaematis, 1 pts. wt. pectate lyase, 1 pts. wt. pectinesterase, 1 pts. wt. Bacillus subtilis protease and 1 pts. wt. cellulase.    USE - Bio-fertilizer used for Euphorbia (claimed).    ADVANTAGE - The bio-fertilizer increases yield of Euphorbia, ensures sustainable development of agriculture, and prevents soil salinity.
NOVELTY - Continuous stirred-tank reactor biogas fermentation system comprises straw storage bin, rapid degradation tank, hydrolyzing tank, independent heat exchanger, continuous stirred-tank reactor integrated reactor, marsh gas purifying device, temporary storage pool, and solid liquid separator. Continuous stirred-tank reactor integrated reactor comprises tank body (1), motor, reverse stirring device and relux system. The tank body wall is set with insulating layer (9) and heating layer (8). The heating layer top end is set with air outlet (4) and discharging mouth (7).    USE - Continuous stirred-tank reactor biogas fermentation system.    ADVANTAGE - The continuous stirred-tank reactor biogas fermentation system has improved efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of continuous stirred-tank reactor biogas fermentation system.    Tank body (1)    Air outlet (4)    Discharging mouth (7)    Heating layer (8)    Insulating layer (9)
NOVELTY - Mesorhizobium zengchengense RITF1218 (CCTCC NO: M 2014492), is new.    USE - The Mesorhizobium zengchengense is useful in preparing nitrogen fixation microbial agents or bio-organic fertilizer (claimed).    ADVANTAGE - The strain has a good resistance property.
NOVELTY - A Bacillus subtilis strain SW002 (KACC 92034P), is new. The B.subtilis strain SW002 is capable of exhibiting antibacterial activity against Staphylococcus and capable of producing insoluble phosphoric acid.    USE - The B.subtilis strain SW002 is useful in fermenting agent, microbial agent for handling excrement, promoting growth of crop, preparing liquefied fertilizer, and improving water quality, and providing antibacterial activity against Staphylococcus, and in livestock feed or feed additive (claimed).    ADVANTAGE - The B.subtilis strain SW002 is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermenting agent, which comprises the above-mentioned B.subtilis strain SW002 as an active ingredient.
NOVELTY - The utility model is a dreg remover for a marsh gas pool. Belongs to marsh gas pool slag technology field. It mainly solves the problem that the existing manual deslagging exist labour intensity large, would have marsh gas poisoning, spiral slag remover exist using effect is bad and problem. Main characteristic of it is: including grasping, lifting, power, hydraulic pressure and walking part, grasping part comprises six-claw grab hook, a grab hook oil jar, upper claw connecting rod, a moving joint pole, moving joint, the top offset oil jar and worm wheel turn by hand device, upper vertical rod, pull-push oil jar and cross arm, lifting part comprises upright post, moving the lifting plate, a chain wheel, a chain, a lifting rotary disk, rotary oil jar, power part comprises engine, hydraulic pressure part comprises distributor, a pressure regulating valve, an oil pump, an oil tank and oil pipe, walking part comprises small four wheel tractor. The utility model is new type equipment with compact structure, simple and convenient operation, energy saving and environment-friendly, the main use is the waste residue in the 5-8 cubic biogas pool eliminating sum.
NOVELTY - Eco-friendly fertilizer comprises livestock and fish waste (100 pts. wt.), pulverized straw (10-40 pts. wt.), and bacteria (1-2 pts. wt.).    USE - Eco-friendly fertilizer.    ADVANTAGE - The eco-friendly fertilizer is economic, and has good effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing eco-friendly fertilizer, which involves:    (A) pulverizing livestock and fish waste to obtain paste;    (B) sterilizing paste;    (C) adding pulverized straw to obtained paste to obtain product having water content of 60-65%; and    (D) adding bacteria to obtained mixture under stirring condition.
NOVELTY - Black pine rejuvenation matrix comprises 500 pts. wt. fermented material, 50 pts. wt. pine soil and 1 pt. wt. additive, and is prepared by mixing raw materials. The fermented material comprises 1000 pts. wt. animal manure, 72 pts. wt. leaves, 0.1 pt. wt. fermenting bacteria, 0.15 pt. wt. functional bacteria and 2.25 pts. wt. additives.    USE - Black pine rejuvenation matrix.    ADVANTAGE - The matrix improves soil structure, increases manganese, zinc, magnesium and potassium content, number of roots and black pine roots around the soil , promotes healthy root growth, increases absorption of nutrient and water, reduces from 100% to 37-8% pine twigs diseases and enhances disease resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of fermented material involves mixing fermenting bacteria, functional bacteria and additives to get mixture; sprinkling animal manure layer into mixture layer, scattering 10-20 cm thick leaves layer overlapping animal manure, stacking into 1 m high, 1 m wide and 3 m long, crossing each stack 50 cm into 2 inch vent pipe layer that has 1.5 m spacing and ahead of hole; and measuring temperature everyday, where after 3-4 days temperature is 60 degrees C, turning stack, repeating piling in second step for 3 days, turning once, and determining fermentation completion where 14-18 days in autumn and 6-9 days in summer.
NOVELTY - Composite biomass fuel particle comprises 40-80 pts. wt. straw, 5-15 pts. wt. bamboo shavings, 5-15 pts. wt. bark, 10-25 pts. wt. anthracite and 0.5-2 pts. wt. desulfurization agent particularly methylendiphenanthridin derivative.    USE - Composite biomass fuel particle.    ADVANTAGE - The biomass fuel value is high compared to conventional biomass fuel. It has synergistic effect of combustion which greatly improves combustion efficiency without harmful combustion and acid gases.
NOVELTY - The apparatus has a minute particle water spray device (124) formed in the chamber, and is provided to supply the water into the chamber from outside. A solenoid valve (125) is installed in the outlet side of the chamber. The water level sensor (127) is connected to the exhausting portion (147). A heating element (133) is provided to heat the chamber in the cultivation mode selected by the user at a temperature in which the cultivation of microorganism is actively made. A control unit (200) is provided to drive exhausting portion, opening/closing valve (148) and solenoid valve.    USE - Food waste disposal apparatus.    ADVANTAGE - The cultivation mode preferences in which the microorganism is actively cultivated are selected reliably. The microbe habitation environment within the chamber is controlled through the water level sensor and odorant sensor so that the decomposition of the food through the microorganism is smoothly accomplished and the oxygen required for the form of the microorganism is produced within the chamber through the electrolysis. The smell of food generated within the chamber is not leaked to the outside.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the chamber outer bottom of the food garbage disposal apparatus.    Minute particle water spray device (124)    Solenoid valve (125)    Water level sensor (127)    Heating element (133)    Exhausting portion (147)    Opening/closing valve (148)    Control unit (200)
NOVELTY - Preparation for continuously crystallizing 6-amino-penicillanic acid comprises mixing 6-amino-penicillanic acid, lysate and butanol; transferring to reaction vessel, reacting, stirring, adding hydrochloric acid and controlling the pH value; passing lower layer reaction solution into continuous crystallization vessel, passing upper layer reaction solution into continuous recovery; adding aqueous ammonia into continuous crystallization vessel and controlling pH value; passing crystals solution into continuous filtration apparatus, filtering to get cake; and washing and drying cake.    USE - Method for continuously crystallizing 6-amino-penicillanic acid used in pharmaceutical industry (claimed).    ADVANTAGE - The method improves uniformity and efficiency of product, enables automatic control and saves energy source.    DETAILED DESCRIPTION - Preparation for continuously crystallizing 6-amino-penicillanic acid comprises mixing 6-amino-penicillanic acid, lysate and butanol; transferring to reaction vessel, reacting at 5-10 degrees C, stirring, adding hydrochloric acid and controlling the pH value of 0-0.5; passing lower layer reaction solution into continuous crystallization vessel when liquid level rises to set height, passing upper layer reaction solution into continuous recovery and maintaining set height; adding aqueous ammonia into continuous crystallization vessel and controlling pH value of 4.0-4.5 to get crystals solution; passing crystals solution into continuous filtration apparatus when liquid level rises to set height, filtering to get cake and maintaining solution of set height; and washing and drying cake.
NOVELTY - Preparing afatinib (I), comprises e.g. carrying out substitution reaction of 7-fluoro-6-nitroquinazolin-4(3H)-one (II) to obtain (S)-6-nitro-7-((tetrahydrofuran-3-yl)oxy)quinazolin-4(3H)-one (III), reducing (III) to obtain (S)-6-amino-7-((tetrahydrofuran-3-yl)oxy)quinazolin-4(3H)-one (IV), performing amidation reaction of (IV) to obtain (S,E)-4-(dimethylamino)-N-(4-oxo-7-((tetrahydrofuran-3-yl)oxy)-3,4-dihydroquinazolin-6-yl)but-2-enamide (V), condensing (V) to obtain (I), and forming dimaleate salt of (I) i.e. (VI).    USE - The method is useful for preparing afatinib.    ADVANTAGE - The method is simple, economical, environment-friendly, and suitable for industrial production.    DETAILED DESCRIPTION - Preparing afatinib of formula (I), comprises carrying out substitution reaction of 7-fluoro-6-nitroquinazolin-4(3H)-one of formula (II) to obtain (S)-6-nitro-7-((tetrahydrofuran-3-yl)oxy)quinazolin-4(3H)-one of formula (III), reducing (III) to obtain (S)-6-amino-7-((tetrahydrofuran-3-yl)oxy)quinazolin-4(3H)-one of formula (IV), performing amidation reaction of (IV) to obtain (S,E)-4-(dimethylamino)-N-(4-oxo-7-((tetrahydrofuran-3-yl)oxy)-3,4-dihydroquinazolin-6-yl)but-2-enamide of formula (V), condensing (V) to obtain (I), and forming salt of (I) to obtain (S,E)-N-(4-((3-chloro-4-fluorophenyl)amino)-7-((tetrahydrofuran-3-yl)oxy)quinazolin-6-yl)-4-(dimethylamino)but-2-enamide dimaleate salt of formula (VI).
NOVELTY - A mixing pelletizing process is performed by taking main medicine for drug dissolution, stirring, and forming solution; adding the solution with adhesive and mixing, and forming uniform mixture; adding the mixture with auxiliary material, adding in high speed mixing machine for mixing pelletizing, and shaping; drying, adding in 2-dimensional mixer, and carrying out total mixing; and tableting and coating.    USE - Mixing pelletizing process for multi-dimension chip (claimed).    ADVANTAGE - The process saves raw material, reduces mixing times, and reduces pollution risk.
NOVELTY - Preparation of lacidipine-containing composition involves carrying out two-step one-pot synthesis reaction for producing lacidipine, and preparing a composition containing lacidipine as active component.    USE - Preparation of lacidipine-containing composition used for industrial and clinical applications.    ADVANTAGE - The method efficiently and safely provides lacidipine-containing composition having increased dissolution rate and excellent illumination stability, by simple method in short period of time without affecting the environment.
NOVELTY - Preparation of methyl 2,2-difluorobenzo (d) (1,3) dioxole-5-carboxylate (III) comprises subjecting 2,2-difluoro-2H-1,3-benzodioxole-5-carbonyl fluoride (II) and methanol to esterification reaction.    USE - Method for preparation of methyl 2,2-difluorobenzo (d) (1,3) dioxole-5-carboxylate (claimed) used for pesticides or pharmaceutical intermediates.    ADVANTAGE - The method is very convenient for large scale commercial production, achieves high purity and stable quality target product, uses inexpensive raw material and reagent, and has short synthesis route, easy to control technique process, complete reaction, high yield, less dosage of solvent, and reduced wastewater production and environmental pollution.    DETAILED DESCRIPTION - Preparation of methyl 2,2-difluorobenzo (d) (1,3) dioxole-5-carboxylate of formula (III) comprises subjecting 2,2-difluoro-2H-1,3-benzodioxole-5-carbonyl fluoride of formula (II) and methanol to esterification reaction.
NOVELTY - Efficient cultivation of anti-disease chrysanthemum includes choosing loose, fertile, well-drained, acidic sandy loam seedbed, and constructing plastic film; mixing wheat straw, rice hulls, manure, and pond scum mix, stirring, adding water mixed with lactic acid bacteria, and applying plastic film; taking amino acids, zinc sulfate, calcium sulfate, ferrous sulfate, boric acid, manganese sulfate solution and acetic acid solution, and urea; plant spacing, mixing seed and river sand, and spreading; transplanting into field, and planting 4500 seeds per acre; and supplying nutrient solutions.    USE - Method for efficient cultivation of anti-disease chrysanthemum (claimed).    ADVANTAGE - The nutrient regulator improves plant condition, prevents diseases. It is safe to use, stable, and low cost with high economical benefits.    DETAILED DESCRIPTION - Efficient cultivation of anti-disease chrysanthemum involves choosing loose, fertile, well-drained, acidic sandy loam seedbed, and constructing 25 cm layer of plastic film around seedbed; mixing wheat straw, rice hulls, manure, and pond scum mix, stirring, adding 66-78 wt.% water mixed with lactic acid bacteria, adjusting pH 5-7, and applying plastic film in seedbed of thickness 28-31 cm; taking 15 wt.% amino acids, 12 wt.% zinc sulfate, 13 wt.% calcium sulfate, 10 wt.% ferrous sulfate, 15 wt.% EDTA, 10 wt.% boric acid solution for chelating reaction, 4 wt.% manganese sulfate solution and acetic acid solution, and 12-16 wt.% urea, adjusting pH 4-5, and obtaining nutrient agent; plant spacing 23-26 cm, wide row spacing 75-80 cm and narrow row spacing 42-44 cm, opening drain, mixing seed and river sand at 1:3 mass ratio, and spreading; transplanting into field after chrysanthemum seedlings grow 5-6 leaves, controlling 45 cm spacing, 34 cm row spacing, and planting 4500 seeds per acre; and supplying 40-50 L different nutrient solutions depends on stages of growth.
NOVELTY - Production of composite fertilizer involves recovering sulfur-containing flue gas, introducing into desulfurization tower, and generating ammonium sulfate by oxidizing ammonium sulfite solution by heat-exchanging by spraying aqueous ammonia to desulfurization tower, reacting aqueous ammonia and sulfur dioxide of flue gas, obtaining ammonium sulfite, oxidizing the resultant product, and obtaining ammonium sulfate.    USE - Production of composite fertilizer used for agricultural applications.    ADVANTAGE - The method enables simple, economical, safe, environmentally-friendly, stable and easy production of composite fertilizer directly using ammonium sulfate byproduct generated during desulfurization of flue gas, by recycling waste materials.
NOVELTY - Method for producing biogas from fruit and vegetable wastes, involves (a) grinding fruit and vegetables to obtain paste, (b) performing solid-liquid separation to obtain juice and solid residue, (c) adding the juice to methane producing reactor, adding acid-producing bacteria, performing methane reaction, adding obtained product to fiber-ball fixed bed reactor, and carrying out reaction to produce biogas, (d) adding solid residue to acid hydrolysis reactor, and performing hydrolysis, and (e) adding acid-producing bacteria to the reactor, and performing fermentation.    USE - The method is useful for producing biogas from fruit and vegetable wastes (claimed).    DETAILED DESCRIPTION - Method for producing biogas from fruit and vegetable wastes, involves (a) grinding fruit and vegetables using ball mill for degrading cellulose structure, releasing intracellular water and intracellular material from obtained product to obtain paste, and adding the paste to storage tank, (b) subjecting the paste to solid-liquid separation to obtain juice and solid residue, (c) directly adding the juice to methane producing reactor, adding acid-producing bacteria to the reactor, performing methane reaction in presence of hydrogen and carbon dioxide, adding obtained product to fiber-ball fixed bed reactor, adding acid-producing bacteria to the reactor, determining concentration of methanogens, and carrying out reaction to produce biogas, (d) adding solid residue to acid hydrolysis reactor, adding methanogens, preferably acid-producing bacteria to the reactor, and performing hydrolysis, and (e) adding acid-producing bacteria to the reactor, performing fermentation to produce methane and carbon dioxide, and regulating obtained product using upflow anaerobic sludge blanket (UASB) effluent.
NOVELTY - A high calorific value synthetic chemical liquid fuel comprises 10-25 pts. wt. sorbifolia oil, 1-2 pts. wt. ferrocene, 1-5 pts.wt. butylated hydroxytoluene, 60-80 pts. wt. methanol, 1-5 pts. wt. diesel oil, 1-5 pts. wt. ethanol, and 1-5 pts. wt. acetone.    USE - High calorific value synthetic chemical liquid fuel used for boiler in foundry and cement and ceramic industries.    ADVANTAGE - The high calorific value synthetic chemical liquid fuel has high calorific value, and is non-volatile and obtained at low cost by simple process. The transportation safety of liquid fuel is improved.
NOVELTY - The utility model is new type supply have one kind second time oxygen fermentation device, including of side wall and floor and upper cover form the box body, wherein the side wall set with over one feedstock and, on the floor set with oxygen-increasing device, on the upper cover set with air outlet and air exhaust pipe, wherein, the oxygen-increasing device comprises pipe column, wherein several ventilating set at the pipe mouth of the oxygen-increasing device through the external oxygen-increasing fan is the box body of wind. The utility model is new type of quadratic oxygen supply device not only can fast not fermented and decomposed to the raw material for fermentation again, but also can make only can be aerobic fungus fermentation and raw material for fermentation, using raw material full, in addition, not need natural cooling fermentation, that have peculiar smell problem, increase have fertilizer effect, because of fertilizer all, ferterlization after would no burning crop root.
NOVELTY - The utility model is new type category in compost fermentation facility construction technology field, relating to one kind used for strip stack type compost fermentation and aeration pipe. It comprises compost bed, pipe, a fan, a compost bed is lower part board frame is set with stacking type strip shape , pipe for sealing, inner end of gas-guide tube two rows of equidistant circular vent hole periphery is set with symmetrical distributing of fan is in pressing air blower, pipe left and right insert for compost bed in transverse set is compost bed lower part left right two side slat frame seat and is extended compost bed a portion of each side pipe every adjacent two of the gap at 3.0-4.5 m between, a fan set for the compost bed outside position and ventilating main pipe through the joint and the end outside each pipe connection. The utility model is new type comprises following characteristics: simple structure, equipped with suitable operation, can cause organic matter fast decomposing, compost effect obvious increase.
NOVELTY - An alfalfa cultivating method involves selecting excellent alfalfa varieties as breeding species, sowing seeds in mild and moderate saline grasslands after 10-15 days emergence under ground temperature in june, performing field management by subjecting rational fertilization, weeding and controlling pest, followed by harvesting seedlings in first year before winter for 10-20 days for allowing root to accumulate certain amount of carbohydrates and harvesting seedlings in second year during early flowering period in late august.    USE - Method for cultivating alfalfa.    ADVANTAGE - The method enables cultivating alfalfa with high yield, effect of promoting alfalfa industry and improving ecological environment with important practical significance, in simple manner.
NOVELTY - A low temperature anaerobic ammonium oxidation reactor operation method comprises taking untreated sewage containing ammonium and nitrite ions, carrying out initial hydraulic retention time to obtain sewage, reacting, determining nitrite ion concentration deviation, and adjusting reactor run via reducing reactor hydraulic retention and increasing influent concentration of ammonium and nitrite ions.    USE - Low temperature anaerobic ammonium oxidation reactor operation method (claimed).    ADVANTAGE - The method has increased nitrogen removal performance.    DETAILED DESCRIPTION - A low temperature anaerobic ammonium oxidation reactor operation method comprises taking untreated sewage containing 210-280 mg/L ammonium and nitrite ions, carrying out initial hydraulic retention time of 3.0-6.0 hours to obtain sewage at final concentration of 2.00-4.00 mL/L composite metal ion solution comprising 8.549 g/L nitrilotriacetic acid, 9.443 g/L iron(III) sulfate, 1.791 g/L nickel(II) chloride hexahydrate and 1.844 g/L copper sulfate monohydrate having water as solvent, reacting at 14-30 degrees C for 3 days, determining nitrite ion concentration deviation at 10% or 10 mg/L, and adjusting reactor run via reducing reactor hydraulic retention time comprising adjusting original hydraulic retention time of 5-20%, and increasing influent concentration of ammonium and nitrite ions comprising at increase rate of 14-70 mg/L, preferably 14-56 mg/L.
NOVELTY - 6-(3-N,N-dimethylsulfamoyl-2-fluoro-2-propen-1-yl)-4-fluoro-1-isopropyl-2-methyl-1H-benzimidazole (I) is new.    USE - Compound (I) useful as intermediate for bemaciclib or abemaciclib for treating breast cancer.    ADVANTAGE - The compound (I) has simple and easy preparation method, uses raw materials that can be easily obtained, and is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - 6-(3-N,N-dimethylsulfamoyl-2-fluoro-2-propen-1-yl)-4-fluoro-1-isopropyl-2-methyl-1H-benzimidazole of formula (I) is new.    INDEPENDENT CLAIMS are also included for:    (1) preparation of compound (I); and    (2) method for preparing abemaciclib or bemaciclib of formula (II) comprising reacting 5-(4-ethyl-piperazin-1-ylmethyl)-2-amino pyridine with cyanamide generating guanidyl compound to obtain N-(5-(4-ethyl-piperazin-1-ylmethyl) pyridin-2-yl) guanidine; and reacting N-(5-(4-ethylpiperazin-1-ylmethyl)pyridin-2-yl) guanidine with the compound (I) and third alkali accelerant to obtain the compound (II); or comprising third cyclization reaction of N-(5-(4-ethyl-piperazin-1-ylmethyl)pyridin-2-yl) guanidine nitrate and the compound (I) at a mol ratio of 1:05-1.5 to obtain the compound (II), where the third cyclization accelerator is sodium hydroxide, potassium hydroxide, potassium carbonate, cesium carbonate, sodium methoxide, sodium amide, sodium hydride or sodium ethoxide, the third cyclization reaction at 60-130 degrees C, and the third cyclization reaction solvents are toluene, acetonitrile, tetrahydrofuran, methanol, ethanol, n-butanol, isopropanol or tert-butanol.
NOVELTY - A 1-chlorobutane is prepared by mixing catalyst and chlorination reagent with water, stirring at 15-45 degrees C, mixing with n-butanol, and carrying out chlorination reaction to obtain 1-chlorobutane. The catalyst is dimethyl sulfoxide. The chlorination reagent is hydrogen chloride. A molar ratio of chlorination reagent to n-butanol is 2.5:1-5:1.    USE - Method for preparation of 1-chlorobutane (claimed).    ADVANTAGE - The method has few wastes making it environment-friendly, uses simple device, has low cost and convenient operation, has high yield and purity, and is suitable for industrial production.
NOVELTY - Treating biochemical, enzymatic and organic mineral manure, comprises disaggregating the complex compound present in the slurry using organic bioactive agent; digesting the broken fractions, anionic, cationic and carboxylic groups of bacteria by using enzymes; coagulating disaggregated and digested manure using organo mineral and bioactive polymer; separating the solids by flotation tank with air microbubbles; removing polishing process water through a biological filter and roots filter; and digesting the solids in drying beds.    USE - The process is useful for treating biochemical, enzymatic and organic mineral manure.    ADVANTAGE - The process allows biochemical treatment of manure and separation of water soluble and suspended solids to allow the classification of water for reuse.
NOVELTY - Use of sewage sludge is claimed to produce biogas and organic fertilizer which involves using closed large septic tank, gas wells and gas feedstock    USE - The method is useful for producing fertilizer (claimed).    ADVANTAGE - The method enables to produce product in an environmentally-friendly manner, with reduced energy consumption, and which improves fertility of soil.
NOVELTY - Producing and storing atomic hydrogen comprises electrolysis of water by using electrolytic cell of copper anode and cathode duralumin (alloy D16), and periodically activating by electric current. The hydrogen is activated by the magnetic field with an amplitude of the magnetic induction at 100-120 G and passing through the nano-dispersed carbon containing carbon nanotubes.    USE - The method is useful for producing and storing atomic hydrogen (claimed).
NOVELTY - Device for producing and storing atomic hydrogen, comprises reactor, which works on decomposition of solid reagent, anode, cathode and main unit with reinforcement for input of initial feedstock in reactor and outlet from it of hydrogen and reaction products. The solid reagent is selected from nano-dispersed carbons placed on anode surface in water between anode and cathode. On the main unit, the reactor is installed with electromagnet, control unit for magnetic induction, and storage battery of hydrogen with carbon nano-tubes.    USE - The device is useful for producing and storing atomic hydrogen.    DETAILED DESCRIPTION - Device for producing and storing atomic hydrogen, comprises reactor, which works on decomposition of water solid reagent, anode, cathode and main unit with reinforcement for input of initial feedstock in reactor and outlet from it of hydrogen and reaction products. The solid reagent is selected from nano-dispersed carbons placed on anode surface in water between anode and cathode. On the main unit, the reactor is installed with electromagnet, control unit for magnetic induction, and storage battery of hydrogen with carbon nano-tubes. The device also comprises regulator of applied reactor electrical power depending on the temperature of nano-dispersed carbon in space near anode and predetermined rate for obtaining hydrogen.
NOVELTY - The utility model claims a dust-removing tower of biomass material for production gas, wherein (2) the air inlet pipe on bottom is set with centre leading from tank (21), (2) provided with the water inlet pipe (27) and used for discharging the drain valve (28), spray pipe (25) setting on the water inlet connecting pipe (27) on the lower part of inside (2), upper spray pipe (25) provided with water spraying part used for spraying hole (26), (2) provided with the rotating guide plate (24), drain valve (28) setting on (2) the bottom end enclosure (20). Unique design, scientific and full contact in the water fog inside and tower in gas dust-removing tower, the dust and particle and gas entrance and water fog, discharging tower with the water, purification of combustible gas, energy saving, environmental protection, high efficiency and be popularized ideal energy-saving stove.
NOVELTY - The utility model claims a device using biomass material producing gas, wherein the biomass material for production of fuel gas device of gasification furnace (1), dust tank (2), drying tank (3), removing the coke tank (4), fan (5) and air storage tank (6) through pipeline composed of connected in series, and the gasification furnace (1) equipped with upper sleeve, gasification furnace (1) equipped with top for hopper (11) set with grate at lower combustion area (17), bridge (17) equipped with dust-removing cylinder (15) and baffle plate (16), the fan (5) is Roots draught fan, as combustion gas of the whole system power supply, making combustion gas from gasification furnace (1) through dust-removing tank (2), drying tank (3) and remove the coke tank (4) dust removing, water removing and remove tar, again taking fuel gas pressure into the air storage tank (6). The utility model is heat efficiency high, energy saving more than 30%, is an ideal furnace using the biomass fuel.
NOVELTY - This new utility model claims of one of supply heat for the biomass gasification device, aiming at providing a kind of one work stable and supply heat for the biomass gasification device. It comprises machine frame, gasification furnace, a material bin, a shaking grate, an ash cleanout door, wind chamber and the first air blower, and part of said gasification furnace with through hearth and gas collecting tube, the gas collecting tube on the outside wall of the inner hearth is set with part with several set air hole, one end the gas collecting pipe is closed, the other end is gas outlet pipe and connected with injection combustion device, the combustion device comprises injection and gas collecting pipe outlet connected the injection-type burner of air pipe, and an ejector air blower is connected with the other end of wind pipe, combustion chamber outside wall of the injection-type burner end and one end set with nozzel and nozzel into injection-type burner entrance has the second are is set with wind chamber, the wind chamber and between the second combustion chamber and injection-type burner is set with ventilating port, and the second wind chamber through pipe connected with the second air blower.
NOVELTY - A catalyst comprises component (A) containing alkali metal and/or alkaline earth metal, and component (B) containing zinc, copper, chromium, tin and/or iron, supported on an inorganic support. The catalyst is used for synthesizing alcohol by condensing primary and/or secondary alcohol and increasing carbon chain, by gas-phase reaction.    USE - Catalyst is used in manufacture of beta -position branch alcohol by condensation of alcohol (claimed) by hydration by Guerbet reaction, e.g. synthesis of butanol from ethanol for use in biofuel applications.    ADVANTAGE - The catalyst enables efficient manufacture of beta -position branch alcohol at low temperature, with sufficient reproducibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of beta -position branch alcohol.
NOVELTY - Formation of pellets involves crushing biomass to a smaller particle size to form crushed biomass, steaming the crushed biomass in a conditioner for more than 20 seconds to form steamed and crushed biomass and pelletizing the steamed and crushed biomass.    USE - Formation of pellets e.g. wood pellets used as fuel in electric power plants and homes.    ADVANTAGE - The method increases the production rate of the pellets.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the formation of pellets.
NOVELTY - The system has main portion for performing search process, so that electric power point is explored and appropriate maximum electric power point is obtained, when variation is more uniform than maximum electric power point. The resistance value is changed based on temperature characteristic of switching element consisting of semiconductor elements. A control circuit carries out regular response of nonlinear characteristics of energy generation system with respect to electric power characteristic of energy generation array.    USE - Maximum electric power point tracking system of solar energy generation system such as window turbine type energy generation system and fuel cell type energy generation system and arbitrary type energy generation system.    ADVANTAGE - The maximum power point tracking is calculated effectively in real time in solar panel based on conditions which continue to change for every moment, under the influence of shadow or foreign material, even when two heaps are made into power-voltage curve.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating the relationship between electric power and voltage. (Drawing includes non-English language text)    Electric power and voltage curve graph (300)    Maximum power point tracking point (301)    Electric power (P)    Voltage (V)
NOVELTY - Separation membrane comprises high molecular weight polyimides obtained from 4-fluoro-4',4''-diaminotriphenylmethane, and having substituted 2-(4-((4-fluoro-phenyl)-phenyl-methyl)-phenyl)-tetrahydro-cyclobuta(1,2-c;3,4-c')dipyrrole-1,3,4,6-tetraone compounds (r1) as a repeating unit.    USE - The membranes are useful in gas separation from a mixture of hydrogen and methane, helium and nitrogen, hydrogen and carbon dioxide, oxygen and nitrogen, carbon dioxide and methane, or carbon dioxide and nitrogen (all claimed).    ADVANTAGE - The membrane: present solubility in aprotic polar solvents, vitreous transition temperatures close to 300 degrees C and a decomposition temperature above 450 degrees C; and exhibits excellent permeation and gas separation properties.    DETAILED DESCRIPTION - Separation membrane comprises high molecular weight polyimides obtained from 4-fluoro-4',4''-diaminotriphenylmethane and having substituted 2-(4-((4-fluoro-phenyl)-phenyl-methyl)-phenyl)-tetrahydro-cyclobuta(1,2-c;3,4-c')dipyrrole-1,3,4,6-tetraone compounds of formula (r1) as a repeating unit.    Ar1 = aromatic organic group derived from tetracarboxylic acids, preferably 4,4'-sulfonylbis(1,2-dimethylbenzene), 3,3',4,4'-oxydiphthalic anhydride, 3,3',4,4'-benzophenontetracarboxylic dianhydride, 4,4'-(hexafluoroisopropylidene)diphthalic anhydride or 3,3',4,4'-biphenyltetracarboxylic anhydride.
NOVELTY - A fuel additive comprises 50-75 wt.% cyclic dienes and/or cyclic trienes that thermally crack into only chain branching radicals and 25-50 wt.% organo-nitrates and/or nitro-organics in which fuel additive is combined with fuel at a combined treat rate of 1000-3000 (wt.) ppm.    USE - A fuel additive for diesel fuel or biodiesel fuel (claimed). Uses include but not limited to railroad and marine applications.    ADVANTAGE - The fuel additive provides a way to significantly upgrade the performance of a medium or a heavy duty diesel engine without changing the safety characteristics of the fuel or without changing engine hardware.
NOVELTY - Method of increasing yield of isomerization zone involves separating portion of carbon (C6) cyclic hydrocarbons from naphtha stream comprising C4+ hydrocarbons to provide C6 cyclic hydrocarbons lean stream, separating iC4 hydrocarbons, iC5 hydrocarbons, and iC6 hydrocarbons from C6 cyclic hydrocarbons lean stream, and passing greater than or equal to 1 stream being rich in iC4 hydrocarbons, iC5 hydrocarbons, and/or iC6 hydrocarbons to isomerization zone.    USE - Method of increasing yield of isomerization zone.    ADVANTAGE - Suppression of iC4 hydrocarbons does not occur, allowing the iC4 hydrocarbons to be isomerized in the same isomerization zone as the iC5 hydrocarbons and iC6 hydrocarbons.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the method of increasing yield of isomerization zone.    Feed stream (10)    1st separation zone (12)    Overhead stream (16)    Bottoms stream (18)    2nd separation zone (20)
NOVELTY - The device (100) has a position sensor (60) for sensing position of two cathode catalyst electrode layers (3, 5). A dimorphism bar (70) is adhered with two release films (21, 31). Top and bottom junction rolls (40, 50) transfer and compress the roll shaped cathode catalyst electrode layers with upper side and lower-sides of a roll shaped polymer electrolyte membrane (1) that are arranged between top and bottom sides of a travel route. The roll shaped cathode catalyst electrode layers are coated with the release films with constant interval.    USE - Device for manufacturing a film of a fuel cell-electrode assembly.    ADVANTAGE - The device ensures that a controller effectively controls operation of an operating source unit, the top and bottom junction rolls and a film rewinder according to progressing location of the release films and sensing signal of the position sensor so as to automatically arrange the catalyst electrode layers and reduce mutual compression of the electrode layers, thus improving processing quality of a membrane-electrode assembly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a film of a fuel cell-electrode assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a device for manufacturing a film of a fuel cell-electrode assembly.    Polymer electrolyte membrane (1)    Cathode catalyst electrode layers (3, 5)    Release films (21, 31)    Top junction roll (40)    Bottom junction roll (50)    Position sensor (60)    Dimorphism bar (70)    Manufacturing device (100)
NOVELTY - Hydrocarbon modified catalyst paste composition comprises a catalyst, a carrier, an organic binder, and metal powders having a melting point lower than the melting point of the carrier and the catalyst.    USE - The composition is useful to produce reformer for fuel cell system (all claimed).    ADVANTAGE - The composition has stability and catalytic activity for a long time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) reformer comprising a support, and a catalyst coating layer made of sintered product of the composition, and provided on the support; and    (2) fuel cell system comprising the reformer, and a fuel cell laminate for generating electricity using hydrogen as fuel which is generated from the reformer.
NOVELTY - The apparatus has an anaerobic-treatment apparatus (10) which carries out the anaerobic treatment of the organic waste. A reverse osmosis membrane apparatus (20) carries out the membrane separation of the treated water which arises with anaerobic-treatment apparatus by a reverse osmosis membrane (21). An evaporative concentration apparatus (31) carries out the evaporative concentration of the concentrated water of the reverse osmosis membrane apparatus with the sludge which arises with the anaerobic-treatment apparatus.    USE - Organic-waste processing apparatus.    ADVANTAGE - Since the evaporative concentration apparatus carries out the evaporative concentration of the concentrated water of the reverse osmosis membrane apparatus with the sludge which arises with the anaerobic-treatment apparatus, the sludge is used effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic-waste processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the structure of the organic-waste processing apparatus.    Anaerobic-treatment apparatus (10)    Anaerobic tank (11)    Reverse osmosis membrane apparatus (20)    Reverse osmosis membrane (21)    Evaporative concentration apparatus (31)
NOVELTY - The utility model claims a new one of a kind of high-efficient marsh gas purifying system, comprising desulfurizing device, removing device, dehydrating device, compressor, an air storage tank, and pipeline and valve. Desulphurization device using alkaline solution spray method of removing H2S in the gas, by gas uniform distributor and liquid distributor evenly respectively diffusion layer marsh gas and alkaline solution, and by two level reacting plate, using H2S gas and marsh gas and full reaction and alkaline solution, this utility new type has simple structure, reasonable design, effective increase desulfurization efficiency and desulfurization solution and use ratio, at the same time, the system can effective using CO2 gas and alkaline solution phase full contact, when at the same time using sensor and valve realize new supply of alkaline solution, the concentration of alkaline solution, and lasting the compare and high decarburization efficiency.
NOVELTY - Natural product composition comprises citral and methylheptenone.    USE - Natural product composition is useful for preventing and treating rice blast, and inhibiting mycelial growth and spore germination.    ADVANTAGE - The natural product composition has excellent synergistic effect, treats rice blast with good curative effect of 70%, can effectively reduce amount of pesticides, and can be prepared with reduced labor intensity in a simple and economical manner.
NOVELTY - An recombinant yeast which is genetically engineered to exhibit reduced amounts of functional iron-sulfur cluster assembly protein (Isu1) polypeptide or functional Isu1 and Hog1 polypeptides, and at least one of functional Gre3, inhibitory regulator protein (Ira1), and Ira2 polypeptides, is new.    USE - The recombinant yeast is useful for fermenting cellulosic material into ethanol (claimed), and producing biofuels and chemical feedstock.    ADVANTAGE - The recombinant yeast enables to produce product with high yield.    DETAILED DESCRIPTION - An recombinant yeast which is genetically engineered to exhibit reduced amounts of functional iron-sulfur cluster assembly protein (Isu1) polypeptide or functional Isu1 and Hog1 polypeptides, and at least one of functional Gre3, inhibitory regulator protein (Ira1), and Ira2 polypeptides, is new. The genetically engineered recombinant yeast is (a) capable of increased aerobic xylose fermentation relative to wild-type yeast or another recombinant yeast not exhibiting reduced amounts of functional Isu1 polypeptide, or (b) increased anaerobic xylose fermentation relative to a wild-type yeast or another recombinant yeast not exhibiting reduced amounts of functional Isu1 and Hog1 polypeptides, and at least one of functional Gre3, Ira1, and Ira2 polypeptides. INDEPENDENT CLAIMS are included for the following:    (1) yeast inoculum, comprising (a) recombinant yeast and (b) a culture medium; and    (2) method for fermenting cellulosic material into ethanol, involves contacting under ethanol-producing conditions the recombinant yeast to cellulosic material for a period of time to allow fermentation of at least a portion of the cellulosic material into ethanol.
NOVELTY - A composition comprises at least one 3,4-dihydro-2H-1,3-benzoxazine derivative (I) and 1,3-oxazinane derivative (II).    USE - Composition is used for electrode and electrolyte membrane of fuel cell (all claimed).    ADVANTAGE - The electrolyte membrane using the composition has excellent mechanical property, chemical stability, thermal stability and capability to retain phosphoric acid at high temperature. The electrode using the composition has reduced activation time and excellent cell voltage characteristics.    DETAILED DESCRIPTION - A composition comprises at least one 3,4-dihydro-2H-1,3-benzoxazine derivative of formula (I) and 1,3-oxazinane derivative of formula (II).    R1-R4=H, halo, hydroxy, cyano, or 1-20C alkyl, 1-20C alkoxy, 2-20C alkenyl, 2-20C alkynyl, 6-20C aryl, 6-20C aryloxy, 2-20C heteroaryl, 2-20C heteroaryloxy, 4-20C carbocyclyl, 4-20C carbocyclyloxy, 2-20C heterocyclyl or 2-20C heterocyclyloxy (all optionally substituted);    R6=-C(=O)-, -SO2- or 1-20C alkylene, 2-20C alkenylene, 2-20C alkynylene, 6-20C arylene, 2-20C heteroarylene (all optionally substituted);    R5,R'5=-(CF2)n-CF3 or group of formula (III);    n=1-20;    b=1-5;and    R7=H, F, 1-20C alkyl, 1-20C fluoroalkyl, 6-20C aryl or 6-20C fluoroaryl.    An INDEPENDENT CLAIM is included for fuel cell, which comprises a cathode, an anode, and electrolyte membrane arranged between the cathode and the anode. At least one of the cathode, anode and electrolyte membrane comprises the composition.
NOVELTY - A Klebsiella IR21 strain (KCTC 12571BP) or Candida IR11 strain (KCTC 12570BP), is new.    USE - The Klebsiella IR21 strain or Candida IR11 strain is useful in composition for processing or purifying wastewater, and microbial fuel cell for producing electricity (all claimed).    ADVANTAGE - The method does not require external power source.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition for wastewater treatment or wastewater purification;    (2) microbial fuel cell;    (3) method for producing electricity;    (4) wastewater treatment apparatus;    (5) method for producing electricity; and    (6) method for performing wastewater purification and electricity production at the same time.
NOVELTY - Method for producing methane, involves taking first microorganism capable of producing hydrogen by fermentation in presence of substrate and/or culture medium comprising or supplemented with hydrocarbons, second microorganism capable of producing methane from hydrogen by fermentation in presence of substrate and/or culture medium comprising or supplemented with hydrocarbons and co-culturing the first and second microorganism in substrate comprising culture medium containing organic and inorganic components and supplemented with hydrocarbons and antioxidants.    USE - The method is useful for producing methane (claimed).    DETAILED DESCRIPTION - Method for producing methane by co-culturing in a reactor in an aerobic environment, preferably air, involves taking first microorganism, preferably anaerobic bacteria capable of producing hydrogen by fermentation in presence of substrate and/or culture medium comprising or supplemented with hydrocarbons, second microorganism, preferably methanogenic Archaea capable of producing methane from hydrogen by fermentation in presence of substrate and/or culture medium comprising or supplemented with hydrocarbons, and co-culturing the first and second microorganism in substrate comprising culture medium containing organic and inorganic components, and supplemented with hydrocarbons and antioxidants to obtain product.
NOVELTY - Producing methane gas comprises co-culturing in a reactor in an aerobic atmosphere, preferably air, at least: first microorganism comprising anaerobic bacterium capable of producing hydrogen by fermentation in presence of substrate and/or culture medium; second microorganism consisting of a methanogenic Archaea adapted to produce methane from hydrogen and a substrate and/or culture medium; and an organic and inorganic substrate comprising culture media components capable of allowing the culture of both the first and second microorganisms.    USE - The method is useful for producing methane gas (claimed), which is used as biogas.    ADVANTAGE - The method provides methane at high yields by utilizing the co-culture of combination of anaerobic bacteria and methanogenic Archaea in the culture medium supplemented with carbon source and antioxidant under aerobic conditions.    DETAILED DESCRIPTION - Producing methane gas comprises co-culturing in a reactor in an aerobic atmosphere, preferably air, at least: a first microorganism comprising an anaerobic bacterium capable of producing hydrogen by fermentation in the presence of a substrate and/or culture medium comprising or supplemented with hydrocarbon compounds; a second microorganism consisting of a methanogenic Archaea adapted to produce methane from hydrogen and a substrate and/or culture medium comprising or supplemented with hydrocarbon compound; and an organic and inorganic substrate comprising culture media components capable of allowing the culture of both the first and second microorganisms, where the culture medium comprises or is supplemented with hydrocarbon compound, and further supplemented with antioxidants.
NOVELTY - The preparation method of 2,4-bis-ethoxycarbonyl-3-thiophen-2-yl-pentanedioic acid diethyl ester (I) involves reacting thiophene-2-carbaldehyde (II) and diethyl malonate (III) in the presence of base catalyst and acid catalyst.    USE - The method is useful for preparing compound (I), which is useful as eprosartan intermediate impurity EP9A.    ADVANTAGE - The method enables simple and rapid preparation of compound (I) with less by-product and high yield and purity under mild reaction conditions.    DETAILED DESCRIPTION - The preparation method of 2,4-bis-ethoxycarbonyl-3-thiophen-2-yl-pentanedioic acid diethyl ester of formula (I) involves reacting thiophene-2-carbaldehyde of formula (II) and diethyl malonate of formula (III) in the presence of base catalyst and acid catalyst.
NOVELTY - Production of taurine from alkali ditaurinate and/or alkali tritaurinate involves adding excess amount of ammonia to solution of alkali ditaurinate and alkali tritaurinate and subjecting the solution to ammonolysis reaction to yield a mixture of alkali taurinates in the presence of catalysts, removing excess ammonia and neutralizing alkali taurinates with an acid to form a crystalline suspension of taurine, recovering taurine by solid-liquid separation.    USE - Production of taurine from alkali ditaurinate and/or alkali tritaurinate used as ingredient for animal and human nutrition.    ADVANTAGE - The method is performed discontinuously, continuously and semi continuously. The method generates no waste because the products are recycled, and provides high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart explaining the cyclic production of taurine from sodium isethionate and sodium vinyl sulfate.
NOVELTY - Manufacture of aromatic urea compound involves reacting tetrachloro ketone compound (I) and aromatic compound comprising one amino group in presence of a catalyst chosen from basic salt and organic base, and obtaining aromatic urea compound having urea bond.    USE - Manufacture of aromatic urea compound used as functional compound e.g. agrochemical intermediate, pharmaceutical intermediate and pigment.    ADVANTAGE - The method enables efficient manufacture of symmetrical or asymmetrical aromatic urea compound with high yield at relatively low temperature, without using toxic compounds as raw material, and by-producing corrosive and toxic gas.    DETAILED DESCRIPTION - Manufacture of aromatic urea compound involves reacting tetrachloro ketone compound of formula (I) and aromatic compound comprising one amino group in presence of a catalyst chosen from basic salt and organic base, and obtaining aromatic urea compound having urea bond.    X1,X2=H or chloro.
NOVELTY - The utility model is a small portable domestic sewage processing device, a cut-off in turn sediment and ferment pool, fermentation pool and manure, the cut-off sediment and ferment pool connected with a waste pipe of at the side wall, the top wall is opened with a slag, and a first cover plate for sealing, the manure and a side wall connected with a water pipe, a top wall is opened with a waste port, and a second cover plate for sealing, the cut-off sediment and fermentation pool and fermentation pool again, and again a fermented manure between and respectively connected with a connected pipe, is set on the cut-off sediment and fermentation and then fermented.... connected between a import end of height as a precipitate and a depth of one third of fermentation, re-ferment between pool and a manure and connect a import end of height for the fermentation to a depth of one half. By the reasonable structure and is set with, implementation of a treatment to the dejecta, and can process a to make the excrement is used as a....
NOVELTY - Preparing microbial agents, comprises (i) activating Staphylococcus aureus, Bacillus megaterium and Aspergillus niger, and adding into slant culture; and (ii) mixing activated microorganism, adding into a flask, placing in a shaker, culturing under conditions of 28 degrees C for 2 days, controlling pH to 6-6.5, so that the number of bacterial content reaches 500-600000000 cells/ml, to obtain the final product.    USE - The microbial agents are useful in preparation of fertilizer (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing fertilizer by fermentation, comprising carrying out steps mentioned in step (i) and (ii), and extracting navel orange juice and residue, mixing with soybean slag.
NOVELTY - Processing toxic substances (TS) including persistent organic pollutants (POPs), involves continuously supplying TS into thermochemical reactor, heating TS, subsequent cooling of converted products and output from the reactor of the products of thermochemical transformations, where in the thermochemical reactor are created the supercritical conditions according to pressure and temperature of at least one of the components involves in the process of thermochemical transformation.    USE - The method and device are useful for processing toxic substances (TS) including persistent organic pollutants (POPs) (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for processing TS in accordance with the method above, comprising a device for continuously supplying TS and the dehalogenating agents into the thermochemical reactor; a thermochemical reactor; a device for separating the products of thermochemical transformations; a device for operating temperature and pressure in the thermochemical reactor, where the device for delivery of TS contains a pump of high pressure and heater for transmitting in more fluid condition TS with the dehalogenating agent prior to their supply into the thermochemical reactor; inlet and outlet of thermochemical reactor installed recuperative to the heat exchanger ensuring preheating TS cooling converted products due to heat exchange between their flow; after the thermochemical reactor and the recuperative heat exchanger limited to the flow of TS processed products installed at additional heat exchanger for cooling the converted products, a pressure in the thermochemical reactor and a separator of converted products, which divides products into the solid, liquid and gaseous fraction.
NOVELTY - The device has water tank (2) whose upper portion is installed with water level valve (27) and water supply pipe (29). The lower portion of methane purification tower (16) is connected with oxygen purification tower. The oxygen compressor (44), tube (23) and oxygen storage tank (25) are connected with each other. The methane purification tower is connected with methane storage tank (19). The valves (15,18,21,24) are installed at lower portions of methane purification tower, methane storage tank, oxygen purification tower and oxygen storage tank, respectively.    USE - Wind-light-electricity-water carbon dioxide methane preparing device used in chemical industry.    ADVANTAGE - The pollution to the air by the use of the wind-light-electricity-water carbon dioxide methane preparing device is reduced.    DETAILED DESCRIPTION - The device has a negative plate (12) which is manufactured from copper and copper alloy. The methane and carbon dioxide liquid portion is provided in potassium carbon liquid solution. An electrolyte (35) is manufactured using carbon hydrogen electric liquid solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the wind-light-electricity-water carbon dioxide methane preparing device.    Water tank (2)    Negative plate (12)    Valves (15,18,21,24)    Methane purification tower (16)    Methane storage tank (19)    Tube (23)    Oxygen storage tank (25)    Water level valve (27)    Water supply pipe (29)    Electrolyte (35)    Oxygen compressor (44)
NOVELTY - Extracting puerarin from kudzu slag comprises (i) drying kudzu slag to obtain kudzu powder and ultrafine grinding to obtain product with particle diameter of 20 mu m; (ii) crushing kudzu slag and then mixing with ethanol, adding beta -cyclodextrin, carrying out ultrasonic extraction, heating and refluxing, and then suction extracting to obtain puerarin; (iii) rotary evaporating the filtrate to obtain thick paste and recovering ethanol, and the drying the resultant extract under vacuum; and (iv) extracting supercritical carbon dioxide to obtain final product.    USE - The method is useful for extracting puerarin from kudzu slag (claimed).    ADVANTAGE - The puerarin is suitable for medicine and food industry, does not has toxicity.
NOVELTY - This new utility model claims an automatic spiral quantitative feeding device used in marsh gas engineering, the device is set with marsh gas engineering in feedstock pool and pre-process system mixing slurry pool between, on mixing slurry pool provided with liquid inlet pipe, also comprising spiral transport machine and controller, spiral transporting machine respectively connected to the feedstock pool and slurry mixing pool, spiral transport machine of measuring device provided with the upper liquid inlet pipe set with flow meter and the electric control valve, drive device of the spiral transporting machine and the measuring device and flow meter and the electric control valve are connected to controller circuit; the utility model use new spiral transport mechanism reach uniform feedstock of target, and the lower part of spiral transport level four is set with gravity sensor under the whole in feedstock pool, according to the gravity sensor to measure the data automatic precise proportion proper amount of dilution water (or liquid), marsh gas engineering realize feeding automation, intelligence, reducing of artificial operation, increase of operation precision and working efficiency.
NOVELTY - The utility model belongs to a feedstock device technology area, especially relates to a feeding device used for straw anaerobic fermentation gas generation, provided with a reactor main body upper part, a feedstock comprising feeding buffer device, a feeding buffer middle part set with stirrer, a stirrer is set with with a feeding port, a feeding port is set with position with a butterfly valve, the other side is set with stirrer with air inlet pipe and air outlet pipe, a feeding buffer top part set with sealing cover, inlet bottom equipped with buffer with vertical spiral propeller stirrer and under a vertical spiral propeller is set with feed opening, with vertical spiral propeller discharge end provided with a reactor main body in upper part of the vertical spiral propeller discharging end is set with the lower part has discharge port, vertical spiral propeller internal set with spiral pushing rod, vertical spiral propeller outside end set with motor, is easy to block when the utility model solves a feedstock is a problem, a straw Anaerobic fermentation producing gas and feedstock device feedstock continuous, stable, increase of production efficiency.
NOVELTY - The utility model claims a high-efficient straw marsh gas fermentation device, comprising a crusher, a fermentation, a discharge and a waste lifter, a crusher and water discharge in a pool in the fermentation pool is set with a side, the crusher upper part mounted with a vibration sieve, set with a guide part on a vibration sieve, set with grinding gear. In a material between, with fine grinding gear is set with lower part in a group material, the device is set with a crusher for a straw into a straw powder, a fermentation process is easy to carry out, increase fermentation efficiency, increase gas yield, is set with a hydraulic pressure discharge pool for fermentation liquid extracting redundant and a fermentation pool, avoiding fermentation in a liquid through a straw ferment multiple effect, is set with a waste lifter in a fermentation pool, a complete fermentation of waste discharging, the difference convention marsh gas ferment device need a manual cleaning, using suitable, wherein suitable for vast rural areas, grain for producing area.
NOVELTY - This utility model relates to a marsh gas fermentation tank precise temperature control device, comprising heat preservation tank body (1), a heating coil (2), stirrer (3), a temperature sensor (4), a hot water circulation pump (5), electric control valve (6) and control system (7), the heating coil, stirrer and temperature sensor set up on tank body internal heat, the hot water circulation pump and electric control valve and heating plate pipe connected with, the control system separately and connected with stirrer, temperature sensor, hot water circulation pump and electric control valve power, heat preservation tank body lower heating coil and middle part is set with two annular layer, double layer heating plate pipe is set with upper parallel in height. This new utility model is set with double layer heating plate and multi-tube of temperature sensor, precise temperature control of ferment tank body can realize time.
NOVELTY - A fertilizer comprises 0.1-20 pts. wt. casein phosphopeptide, 1-10 pts. wt. trace element, 1-10 pts. wt. pH regulating agent and 60-97.9 pts. wt. deionized water.    USE - Fertilizer.    ADVANTAGE - The fertilizer is water-soluble, and contains natural and unpolluted biological active polypeptide, and has large economic benefit and social benefit, and increases comprehensive efficiency of resources greatly, reduces notable usage of fertilizer, improves absorption efficiency of trace elements, organic nitrogen, organic carbon and organic phosphorus by plants and satisfies energy-saving agriculture requirements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing the fertilizer, which involves mixing casein phosphopeptide, trace element and deionized water to obtain aqueous solution, heating the mixture at 65-85 degrees C, adding pH regulating agent to the mixture, regulating pH at 6.5-8.5, reacting the mixture for 80-120 minutes, reducing reaction temperature to room temperature, and filtering the mixture to obtain finished product.
NOVELTY - Organic fertilizer is produced by mixing 12 pts. wt. effective microorganism, 20 pts. wt. silkworm dropping, 15 pts. wt. humic acid, 50 pts. wt. passion fruit leaves, 24 pts. wt. lees, and 25 pts. wt. water, fermenting the mixture at 50 degrees C for 50-80 days, drying the fermented product at 70 degrees C, and pulverizing the dried product using pelletizer.    USE - As organic fertilizer for crops (claimed).    ADVANTAGE - The organic fertilizer is environmentally-friendly.
NOVELTY - Preparing alkaline protein bio-organic fertilizer comprises uniformly mixing seaweed slag, bean pulp, grape peel, lees, mushroom residue and tobacco leaves to prepare mixture, controlling pH value, stacking, fully contacting and mixing alkaline filter residue and other material, adding composite microorganism microbial inoculum, fermenting, completely deodorizing the material, fermenting, subjecting to insecticidal sterilization process, reducing temperature to room temperature, and then adding high-efficient nitrogen-fixing soluble-potassium and soluble-phosphate strain.    USE - The method is useful for preparing alkaline protein bio-organic fertilizer (claimed).    ADVANTAGE - The bio-organic fertilizer: breaks macromolecular organic matter into small organic molecules; is suitable for absorption of latter parts of the crop; greatly improves the nutritional value of the raw materials; and has improved fertilizer quality.    DETAILED DESCRIPTION - Preparing alkaline protein bio-organic fertilizer comprises uniformly mixing seaweed slag (alkaline, pH value of 8-11), bean pulp, grape peel, lees, mushroom residue and tobacco leaves to prepare mixture, controlling pH value to 7.5-9, stacking for 2-3 days, fully contacting and mixing alkaline filter residue and other material, adding composite microorganism microbial inoculum, which is 2 g/kg mixture, fermenting at temperature of 50-60 degrees C for 5-7 days, completely deodorizing the material, fermenting, subjecting to insecticidal sterilization process, reducing temperature to room temperature, and then adding high-efficient nitrogen-fixing soluble-potassium and soluble-phosphate strain, which is 5 g/kg mixture.
NOVELTY - The steam heating aerobic fermentation tank has a solid shaft that is vertically fixed on a hollow stirring rod. The hollow stirring rod is connected with hollow rotating shaft. A coaxial core stirring rod is fixed on outside wall of hollow rotating shaft. The hollow stirring rod is connected to lower end of internal portion of rotating shaft. An upper portion of rotating shaft is connected with an oxygen input port through a fast rotation joint. The hollow stirring rod is set with oxygen exhaust port which is connected with one sterilizing filter.    USE - Steam heating aerobic fermentation tank based on organic garbage composting system.    ADVANTAGE - The steam heating aerobic fermentation tank has simple structure and scientific and reasonable design. Strong temperature control ability is attained. The organic waste resource utilization is increased effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the steam heating aerobic fermentation tank based on organic garbage composting system. (Drawing includes non-English language text)
NOVELTY - The system has a high temperature aerobic fermentation tank that comprises tank portion and base. The tank portion is mounted with a temperature sensor and is installed with a stirring rod. The stirring rod comprises a rotate shaft and stirring rod portion. The hollow stirring rod is internally connected between lower ends of hollow shaft. An upper hollow rotate shaft portion is connected with oxygen input pipe through fast rotation joint. An upper portion of a hollow stirring rod is set with radio oxygen port, and exhaust port that is connected with a sterilizing filter.    USE - Organic substance trash fertile system for controlling fungus temperature in radio removable oxygen stirring aerobic fermentation tank.    ADVANTAGE - The simple structure, scientific and reasonable design of system is achieved. The aerobic fermentation tank is fullly supported with aerobic bacteria to make full contact with oxygen organic waste. The stirring process is performed uniform to supply full use of organic matter garbage. The resource utilization rate of organic substance is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the organic substance trash fertile system for controlling fungus temperature in radio removable oxygen stirring aerobic fermentation tank. (Drawing includes non-English language text)
NOVELTY - The device has a fish-catcher arranged with a fish ring and an adjustable outlet. The fish ring is connected with the adjustable outlet by a sleeve. A rear side of a stop band is arranged with a handle. A medicine feeding bottle (2) is provided with a bottle body (2-1). A side of the bottle body is matched with a bottle cover (2-2). The bottle body is made of elastic material. The bottle cover is inserted with a soft conduit (2-3). The bottle body is marked with a scale body (2-4). The soft conduit is marked with a scale (2-5).    USE - Device for feeding medicine to an ornamental fish.    ADVANTAGE - The device is reasonable in structure, simple and convenient to use and convenient to capture a fish. The device has better practicability, and can improve ornamental fish treating efficiency and drug effect, reduce fish feeding material wastage and pollution and improve environmental protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an ornamental fish feeding method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a medicine feeding device.    Medicine feeding bottle (2)    Bottle body (2-1)    Bottle cover (2-2)    Soft conduit (2-3)    Scale body (2-4)    Scale (2-5)
NOVELTY - Peeling mousse composition comprises 30-60 wt.% liquid agent and 40-70 wt.% propellant where liquid agent contains 1-10 wt.% glycerol, 3-10 wt.% sodium laureth sulfate, 3-5 wt.% cocamidopropyl betaine, 1-3 wt.% carbomer, 1-3 wt.% behenyl trimethyl ammonium chloride and balance water.    USE - Peeling mousse composition used for removing dead skin cells and promoting skin metabolism.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of peeling mousse composition comprising weighing raw materials, mixing glycerol, sodium laureth sulfate and cocamidopropyl betaine, heating at 75-95 degrees C, dissolving in water, adding carbomer and behenyl trimethyl ammonium chloride, stirring, filling in opaque container and filling with propellant.
NOVELTY - Manure fermentation tank sewage solid-liquid separation systems, including breeding shed, the breeding shed with a side of the outfall, sewage outlet digging a 1 cubic sedimentation tanks, sewage sedimentation tank with 1 cubic Unicom, a cube with a sedimentation tank sewage pipes, sewage pipes and manure separator Unicom, the upper side of manure separator has a water filtration tank, the bottom has a fecal residue outlet, the other end of the water filtration tank and fermentation tank Unicom, the net water filtration tank provided with a filter material, the bottom of the fermentation tank with a water pipe, a water pipe and breeding shed Unicom, the water pipe with a valve. Beneficial effects: no longer farming sewage efflux, the sewage is filtered back to the fermentation tank re-use, no longer pollute the water environment and achieve environmental farming zero emissions, the technology can greatly improve the efficiency of farmers.
NOVELTY - This new utility model claims of multi-cell fermentation biogas liquid turbulent flow stirring novel energy fermentation system, comprising the feedstock tube, discharging tube, fermentation pipe, hydraulic pressure room, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve has, in fermentation system also comprises cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure connection, bacteria distributing pipe is circular pipe fixed on annular ferment bacteria distributing pipe in side wall, Brucella and pipe shape is annular pipeline phase, ferment bacteria distributing pipe set with multi-number of vertical direction of the cloth fungus through hole.
NOVELTY - This new utility model claims of disordered turbulent flow type novel energy generating device, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline ferment is ferment annular pipe, set annular fermentation pipe on top, annular pipe of fermentation set with opening, the opening center position is set up with extending to two side insert clapboard to separator, feedstock pipe and discharging pipe and annular pipe bottom respectively vertical and fermentation of the feedstock pipe and side wall of discharging pipe extending to biogas liquid face of annular fermentation pipe below seat; between water pressure and feedstock pipe connected with feedstock pipe drain pipe, water discharging pipe and connected with discharging pipe between pipe, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve with the upper discharge pipe arrange water pipe set with controlling liquid discharging tube one-way flow into from the one-way valve in water pressure, feedstock pipe arrange water pipe set up with liquid from the hydraulic control one-way flow into feedstock tube and one-way valve; This new utility model adopt annular fermentation system, fermentation line longer, which ensures full fermentation, by multi-plate for the whole fermentation system divided into multiple of cell fermentation, using pressure difference, promoting biogas fungus, flow of fermentation raw material, increase fermentation efficiency.
NOVELTY - This new utility model claims of multi-area pressure disturbance model to promote uniform strain distribution of marsh gas generating device, inlet and outlet of material cylinder, annular fermentation pipeline, composed of marsh gas ferment system main body, an oil inlet and outlet cylinder vertical connected with annular fermentation material pipe, material cylinder comprises between feedstock tube and discharging tube, feedstock tube and discharging tube of one vertical extending to ferment pipe bottom of clapboard separate, mounted in annular fermentation pipe top, and feedstock pipe connected with feedstock pipe between pipe, discharging pipe and connected with discharging pipe between pipe, annular pipe and fermentation feedstock pipe connection seat to set up with feedstock tube plate, annular pipe and discharging pipe connected with ferment site to set up with discharge tube plate, tube blocking plate and feedstock material-blocking pipe board between set up with at least one of plate, and between adjacent blocking plate forming one of ferment cell.
NOVELTY - The utility model claims a pressure disturbance of a mixed flow marsh gas generating device, a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe and fermentation feedstock a position... feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and a discharging blocking plate formed with at least one between a plate, between the adjacent blocking plate forming one of ferment cell of marsh gas ferment system also comprises annular cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and a water in a, bacteria distributing pipe is annular; Pipeline fixed on annular ferment bacteria distributing pipe in a wall, Brucella and pipe shape is annular pipe. fermentation, bacteria distributing pipe is set with a with a vertical upper direction of the cloth through a fungus, ferment efficiency of a fermentation of a different, cause different production rate, a gas pressure of different fermentation are a, promoting a biogas slurry flow stirring in the fermentation system to promote a uniform distribution of strain fermentation system, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. fermentation, the fermentation zone forming in the enough air pressure a and promote flow of liquid.
NOVELTY - The utility model claims a marsh gas fermentation system for promoting uniform strain distribution by using multi-area biogas slurry convection, comprising a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe and fermentation feedstock a position... feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and a discharging blocking plate formed with at least one between a plate, between the adjacent blocking plate forming one of ferment cell, ferment cell top part set with mutually independent and gas-guide tube, the gas-guide pipe is set with a valve with the fermentation efficiency of the whole multi-fermentation are different. Several different cause, a gas pressure and a different fermentation area, promote the biogas slurry in the stirring flow in fermentation system to promote a uniform distribution of strain fermentation system, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. ferment, the ferment cell in forming enough air pressure a and to promote flow of liquid.
NOVELTY - The utility model claims a channel-type environment-friendly energy-saving biogas pool, comprising a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate,... in a top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe and fermentation feedstock a position... feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and a discharging blocking plate formed with at least one between a plate, between the adjacent blocking plate forming one of ferment cell, ferment cell top part set with mutually independent and gas-guide tube, the gas-guide tube is set with with a valve, a discharge pipe of water pipe is set with arrange in a discharge tube with liquid one-way flow into the one-way valve in water pressure; Efficiency of a fermentation of fermentation are different, cause different production rate, a gas pressure of different fermentation are a, promoting a biogas slurry flow stirring in the fermentation system to promote a uniform distribution of strain fermentation system, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. ferment, the ferment cell in forming enough air pressure a and to promote flow of liquid.
NOVELTY - The utility model claims a pressure disturbance novel energy generating device, comprising a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe fermentation feedstock and a location to set up between a feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and material-blocking plate is set with a plate has, between the adjacent blocking plate forming fermentation area, formed at a top part of a fermentation and gas-guide tube., can be each of the cell a. ferment, the ferment cell in forming enough air pressure a and to promote flow of liquid.
NOVELTY - The utility model claims a super-high efficient convection mixing stirring marsh gas fermentation system, comprising a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and discharging pipe by separate a separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe fermentation feedstock and a location to set up between a feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and material-blocking plate is set with a plate has, between the adjacent blocking plate forming fermentation area, formed at a top part of a fermentation and gas-guide tube., can be each of the cell a. ferment, the ferment cell in forming enough air pressure a and to promote flow of liquid.
NOVELTY - This new utility model claims of multiple annular area beyond efficient marsh gas ferment system improves biogas liquid turbulent flow effect and device, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline ferment is ferment annular pipe, set annular fermentation pipe on top, annular pipe of fermentation set with opening, the opening center position is set up with extending to two side insert clapboard to separator, feedstock pipe and discharging pipe and annular pipe bottom respectively vertical and fermentation of the feedstock pipe and side wall of discharging pipe extending to biogas liquid face of annular fermentation pipe below seat; between water pressure and feedstock pipe connected with feedstock pipe drain pipe, water discharging pipe and connected with discharging pipe between pipe, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve with the fermentation system also comprises cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure in connection. Brucella pipe is circular pipe fixed on annular ferment bacteria distributing pipe in side wall, Brucella and pipe shape is annular pipeline phase, ferment bacteria distributing pipe set with multiple of one vertical direction of the cloth fungus through hole.
NOVELTY - The utility model claims a new a kind of stirring device, specifically an organic matter fermentation stirring device, comprising a stirring tank mounted microwave heater, stirring tank. terminal a. front relux zone and a relux zone, relux zone and before a relux between a cell as main stirring area and assistant area, the main stirring shaft and assistant stirring shaft parallel installed, main stirring shaft and stirring shaft of assistant with the same to the spiral blade, main shaft front end of stirring blade and stirring shaft rear end assistant blade and other blade spiral direction opposite the main stirring shaft connected with driving gear, assistant stirring shaft connected with driven gear, driving gear and driven gear... a mesh of a gear. The organic material in the main stirring shaft pushing forward area relux at main stirring area, again the front relux cell enter into to sub-area, the push again to later relux area of the secondary stirring shaft, wherein after relux in cell, organic material to enter into main area, the organic material circulation in stirring in stirring tank, carrying out the full stirring, increasing the fermentation efficiency.
NOVELTY - Obtaining ethanol involves bioprocessing of crude glycerol by using Escherichia coli. The crude glycerol is derived from biodiesel. The crude glycerol contains ethanol and methanol in proportion of less than 0.1% v/v, nutrients (10-20%) and nutrient media at pH 7.0.    USE - Method for obtaining ethanol used in trans-esterification of vegetable oils or animal fats, and as automotive biofuel or bioethanol for cleaning and sterilizing.    ADVANTAGE - The method enables to produce better yield of ethanol, and is cost-effective.
NOVELTY - Tie-dye ink aerosol comprises 1-15 wt.% active dye, 5-15 wt.% alkaline dye, 1-5 wt.% triethanolamine, 1-10 wt.% colorant, 1-5 wt.% leveling agent, 5-20 wt.% deionized water, 5-28 wt.% alcohol, 5-25 wt.% butane and 2-20 wt.% propane.    USE - The tie-dye ink aerosol is used for dyeing textile clothes (claimed). It is useful for do it yourself craft.    ADVANTAGE - The tie-dye ink aerosol uses butane and propane as propeller for reinforced ink propulsion effect and provides the textile with unique design and style.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dyeing method using tie-dye ink aerosol comprising taking tie-dye ink aerosol contained in aerosol package with valve, taking textile clothes, tying into bundles or twisted rope, clamping the ends, aligning spinning cylinder with nozzle, injecting tie-dye ink aerosol into textile clothes for absorption, spreading the textile clothes, where irregular pattern is formed, drying or airing and washing with water, where irregular pattern does not fade after washing.
NOVELTY - Preparation of biofertilizer involves (a) preparing egg shell broth by performing enzymolysis, (b) preparing Saccharina japonica broth by performing enzymolysis, (c) fermenting cattle and sheep manure to obtained fermented manure, (d) mixing egg shell broth, S. japonica broth and fermented manure, inoculating mixture with effective microorganism (EM) inoculant and fermenting mixture, and (e) drying fermented mixture, crushing, packing and storing.    USE - The method is useful for preparing biofertilizer for Fuji apple (claimed).    ADVANTAGE - The prepared fertilizer improves storage quality of apple, increases yield of apple, improves soil quality and is rich in calcium.
NOVELTY - Degrading phthalic acid esters involves inoculating Microbacterium sp. strain J-1 into a medium, which contain plant phthalic acid esters. The inoculated medium is placed at 20-40 degrees C for 3-7days at 100-200 revolutions per minute. The bacterial strain is preserved on 22nd January 2015, in China typical culture preservation center (CCTCC NO: M 2015055). The phthalic acid esters is combination of two, which are di-methyl phthalate (DMP), di-ethyl phthalate (DEP), di-butyl phthalate (DBP) or di-(2-ethylhexyl) phthalate (DEHP or DOP).    USE - Method for degrading phthalic acid esters used in sewage treatment plant (claimed).    ADVANTAGE - The method enables to degrade phthalic acid esters, which effectively repairs phthalic acid esters contaminated medium.
NOVELTY - High-pressure hydrogen generator comprises an electrolytic groove and an electrolyte storing groove provided for storing electrolyte, where a storage tank is set at upper side of the electrolytic groove. The electrolytic groove is connected to the storage tank through a pipeline. An insulation screen layer is formed between and anode plate and a cathode plate.    USE - High-pressure hydrogen generator.    ADVANTAGE - The high-pressure hydrogen generator ensures improved hydrogen generation efficiency.
NOVELTY - To-be-processed biomass materials are pulverized, agitated, and portion of exhaust gas is discharged from the outlet. Feed powder is added to drum, and dried to control moisture content of the powder mixture at 8-15%. Dried powder is added to storage hopper, subjected to extrusion molding machine and squeezed into granular particles. Resultant biomass particles are screened, and transported to storage for measuring package. The resultant material is further screened, and biomass powder is stored in storage hopper.    USE - Preparation of biomass pellet fuel (claimed).    ADVANTAGE - The method efficiently and economically provides biomass pellet fuel having excellent flame retardant property, by simple method with reduced consumption of energy.    DETAILED DESCRIPTION - To-be-processed biomass materials are added to a crusher, pulverized and subjected to a mixer using a blower. The biomass material powder is then added to agitator, agitated, and portion of exhaust gas is discharged from the outlet. The feed powder is added to a drum, and dried by hot air to control the moisture content of the powder mixture at 8-15%. The dried powder is added to storage hopper, subjected to an extrusion molding machine by lift conveyor belt and squeezed into granular particles. The resultant biomass particles are added to screening machine for four-level screening, and biomass particles of different sizes are transported by conveyor belt to storage for measuring package. The resultant material is further screened, and biomass powder is stored in storage hopper.
NOVELTY - Treating wastewater involves hydrolyzing waste gas of wastewater from catcher, and then recrystallized to obtain wasted product. Potassium hydroxide aqueous solution is mixed with wastewater process to absorb flue gas to obtain alkaline liquid and its pH is less than 10. Alkaline liquid and processed wastewater mixture are mixed uniformly to obtain desired product.    USE - Method for treating wastewater used for producing organic potassium aqueous solution used as organic fertilizer for crops (all claimed).    ADVANTAGE - The method is eco-friendly, easy to operate and suitable for large-scale popularization, and facilitates industrial implementation.
NOVELTY - Active component comprises Aspergillus niger, Trichoderma pseudokoningii, Penicillium verrucosum, Paenibacillus xylanilyticus, Bacillus subtillis and Azotobacter chroococcum.    USE - Active component used for improving crop straw decomposition rate, and increasing soil fertility and increasing crop yield and increasing products, which are microorganism fertilizer (all claimed).
NOVELTY - Cultivating Hypsizygus marmoreus involves crushing 46-54% sawdust, 26-34% corn, 11-13% bean cake, 3-4% mushroom, 3-4% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) at low temperature for 18-24 hours, and then performed piling of product with height of 1.0-1.2m and width 2-3m to obtain stack (300-500kg), covered it with tarpaulin, and then carried out natural fermentation at 60 degrees C for 24 hours. Gypsum is mixed with fermented product and wrapped in polyethylene cylindrical bag to obtain seeding bed.    USE - Method for cultivating Hypsizygus marmoreus (claimed).    ADVANTAGE - The method is eco-friendly, and enables to promote mycelial growth of Hypsizygus marmoreus.    DETAILED DESCRIPTION - Cultivating Hypsizygus marmoreus involves crushing 46-54% sawdust, 26-34% corn, 11-13% bean cake, 3-4% mushroom, 3-4% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) at low temperature for 18-24 hours, and then performed piling of product with height of 1.0-1.2m and width 2-3m to obtain stack (300-500kg), covered it with tarpaulin, and then carried out natural fermentation at 60 degrees C for 24 hours. Gypsum is mixed with fermented product and wrapped in polyethylene cylindrical bag to obtain seeding bed. Hypsizygus marmoreus is placed into seeding bed, and then lixiviums (0.01-0.02g/ml) and mixture (4-6kg) are sprayed. The seeding bed is soaked in water (20 times ) for 18-24 hours, and filter residue is removed.
NOVELTY - Cultivating white fungus involves crushing 46-54% sawdust, 24-32% corn, 13-15% bean cake, 4-5% mushroom, 2-3% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) at low temperature for 18-24 hours, and then performed piling of product with height of 1.0-1.2m and width 2-3m to obtain stack (300-500kg), covered it with tarpaulin, and then carried out natural fermentation at 60 degrees C for 24 hours. Gypsum is mixed with fermented product and wrapped in polyethylene cylindrical bag to obtain seeding bed.    USE - Method for cultivating white fungus (claimed).    ADVANTAGE - The method is eco-friendly, and enables to promote mycelial growth of white fungus.    DETAILED DESCRIPTION - Cultivating white fungus involves crushing 46-54% sawdust, 24-32% corn, 13-15% bean cake, 4-5% mushroom, 2-3% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) at low temperature for 18-24 hours, and then performed piling of product with height of 1.0-1.2m and width 2-3m to obtain stack (300-500kg), covered it with tarpaulin, and then carried out natural fermentation at 60 degrees C for 24 hours. Gypsum is mixed with fermented product and wrapped in polyethylene cylindrical bag to obtain seeding bed. White fungus is placed into seeding bed, and then lixiviums (0.01-0.02g/ml) and mixture (4-6kg) are sprayed. The seeding bed is soaked in water (20 times ) for 18-24 hours, and filter residue is removed.
NOVELTY - Tomato organic seedling matrix comprises rice straw compost and corn straw compost.    USE - The tomato organic seedling matrix is useful for applying on tomato and other crops.    ADVANTAGE - The method is simple and easy to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing tomato organic seedling matrix, comprising (i) taking the above mentioned raw materials and crushing; (ii) wetting the straw, adding fermenting broth and uniformly mixing, and then stacking; (iii) turning and carrying out decomposing process; and (iv) uniformly mixing water, rice straw compost and corn straw compost to obtain desired product.
NOVELTY - Composite foliar fertilizer comprises Lactobacillus fermentation liquid (200-350 pts. wt.), Bacillus subtilis fermentation liquid (200-350 pts. wt.), and composite amino acid powder (30-50 pts. wt.). Lactobacillus is Lactobacillus (CGMCC Number 8833). Bacillus subtilis is Bacillus subtilis (CGMCC Number 8834).    USE - Composite foliar fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing composite foliar fertilizer, which involves mixing Lactobacillus fermentation liquid, Bacillus subtilis fermentation liquid, composite amino acid powder, light rare earth elements, humic acid, urea, monopotassium phosphate, borate, and zinc sulfate to obtain the final product.
NOVELTY - Preparing cultivation material involves taking cottonseed hull (48-52%), bagasse (20-26%), soybean meal (18-20%), mushroom (3-4%), lime (3-4%), and gypsum (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days.    USE - Method for preparing cultivation material used for cultivating Pleurotus abalonus (claimed).    ADVANTAGE - The method is eco-friendly.    DETAILED DESCRIPTION - Preparing cultivation material involves taking cottonseed hull (48-52%), bagasse (20-26%), soybean meal (18-20%), mushroom (3-4%), lime (3-4%), and gypsum (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing diosgenin involves crushing raw materials in colloid mill to obtain finely crushed slurry. The obtained slurry is incubated at 25-30 degrees C for 24-48hours for natural fermentation to obtain fermented slurry. The fermented slurry is added with water (1-5%) and non-polar or low polar solvent (5-10 times) in colloid mill to obtain finely crushed slurry. The obtained slurry is centrifuged to separate cellulose and starch. The obtained supernatant is added with acid solution of 2mol/L sulfuric acid, 2mol/L hydrochloric acid or 2mol/L phosphoric acid in ratio of 1-5:1 with stirring at 30 degrees C.    USE - Method for preparing diosgenin (claimed).    ADVANTAGE - The method enables to prepare high purity diosgenin in cost-effective manner. The method is eco-friendly, and enhances yield by 98%.    DETAILED DESCRIPTION - Preparing diosgenin involves crushing raw materials in colloid mill to obtain finely crushed slurry. The obtained slurry is incubated at 25-30 degrees C for 24-48hours for natural fermentation to obtain fermented slurry. The fermented slurry is added with water (1-5%) and non-polar or low polar solvent (5-10 times) in colloid mill to obtain finely crushed slurry. The obtained slurry is centrifuged to separate cellulose and starch. The obtained supernatant is added with acid solution of 2mol/L sulfuric acid, 2mol/L hydrochloric acid or 2mol/L phosphoric acid in ratio of 1-5:1 with stirring at 30 degrees C at 1 atm pressure for 3-6 hours. The obtained mixture is neutralized with ammonia and then washed with water. The obtained material is added with 70% ethanol to extract diosgenin, which is filtered, concentrated and purified to obtain crystals.
NOVELTY - Bio-organic fertilizer comprises organic substance, fermented composition, microbial composition, amino acid composition and trace element composition.    USE - The bio-organic fertilizer is useful for improving crop yield, and soil fertility or soil structure (claimed).    ADVANTAGE - The bio-organic fertilizer improves quality of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bio-organic fertilizer, which involves crushing the organic substance, uniformly mixing obtained powder with remaining components, and drying obtained product.
NOVELTY - Method for biomethanation of carbon dioxide and hydrogen, involves adding fermented bacteria into bottle, further adding carbon and nitrogen into the bottle, determining periodic determination, adding the obtained mixture into fermentor, maintaining the mixture, filling the fermentor with carbon dioxide and hydrogen, further introducing carbon dioxide and hydrogen into the fermentor, converting methane, separating methane from carbon dioxide, and continuously circulating residual carbon dioxide in anaerobic fermentor.    USE - The method is useful for biomethanation of carbon dioxide and hydrogen (claimed).    DETAILED DESCRIPTION - Method for biomethanation of carbon dioxide and hydrogen, involves (a) adding 15-20% fermented bacteria into 10 l bottle, further adding carbon and nitrogen in a ratio of 20:1-30:1 into the bottle, and determining periodic determination of gas production and methane content, when the fermentation substrate is consumed in biogas production, (b) adding the obtained mixture into fermentor, maintaining the mixture at concentration of 25-35%, filling the fermentor with carbon dioxide and hydrogen, filling the fermentor with air under anaerobic conditions, further introducing carbon dioxide and hydrogen into the fermentor, converting methane, and separating methane from carbon dioxide, and (c) continuously circulating residual carbon dioxide in anaerobic fermentor to achieve carbon recycling process of carbon dioxide-fuel-carbon dioxide.
NOVELTY - The utility model is new type category in compost fermentation facility construction technology field, relating to one kind compost reaction device. It comprises reaction chamber, stirring device, carrying on hopper, a discharging mouth, discharge pipe, a feeding system, a ceiling, driving device, ventilating device, stirring device is equipped with reaction chamber inner side upper part of reaction room center seat and at lower end and reaction room and the setting is connected with rotating shaft seat, for hopper is equipped with reaction chamber on the left position, the discharging mouth is equipped with reaction chamber reaction room right lower part position, discharge pipe is equipped with reaction chamber on the right position, the feeding system is equipped with reaction chamber left seat, equipped with reaction chamber at the upper part position, drive device equipped with reaction chamber lower part of machine room at the right position, the vent device is equipped with reaction chamber lower part of machine room left position. The utility model is new type comprises following characteristics: low cost, compost time needed is short, deodorizing ability is strong, compost product quality.
NOVELTY - This new utility model claims of one water dividing separation circulation use of the biomass gasification furnace, gasification chamber from, a horn type lower material device, a feeding port, a fuel gas outlet, the water dividing separating recycling pipe, air inlet, a furnace body, a separated chamber composed of a horn type lower material device separating out and most moisture and volatile fuel, thus reducing of the water content in fuel gas, increase of thermal value, reducing of follow-up the gas water dividing separation device, separating out the water and volatile with a certain of temperature, led to the gasification furnace air inlet and air inlet mixing, can heating air inlet, increase of energy use ratio, the water dividing and volatile dividing too is participation gasification reaction of raw material, to increase of gasification efficiency.
NOVELTY - This new utility model claims of a kind of cooling one lower suction type biomass gas in station, comprising gasification furnace, cooling tower and purification system and used for suction after biomass gasification and combustion gas can and a fan, the purification system includes the third class purification device, one time filter, the second time filter, the third time filter, the cooling tower and gasification furnace connection, said fan and said cooling tower connected, the one time filter and the fan connect, the second time filter and the one one filter connection, the third time filter and the said second filter connection time, between each two through pipe connection device, in the cooling tower installed with cooling liquid from the gasification furnace and generating the combustion gas can pass high temperature gas pipe into the cooling liquid in cooling process, at the time the third filter also set with air outlet and user pipeline connection. From gasification furnace taking out of high temperature gas directly into the cooling liquid and cooling, has simple method and cooling speed pole.
NOVELTY - This new utility model claims have the following one of coil cooling suction type biomass gas in station, comprising gasification furnace, cooling tower and purification system and used for suction after biomass gasification and combustion gas can and a fan, the cooling tower and gasification furnace connection, said fan and said cooling tower connected, inside the cooling tower installed with cooling liquid, a coil, the plate tube immersed in the cooling liquid, the gasification furnace and generating the combustion gas into the can pipe by cooling plate, at the time the third filter also set with air outlet and user pipeline connection. After biomass gasification after obtain the high temperature gas induce disk pipe, plate pipe by discharging heat, a cooling coil pipe for cooling, rapid taking of high temperature gas cooling, at the same time the cooling liquid not be pollute, can be long time use.
NOVELTY - This new utility model provide a kind of automatic following arrange one ash suction type biomass gas in station, comprising gasification furnace, cooling tower and purification system and used for suction after biomass gasification and combustion gas can and a fan, the gasification furnace comprises hearth, furnace, hearth is set with the lower part has bridge, bridge the divide up furnace bridge, under furnace bridge, said bridge comprising upper of furnace bridge main body, furnace bridge main body is triangular prism cone or several strip-shaped iron bar of prism frustum shape, one end of each iron bar is connected on upper centre shaft at the other end composed of one of round fixed on inner hearth, one plane of each horizontal iron bar is fixed on inner hearth, one of lower corrugated faces facilitate ash slag arrange. This new utility model when using bridge set is on furnace bridge, furnace bridge under the rotating bridge, can make bridge between the shape distance enlargement, ash and convenient cleaning.
NOVELTY - This new utility model claims of a kind of clean fuel gas and one lower suction type biomass gas in station, comprising gasification furnace, cooling tower and purification system and used for suction after biomass gasification and combustion gas can is fan, purification system comprises one time filter, the second time filter, the third time filter, the cooling tower and gasification furnace connection, a fan and cooling tower connected, one time filter, the second time filter, the third time filter connected in turn, between each individual device via pipeline connection, the one time filter, the second time filter, the third time of filter are set with at least one of vertical filter board, filter board are set with upper partition for space and part of the filter board divide one side connection and air inlet pipe, two other one edge portion for air outlet pipe is connected. This new utility model is the third level filter, filter device is set with one of the whole filter plate too can be set with multi-number filter plate, and flexible structure, low cost.
NOVELTY - This new utility model provide a kind of one lower suction type biomass gas station for waste heat use system, comprising gasification furnace, cooling tower and purification system and fan, the gasification furnace comprises hearth, furnace, hearth is set with furnace on frame on the upper hearth from up to down in turn divided drying area, splitting area, a combustion area, reduction area, also set with jacket up on hearth wall, upper jacket connected with return pipe, water outlet pipe, also comprising hot water air conditioner system or domestic hot water system, hot water air conditioner system one end and water outlet connection pipe, the other end and back water pipe connect, hot water using tube through one valve connected at behind of the hot water air conditioner system or direct connect and outlet water pipe, water supplement pipe through valve and second water back pipe connection, back also has valve is set with the third water pipe of the hot water air conditioner system low temperature end also set with four valve. Jacket is set with up on hearth wall, combustion zone product and absorb heat for temperature increase of water in jacket, full use biomass fuel and energy.
NOVELTY - This new utility model claims of a kind of easy to clean one lower suction type biomass gas in station, comprising gasification furnace, cooling tower and purification system and used for suction after biomass gasification and combustion gas can and a fan, the purification system includes the third class purification device, the cooling tower and gasification furnace connection, said fan and said cooling tower connected, the gasification furnace comprises hearth, furnace, hearth and grate is connected the round seal structure, is set with hearth in furnace frame on the hearth is set with the lower part with bridge, also set with frame in combustion in the hearth of furnace bridge, set up with ignition port on the furnace frame of lower furnace bridge, an ash and inclined plate, also set with gas pipe and communicated up on furnace bridge frame. Because of setting of the combustion frame, increase of the space of furnace core, increase of oxygen supply amount, using biomass fuel combustion more full, because of setting of the inclined plate, make the cleaning ash in furnace is more suitable.
NOVELTY - An efficient comburant comprises 20-40 wt.% zinc permanganate, 15-30 wt.% magnesium dioxide and remainder of activated carbon.    USE - Efficient comburant is used for biomass briquette transmitter (claimed).    ADVANTAGE - The briquette obtained using the comburant has high thermal efficiency and fuel efficiency. The comburant efficiently reduces ignition point of biomass briquette, and shortens the ignition time of biomass briquette. The biomass briquette transmitter obtained using the comburant has simple structure, and is easy to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass briquette transmitter.
NOVELTY - The utility model claims a new air system, specifically a kind of comprising methane and one full products for air separation system, comprising methane and air enter into pre-processing system 101, after processing the impurity after enter into primary heat exchanger 102 cooling to-120 to-150 degrees centigrade, enter into expansion machine 103 expand, entering into hydrocarbon separation device 104 to obtain LNG; after removing hydrocarbon of low temperature gas through main heat exchanger 105 further cooling, entering into dual tower separating 106 the lower tower bottom through condensing and condensing evaporator 110, obtaining liquid oxygen in dual stage separation tower 106 and bottom, removing oxygen and gas of dual tower separating 106 below the tower top outlet, through sewage nitrogen throttling valve 108 enter into argon separating device 107 for liquid hydrogen separation, obtaining liquid argon, nitrogen by nitrogen throttle valve 109 throttle after enter into double separating tower 106 the middle part of tower, obtaining liquid nitrogen in dual stage separation tower 106 and tower bottom.
NOVELTY - It passes through an electro-static separator in the process of its conversion into the gaseous state. Between precipitation and discharge electrodes of an electrofilter surfaces are placed from an isolating material, on which water, released from the gas, when it transfers from hydroxide, is collected and condensed under an impact of an electric field, with the purified from water gas being supplied by pipelines for intermediate storage or processing, with water flowing down the surface, which it condensed on, into the zone of methane hydroxide evaporation.    USE - Chemistry.    ADVANTAGE - Simplification of the methane obtaining process.2 cl, 1 dwg
NOVELTY - The method involves separating granular heat-resistant material completely from dried sludge and municipal wastewater. The separated granular heat-resistant material is re-directed to warm in a heat exchanger (2), and dried precipitate is carbonized in a reactor (18) at temperatures above 300 degree Celsius. A solid fuel gasification furnace (3) is connected to a channel unit (15, 16), and a tray (8) is connected with a mixer (6). Part of sludge is transported to the reactor for carbonization sludge to produce biochar.    USE - Method for drying sewage sludge to prepare biofuels and organic fertilizers by heat treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for drying sewage sludge to prepare biofuels and organic fertilizers by heat treatment.    Heat exchanger (2)    Solid fuel gasification furnace (3)    Mixer (6)    Tray (8)    Channel units (15, 16)    Reactor (18)
NOVELTY - The furnace has a furnace body provided with an internal oxygen supply tube. Top cover of the furnace body is provided with a smoke exhaust pipe. Internal side wall of the furnace is fixedly connected downward to de-sulfur plate that is formed in a staggered arrangement. Lower part of the furnace is fixedly connected with a back pipe. The back pipe is provided with a reduction combustion layer that is connected with the furnace body.    USE - Non-tar biomass gasification furnace.    ADVANTAGE - The furnace utilizes the de-sulfur board so as to eliminate tar completely, remove oil with water, separately process the tar trouble in unsanitary manner, and avoid pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a non-tar biomass gasification furnace.
NOVELTY - The utility model claims a... zero discharge, energy from consume a complete waste cracking processing system, belonging to the garbage processing area, it comprises garbage automatic feedstock system, pyrogenation gastification furnace for life garbage processing furnace, smoke purification system, gas collecting system, a garbage automatic feedstock system connected to top end of pyrogenation gastification furnace for life garbage processing furnace, a top smoke pipe and a pyrogenation gastification furnace for life garbage processing furnace a waste feedstock system then automatically connect a smoke purification system, garbage pyrolysis process... a air outlet pipe connected with collecting gas collecting system for the combustible gas, a gas collecting system set up with a residual air pipe connected in the combustion chamber a pyrogenation gastification furnace for life garbage process... The utility model is a type of target is a supply of zero discharge, energy from consume a complete waste cracking processing system, a flue gas discharge, using a gas and a self-supply, realize a gas discharge reach state standard, at the same time saves resource, environmental protection energy saving.
NOVELTY - This new utility model claims of the gas and one of biomass carbonizing furnace recycling cooling system, including the biomass, has set up with nozzel and combustion chamber of biomass carbonizing furnace in furnace cavity, formed to have high temperature and biologic carbon after carbonizing the biomass carbonizing furnace in furnace cavity for cooling the cooling device in biomass carbonizing furnace bottom furnace cavity, gas outlet of the biomass carbonization furnace top part through gas channel and air inlet port of gas purification cooling system connected with the air outlet of gas purification cooling system through transporting pipeline respectively and air inlet port of the air inlet and cooling device connecting nozzel, also set with fan up at transport pipeline, lower in driving the fan, gas purification cooling system from the purification air inlet and air input, and after cooling by gas transporting pipeline is send to air inlet and cooling device and the middle nozzel. This new utility model is advantages as: recovery can use in biomass carbonizing furnace discharging the mixed gas, reduce energy consumption, and can high efficient cooling high temperature biological carbon.
NOVELTY - The system has a setting feed inlet (3) connected with a gasification furnace feeding port (5) through a pneumatic transport pump (2). Three gasification furnaces (7-9) are connected with each other. A bottom part of one of the furnaces is fixed with a setting air port (6). A fuel gas outlet (10) is connected with a burner (13) and an air import unit through an air pipe (11). The burner and the air import unit are connected with a burner fan (16). The air pipe and the air import unit are linked with an air import regulator (12). The burner fan is linked with another air import regulator (15).    USE - Positive pressure air-breathing biomass powder coal powder fluidization and air flow bed gasification furnace coal heating system.    ADVANTAGE - The system ensures better gas combustion effect and high fuel gas regulating quantity.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a positive pressure air-breathing biomass powder coal powder fluidization and air flow bed gasification furnace coal heating system.    Pneumatic transport pump (2)    Setting feed inlet (3)    Gasification furnace feeding port (5)    Setting air port (6)    Gasification furnaces (7-9)    Fuel gas outlet (10)    Air pipe (11)    Air import regulators (12, 15)    Burner (13)    Burner fan (16)
NOVELTY - This new utility model claims of one of biomass gasification furnace, wherein the upper part of bin respectively is smoke room and plenum; the middle pumping chamber equipped with storage hopper cover; between water tank and furnace core set with smoke gas channel, the gasification furnace core respectively connected and bin and an ash chamber, gasification furnace cylinder between ash dropping chamber equipped with belt device and moving grate door is funnel type furnace grate, gasification furnace cylinder and inside out between wall and provided with insulating layer, gasification furnace core gasification reaction chamber and the inner wall as can free telescopic of the telescopic pipe, side wall of gasification reaction chamber upper part equipped with air nozzel, insulating layer set with ignition device. The advantage is: structure is compact, gasification reaction high temperature reaches 1200 degree, heating starting time short, suitable ignition, high efficient, heating water tank can produce hot water, also for mixing the tar eliminating, environmental protection energy saving in fuel gas in biomass, increase of use life of related. eliminating accumulated ash or coke block is suitable.
NOVELTY - This new utility model relates to a kind of one mini-type natural gas and liquefying device, comprising purification air compressor, compressor after cooling device, BOG compressor, the first heat exchanger, a refrigerator, the second heat exchanger, LNG/NG heat exchanger, the first tank, the second tank, LNG flash tank, the first throttle valve, the second throttle valve, the throttle valve and the third one each adjusting valve, using the process characteristic is wherein: using natural gas purification, using high pressure natural gas pre-cooling process and then throttling cooling process, high pressure natural gas is pre-cooling refrigerator by providing the single refrigerant and natural gas liquefying generating oneself and partially LNG supply, technique process is simple, no existing refrigerant proportion of problem, device operation is stable, turn on suitable parking, and throttle expansion by the way can make the nitrogen of LNG comprising weight removing to 1% below.
NOVELTY - The present invention provides a soil amendment for anaerobic fermentation and a manufacturing method thereof. The soil amendment comprises an animal excrement and a bacteria-containing liquid, in which the bacteria-containing liquid comprises a bacterial powder which comprises Pseudomonassolanacearum and a Bacillus megaterium. The manufacturing method of the soil amendment comprises mixing the bacterial powder and water to form the bacteria-containing liquid; then the bacteria-containing liquid is added into the animal excrement to form a product to be fermented; finally after sealing and packaging, the product to be fermented is placed for a fermentation period to form the final product. By adding the bacterial powder, the animal excrement can be prevented from producing gases such as methane gas and ammonia gas, which not only solves the problem of odor emanated from the gases, but also avoids the danger of inflammable gases produced in the closed environment.
NOVELTY - The installation (1) has spin-drying installation (13) to dehydrate organic waste water accepted in purification-tank sludge acceptance tank (10). Biological treatment tank (15) and solid-liquid-separation tank (16) biologically treat organic waste water by which solid liquid separation is performed. A reactor (17) is filled with biological treatment adjuvant that dominates specific microorganisms group and is comprised so that sludge by which specific microorganisms group is dominated by reactor is supplied to organic waste water before dehydrating by spin-drying installation.    USE - Waste-water-treatment installation for biologically treating organic waste water such as purification-tank sludge (claimed).    ADVANTAGE - The waste-water-treatment installation reduces the generation amount of solid content by which the solid liquid separation is performed even the generation amount of the surplus sludge is reduced while improving the process efficiency of the waste liquid after solid-liquid separation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste-water-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the waste-water-treatment installation.(Drawing includes non-English language text)    Waste-water-treatment installation (1)    Purification-tank sludge acceptance tank (10)    Spin-drying installation (13)    Biological treatment tank (15)    Solid-liquid-separation tank (16)    Reactor (17)
NOVELTY - This new utility model claims of one straw of producing marsh gas desulfurizing dry device, comprising desulfurizing tower, alkaline solution tank, electric control valve and pipeline, a desulfurizing tower set with air inlet, an air outlet, a liquid inlet and a liquid outlet port, desulfurizing tower is also set with internal gas uniform distributor, the first level reaction plate, the second level reaction plate and liquid uniformly. This new utility model using alkaline solution spray method of removing H2S in the gas, by gas uniform distributor and liquid distributor evenly respectively diffusion layer marsh gas and alkaline solution, and by two level reacting plate, using H2S gas and marsh gas and full reaction and alkaline solution, this utility new type has simple structure, reasonable design, effective increase desulfurization efficiency and desulfurization solution is.
NOVELTY - This new utility model claims of a kind of biomass pyrolysis reactor and one double lever pyrolysis reactor, pyrolysis reactor comprises main body, side wall of cavity in said pyrolysis reactor main body is set with several block with the inclined clapboard. Biomass raw material depend on gravity automatically falling, by automatic scattering at lower clapboard barrier force effect, realize good mix heat transfer effect, make reactor internal reaction more full, more uniform, improves pyrolysis reaction efficiency, stirring process and biomass raw material without the help of gas fluidization medium or extra power, not only simplify pyrolysis process, and the pyrolysis reactor structure is simple.
NOVELTY - A biochemical fuel comprises 95.3-96.4 %mass light oil, 2.6-2.7 %mass water, 0.025-0.05 %mass potassium hydroxide, 0.025-0.05 %mass sodium hydroxide, 0.3-0.6 %mass ethyl acetate, 0.55-1.1 %mass ethanol and 0.1-0.2 %mass ferrocene. The light oil has density of 0.84-0.86 g/cm3, kinematic viscosity of 4.638 mm2/second at 20 degrees C, closed flash point of 42 degrees C and no mechanical impurities. Potassium hydroxide, sodium hydroxide, ethyl acetate and ethanol have analytical grade purity.    USE - The biochemical fuel is useful for power boiler, ordinary boiler, catering industry and variety of oil burner.    ADVANTAGE - The biochemical fuel can be prepared in a simple, safe, economical and environmentally-friendly manner with high calorific value and combustion effect and reduced impurities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biochemical fuel.
NOVELTY - An environmentally-friendly alcohol-diesel fuel contains 35-50 wt.% petroleum diesel, 25-30 wt.% modified biodiesel, 15-20 wt.% ethyl alcohol, 10-15 wt.% methanol and 0.05-0.5 wt.% additive.    USE - Environmentally-friendly alcohol-diesel fuel (claimed).    ADVANTAGE - The alcohol-diesel fuel is environmentally-friendly, has excellent quality and stable performance and low side effects and saves petroleum resource.
NOVELTY - Lipids are produced from biomass containing greater than or equal to 1 polysaccharide by hydrolyzing biomass to obtain mixture of 1st solid phase and 1st aqueous phase, preparing inoculum containing greater than or equal to 1 oleaginous microorganism in 1st fermentation device to obtain 1st fermentation broth, feeding 1st aqueous phase and 1st fermentation broth to 2nd fermentation device to obtain 2nd fermentation broth, micro-filtering portion of 2nd fermentation broth to obtain 1st retentate and 1st permeate, purifying 1st permeate to obtain 2nd permeate and 2nd retentate, and separating 2nd fermentation broth.    USE - Production of lipids from biomass containing polysaccharide for fuel production.    ADVANTAGE - The method has reduced process costs and improved yield of lipids.    DETAILED DESCRIPTION - Lipids are produced from biomass containing greater than or equal to 1 polysaccharide by hydrolyzing biomass to obtain mixture of 1st solid phase and 1st aqueous phase, preparing inoculum containing greater than or equal to 1 oleaginous microorganism in 1st fermentation device to obtain 1st fermentation broth, feeding 1st aqueous phase and 1st fermentation broth to 2nd fermentation device to obtain 2nd fermentation broth, micro-filtering portion of 2nd fermentation broth to obtain 1st retentate and 1st permeate, feeding 1st retentate to 2nd fermentation device, purifying 1st permeate to obtain 2nd permeate and 2nd retentate, feeding 2nd retentate to 2nd fermentation device, and separating 2nd fermentation broth to obtain aqueous suspension of oleaginous cellular biomass containing lipids and 2nd aqueous phase in which microfiltration and purification treatment are carried out continuously during the fermentation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the production process of lipids from biomass containing polysaccharide.
NOVELTY - The device has a gasification furnace (1) that is equipped with a hopper connected to combustion zone connected to the dust-removing cylinder and baffle plate. The baffle plate is set on air suction pipe and dust removing cylinder. A fan (5) is equipped with air inlet pipe and air outlet pipe. The gasification furnace is connected with a dust removing tank (2). A drying tank (3) is connected with a coke tank (4). The fuel gas is stored in air storage tank (6).    USE - Device for producing fuel gas via biomass material.    ADVANTAGE - The efficiency for producing fuel gas is improved. The energy saving effect for producing the fuel gas is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing fuel gas via biomass material.    Gasification furnace (1)    Dust removing tank (2)    Drying tank (3)    Coke tank (4)    Fan (5)    Air storage tank (6)
NOVELTY - The biomass gasification furnace has a furnace main portion (2) which is provided with a round oxidation layer gate (9) and a reduction furnace gate (10) whose periphery is provided with a recovery device (11). The lower portion of a heat recovery unit is provided with a cool carrier gas import. The outer side of the furnace main portion is provided with a fan power supply. The heat high temperature gas is transferred to the biomass raw material in a furnace main portion through the carrier gas circulation.    USE - Biomass gasification furnace.    ADVANTAGE - The reduction gas production effect is improved, and the large-scale popularization of the biomass gasification is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification furnace.    Furnace main portion (2)    Round oxidation layer gate (9)    Reduction furnace gate (10)    Recovery device (11)    Ash outlet (15)
NOVELTY - The utility model claims a new plant biomass without a low temperature dry distillation product separating system, comprising a cold tank, a a a a cold tank is respectively set with a gas pipe and an air outlet pipe, the air inlet pipe connected with dry distillation furnace, air outlet pipe connected with the high pressure electrostatic tar capturing device, a high pressure static top the tar capturing device through air pipe connected with one or more of a liquor spray tank, a liquor spray tank by gas pipe connected with the adsorption tank, the adsorption tank by gas pipe connected with a fan, a fan through air pipe connected with gas storage device. The utility model is a model for a mixed gas by cooling separation step by step, finish wood acetic acid, wood tar and biomass combustible gas and a separate, it is suitable for modern large scale of production requirement, the whole system by a multi-circle realize low energy consumption and low cost.
NOVELTY - The utility model is a new supply of a biomass organic coal preparation device, relating to biomass carbonizing technique and carbonizing device area, in the carbonization furnace comprises a furnace body, a furnace body of carbonization tube type heat exchanger and catalyst guide pipe, a furnace body of carbonization of the following two elliptic seal head of the furnace body and a cylindrical body composed of jacket, tube type heat exchanger present delamination tube arranged in a carbonization furnace; a furnace body sealing head left right two side are provided with a catalyst of import, catalyst and catalyst guide pipe connected with import. The utility model using a tube type heat exchanger structure, inside the heating pipe carrier, a control in a carbonization furnace temperature and reaction time, and adding a catalyst, implementation of organic biomass and coal a clean, increase biomass organic coal and obtain coal rate.
NOVELTY - The utility model claims a new plant and thermal cracking of biomass heating furnace, wherein it comprises: a present a cylindrical furnace body, a supporting leg of the said furnace body, is set with a annular baffle plate and the furnace body at the top of a wall, a set up of the furnace body outside wall on the lower part along the circumferential direction evenly and the first burner is arranged, a set up of the furnace body outside wall at middle part along the circumferential direction evenly and the second burner is arranged, and at least one of a connection in the exhaust window of the furnace body close to the top end of the out wall, wherein, the said the first vertical burner through a wall of a furnace body, a terminal connected with fuel gas pipe, the second gas burner head end inclined through out of the side wall of the furnace body, a connected with a fuel gas pipe, a first burner and a greater than or equal to a and a tail gas burner. The utility model can be widely applied to a biomass energy using system.
NOVELTY - The utility model is a new supply of a biomass organic coal preparation device of heat exchange and catalyst flow machine, relates to a biomass carbonizing technique and carbonizing device area, a carbonizing furnace body, a carbonization furnace body installed with tube type heat exchanger and catalyst guide pipe, tube type heat exchanger in carbonizing furnace body in present delamination tubular arrangement, each heat exchange tube of a front of a symmetrical part one,... are present half cylinder face shape, heat exchange tube and a carbonization furnace body axis as center line present cylinder type arrangement, catalyst guide pipe and carbonizing furnace body axis as center line present a plurality of circle array vertical in a carbonization furnace in a furnace body, a catalyst guide pipe wall of pipe is provided with multiple uniform small holes. The utility model using a tube type heat exchanger structure, inside the heating pipe carrier, a control in a carbonization furnace temperature and reaction time, and adding a catalyst, implementation of organic biomass and coal a clean, increase biomass organic coal and obtain coal rate.
NOVELTY - Microbiological production method involves producing gaseous metabolic products, preferably hydrogen, or liquid metabolic products, preferably 2,3-butanediol in proposition to time and volumetric units without optimizing actual cell growth metabolism or activating it on high level.    USE - The microbiological production method is useful for producing formed gases, liquids and suspensions which are useful as fuels (all claimed).    ADVANTAGE - The method is performed in controlled-manner, and releases gaseous hydrogen without emitting carbon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for performing the above-mentioned method, which comprises incineration tower, where liberated hydrogen and other combustible gases are conducted into an incineration tower from depository storage or reaction pool of the waste or other biomass.
NOVELTY - Method for photoreduction of molecules involves illuminating fluid sample comprising to-be-reduced molecules and hydrogen surface-terminated diamond electrode having negative electron affinity with light comprising wavelength that excites electrons from the valence band of the diamond to the conduction band of the diamond, such that inducing emission of excited electrons from diamond into fluid sample, reducing to-be-reduced molecules using emitted excited electrons, forming reduced product and collecting the reduction product. The counter electrode is immersed in the fluid sample.    USE - Method for photoreduction of molecules e.g. nitrogen to ammonia, and carbon dioxide to carbon monoxide, methane, formaldehyde and methanol.    ADVANTAGE - The method provides photoreduced molecules having excellent stability, without performing adsorption of reactant.
NOVELTY - A carbon dioxide removing device used in process of producing liquefied natral gas from coke furnace gas, belonging to coke furnace co-produced liquefied natural gas technology area, it comprises absorption tower, air cooling device, rich amine flash tank, a regeneration tower, carbon dioxide cooling device, a gas-liquid separator, regeneration tower relux pump, absorption tower top part and de-acidifying gas cooling device import end pipe connected with the bottom and rich amine flash tank pipeline connected with the rich amine flash tank and regeneration tower pipe connected with upper part of the regeneration tower top end and carbon dioxide cooling device pipe connected with the gas-liquid separator of part and carbon dioxide cooling device pipe connected with the bottom pipeline connected with regeneration tower relux pump, regeneration tower relux pump pipeline connected to regeneration tower. The device for MDEA for the redundant carbon dioxide by absorb, greatly reducing SNG mixture of air and carbon dioxide content, in effective problem of cold box pipeline is easy to be blocked, the increase of SNG, the device MDEA to carry out regeneration and circulation use, production cost reducing notable.
NOVELTY - The utility model claims a new kind of coking waste water depth processing system, a system of main pipe in turn connected in series with add medicine coagulation reaction pool, deposition pool, chemistry oxidation pool, to multi-medium filter, the middle pool and aeration biological filter pool, a coagulating add waste water enter into a medicine and a set with a flocculating agent dosing polymeric ferric sulfate, the chemistry oxidation pool is set with upper part has input a calcium hypochlorite. The utility model is a system design reasonable, operation cost is low, a treatment water outlet is a " coking industrial chemistry pollutant discharge standard " (GB16171-2012) for existing coking enterprise and standard requirement, which solves a problem of the coking waste water depth treatment and recycling, it has a strong engineering application value.
NOVELTY - Apparatus comprises a receiving chamber (1) charged with a substrate, which associated with a heating device, and which is provided with an access associated cover, accessible from above. The heating device comprises at least one heat exchanger (7) immersed in the substrate, which is accommodated with a supporting bar (13) arranged on a stand in the receiving chamber, in a height displaceable manner, and moves out at least partially from the receiving chamber via the open access.    USE - The apparatus is useful for treating a substrate formed by biomass, for producing biogas (claimed).    ADVANTAGE - The apparatus: has simple and inexpensive parts, such that the heating device can be cleaned without emptying the receiving chamber; and ensures a reliable heating of the substrate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a heating device for heating the substrate formed by biomass, comprising a ring-shaped heat exchanger submersible in the substrate, which comprises two walls limiting at outwardly sealed interior chamber, which is permeable by a heat carrier fluid, which abut one another, preferably welded together at several grid-like points distributed over the surface of the heat exchanger and in between form communicating chambers that are spaced from one another.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a biogas plant.    Receiving chamber (1)    Heat exchanger (7)    Supporting bar (13)    Bottom support (14)    Holder (16)
NOVELTY - This new utility model relates to one of refuse derived fuel preparation and incineration power generation integrated complete device, belonging to the garbage treatment area. The integrated complete device comprises out shell, header and garbage feedstock seal door, the garbage feedstock door setting on one side of outside shell, sealing the top header part of outside shell, wherein, in outside shell is set with sealing bin, a garbage storage pool, garbage sorting workshop biochemical processing chamber, fuel bin and combustion furnace. The utility model new implement of clean burning the domestic garbage and waste resource and comprehensive use, at the same time reducing floor area and construction investment of the waste incineration plant for household garbage, and reducing processing supply of technology condition.
NOVELTY - An organic substance is manufactured by performing organic substance production process of producing organic substance by carrying out microbial fermentation in fermentation device (13) in which liquid (13b) containing microorganisms is accommodated, performing gas-liquid contact process of carrying out gas-liquid contact of liquid containing organic substance and carrier gas while introducing carrier gas into fermentation device, and performing condensation process of condensing carrier gas after gas-liquid contact from fermentation device.    USE - Manufacture of organic substance for plastic, resin, and fuel.    ADVANTAGE - Organic substance can be extracted, without heating or reducing pressure of liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of organic substance comprising fermentation device which accommodates liquid containing microorganisms and purifies organic substance by carrying out microbial fermentation, feed mechanism which feeds carrier gas to fermentation device, gas-liquid contacting mechanism (15) which carries out gas-liquid contact of liquid containing organic substance and carrier gas, condensation part (16) which condenses off gas from fermentation device, and purification machine (18) which purifies organic substance from condensation liquid (17) collected from condensation part.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the manufacturing apparatus of organic substance. (Drawing includes non-English language text).    Fermentation device (13)    Liquid (13b)    Gas-liquid contacting mechanism (15)    Condensation part (16)    Condensation liquid (17)    Purification machine (18)
NOVELTY - The utility model claims a new methanol gasoline special for a kind of complete production device, a heater, dryer, filter and vaporizing a mchine, vaporizing the mchine a distiller and a condenser, between the distiller and the condenser by pipeline connected with, in the condensing set with exhauster to pump, and pipeline connecting, convenient maintenance, saving of cost.
NOVELTY - The method involves filling baskets with biomass. A blank reactor is placed in a forklift that is placed above a self-propelled-guided platform. The platform is located in a space that is formed between guide rails. The guide rails are located on a floor of a reactor. A mobile guidance platform is extended from the reactor. An iron structure, transversal side elements (1) and a floor are filled with sheets, in which openings (2) and the floor are attached with legs (3).    USE - Method for filling and emptying a reactor container in biogas plants.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a reactor.    Transversal side elements (1)    Openings (2)    Legs (3)
NOVELTY - Straw fermentation organic fertilizer comprises 150-200 pts. corn straw, 60-100 pts. sorghum, 50-80 pts. sawdust, 50-80 pts. silt, 30-60 pts. bean cake, 3-5 pts. shrimp powder, 5-8 pts. refined manure, and 0.2-0.6 pts. biological microbial inoculum.    USE - The organic fertilizer is useful for promoting crop growth and development.    ADVANTAGE - The organic fertilizer fully utilizes the resources, reduces corn stalks and sorghum straw waste, prevents environmental pollution, increases farmer's income, greatly increases crop yields, improving crop quality, and preventing soil compaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the straw fermentation organic fertilizer, comprising (i) crushing corn stalks and sorghum to less than 1 cm short material, and taking sawdust, silt, bean cake, shrimp powder, refined manure and biological microbial inoculum; (ii) mixing all the ingredients except biological microbial inoculum, adding water, mixing until the moisture content is 60-70%, then adding into a fermentation tank, adding biological microbial inoculum, mixing, and covering the fermentation tank opening with black film; (iii) checking the material temperature in the fermentation tank every day, when the temperature is increased to 40 degrees C, turning the material, and adding water to maintain material at humidity at 60-70%; and (iv) after fermenting for two months, taking out the fermented material, and drying until humidity is less than or equal to 20%, to obtain organic fertilizer.
NOVELTY - Aeration turning integrated machine comprises a U-shaped base and an arc cover located at the top of the U-shaped base. The arc cover is provided with a spiral propeller comprising a hollow shaft and a spiral blade of main shaft. The main shaft extends into arc end cover. The main shaft is connected with a motor through a speed reducer. The other end is connected with a blast pipe. A wind pipe is connected with a fan. The upper part of the arc cover is orderly provided with hopper, exhaust pipe and additive pipe. The lower part of the U-shaped wind pipe is provided with discharging hopper.    USE - Used as an aeration turning integrated machine.    ADVANTAGE - The aeration turning integrated machine: achieve turner and aeration process at same time; meets ventilation requirements, hence oxygen in the material can uniformly be distributed; saves energy; maintains optimal operation; does not add leaves, rice husk and straw as auxiliary filler.    DETAILED DESCRIPTION - Aeration turning integrated machine comprises a U-shaped base and an arc cover located at the top of the U-shaped base. The arc cover is provided with a spiral propeller comprising a hollow shaft and a spiral blade of main shaft. The main shaft extends into arc end cover. The main shaft is connected with a motor through a speed reducer. The other end is connected with a blast pipe by the shaft. A wind pipe is connected with a fan. The upper part of the arc cover is orderly provided with a hopper, an exhaust pipe and an additive pipe. The lower part of the U-shaped wind pipe is provided with a discharging hopper. Aeration holes are arranged between the hopper and discharging hopper. The upper part of the aeration holes is equipped with an aeration head.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the aeration turning integrated machine.
NOVELTY - Organic fertilizer fermentation complex strain having deodorizing function, comprises 20-30 pts. Bacillus subtilis, 10-15 pts. Saccharomyces cerevisiae, 1-5 pts. Trichoderma reesei, 1-5 pts. nitrifying bacteria, 1-5 pts. alkaliphilic bacteria, 10-30 pts. thermophilic cellulose decomposing bacteria and 20-30 pts. Thiobacillus denitrificans.    USE - The complex strain is useful for producing bio-organic fertilizer.    ADVANTAGE - The complex strain breaks down ammonia, amine salt, sulfide and phenols, has synergistic effect between different strains and achieves the reduction of deodorant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer fermentation complex strain, comprising carrying out high-density culturing of above mentioned strains, then inoculating into 30-40% activation culture medium-containing flasks and culturing respectively under shaking condition, inoculating the activated inoculum into 70-80% fermentation medium-containing fermentation tank, fermenting to expand culture, dehydrating and preparing into powder and mixing the strain powders.
NOVELTY - Manufacture of metal sulfide electrode involves removing oxide film on surface of a molybdenum electrode substrate by immersing the substrate in an alkaline solution, electrically-depositing a coating solution obtained by mixing cobalt chloride with distilled water and methanol on the substrate, thermally-processing the coated substrate and then sulfiding substrate.    USE - Manufacture of metal sulfide electrode used for alkaline water electrolysis system for producing hydrogen used as fuel.    ADVANTAGE - The method efficiently and economically provides metal sulfide electrode. The electrode improves the efficiency of the system. The alkaline water electrolysis system using the electrode produces high-purity hydrogen. The combustion of hydrogen fuel generates reduced amount of nitrogen oxide to environment.
NOVELTY - The apparatus has a funnel (2) whose lower portion is formed with a inner cavity (42) that is matched with a sounder. The sounder is formed with an open port. A sound film base (46) is formed with a multi-way hole that is matched with an outside of the inner cavity. An audio hole is matched with a side of an alarm installation hole way (43). A bottom portion of the film base is provided with a ring. A front wall of the audio hole is matched with the alarm installation hole way. A bottom wall of the audio hole is formed as an arc-shaped structure.    USE - Disposable drop stopping automatic alarm infusion apparatus for use by patient.    ADVANTAGE - The apparatus is environment-friendly, convenient to use and safe to use, and has high reliability and practicability, and can prevent backflow to ensure transfusion safety of patient, and avoids safety hidden accident, and can relieve mental pressure and working pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the disposable drop stopping automatic alarm infusion apparatus.    Funnel (2)    Ring filter (9)    Inner cavity (42)    Alarm installation hole way (43)    Sound film base (46)
NOVELTY - Sludge clean fuel comprises 10-15 pts. wt. carbide slag, 5-15 pts. wt. ferromanganese slag, 25-30 pts. wt. sphalerite ore, 1-5 pts. wt. furnace slag, 30-40 pts. wt. sludge, 1-5 pts. wt. oxidizing agent and 0.5-3 pts. wt. synergist.    USE - Sludge clean fuel.    ADVANTAGE - The fuel is environment-friendly and reduces industrial waste accumulation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of sludge clean fuel comprising high temperature baking sludge, adding remaining raw materials, mixing and crushing to 100-200 mesh.
NOVELTY - Biomass carbonization involves entering biomass into input hopper (1) conveyed by material transport pipe (2), where transported and handled axle coil (3) is provided for carbonizing of inlet tube (4). A liquid evaporation chamber (5) facilitates working at 100 degrees C to evaporate water, where an evaporation chamber oils (6) facilitates working at 600 degrees C to evaporate oil. The material free of water and oil is dried in the carbonization chamber at 500 degrees C to form carbon or carbon fuel.    USE - Method for carbonizing biomass for generating carbon for use in oven.    ADVANTAGE - The method generates carbon under precise control of driving and heating biomass during whole transformation process on carbon, and thus obtains better yield of carbonization without any combustion during carbonization process, and coal with very high thermal efficiency and greater power capacity in burning.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic overview of the method to carry out biomass carbonization.    Input hopper (1)    Material transport pipe (2)    Axle coil (3)    Inlet tube (4)    Liquid evaporation chamber (5)    Evaporation chamber oils (6)
NOVELTY - The utility model belongs to a marsh gas pool technology area, especially claims an elliptic ball type water pressure marsh gas tank, in providing a structure of simple and stable, improves biogas pool production rate, and simply and conveniently discharging elliptic ball type water pressure marsh gas pool,... on the underground marsh gas pool substrate, marsh gas pool basal body internal cavity is left and a fermentation chamber, a substrate set with feeding port, marsh gas feedstock pipe incline is set with import of feedstock and a set with a filter plate, a marsh gas pool basal body and right side set with water pressure, bottom of water pressure through the discharge port in a fermentation chamber mutually connected, top part of marsh gas pool is set with basal body with the cover top part and between floor set with sealing water tank, middle part of marsh gas pool substrate formed with a stirring device, the stirring device comprises stirring shaft, stirring shaft through extending a fermentation chamber of cover body, a stirring shaft is set with stirring with blade, stirring blade is set with delamination of a stirring shaft, top part of shaft is set with stirring with rotating rod, rotating rod and stirring shaft vertical to welding fixed.
NOVELTY - A medicine decocting preparing furnace, belonging to pharmaceutical equipment technology area. This utility model of new technology scheme is: a medicine jar and pedestal, wherein a medicine tank at a set with exhaust port, the middle exhaust port provided with a chute, a middle chute type provided with a discharge door, discharge door right side provided with draw-out handle, extracting handle outer side set with insulating protecting sleeve, a chute right side provided with a door fixing buckle, provided with a smoke gas filter of an exhaust port, a suction cover equipped with smoke gas filter on. This utility new type strong practicability, simple operation, can be uniformly by stirring, can take a medicine boiling out, not only reducing of environment pollute and saving of labour, big pole and increase of working efficiency.
NOVELTY - Microbial treatment of wastewater contaminated with snow removing agent and calcium lactate comprises taking fungal culture medium I, fungal culture medium II, preparing sodium alginate (SA) solution, adding polyvinyl alcohol, mixing, sterilizing, cooling, adding Aspergillus niger bacteria in log phase of growth to extrude beads, cross-linking, adding the beads and calcium lactate-magnesium sewage into Erlenmeyer flask, filtering and measuring the chemical oxygen demand (COD) value.    USE - The method is useful for microbial treatment of wastewater contaminated with snow removing agent and calcium lactate (claimed).    ADVANTAGE - The method is simple, carries out easy solid-liquid separation after degradation, reuses the immobilized microbes, and is economical and environmentally-friendly.    DETAILED DESCRIPTION - Microbial treatment of wastewater contaminated with snow removing agent and calcium lactate, comprises taking fungal culture medium I, fungal culture medium II, preparing sodium alginate (SA) solution, adding poly vinyl alcohol, mixing, sterilizing at 121 degrees C for 20 minutes, cooling to 25-30 degrees C, adding Aspergillus niger bacteria in log phase of growth to extrude beads in beaker containing 2 wt.% calcium chloride using 1 ml sterile syringe and curing for 1 hour, washing the beads with distilled water for 2-3 times, soaking the beads in 3 wt.% boric acid solution for 2-3 hours, cross-linking, washing with saline for 2-3 times and storing in refrigerator; according to solid-liquid ratio of 1:1, 2:1, 4:1, 6:1, 8:1 adding the immobilized beads and calcium lactate-magnesium sewage into 50-250 ml Erlenmeyer flask, placing in air bath shaker, culturing by vibrating at 150 rotations per minute for 48 hours and filtering, measuring the chemical oxygen demand (COD) value of the filtrate using COD analyzer by taking three trials from each group and taking the mean value.
NOVELTY - Grape selenium-enriched special fertilizer comprises 100-120 pts. wt. wet chicken manure, 100-130 pts. wt. straw, 50 to 55 pts. wt. corn powder, 30-35 pts. wt. nitrogenous fertilizer, 20-25 pts. wt. phosphate fertilizer, 30-32 pts. wt. potash fertilizer, 5-10 pts. wt. wood saw dust, 1-5 pts. wt. chitin, 10-15 pts. wt. selenium fertilizer, 10-12 soil conditioner, 1-5 pts. wt. bioenzyme, 1-5 pts. wt. yeast, 500-1000 pts. wt. rice water, and 50-60 pts. wt. clean oleander leaves.    USE - Used as grape selenium-enriched special fertilizer.    ADVANTAGE - The fertilizer contains nutrients, including six nutrient elements e.g. nitrogen, phosphorus, and potassium, is rich in amino acid, humic acid, calcium, sulfur, zinc, iron and boron necessary for crops, has function of regulating soil and balancing nutrition, contains high pure raw material, maintains grape growth, makes soil more loose, retains water, contains natural mineral and plant growth material, improves soil fertility, can regulate plant resistance, relieves disease, and increases yield.
NOVELTY - This new utility model claims of one of biologic diesel esterification reaction device, comprising baffle plate, and alcohol feedstock distributor, at lower side of reaction kettle respectively on the rotate shaft of the second stirring leaf and equipped with the first stirring leaf, the middle part of the reaction kettle rotate shaft is equipped with a connecting rod, upper end of the connecting rod connected with the baffle plate, the alcohol feedstock distributor located at the middle side wall of the reaction kettle of the alcohol feedstock distributor via the heat exchanger and alcohol feedstock pipe connected with, the reaction kettle upper part left and right two side respectively via hole provided with catalyst feedstock tube and steam tube, upper side and lower side of the reaction kettle respectively equipped with over temperature monitor and temperature monitor, lower bottom of the reaction kettle is set with mixed liquid outlet pipe, said mixed liquid outlet pipe and right end in turn connected with sediment tank and filter. This new utility model is simple structure, lifting of esterification reaction, reducing of carbonizing, the increase of production efficiency and production benefit.
NOVELTY - This new utility model claims of a kind of biological diesel oil one circulation extraction device, comprising oil groove, a tank body, a fixing plate and upper relux pipe, internal side wall of the jar body set with several fixing plate, the upper fixing plate set with catalyst layer, lower side of the tank body set with filter screen, the lower side of the filter screen in side wall of tank body of set with methanol steam entrance, left side of the jar body set with relux tube, on the relux tube equipped with relux pump, the top end of the tank body set with oil entrance, said tank body and right side upper part set with methanol steam outlet, of the methyl alcohol steam outlet set with temperature monitor, the lower end in the tank body and the oil groove, the middle part of the bottom oil groove set with heating pipe. This new utility model structure is simple, the purifying efficiency is high, the raw material using rate high, reducing of production cost.
NOVELTY - The box has a square-shaped box body provided with two box connection surfaces, three box side walls, a bottom plugging tongue page and a right-angle fixing surface. The first box connection surface is formed of a package material i.e. hard card paper. The second box connecting surface is fixed with a socket. Two end parts of the second box connection surface are provided with the right-angle fixing surface. A side part of the first and third box side walls is fixed with a box bottom. The second box connection surface is formed of a character print surface.    USE - Medicine packaging box.    ADVANTAGE - The box is energy-saving, and has better environment protection effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a medicine packaging box.
NOVELTY - The system has vacuum box assembly that includes vacuum pump (3) that is connected between vacuum tank (2) and centrifugal cylinder (4). The vacuum tank is provided with central electric control box (A). A drain pump (6) is connected with the first water outlet (7). A dewatering machine (8) is connected with fine dreg outlet (13). A sediment pool (15) is set with electric control medicine box (B) by second transporting pump. The electric control medicine box and dehydrating electric machine control box (C) are electrically connected with each other.    USE - Intelligent mobile septic tank sewage processing system.    ADVANTAGE - The transparent quality of the system can be improved. The purified water can be effectively discharged into municipal sewer network. The energy of the system can be saved and low-carbon economy can be realized. The safety of the system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic perspective view of the intelligent mobile septic tank sewage processing system.    Vacuum tank (2)    Vacuum pump (3)    Centrifugal cylinder (4)    Drain pump (6)    First water outlet (7)    Dewatering machine (8)    Fine dreg outlet (13)    Sediment pool (15)    Central electric control box (A)    Electric control medicine box (B)    Dehydrating electric machine control box (C)
NOVELTY - High-efficient grape fertilizer comprises 40-60 pts. wt. chicken manure, 30-50 pts. wt. plant ash, 4-6 pts. wt. borax, 8-10 pts. wt. vermiculite, 30-40 pts. wt. river mud, 20-30 pts. wt. cottonseed, 10-15 pts. wt. potassium ore, 10-12 pts. wt. traditional Chinese medicinal slag, 15-20 pts. wt. soybean, 8-12 pts. wt. ammonium phosphate, 10-15 pts. wt. urea, and 1-1.5 pts. wt. water-retaining agent.    USE - High-efficient fertilizer is useful for promoting growth of grape.    ADVANTAGE - The grape fertilizer has high efficiency and rich in nutrients, can avoid soil salinization, and can maintain long-term soil fertility.
NOVELTY - The system has fermentation tank (10) which is connected to left and right gas storage covers (20,30). Interval is formed between left and right gas storage covers. Feed inlet is provided with left inlet (22) and right inlet (32). Left inlet is inserted into left gas storage cover. Right inlet is inserted into right gas storage cover. Discharge port (40) is provided between left and right gas storage covers. Stirring rod is provided with pull rod and crossbar. Pull rod is perpendicular to central portion of crossbar. Pull rod is configured to move in gap between gas storage covers.    USE - Double interval hood type gas storage biogas fermentation system.    ADVANTAGE - The energy saving of the double interval hood type gas storage biogas fermentation system is improved. The environmentally friendly gas storage biogas fermentation system is obtained efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the double interval hood type gas storage biogas fermentation system.    Fermentation tank (10)    Left gas storage cover (20)    Left inlet (22)    Right gas storage cover (30)    Right inlet (32)    Discharge port (40)
NOVELTY - The device has fermentation pool whose middle portion is provided with fermentation chamber. Fermentation chamber is provided with inlet port and discharge port. Fermentation chamber is fixedly connected with air plate through supporting device. Fermentation pool is provided with pull rod comprising cross rod and vertical rod. Fermentation system is provided with first and second pipes. Center portion of pump portion is provided with control valve. Control valve is connected with pistons (210,220). Air supply passage is connected with air pipe and air guide plate.    USE - Pneumatic diaphragm pump integrated biogas extraction device.    ADVANTAGE - The pneumatic diaphragm pump is driven for automatically extracting the biogas efficiently. The electric power is not required. The environmental friendly biogas extraction is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pneumatic diaphragm pump integrated biogas extraction device.    Pistons (210,200)    Three-way water inlet pipe (410)    Three-way water outlet pipe (420)    Ball (430)    Liquid cavities (610,620)
NOVELTY - Biogas extraction using biogas pressure comprises passing gas through gas-guide tube into biogas fermentation pool, storing and transporting gas via pneumatic diaphragm pump, promoting the operation of the water pressure inside the pneumatic diaphragm pump, discharging stored biogas through water outlet pipe of pneumatic diaphragm pump.    USE - The method is useful for biogas extraction using biogas pressure (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biogas extraction device.
NOVELTY - Straw fermentation decomposition system comprises fermentation tank body, gas plate and partition plate; where the left and right ends of the fermentation tank body are respectively provided with inlet and outlet. The fermentation tank body has many fixed gas plates; the partition plate separates the fermentation tank body and is disposed between adjacent gas plates. A stirred tank is set between the fermentation tank body and the gas plate. The stirring tank is provided with a stirring device; and the partition plate is provided with multiple water openings.    USE - Used as straw fermentation decomposition system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straw fermentation decomposition system.
NOVELTY - A flavonoid isopentenyl transferase, namely AhFDT2 comprising a 402 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The flavonoid isopentenyl transferase, namely AhFDT2 is useful in preparation of prenylflavonoids, and for catalyzing isopentenyl apigenin (all claimed).    ADVANTAGE - The flavonoid isopentenyl transferase, namely AhFDT2 improves conversion rate of isopentenyl donor substrate and flavonoid by 26%. The method is performed environmentally-friendly, and simply improves purity of product by 76-95%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) flavonoid isopentenyl transferase, namely AhFDT2 gene encoding the flavonoid isopentenyl transferase, namely AhFDT2, where the gene comprises a 1209 base pair sequence (SEQ ID NO: 1) fully defined in the specification; and    (2) use of flavonoid isopentenyl transferase, namely AhFDT2 in preparation of prenylflavonoids.
NOVELTY - The method involves providing fermentation biogas generated collected storage plate at upper portion of fermentation chamber. Top portion of air plate is connected to air supply channel of biogas transporting pneumatic pump through setting gas-guide tube. Inner side wall of right baffle plate (220) is connected between pump main portion and right air cavity. The air pressure in air inlet chamber is set larger than air pressure of left end control shaft. The reciprocating center valve core is moved to left and right, to extract or absorb biogas from biogas slurry pump.    USE - Marsh gas pool biogas slurry automatic extraction method.    ADVANTAGE - The obtained marsh gas can be effectively transformed, without providing any harm to the environment. The working of gas pressure driven pneumatic pump can be achieved and the liquid can be extracted automatically.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram illustrating the marsh gas pool biogas slurry automatic extraction process.    Regulating type control valve (100)    Left baffle plate (210)    Right baffle plate (220)    Left liquid cavity (610)    Right liquid cavity (620)
NOVELTY - Method for producing bioalcohol from organic wastewater involves adding Rhodotorula mucilaginosa, Issatchenkia occidentalis, Comamonas, Sphingobium yanoikuyae, Pseudoalteromonas sp., and Pseudoxanthomonas Mexicana in wastewater, and stirring the wastewater along with strains.    USE - The method is useful for producing bioalcohol from organic wastewater (claimed).    ADVANTAGE - The method is simple, and cost-effective, and conserves energy.
NOVELTY - Extracting total flavonoids from effluent of extracted rose oil, comprises removing the solid residue from effluent of extracted rose oil via macroporous resin column, carrying out gradient elution using 0-100% ethanol/aqueous solution, vacuum concentrating in polyamide column, carrying out gradient elution using 0-100% ethanol/aqueous solution, concentrating in MCI column, and carrying out gradient elution using 0-100% ethanol/aqueous solution.    USE - The method is useful for extracting total flavonoids from effluent of extracted rose oil (claimed).    ADVANTAGE - The method avoids waste generation and environmental pollution; and uses nontoxic solvent.
NOVELTY - This new utility model claims of one of medical checking for urine collecting device, comprising one side edge provided with the first transparent plastic cup scale size and weight, the first transparent plastic weight cup lower end provided with two parallel set with one of the first and the second screw thread hole way, the first, the second thread bottom hole way respectively thread connected with the second, the third light weight plastic cup; the first transparent plastic weight cup upper end hinged with one end with one of the handle cover, the handle upper end provided with one bump, the first transparent plastic weight cup side edge set with one cover when rotating to the first transparent plastic and weight cup side when each seat can implant groove and convex block, this utility new type through setting two collecting cup and method of cup at the upper end is set with cover and bottom on cup, make one time it can acquire to acquire two parts urine sample to prevent pouring turn of needed re-collecting, at the same time the urine scattering to the outside will not pollute environment.
NOVELTY - This utility new type is a kind of a urine sample collection. It comprises the first handle, the second handle, the first handle and the second handle through the middle rotary pin shaft connection, the handle and the first end of a second handle respectively set with hand-hold ring, front part and front part of up and down of the second handle and the first clamp handle, front end of the first clamp handle provided with the first clamping ring and the second clamp handle front end is equipped with the second clamping ring, the clamping ring at a first and a second clamping ring in a mutually parallel, the first clamping ring and the distance between the second clamping ring is 1 to 3, the clamping ring and the second diameter less than the first diameter of the clamping ring. The utility model convenient patient take a urine sample, at the same time too would not dirty hand of patient, using suitable, clean and sanitary.
NOVELTY - A dairy potable water system of dairy farm, comprising a biogas generating subsystem, a direct-fired machine water supply subsystem, and a dairy water drinking and supply subsystem, wherein, the biogas outlet of the biogas generating subsystem is connected to the biogas inlet pipe of the direct-fired machine burner in the direct-fired machine water supply subsystem through pipes, further powering the direct-fired machine by biogas burning so that the direct-fired machine water supply subsystem can supply hot or cold water; the hot/cold water of the direct-fired machine water supply subsystem is connected to the plate heat exchanger of the diary water drinking and supply subsystem through a water supply pipe and a backwater pipe; the plate heat exchanger can heat or cool the natural water (cold or hot water) from the makeup water tank; the natural water treated by the plate heat exchanger is delivered to a constant temperature water tank for standby; the constant temperature water tank is connected to the makeup water tank and insulating water drinking trough through an electrical converging three-way regulating valve.
NOVELTY - This new utility model belongs to the agricultural herbicide production manufacturing technology area, especially claims a totally enclosed agricultural suspension automatic generation system. Along material running direction in turn includes automatic feedstock device, dispersing kettle, a vertical mill, circulation, sand mill, cutting kettle, a finished product tank and package device, comprising automatic feedstock device installed in dispersing kettle top, the discharge port and the lower part opposite to the dispersing kettle feeding port, a dispersing kettle discharging port under a vertical mill, vertical mill, circulation, sand mill, cutting kettle, a finished product tank and package device between two adjacent two through transporting pipeline sealing connection, install fan equipped with on a transporting pipeline, automatic feedstock device is totally enclosed structure, non-woven fabric bag with a flexible connection between automatic feedstock machine discharging port and dispersing kettle. The utility model is a new mechanical degree high, production efficiency greatly increase, a processing cost and labour intensity reducing notable, and the whole is totally-enclosed structure, reducing of environment pollute.
NOVELTY - On the new utility model claims of a improvement of safety and environmental protection, it includes the injector cylinder (1), mounting a syringe barrel (1) and an injection needle (2), mounting a push rod in the syringe barrel (1) (3), set the week. needle cap. In injection needle head (2) (4), syringe barrel (1) set with label (6), an injector cylinder (1) front end is provided with external screw thread,. needle cap (4) inner wall of open end equipped with screw thread,. needle cap (4) is threaded connection in a syringe barrel (1) of front end of needle cap. (4) front end is provided with reservoir, push rod (3) front end is set with piston (5), piston (5) and outside diameter is large syringe barrel (1) and inner diameter of the push rod (3) is cylinder, push rod (3) and a terminal equipped with injection plate arrive. The utility model new the injector, a reasonable design, using a suitable, can prevent the puncture and prevent medicine liquid loss, can ensure the administration dosage and effect, safety and environmental protection character is good, the application range is wide.
NOVELTY - The utility model claims a super-efficient biogas fermentation system, comprising a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe fermentation feedstock and a location to set up between a feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and a blocking plate is set with material with at least one of plate, between the adjacent blocking plate forming one of ferment cell of marsh gas ferment system also comprises annular cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and a water in a, bacteria distributing pipe is annular; Pipeline fixed on annular ferment bacteria distributing pipe in a wall, Brucella and pipe shape is annular pipe. fermentation, bacteria distributing pipe is set with a with a vertical upper direction of the cloth through a fungus, ferment efficiency of a fermentation of a different, cause different production rate, a gas pressure of different fermentation are a, promoting a biogas slurry flow stirring in the fermentation system to promote a uniform distribution of strain fermentation system, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. fermentation, the fermentation zone forming in the enough air pressure a and promote flow of liquid.
NOVELTY - This new utility model claims of disordered turbulent flow type efficient beyond marsh gas ferment system, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline ferment is ferment annular pipe, set annular fermentation pipe on top, annular pipe of fermentation set with opening, the opening center position is set up with extending to two side insert clapboard to separator, feedstock pipe and discharging pipe and annular pipe bottom respectively vertical and fermentation of the feedstock pipe and side wall of discharging pipe extending to biogas liquid face of annular fermentation pipe below seat; between water pressure and feedstock pipe connected with feedstock pipe drain pipe, water discharging pipe and connected with discharging pipe between pipe, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve has, in fermentation system also comprises cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure connection, bacteria distributing pipe is annular; Pipeline fixed on annular ferment bacteria distributing pipe in side wall, Brucella and pipe shape is annular pipeline phase, ferment bacteria distributing pipe set with multiple of one vertical direction of the cloth fungus through hole.
NOVELTY - This new utility model relates to a kind of one full-mixing methane gas production system, comprising: in preparing and feeding sub-system, fermentation sub-system, a marsh gas purification and storage sub-system and discharging and waste processing sub-system, wherein, the material of preparing and feeding sub-system for material temperature after storage for lifting regulating pool, for again sending material to fermentation tank and fermentation sub-system, and in the marsh gas fermentation for producing biogas, biogas purification and storage sub-system for producing and processing purification after storage, the discharging and waste treatment sub-system comprises, solid liquid separating machine, set liquid tank, liquid pool and liquid pour, the material discharging machine for fermentation after fermentation tank bottom by using spiral extrusion method, solid liquid separating machine for the material discharge machine carrying out solid liquid separation, separating out liquid is collected by collecting liquid tank to marsh liquid pool again further storage in liquid pour. This utility new type use the premise of increasing the organic matter content and changed in material cost is low, which greatly increase marsh gas yield, get more and more energy.
NOVELTY - The utility model claims a have a reasonable use of process gas and a fermentation tank, comprising a tank body, a support and purification cavity, the tank top provided with a feedstock and electrical machine, electric machine and stirring shaft connected with the stirring shaft into tank body and installed with several internal agitator blade, internal tank body equipped with temperature sensor, temperature sensor and controller and connected with a controller via a observation. Cake shape a. drum is set with a micro-pore ceramic aeration head on bottom fermentation tank body, can make a compare and a small bubble form into a fermentation liquid internal, again by agitator blade stirring, using a bubble full contact and fermentation liquid, the amount of the fermentation process, increase fermentation efficiency, purification in a fermentation tank equipped with a side, by purification in a fermentation tank internal generation of gas by purification to prevent fermentation tank internal generation is set with gas and harmful chemistry material direct discharge of air entering into a air, harm human body health.
NOVELTY - Preventing and treating kiwi canker involves mixing germinated fruits, organic fertilizer and fungus in a ratio of 60-70:10:20. Obtained mixture is fermented. Fermented product is mixed with branches in a ratio of 20:10 at 5-29 degrees C to obtain dormant fruit. Dormant fruit is coated with dry coating agent comprising bromothalonil (0.1-5 parts), lime sulfur (0.1-5 parts), acrylic acid (10-15 parts), crosslinked resin (15-20 parts) sodium carboxymethylcellulose (25-35 parts), and vegetable oil. Fruits are refrigerated to prevent the fruits from low temperature.    USE - Method for preventing and treating kiwi canker (claimed).    ADVANTAGE - The method is cost effective and ensures improved disease resistance.
NOVELTY - Rhizopus oryzae JHSW01 (CCTCC M 2015189) screened from rotten straw, is new.    USE - The Rhizopus oryzae JHSW01 is useful for producing glucoamylase and cellulase (claimed), and for fermenting straw and other agricultural and forestry waste.    ADVANTAGE - The strain is simple to prepare, economical, easy to control and suitable for industrial production.
NOVELTY - The oxygen pump (100) has a pump main portion whose upper and lower ends are respectively provided with air inlet and outlet. The left and right ends of pump main portion are provided with air inlet and outlet three-way pipes (140,150) respectively. A main air chamber is provided with a piston rod connected with a piston baffle plate fixed with a centre valve core. A control shaft is connected with left and right heave portions. The air inlet groove is connected with a pump main portion. A left air groove and a right air groove are separately connected with the main air chamber.    USE - Oxygen pump.    ADVANTAGE - The circulation flow of biogas is improved, the uniform distribution of strain is promoted, and the fermentation efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oxygen pump.    Oxygen pump (100)    Left air chamber (110a)    Right air chamber (110b)    Center shaft (130)    Air inlet and outlet three-way pipes (140,150)
NOVELTY - The method involves providing cylindrical tank (1) whose center portion is provided with a central guide pipe (5). An upper end of the guide pipe is arranged on arc tank top (3) of the cylindrical tank. A top end of a gas collecting chamber is provided with an air collecting pipe. An end of the cylinder tank is provided with an exhaust pipe (12). An exhaust valve is arranged on the exhaust pipe. An upper end of the exhaust pipe is communicated with the air collecting pipe through a water tank (8). The upper end of the central guide pipe is provided with a water inlet pipe (6).    USE - Anaerobic biogas tank water purification method.    ADVANTAGE - The purification of gas rate is increased. The gas collection rate is improved. The water sealing effect is improved. The wastewater treatment effect is improved. The gas liquid separation effect is increased. The gas production rate is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic biogas tank water purification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the anaerobic biogas tank water purification process.    Cylindrical tank (1)    Arc tank top (3)    Central guide pipe (5)    Water inlet pipe (6)    Water tank (8)    Exhaust pipe (12)
NOVELTY - The system has a marsh gas pool (1) whose top portion is formed, so as to seal liquid leakage of biogas from marsh gas pool. Marsh gas pool is connected to biogas storage pool (4) by first liquid outlet pipe (3). Biogas storage pool is connected to sediment pool (6) through second liquid outlet pipe (5). Sediment pool is connected to liquid storage regulating biogas by biogas liquid lifting pipe (7). Biogas liquid storing pool is connected to irrigation outlet (9) by third liquid outlet pipe (8). Biogas liquid lifting pipe is set to improve biogas slurry with water pump (10).    USE - Zero-emission biogas discharge system.    ADVANTAGE - The simple structure and reasonable design of system is achieved. The air leakage of discharge system is prevented. The larger power of biogas liquid storing pool is achieved. The good long-range crop is achieved without using power for irrigation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a zero-emission biogas discharge method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas zero discharge system.    Marsh gas pool (1)    First liquid outlet pipe (3)    Biogas storage pool (4)    Second liquid outlet pipe (5)    Sediment pool (6)    Biogas liquid lifting pipe (7)    Third liquid outlet pipe (8)    Irrigation outlet (9)    Water pump (10)
NOVELTY - Fertilizer comprises 1000-1500 pts. wt. animal manure, 800-1200 pts. wt. wheat bran, 500-800 pts. wt. cake fertilizer, 1000-2000 pts. wt. straw and 30-60 pts. wt. composite strain.    USE - Fertilizer (claimed).    ADVANTAGE - The fertilizer is simple to prepare, non-toxic to human and environmentally-friendly, hence safe for use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer, which involves mixing animal manure, wheat bran, cake fertilizer and composite strain, adding water to maintain humidity at 60-70%, allowing to stand for 1 day, adding crushed straw to mixture, adding water to maintain humidity at 60-70%, stacking mixture, where the stacking height does not exceed 2 m and the stacking width does not exceed 3 m, turning the mixture once for every day for 24 hours and fermenting mixture for 10-20 days to obtain product.
NOVELTY - Fertilizer comprises 50-55 pts. wt. rice bran, 12-14 pts. wt. pig manure, 22-25 pts. wt. wheat straw, 7-9 pts. wt. corn straw, 60-65 pts. wt. mushroom, 0.1-0.5 pt. wt. microbial preparation comprising Aspergillus niger, Penicillium purpurogenum, Bacillus subtilis and Bacillus megaterium.    USE - The fertilizer is useful for cucumber (claimed).    ADVANTAGE - The fertilizer improves soil structure, increases yield and quality of cucumber and is rich in nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer, which involves (a) weighing raw materials, (b) crushing mushroom and adding 50-55% water to rice bran, pig manure, wheat straw, corn straw and crushed mushroom, (c) then inoculating with A. niger, P. purpurogenum, B. subtilis and B. megaterium, and fermenting mixture at 55-60 degrees C for 20-30 days, and (d) spreading fermented mixture, drying mixture, crushing and sealing.
NOVELTY - Synthesis of isocyanate compound, involves catalytically transesterifying methyl isocyanate and an alcohol, to obtain an isocyanate and methanol.    USE - Synthesis of isocyanate compound useful as hypoglycemic-drug intermediate.    ADVANTAGE - The method enables simple, easy and environmentally-friendly synthesis of isocyanate compound with high yield.    DETAILED DESCRIPTION - Synthesis of isocyanate compound, involves catalytically transesterifying methyl isocyanate and an alcohol of formula: ROH, to obtain an isocyanate of formula: RNCO and methanol.    R=not defined.    N.B: R is not defined.
NOVELTY - Cultivating fungi includes vegetable waste and fruits, where vegetables waste such as bagasse, stalks, seeds and peels are processed. The fungi is preferably basidiomycetes and ascomycetes.    USE - Method for cultivating fungi for producing plant product, which contains bioactive molecules (claimed).    ADVANTAGE - The method enables to produce mycelium on large sacle.
NOVELTY - Coal-bed methane adsorbent is prepared by crushing industrial waste phenolic resin, drying to obtain crude-like material, mixing, adding binder, additives and water, kneading, performing extrusion molding, performing carbonization process under inert gas to obtain carbonized material, and adding activating agent and pore forming agent.    USE - Coal-bed methane adsorbent used for adsorption separation of methane/nitrogen gas mixture (claimed).    ADVANTAGE - The coal-bed methane adsorbent is environmental-friendly, inexpensive and has wide material source.
NOVELTY - Treating municipal sewage involves weighing dewatered sludge. The obtained dewatered sludge is added with calcium oxide and deionized water. The obtained mixture is filtered with nylon filter cloth. The obtained product is entered in a hydraulic cylinder. The obtained mixture is added with iron powder, alkyl fungus inhibitor and 2-bromoethanesulfonic acid. The obtained mixture is stirred.    USE - Method for treating municipal sewage (claimed).
NOVELTY - Stirring device includes fermentation material, which is poured into fermentation system (10) through feedstock (12) for producing biogas. The produced biogas is stored in plate in air. Increase in gas pressure pushes gas (30) upward through top plate (32) provided on pneumatic piston (52). The pneumatic piston moves upward by pulling stirring process to net upward movement for stirring slurry. Biogas pressure dropped in plates when the top plate pushes biogas outward and the pneumatic piston pushes to downward movement. The device reset for next stirring.    USE - Stirring device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the stirring device.    Fermentation system (10)    Feedstock (12)    Gas (30)    Plate (32)    Pneumatic piston (52)
NOVELTY - Extracting biogas involves storing feedstock (13) material into fermentation tank (10). The fermentation tank comprises number of same size sub-fermentation tank to produce biogas, which is accumulated into fermentation chamber. Upper part of the fermentation chamber (16) is provided with air board (18). The biogas slurry squeezed out with air board into plate with rising biogas level. The fermentation tank has high efficiency by connecting number of sub-fermentation tank. The fermentation tank is provided with drain pipe. The biogas slurry flows to second water pipe.    USE - Method for extracting biogas through parallel digesters (claimed).    DETAILED DESCRIPTION - Extracting biogas involves storing feedstock material into fermentation tank. The fermentation tank comprises number of same size sub-fermentation tank to produce biogas, which is accumulated into fermentation chamber. Upper part of the fermentation chamber is provided with air board. The biogas slurry squeezed out with air board into plate with rising biogas level. The fermentation tank has high efficiency by connecting number of sub-fermentation tank. The fermentation tank is provided with drain pipe. The biogas slurry flows to second water pipe when level of slurry reaches to lowest point of the first water pipe. The biogas flows with unidirectional pressure (40). Gas-guide tube is provided with top plate and pneumatic diaphragm pump that put pressure on biogas and takes to output by reducing methane gas pressure inside the plates. The biogas slurry circulates inside the fermentation tank. The pneumatic diaphragm pump with gas pressure act as driving force between inner pressure of stored slurry to discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the parallel digesters.    Fermentation tank (10)    Feedstock (13)    Fermentation chamber (16)    Air board (18)    Pressure (40)
NOVELTY - Manufacture of molded charcoal involves grinding coffee beans, roasting, extracting coffee beverage, collecting remaining residue byproduct, uniformly stirring byproduct in steam tank, sterilizing, uniformly mixing resulting product and starch binder, extruding, forming char product, cutting, compressing and drying.    USE - Manufacture of molded charcoal (claimed).    ADVANTAGE - The molded charcoal of high quality is manufactured economically with high thermal efficiency.
NOVELTY - Cultivation of enoki mushroom involves taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 57-61 wt.% cotton seed hull and 10-14 wt.% 3-5 mm diameter wood chips, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days, adding 2-3 wt.% lime for first turn and 1 wt.% light calcium carbonate for second turn, controlling moisture content to 63-65% and covering mycelium with 1-2 cm thick loam soil.    USE - Method for cultivating enoki mushroom (claimed).    ADVANTAGE - The method is environment-friendly, saves manpower and coal resources, improves bacterial resistance and growth performance of mushroom, and has high biological conversion rate.    DETAILED DESCRIPTION - Cultivation of enoki mushroom comprises taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 57-61 wt.% cotton seed hull, 10-14 wt.% 3-5 mm diameter wood chips and 20-24 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days, adding 2-3 wt.% lime for first turn and 1 wt.% light calcium carbonate for second turn, controlling moisture content to 63-65%, cooling to obtain cultivation material, adding to enoki mushroom, covering mycelium with 1-2 cm thick loam soil, adding 20 times water to dried shiitake stem, soaking for 18-24 hours, filtering, diluting to obtain 0.01-0.02 g/mL dried shiitake stem solution and spraying to loam soil covered mycelium at 3-5 kg/m2.
NOVELTY - Organic fertilizer comprises dry chicken manure (1-4 pts. wt.), Eupatorium (2-5 pts. wt.), tobacco, actinomycetes, and lactic acid bacteria.    USE - Organic fertilizer used for Panax pseudoginseng (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) pulverizing dried Eupatorium and tobacco;    (B) inoculating actinomycetes and lactic acid bacteria; and    (C) fermenting obtained mixture at 40 degrees C for 40 days to obtain the final product.
NOVELTY - Preparing biological organic fertilizer from rotten organic matter involves fermenting raw fruit and vegetables with inoculation liquid (0.2-0.4ml) for 3-5 days. Concentration of fungus in inoculation liquid is 1asterisk109 colony forming units/ml. Fermentation is performed for 3-5 days to obtain fermented product having pH of 5-6. Growth promoting bacteria are added to obtained fruit and vegetable broth. Obtained mixture is fermented for 3-4 days at 60 degrees C. Obtained product is dried to obtain microbial organic fertilizer having moisture content below 30%. Sulfuric acid is added to obtained product.    USE - Method for preparing biological organic fertilizer from rotten organic matter used for promoting growth of vegetables such as cucumber and tomato.    ADVANTAGE - The method is economic and eco-friendly.
NOVELTY - Stack retting pool structure comprises pool body (1) and heat pipe (2). Pool body is set with filtering layer (4), and heat pipe is set on pool body in lower part of the filter layer. One side of the filter layer is set with liquid fertilizer outlet.    USE - Stack retting pool structure used for preparing liquid fertilizer (claimed).    ADVANTAGE - The stack retting pool structure has high economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing liquid fertilizer, which involves:    (A) crushing 1000 parts dry branches and fallen leaves by using a pulverizer;    (B) mixing 1-3 parts straw rotten agent, 6-8 parts urea or 15-25 parts ammonium bicarbonate to obtain mixture; and    (C) overlapping the dry branches and fallen leaves powder in the mixture to obtain stack with thickness of 15-20 cm by using stack retting pool structure, and then spreading as layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a stack retting pool structure.    Pool body (1)    Heat pipe (2)    Soil engineering cloth cover (3)    Filtering layer (4)    Reinforced concrete flat substrate (5)
NOVELTY - Organic fertilizer comprises 15-20 pts. wt. chicken manure, 10-15 pts. wt. spinach, 5-12 pts. wt. Porphyra or kelp, 8-10 pts. wt. fungus culture material waste, 5-8 pts. wt. rapeseed straw, 10-15 pts. wt. plant ash, 5-8 pts. wt. nitrogen-phosphorus-potassium compound fertilizer, 2-3 pts. wt. ferrous sulfate, 1-2 pts. wt. copper sulfate, 1-2 pts. wt. zinc sulfate and 1-2 pts. wt. borax.    USE - Organic fertilizer used for iron-rich chili (claimed).    ADVANTAGE - The organic fertilizer ensures iron content more than 10%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing pharmaceutical preparation, which involves:    (A) decomposing chicken manure, spinach, Porphyra or kelp, fungus culture material waste, rapeseed straw and plant ash; and    (B) mixing nitrogen-phosphorus-potassium compound fertilizer, ferrous sulfate, copper sulfate, zinc sulfate and borax with decomposed product, and then granulating and drying.
NOVELTY - Fertilizer comprises 20-140 pts. wt. chicken manure, 60-80 pts. wt. plant ash, 30-50 pts. wt. weathered coal, 20-30 pts. wt. bagasse, 10-20 pts. wt. pumpkin vine, 10-15 pts. wt. peanut cake, 8-12 pts. wt. nitrogenous fertilizer, 3-5 pts. wt. phosphate fertilizer and 8-10 pts. wt. potassium fertilizer.    USE - Fertilizer used for planting cucumber (claimed).    ADVANTAGE - The fertilizer satisfies cucumber nutrient need, and ensures good crop growth environment, improved soil property and reduced environmental pollution.
NOVELTY - Low temperature refrigerant comprises 1-35 wt.% difluoromethane, 25-60 wt.% propane, 20-60 wt.% 1,1,1,2-tetrafluoroethane and 1-20 wt.% 2,3,3,3-tetrafluoropropene.    USE - Low temperature refrigerant for freezing refrigerator (claimed).    ADVANTAGE - The low temperature refrigerant is eco-friendly and increases performance of freezing refrigerator.
NOVELTY - An olefin polymer effluent gas recycling device comprises a compressing mechanism, a pre-dissociation mechanism and a cryogenic mechanism, where the compressing mechanism is provided for receiving effluent gas of olefin polymer in the production, the pressure of gas components in the effluent gas is compressed in the same grade, and recycled C4+ high-carbon hydrocarbon flow and residue effluent air flow are output, and the pre-dissociation mechanism is provided for receiving the residue effluent air flow from the compressing mechanism.    USE - Olefin polymer effluent gas recycling device.    ADVANTAGE - The device has capability of recycling low polymer in low energy consumption, and producing hydrocarbon and nitrogen with high recycling rates.    DETAILED DESCRIPTION - An olefin polymer effluent gas recycling device comprises a compressing mechanism, a pre-dissociation mechanism and a cryogenic mechanism, where the compressing mechanism is provided for receiving effluent gas of olefin polymer in the production, the pressure of gas components in the effluent gas is compressed in the same grade, and recycled C4+ high-carbon hydrocarbon flow and residue effluent air flow are output, the pre-dissociation mechanism is provided for receiving the residue effluent air flow from the compressing mechanism, and outputting recycled oligomerization physical flow and the residue effluent air flow, and the cryogenic mechanism is provided for receiving the residue effluent air flow from the pre-dissociation mechanism, and recycling C2+low carbon hydrocarbon flow and nitrogen flow in the residue effluent air flow. An INDEPENDENT CLAIM is also included for method for recycling an olefin polymer effluent gas.
NOVELTY - Biological cathode type microorganism fuel cell wastewater processing system comprises first water inlet pipe (1-1), second water inlet pipe (1-2), biological anode (2), first water outlet pipe (4-1), second water outlet pipe (4-2), anode room (5), separating film (9), cathode room (10) and biological cathode (12).    USE - Biological cathode type microorganism fuel cell wastewater processing system.    ADVANTAGE - The system reduces cost of removing nitrogen in cathode room, promotes degradation of pollutant, realizes synchronized removal of nitrogen in wastewater and biological power generation and recovers nitrogen in wastewater. It has stable performance.    DETAILED DESCRIPTION - Biological cathode type microorganism fuel cell wastewater processing system comprises first water inlet pipe (1-1), second water inlet pipe (1-2), biological anode (2), first water outlet pipe (4-1), second water outlet pipe (4-2), anode room (5), separating film (9), cathode room (10) and biological cathode (12). The anode room is provided with first water inlet pipe on lower part side wall, and first outlet water pipe on side wall upper part. The cathode room is set with second water inlet tube and second outlet water pipe. The anode room is filled with liquid anode. The cathode room is filled with cathode liquid. The anode liquid comprises power producing strain. The cathode liquid comprises denitrifying strain. An INDEPENDENT CLAIM is included for microbial fuel cell wastewater treatment comprising adding denitrifying strain into cathode liquid and power producing strain into anode liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biological cathode type microorganism fuel cell wastewater processing system.    Water inlet pipes (1-1, 1-2)    Biological anode (2)    Water outlet pipes (4-1, 4-2)    Anode room (5)    Separating film (9)    Cathode room (10)    Biological cathode (12)
NOVELTY - Bacillus subtilis strain JF is preserved at China General Microbiological Culture Collection Center on July 22, 2013, which is located at West Road 1, Chaoyang District, Beijing (CGMCC NO: 7950) is new.    USE - Bacillus subtilis strain JF used for degrading environmental diethylstilbestrol and eliminating residual bacteria (claimed).    ADVANTAGE - The Bacillus subtilis strain JF metabolizes diethylstilbestrol, environment-friendly and has good application prospect.
NOVELTY - In-situ growth of graphitic carbon nitride (g-C3N4) on titanium dioxide (TiO2) nanocrystal surface comprises heat polymerizing melamine precursor to obtain g-C3N4, fully mixing titanium source tetrabutyl titanate (TBOT) in anhydrous alcohol solvent to obtain light yellow transparent solution A, dissolving ammonium acetate in anhydrous alcohol solvent by vigorous stirring, adding g-C3N4, vigorously stirring to obtain suspension B, mixing solution A and suspension B by stirring at room temperature, transferring in PTFE lined reaction kettle, and adding anhydrous alcohol solvent to dilute.    USE - In-situ growth of g-C3N4 on TiO2 nanocrystal surface to obtain g-C3N4/TiO2 composite material for use as photocatalyst for photocatalytic degradation of organic pollutant, photocatalytic water splitting and photocatalytic reduction of carbon dioxide (all claimed).    ADVANTAGE - The g-C3N4/TiO2 composite material has greatly increased photocatalytic activity.
NOVELTY - The new type utility claims have one kind environment-friendly clean the modified manganese slag compound fertilizer production system, comprising prefabricate manganese slag system, compound fertilizer production system, manganese slag drying tail sum process system and compound fertilizer drying cooling exhaust sum processing system, prefabricate manganese slag system comprises combustion furnace draught fan I, a combustion furnace I, a slag dryer, modified device acidification and neutralization reactor, compound fertilizer production system comprises combustion furnace draught fan II, burning furnace II, weigh burdening system, a mixer, pulverizer raw material, the compound fertilizer dryer and cooling machine compound fertilizer, manganese slag drying tail sum processing system comprises heat exchanger, buffer tank, washing tower I, sediment pool I and clear water tank I, a compound fertilizer drying cooling exhaust sum processing system comprises settling chamber, a washing tower II, sediment pool II and clean. The utility model is new type aiming at carrying out modified manganese slag, using modified manganese slag as raw material, by adding each kind nitrogen, P, potassium base fertilizer prepared compound fertilizer product, full use resource waste as treasure.
NOVELTY - Preparation of hydrodeoxygenation catalyst involves supporting metal precursor on zirconia-based carrier.    USE - Preparation of hydrodeoxygenation catalyst used in preparation of biofuel (claimed).    ADVANTAGE - The method enables preparation of hydrodeoxygenation catalyst having high activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biofuel.
NOVELTY - A microemulsion comprises synthetic material (A), synthetic material (B) and synthetic material (C) in weight ratio of 5:5:1. The synthetic material (A) contains polar organic material and inorganic raw material. The synthetic material (B) contains weak polar organic raw material. The synthetic material (C) contains combustion and stabilizer composition.    USE - Microemulsion is used for preparing diesel fuel for internal-combustion engine of car (all claimed).    ADVANTAGE - The microemulsion has excellent storage stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of microemulsion, which involves adding synthetic material (A) and (B), uniformly mixing, adding synthetic material (C) to the obtained mixture and uniformly stirring;    (2) microemulsion diesel fuel, which comprises 7 pts. wt. diesel fuel, 1-2 pts. wt. microemulsion and 2 pts. wt. water; and    (3) preparation of microemulsion diesel fuel, which involves adding microemulsion to water, mixing under stirring for 20 minutes to obtain aqueous microemulsion solution, adding diesel fuel to the obtained solution and uniformly mixing while stirring for 20 minutes.
NOVELTY - Preparing ecological cultivation matrix involves adding water (10-35%) to garden waste, and pulverizing obtained product. Pulverized product is dried to obtain product having moisture content of 60-90%. Municipal domestic sludge is added to obtained product in ratio of 1:0.3-2. Obtained mixture is subjected to steam explosion treatment at 180-260 degrees C and 0.8-2.6 megapascals for 10-20 minutes. Obtained product is cooled to 50-65 degrees C, and fermented under aerobic condition in presence of microbial inoculum (0.2-0.5%) for 5-10 days. Fermented product is sieved, dried, and granulated.    USE - Method for preparing ecological cultivation matrix (claimed).    ADVANTAGE - The method is eco-friendly, and ensures increased production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for preparing ecological cultivation matrix, which comprises:    (A) garden waste storing groove connected to bottom outlet;    (B) sludge storage tank having outlet connected to mixing slot having auger conveyor outlet and groove outlet;    (C) steam generator connected to groove outlet;    (D) steam blasting jar having steam inlet and discharging mouth having automatic valve;    (E) aerobic fermentation tank connected to automatic controller having control valve;    (F) pipeline connected to vent of aerobic fermentation tank and belt filter press; and    (G) belt filter press connected to sieving machine, dryer and pelletizer.
NOVELTY - Longifolene and beta -caryophyllene heavy turpentine are added into reaction vessel, and ethyl acetate as organic solvent, catalyst and oxidant are added and epoxidized. Longifolene is reacted. The reaction mixture is cooled, and catalyst precipitation is separated by filtration. The obtained organic phase is vacuum-distillation-separated, to obtain two oily liquid products. Seed is added to ethylene-caryophyllene oily liquid and crystallized. Crystals are vacuum-filtered and vacuum-dried, to obtain ethylene-caryophyllene crystal products.    USE - Preparation of ethylene-caryophyllene (claimed).    ADVANTAGE - The method enables environmentally-friendly preparation of ethylene-caryophyllene with high purity, by simple method under mild reaction conditions.    DETAILED DESCRIPTION - 65-70 %mass Longifolene and 10-30 %mass beta -caryophyllene heavy turpentine are added into reaction vessel, and ethyl acetate as organic solvent, catalyst and oxidant are added and epoxidized. Longifolene is hardly oxidized, and reacted at 30-50 degrees C for 40 minutes to 12 hours, and samples are gel chromatography analyzed, and beta -caryophyllene and longifolene conversion and yield of ethylene-caryophyllene are determined. The reaction mixture is cooled to 10-20 degrees C, and catalyst precipitation is separated by filtration. The filtrate is removed by phase separation of aqueous phase. The organic phase is recovered by vacuum distillation of organic solvents, and vacuum-distillation-separated, to obtain two oily liquid products comprising longifolene with purity of more than 92% and ethylene-caryophyllene with purity of more than 95%. Small amount of seed is added to ethylene-caryophyllene oily liquid and crystallized. Crystals are collected, vacuum-filtered and vacuum-dried, to obtain ethylene-caryophyllene crystal products with purity of more than 96%.
NOVELTY - The medical device substrate comprises 100 parts biodegradable polymer ingredients and 2-5 parts lubricants. The biodegradable polymer ingredient is polylactic acid base having molecular weight of 2000000. The lubricant is ethylene bis stearamide.    USE - Medical device substrate.    ADVANTAGE - The medical device substrate is degraded by microorganisms, prevents pollution of the environment, and thus improves safety and health.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing medical device, which involves:    (A) drying biodegradable polymer having molecular weight of 2000000 and bis-stearamide at 45-60 degrees C in vacuum for 3-6 hours to form dried pellets; and    (B) placing the dried pellets into injection molding machine hopper at 150-170 degrees C for 4-6 seconds.
NOVELTY - Apparatus comprises (a) exothermic reactor (20) for culturing microorganisms which are processed with organic wastewater (10), (b) heating tank, and (c) heat-batch fermentation tank (30) which is installed with heat exchanger (40).    USE - The apparatus or method is useful for treatment of high concentration organic wastewater (all claimed).    ADVANTAGE - The apparatus minimizes growth rate of microorganism.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treatment of high concentration organic wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of apparatus.    Organic wastewater (10)    Exothermic reactor (20)    Heat-batch fermentation tank (30)    Heat exchanger (40)    Aeration tank (50)
NOVELTY - Stabilizing material comprises organic waste and microorganism inoculums. Microorganism inoculum comprises brown nitrogen-fixing bacteria, adipogenic nitrogen fixing bacteria Pseudomonas fluorescens, Azotobacter chroococcum, Bacillus subtilis, Bacillus, Bacillus firmus or inorganic compound.    USE - Stabilizing material used for bio-fertilizer (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing stabilizing material, which involves:    (A) drying organic waste material, and then decomposing organic waste material;    (B) inoculating microorganism inoculum in decomposed organic waste material and adding inorganic compound; and    (C) crushing the mixture into powder, and pelletizing into pills.
NOVELTY - Oxytetracycline crystallization mother liquor is pretreated and subjected to an organic film having molecular weight cutoff value of 800-2500 Daltons to obtain permeated liquid crystal liquor and membrane retentate. The permeated liquid crystal liquor is subjected to aerobic and anaerobic treatment, and the resultant wastewater has chemical oxygen demand of less than 10 ppm. The membrane retentate is subjected to separation membrane, and the pH of the membrane retentate is adjusted to pH4-pH5, and the resultant product is precipitated to obtain crude oxytetracycline.    USE - Wastewater treatment of oxytetracycline crystallization mother liquor (claimed).    ADVANTAGE - The method efficiently processes oxytetracycline crystallization mother liquor and provides oxytetracycline recyclable product, by simple method.    DETAILED DESCRIPTION - Oxytetracycline crystallization mother liquor is pretreated by adding an acid solution to oxytetracycline crystallization mother liquor, adjusting the pH value to pH2-pH3, and adding 10-50 ppm polyacrylamide. The resultant pretreated mother liquor is subjected to an organic film having molecular weight cutoff value of 800-2500 Daltons to obtain permeated liquid crystal liquor and membrane retentate. The permeated liquid crystal liquor is subjected to aerobic and anaerobic treatment, and the resultant wastewater has chemical oxygen demand of less than 10 ppm. The membrane retentate is subjected to separation membrane, and the pH of the membrane retentate is adjusted to pH4-pH5, and the resultant product is precipitated to obtain crude oxytetracycline.
NOVELTY - Method for fermenting organic solid waste, involves (a) obtaining organic solid wastes as raw materials, adjusting carbon/nitrogen ratio of 20-35:1, and controlling moisture content reaches 55-70%, and (b) adding organic solid waste material to 5-15 %mass gypsum, uniformly mixing materials, and fermenting mixture.    USE - The method is useful for fermenting organic solid waste (claimed).
NOVELTY - Cultivation of Pleurotus eryngii comprises storing Pleurotus eryngii strain at 20-26 degrees C and relative air humidity of 60-65% and culturing with culture medium; taking out, storing at 15-26 degrees C and relative air humidity of 60-65% and culturing with culture medium; taking out, storing at 15-26 degrees C and relative air humidity of 60-65% and culturing with culture medium; taking out, storing at 15-26 degrees C and relative air humidity of 60-65% and culturing with culture medium; and culturing, taking out fruiting body, growing, and culturing.    USE - Method for cultivation of Pleurotus eryngii used for producing microbial fertilizer (claimed).    ADVANTAGE - The microbial fertilizer is rich in zinc and selenium. The product is highly nutritious to human. The method is simple and suitable for large scale production, can recycle waste, and saves manpower and resources.    DETAILED DESCRIPTION - Cultivation of Pleurotus eryngii comprises storing Pleurotus eryngii strain at 20-26 degrees C and relative air humidity of 60-65% and culturing with culture medium for 6-8 days; taking out, storing at 15-26 degrees C and relative air humidity of 60-65% and culturing with culture medium for 34-36 days; taking out, storing at 15-26 degrees C and relative air humidity of 60-65% and culturing with culture medium for 34-36 days; taking out, storing at 15-26 degrees C and relative air humidity of 60-65% and culturing with culture medium for 34-36 days; and culturing for 4-6 days, taking out fruiting body, growing, and culturing. An INDEPENDENT CLAIM is included for producing microbial fertilizer comprising crushing cultured Pleurotus eryngii and germ bran, adding 1-2 wt.% composting agent, and fermenting at 50-70 degrees C and humidity of 55-65% for 5-10 days; and drying, adding active strain, and manufacturing into fertilizer.
NOVELTY - Preparing fertilizer involves crushing herbal raw material (15-25 parts) to obtain particles of size 100 mesh. Mixture of cow dung (10-20 parts), chicken (10-20 parts), and chaff (20-30 parts) is fermented for 45 days. Fermented product is dried to obtain particles of size 100 mesh. Bentonite (2-5 parts), urea (10-20 parts), calcium superphosphate (10-20 parts), ammonium sulfate (10-20 parts), potassium sulfate (15-20 parts), potassium chloride (5-10 parts), zinc sulfate (1-3 parts), borax (2-5 parts), and sodium selenite (1-2 parts) is ground to obtain particles of size 100 mesh.    USE - Method for preparing fertilizer for papaya (claimed).    DETAILED DESCRIPTION - Preparing fertilizer involves crushing herbal raw material (15-25 parts) to obtain particles of size 100 mesh. Mixture of cow dung (10-20 parts), chicken (10-20 parts), and chaff (20-30 parts) is fermented for 45 days. Fermented product is dried to obtain particles of size 100 mesh. Bentonite (2-5 parts), urea (10-20 parts), calcium superphosphate (10-20 parts), ammonium sulfate (10-20 parts), potassium sulfate (15-20 parts), potassium chloride (5-10 parts), zinc sulfate (1-3 parts), borax (2-5 parts), and sodium selenite (1-2 parts) is ground to obtain particles of size 100 mesh. Obtained products are mixed with water, and obtained product is granulated. Obtained granules are dried to obtain fertilizer.
NOVELTY - Wattle structure anaerobic power supply station comprises an anaerobic tank unit, a purification tower, an anaerobic tank heating system and a generator. The construction material for the anaerobic tank is fruticose and plastic film or rubber film. The structure of fruticose is plastic film or rubber film structure.    USE - Used as wattle structure anaerobic power supply station.    ADVANTAGE - The power supply station realizes clean energy production, ensures recycling of the farm, the livestock and the urban waste, and is environmentally friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the wattle structure anaerobic power supply station.
NOVELTY - Glass steel anaerobic power generating gas station comprises anaerobic tanks, purification tower, anaerobic tank warming system, generator sets having four parts which is constructed of anaerobic tank glass steel building materials, glass fiber reinforced plastic materials.    USE - The gas station is useful for generating biogas from the wastes (claimed).    ADVANTAGE - The gas station produces efficient biogas fluid and biogas. The anaerobic tank column, the purification column, generators, pumps and gas pressure, boiler together can complement each other. The raw materials is saved and the process is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the production of bio gas using glass steel anaerobic power generating gas station comprising using of the town waste, farm waste, wastewater and straw as raw material, and carrying out multi stage multi-stage anaerobic fermentation which includes internal mixing, insulating, warming, automatic alarming or using any other alarming devices, stirring the body of the tank with the biogas fluid and warming to obtain biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the glass steel anaerobic power generating gas station.
NOVELTY - Reducing application of whole film double-furrow sown maize soil closed herbicide involves deep ploughing of double furrowed soil after maize crop harvesting and applying high-quality manure, urea and diammonium phosphate to the soil for autumn or the following year. Herbicides are uniformly sprayed in windless conditions after harrowing and forming ridges at the bottom of the ditches formed by the ridges, by using a spray machine. Film is covered over the whole ground. Sowing of maize is carried out in late April and field management is carried out.    USE - Reducing application of whole film double-furrow sown maize soil closed herbicide (claimed).    ADVANTAGE - The method enables applying whole film double-furrow sowing maize soil closed herbicide with reduced herbicide dose and residues in a cost-effective, eco-friendly and simple manner.    DETAILED DESCRIPTION - Reducing application of whole film double-furrow sown maize soil closed herbicide involves deep ploughing of double furrowed soil after maize crop harvesting and applying 45000 kg/hm2 high-quality manure, 300 kg/hm2 urea and 225 kg/hm2, 64% diammonium phosphate to the soil for autumn or the following year. Herbicides are uniformly sprayed in windless conditions after harrowing and forming ridges at the bottom of the ditches formed by the ridges, by using a spray machine. Film is covered over the whole ground after spraying herbicide. Sowing process is performed by sowing the maize in late April. Field management is carried out after sowing.
NOVELTY - Invention relates to a method for water electrolysis under pressure in an electrolysis system which includes accumulators operating with a working cycle closed through water. The method includes supplying dc voltage from a power supply and water; partial decomposition of the water with current during water electrolysis with separate generation of hydrogen and oxygen; separating said gases from water in gas separators while ensuring pressure equilibrium of said gases during the generation process and filling system vessels with the obtained gases, wherein generation of the gases and filling the vessels with said gases is carried out in turns, with pneumatic isolation of the gas separators of the system from the vessels when generating hydrogen and oxygen, and from the electrolysis cell when filling the vessels, wherein before filling the vessels the gas separators are isolated from each other and then reconnected after filling.    USE - Chemistry.    ADVANTAGE - Enabling generation of hydrogen and oxygen with the same pressure without power load on cell membranes and filling vessels of the electrolysis system with gases with different pressure without losing gases owing to a two-step operating algorithm of the electrolysis gas accumulator, ie time-separation of the processes of generating gases and filling vessels with said gases.
NOVELTY - Method of making of secondary energy carrier - hydrogen by wind energy conversion includes wind kinetic energy conversion by means of sailing mover to the kinetic energy of ship movement in open ocean areas with powerful air flows, and then by means of the hydraulic turbine and electric generator to the electric energy, used for water decompounding to hydrogen and oxygen with hydrogen liquefaction and accumulation in cryogenic tanks. The twin-hull boat with sail mover is used as floating ship, it works under physical principle of wing lift. The hydraulic turbine and electric generator are used temporarily as ballast, moving them through vertical, ensuring required twin-hull boat stability under strong wind blasts.    USE - Power industry.    ADVANTAGE - Increased use factor of wind energy and power of sailing mover.2 dwg
NOVELTY - Method of production of liquefied methane with high purity, including pre-cooling of the liquid hydrocarbons released during gas compression, its separation to process flow, that is cooled, reduced and heated by product and process flows, and product flow, that is cooled, reduced and separated with production of liquefied methane and separation gas. The natural gas is preliminary subjected to soft steam catalytic reforming together with water condensate and demineralised water with reformate production. The reformate is mixed with heated process flow and compressed by the compressor equipped with internal combustion engine as drive, to produced liquid hydrocarbons released during gas compression, its pre-cooling is performed by additional coolant to temperature not below temperature of hydrating. Prior to the liquid hydrocarbons released during gas compression separation to the process and product flows it is dehydrated and cleaned from carbon dioxide with production of the methane with high purity, water condensate and off-gas containing CO2, at that the separation gas is heated by product and process flows, mixed with off-gas containing CO2, and used as fuel for compressor driving.    USE - Machine building.    ADVANTAGE - Increased yield of liquid methane with high purity.3 cl, 1 dwg
NOVELTY - The method involves cooling an impurity-containing gas mixture until a temperature equal or lesser than a solidification temperature of an impurity solidifying in a heat exchanger (3). Cooling passages of the exchanger are covered with a coating and physically or chemically treated, where the coating and the treatment limit or prevent formation and adhesion of the solidified impurity on a surface of the passages. Water (5B) and ice (19) of the solidified impurity exiting the passages are collected. The partially liquefied gas mixture is withdrawn from the heat exchanger and sent to a cold end.    USE - Method for cooling and purification of an gas mixture e.g. air, mixture of hydrogen, carbon monoxide and methane, and mixture of carbon dioxide, hydrogen, carbon monoxide, methane, oxygen, nitrogen and argon, containing an impurity i.e. water (all claimed), utilized for surface treatment of exposed metal surfaces of an atmospheric element e.g. airplanes, wind mills and pylons.    ADVANTAGE - The method enables cooling and purification of the gas mixture in an energy-efficient manner. The method enables simplification and elimination of downstream treatment plants. The method enables simplification of design and/or operation of downstream equipments i.e. evaporators.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for cooling and purification of an impurity-containing gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating air separation by a cryogenic distillation process using an aluminum heat exchanger.    Compressor (C)    Heat exchanger (3)    Water (5B)    Ice (19)    Fractionating column (27)
NOVELTY - This new utility model claims of one of biomass fixed bed gasification furnace is evenly stable blank structure, it comprises rotary kick-out device and cone shell, rotary kick-out device is rotary drawing end from up to down through feedstock after passage in enter into biomass fixed bed gasification furnace below the cone shell is rotary kick-out device is, outside wall of cone shell and biomass fixed bed gasification furnace and furnace wall between forming blank, circle drawing end feedstock wherein the feedstock passage rotary kick-out device is located at upper part. By setting rotary kick-out device and biomass raw material by rotary kick-out disordered after through cone shell after shunting in feedstock passage, blank space along different direction from falling to biomass fixed bed gasification furnace inside, form stable uniform blank, forming no height difference on the same section of material layer, can facilitate material position meter for furnace top material position and determine, implementation biomass fixed bed gasification furnace and add material accuracy of charging time, furnace top temperature maintain stable, which is good for production and response and stability.
NOVELTY - This new utility model claims of one of biomass fixed bed gasification furnace and uniformly air inlet structure, comprising embedded in the annular box, bottom of furnace wall internal wind pipe and multiple annular nozzle, the whole annular wind box through air inlet pipe and air blower connected, back bottom pipe and centre the biomass fixed bed gasification furnace top extending to two terminal centre cloth head, bottom wind pipe through the annular bellows side bear the heat layer and annular bellows connected, center and center nozzle head and cloth biomass fixed bed gasification furnace internal connected, via the annular air inlet uniformity and center, can make air flow uniformly stable, forming uniform air inlet structure, maintain oxidation reaction zone steady. The structure is set with simple structure, easy realization, good for solving furnace in oxidation reaction zone not uniform result in the gasification furnace problem, for controlling reaction zone temperature and promoting response speed are obvious effect.
NOVELTY - This new utility model relates to a kind of outside can at one biomass gasification furnace high temperature cloth wind pipe and line cleaning, comprising air inlet channel and air inlet channel week and water cooling jacket sleeved on the air inlet passage provided with an air inlet and an air outlet, the air outlet of can is provided with cloth and head. The utility model has new water jacket in the air inlet passage coat, to temperature in gasification furnace can carry out control, the air outlet of the air inlet passage and the can is set with head cloth, back cloth head down, biomass fuel gas still can from air outlet, gasification furnace still can make maintain low load operation, does not need to be stopping can realize cloth head for on-line cleaning, reducing have cleaning strength. This new utility model can applied to biomass gasification furnace cloth wind.
NOVELTY - This new utility model claims of one of biomass gasification furnace grate and automatic discharging device, it comprises at least one of automatic slag discharging unit, automatic slag discharging unit includes level transmission device, fire grate and the temperature measuring thermoelectric couple below the biomass gasification furnace, after temperature work end of the thermocouple through furnace wall extending in the biomass gasification furnace, the horizontal transmission device and a temperature measuring thermoelectric couple between mounted with signal conversion controller, level transmission device and the transmission connecting rod and the furnace grate bars connected with the reciprocating moving transmission connecting rod and the horizontal transmission device of temperature thermocouple and signal switching linkage control controller. By is set with temperature measuring thermoelectric couple interaction and control the horizontal transmission device, when time temperature measuring thermoelectric couple detecting furnace bottom temperature offset high, feedback signal to signal conversion controller, the signal switching controller activating level transmission device, transmission connecting rod make horizontal reciprocating movement, drive fire grate, complete automatic slag to control bottom furnace reaction temperature.
NOVELTY - This new utility model claims of a kind of one with using the waste heat steam air unite biomass gasification device, it comprises gasifier, air pre-heater, steam generator and air air blower, the fuel gas gasifier and air pre-heater outlet connection, air pre-heater and air blower air connected, outlet channel of air pre-heater comprises gasification air pipe and combustion-supporting air pipe, combustion-supporting air pipe connected to the steam generator hearth, gasification air pipe connected to oxidation zone of gasifier, oxidation by discharging spiral and connected with hearth, hearth set inside with steam coil pipe, steam pipe and one end plate through water inlet pipe and water pump connected with the water inlet, the other end steam disk pipe of reduction cell by the steam pipeline and connected with gasifier. By waste heat of biomass fuel gas and hot air in preheat air pre-heater, formed with using the waste heat steam air unite biomass gasification integrated circulation, full using waste heat of hot biomass fuel gas and coal slag, increase the utilization rate of the whole system heat.
NOVELTY - This new utility model relates to one kind of biomass fuel gas high efficient spray purification device, comprising spray tower, the spray tower equipped with spray in inside channel and outside channel spray, the spray channel in its top end connected with air inlet pipe, the spray in the bottom channel and spray out channel bottom connected, the spray out channel and top is connected with exhaust pipe, the inner spray in passage provided with atomizing shower nozzle, in the spray out passage equipped with multi-grade spray unit. In this new utility model through setting spray inside channel and outside channel in spray at the same spray tower, and is set with atomizing shower nozzle and spray out channel in on channel inner spray is set with multistage spray unit, using biomass fuel gas through out one level spray and spray spray passage in the multistage spray channel, biomass fuel gas by spray tower travel long, long time and spray atomizing water contact, contact area large, can realize biomass fuel gas full spray, for biomass fuel gas has good purification effect. This new utility model can applied to biomass fuel gas remove tar.
NOVELTY - Inside of one large biomass stove, comprising stove body (1), hopper (2) and set on stove body (1) of the pot body (3), the stove body (1) set with combustion chamber (4), a combustion chamber (4) is located in the gasification chamber (5) of upper part, wherein said combustion chamber (4) side wall is set with annular flue (6) and multi-circle of parts is set with the smoke outlet (7), smoke outlet (7) and annular flue (6) connected, annular flue (6) and smoke on stove body is set with the outside (17) connected. This new utility model is simple structure, would show no fire deviating imaginary, the combustion heat can be uniformly distributed on the pot body, is to use efficient hot can, smoke exhaust effect is good.
NOVELTY - The device (10) has a container portion (11) which accommodates water, and an electrode portion (12) that electrolyzes the water. A voltage supply unit (13) is configured to carry out voltage supply by setting first voltage value as an average supply-voltage value in first voltage supply period, and carry out voltage supply by setting second voltage value lower than first voltage value as average supply voltage value in second voltage supply period.    USE - Hydrogen water generator device.    ADVANTAGE - The production of ozone gas is greatly suppressed and the reduced hydrogen water for high quality drinks is able to be produced in a short time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen water generator method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen water generator device.    Hydrogen water generator device (10)    Container portion (11)    Electrode portion (12)    Voltage supply unit (13)    Housing (41)
NOVELTY - Continuous fuel production, comprises: producing a cover gas comprising at least hydrogen and carbon monoxide; and utilizing the cover gas with respect to a first non-oxidation process to produce at least one reaction product.    USE - The method is useful for continuous fuel production, where the fuel is liquid fuel comprising at least gasoline, diesel or aviation fuel (claimed).    ADVANTAGE - The method is rapid for the production of liquid fuels from biomass or other compounds that include carbon-oxygen-hydrogen compounds.
NOVELTY - Method for pretreating lignocellulosic biomass involves reacting lignocellulosic biomass with acid-base mixture catalyst having pH value of 1-4.    USE - The method is useful for pretreating lignocellulosic biomass which is useful in manufacturing ethanol. The lignocellulosic biomass is one chosen from straw, giant Miscanthus sinensis, sugarcane byproduct, corn byproducts, switchgrass, poplar, palm oil byproducts and oak (all claimed).    ADVANTAGE - The method produces high yield of ethanol, is simple, and cost-effective, and makes use of cost-effective equipment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing ethanol from lignocellulosic biomass which involves performing simultaneous saccharification and fermentation of biomass obtained after pretreatment, where simultaneous saccharification and fermentation is performed by one-pot process.
NOVELTY - System (200) for continuous fuel production, comprises: a cover gas production chamber configured to produce a cover gas comprising at least hydrogen and carbon monoxide; and a non-oxidation process chamber configured to utilize the cover gas with respect to a first non-oxidation process to produce at least one reaction product.    USE - The system is useful for continuous fuel production, preferably liquid fuel comprising at least gasoline, diesel or aviation fuel.    ADVANTAGE - The system provides rapid continuous process for the production of liquid fuels from biomass or other compounds that include carbon-oxygen-hydrogen compounds.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic illustration of the system for conversion of carbon-oxygen-hydrogen compounds into hydrogen, carbon monoxide and/or liquid fuel.    Auger (115)    System (200c)    Tube furnace (250)
NOVELTY - Manufacture of lignin derivative involves performing subcritical water treatment of biomass residue which is bioethanol byproduct of waste liquid obtained by pulp manufacture process. The number average molecular weight of lignin derivative is 300-2000.    USE - Manufacture of lignin derivative used in resin composition (all claimed) used for forming lamented board. Uses include but are not limited to wooden building materials, wooden decorative board, molding material, friction material and templates.    ADVANTAGE - The method enables manufacture of lignin derivative having excellent reactivity and moldability. The resin composition containing the lignin derivative is capable of providing laminated board with excellent mechanical characteristics, durability and external appearance.
NOVELTY - The purifier has a purifier part and a water washing tank that are respectively connected with a cooling water tank and a sewage tank. The cooling water tank is connected with an air inlet tube that is connected with the water washing tank, an air water separator and a multi-pipe condenser. A water washing box is connected with a water pump. A pipeline is connected with the sewage tank. A side filtering cylinder is connected with a drain port.    USE - Biomass pyrolysis gas purifier.    ADVANTAGE - The purifier is simple in structure and environment friendly, and has high purification effect and safe reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass pyrolysis gas purifier.
NOVELTY - This new utility model claims of one liquid phase pulse discharge circuit plasma of hydrogen preparing device, the hydrogen preparing device comprising: liquid phase reaction chamber, pressure cover in liquid phase reaction chamber on the foundation bed, the foundation bed and the liquid phase reaction chamber containing reactant and composed of complete manufacture hydrogen reaction of closeness space; the first electrode in said closeness space in place, and is set with the relative and the second electrode, the first electrode and the second electrode are made of metal material, and said closeness space and mutually connect the guide gas hole, the utility model is novel effective enlargement of space distribution and density of plasma and promote generation of hydrogen.
NOVELTY - This new utility model claims of one of sewage biological alcohol base fuel and conversion device, comprising a tank body, the tank body upper part setting a feeding port, the lower part setting discharging port, provided with filter screen at inside of tank body to discharge port, the tank body from bottom to top the following filling with charcoal block layer, big and small bc pebble layer and sand layer. The utility model use new tank filling composite material filtering layer, material is simple, the effect is good. structure, using suitable.
NOVELTY - This new utility model claims of a kind of one with the biomass gasification furnace combustion gun. Upper part upper part upper part of the new utility model includes furnace body (1), a furnace body (1) side is set with side feedstock port (2), a furnace body (1) lower part is set with converying belt (3), converying belt (3) provided with a combustion cavity (4), a combustion cavity (4) is equipped with heat storage cavity (5), a combustion cavity (4) through way hole (6) and heat storage cavity (5) is connected, the heat storage cavity (5) is provided with combustion gun (7), a combustion gun (7) and includes heat storage cavity (5) is connected vertical tube (8), vertical pipe (8) is connected with inclined downward and inclined pipe (9), inclined pipe (9) is set with the lower part (10). This new utility model not only can effective utilize hot can, reducing loss, increase efficiency, and this utility model is hot air discharge environmental protection clean and new type. This new utility model not only can effective utilize hot can, reducing loss, increase efficiency, and this utility model is hot air discharge environmental protection clean and new type.
NOVELTY - This new utility model relates to one of organic substance waste clean fuel manufacturing device, it comprises storage box, lower side is set with discharging port A, has a discharge port A is set with the lower part with pulverizer, the pulverizer left side is set with discharging port B with the lower discharge port is set with B with mixing pool, mixing pool connected with conveying pump, conveying pump connected with the reaction kettle, the reaction kettle connected with condenser, lower side is set with with arrange, arrange the lower part set up with valve for hopper, hopper for set up on left side of machine body, the machine body is set with inner process chamber A and has process chamber B, the machine body left side connected with motor, a machine body lower side formed with a water outlet, the machine body right side is set with a discharging port with C, the discharging port at the lower part is set with right side with inclined plate, the lower inclined plate is set with right side with driven wheel, driven wheel connecting with driving wheel through transmission belt, transmission belt out side set with shell, shell upper part set with microwave tube, shell of two side end is set with temperature meter A and thermometer with B, driving wheel is set with lower part with hopper, the new utility model has economic benefit is good.
NOVELTY - The utility model is a new supply of a biomass of diesel oil decolouring system, comprising a biomass diesel oil by decolouring process of decolouring reaction unit, a decolouring reaction unit comprises a main body and decolouring in the decolouring reaction is set on the body of stirring structure, and the decolouring reaction a... transporting a hollow air distribution unit, and a output end of the decolouring reaction in turn connected with a filtering unit and a storage unit, the storage unit and pipeline connected with the vacuum processing unit, a vacuum processing unit providing the vacuum environment of the reaction output end output the biomass diesel oil via a vacuum filter filtering a process after storing in a storage unit a. The system has simple technique, low cost, a high efficiency, and produce a biomass diesel oil is clean and sanitary, it is more environmental protection.
NOVELTY - This utility model provides a biomass granular fuel manufacturing device, comprising crushing bucket, an extruder, extrusion head, a transmission belt, a transmission shell, stirring bucket,, controller, button, support, a dust removing device, and dust-removing device, the crushing bucket, a dust removing device, the stirring bucket, an extruder, a cooling device connected in turn, the crushing bucket is provided with feedstock mouth and discharging mouth, said bucket internal installed with crushing, crushing knife, iron corresponding to the position is opened with mounting port, this utility new model is in stirring bucket installed with dryer, for drying and stirring operation combined with the drying process using the more complete, the of extruder raw material entering into the dry, ensuring of complete success of extrusion operation. In this utility model, dryer stirring bucket is located at internal side, which avoids stirring when dropping raw material dryer in the condition of generating.
NOVELTY - The facility (9) has a pre-treatment unit (3) that converts the organic waste into low-molecular weight compounds through hydrolysis. A post-treatment unit (4) ages a portion of fermented compost supplied to a post-aging tank. The pre-treatment unit is isolated from the dry anaerobic fermentation unit (1) through a first barrier. The post-treatment unit is isolated from the dry anaerobic fermentation unit through fixed barrier. A gate is provided in a portion of an upper portion of post-aging tank, to receive the organic waste or discharge the produced compost.    USE - Dry anaerobic composting facility for producing biogas as energy source of self power-generator.    ADVANTAGE - The facility minimizes energy loss using geothermal heat and efficiently uses ground space. The anaerobic fermentation is performed and production of compost is improved. The maintenance and management costs are reduced through full-automation of discharge of compost produced by pre-treatment, anaerobic fermentation and post-treatment of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the dry anaerobic composting facility.    Dry anaerobic fermentation unit (1)    Pre-treatment unit (3)    Post-treatment unit (4)    Power generator (5)    Dry anaerobic composting facility (9)
NOVELTY - Antibacterial composition comprises isolated and/or concentrated extracts from liquid fraction or wash waters of steam pretreated corn stover, wheat straw, rice straw, bagasse, corn fiber, empty fruit bunches or grass adapted for use in first generation bioethanol fermentations of primarily starch biomass by yeast and effective against lactic acid bacteria.    USE - The antibacterial composition is used in yeast fermentation to produce ethanol (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of yeast fermentation to produce ethanol, which involves (a) adding the composition to the fermentation mixture, or (b) preparing a non-sterile yeast fermentation mixture comprising primarily starch biomass and optimized levels of fermentation inhibitors that inhibit contaminating bacterial growth and/or lactate production while having no affect on ethanol fermentive yeast, and fermenting the fermentation mixture, where optimized levels of fermentation inhibitors are achieved by addition of isolated and/or concentrated extracts from liquid fraction or wash waters of pretreated lignocellulosic biomass.
NOVELTY - Treatment of a cellulose-containing material involves: (a) providing a material comprising cellulose; and (b) treating the material in an aqueous solution comprising sulfite or bisulfite, where the treating is at a pH ranging from 0-10 at a temperature of 130-250 degrees C.    USE - The method is useful for the treatment of a cellulose-containing material for use in producing ethanol, and a biofuel or biochemical (claimed).    ADVANTAGE - The method provides sulfite pretreatment processes to overcome recalcitrance of lignocellulose for robust conversion of biomass (SPORL) and processes to reduce energy consumption by optimizing solids-loading and size reduction. Also, the method is particularly suitable for feedstock with strong physical integrity, such as wood, forest biomass, bamboo, giant reed, wood crops, etc. The method may comprise (1) conducting size-reduction of feedstock after chemical or biological pretreatments; (2) using low solids-loading in milling, such as disk milling solids-loading between 0.1-50%, even more particularly between 1-35%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a product comprising ethanol.
NOVELTY - HdrABC nucleic acid molecule comprising a mutation is new.    USE - The HdrABC nucleic acid molecule is useful for encoding HdrB polypeptide, and for producing methane (all claimed).    ADVANTAGE - The HdrABC nucleic acid molecule: provides increased rate of methane production; and is capable of producing methane in a method that requires less feedstock than current methods, and saves plant downtime and labor costs.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a mutant HdrB polypeptide;    (2) a microorganism comprising the nucleic acid molecule or the mutant HdrB polypeptide; and    (3) producing methane, comprising culturing the microorganism under appropriate conditions.
NOVELTY - A recombinant host cell comprising deletion, insertion or other alteration in endoglucanase (EGl-7) gene, is new, where deletion, insertion or other alteration inactivates the above-mentioned gene and prevents EGVII polypeptide production.    USE - The recombinant host cell is useful for producing composition which is useful for cleaning purpose, hydrolyzing lignocellulosic biomass substrate (all claimed), softening and improving feel and appearance of cotton fabrics, and degrading wood pulp or other biomass into sugars (e.g. for bio-ethanol production), and in feed compositions. The composition for cleaning purpose includes household detergents, stonewashing compositions, biopolishing composition and laundry detergents.    ADVANTAGE - The recombinant host cell produces composition which improves feel and appearance of cotton fabrics, and exhibits resistance to surfactants, preferably linear alkyl sulfonates, improved performance under thermal stress, increased or decreased cellulolytic capacity, and/or high level expression in vitro.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) antisense oligonucleotide complementary to mRNA that encodes the EGVII polypeptide comprising a 230 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, where upon exposure to endoglucanase-producing host cell, the oligonucleotide decreases or inhibits production of endoglucanase by the host cell;    (2) composition produced by culturing the recombinant host cell under suitable fermentation conditions to produce proteins; and    (3) method of hydrolyzing lignocellulosic biomass substrate, involves using the above-mentioned composition.
NOVELTY - This utility model belongs to wood processing technique area, especially relates to a wood shavings processing pellet machine, comprising pedestal, the pedestal set with inner cavity, the inner cavity provided with collecting, on the pedestal set with box, in said box set with mould, two side box is respectively set with the first locating block, the second locating block, the first locating block hinged with the first baffle plate, the second locating block hinged with the second baffle plate, the mould set with main shaft, the main shaft on two side respectively set with the first connecting rod, the second connecting rod, the first connecting rod connected with the first press roller and the second connecting rod connected with the second pressure roller, in said box set with a sieve plate, the sieve plate is the first press roller and the second press roller and upper part, the box top equipped with feedstock wherein, on the pedestal also set with support platform, on the supporting platform equipped with electrical machine, the electrical machine connected on rotating shaft, rotating shaft and the outer sleeve shaft with synchronous belt.
NOVELTY - The utility model is a new supply of a honeycomb shape of straw compression block production device, a crushing device, stirring device and forming device, crushing device comprises motor, crushing shaft, crushing motor provided with a driving wheel, the stirring shaft end provided with driven wheel, driving wheel and driven wheel through transmission belt connected with the stirring device comprises stirring chamber and stirring shaft, stirring shaft equipped with a bar, stirring shaft stirring chamber located within the molding device comprises hydraulic pressure device, compression chamber, compressor shaft, a compressing and cutting chamber, hydraulic pressure device and compressor shaft connected with the shaft end provided with compression, the compressed compression chamber, compressing chamber and cutting chamber connect, this utility new type has simple structure, using suitable, provided with compression device, a straw for full compression, not only saves a converying volume, at the same time too suitable carrier, provided with a pipe way, use is made of straw honeycomb coal is burning more full, increase of efficiency of use, provided with a sleeve forming device, increase of efficiency of manufacture.
NOVELTY - The utility model claims a new electrolytic water of hydrogen preparing device, comprising electrolytic groove, electrolytic groove through pipeline and a hydrogen cooling device and cooling device connected with oxygen, hydrogen cooling device via a hydrogen pipeline connected with separator, hydrogen separator by pipeline and washer connected with hydrogen, hydrogen scrubber through pipeline and dewatering tank connected with, dehydrating tank by pipeline and molecule sieve connected with, molecule sieve by pipeline and hydrogen storage tank connected with the oxygen cooling device by pipeline and oxygen separator connected with the oxygen separator by pipeline and oxygen scrubber connected with the oxygen scrubber by pipeline and oxygen storage tank connected with the electrolytic groove through a pipeline and remove salt water tank and alkaline liquor tank connected with, remove salt water tank and alkaline liquor tank connected with a pipeline and a water storage tank. The utility model structure is simple, a suitable operation, hydrogen purity.... hydrogen efficiency is high, the storage effect is good, the simplified of industrial process and industrial cost.
NOVELTY - The utility model claims a new water of electrolytic prepared hydrogen system, especially relates to a kind of... electrolytic pure hydrogen and oxygen in a system. The utility model comprises a electrolytic slot, hydrogen cooling device, hydrogen liquid separator, steam-water separator and hydrogen storage tank, hydrogen electrolytic groove separately connected and pure water device, alkaline liquor device, oxygen and hydrogen cooling device cooling device, cooling device and hydrogen liquid hydrogen separator, hydrogen-water separator, a glue purifier, molecule sieve deaerator, remove nitrogen and a hydrogen storage tank connected in turn, the bottom cooling device and electrolytic groove connected hydrogen, hydrogen separator bottom liquid and liquid collector connected, oxygen cooling device and a liquid separator, a glue purifier, remove nitrogen purifier and oxygen storage tank connected in turn, molecule sieve a deaerator and a pressurizing device and oxygen storage tank connection. This new utility model structure is simple, operation is convenient, in a hydrogen of high purity, at the same time carry out a purification recovery for oxygen, with high economic benefit.
NOVELTY - Enzymatic hydrolysis of cellulosic biomass involves providing lignocellulosic material, preparing mixture of lignocellulosic material in water, pretreating mixture with one or more acids, adjusting pH of the stream (a) with a base, obtaining a stream (b), treating the stream (b) with sodium sulfite at a desired temperature for a desired time period, obtaining stream (c), contacting stream (c) with one or more cellulolytic enzymes, obtaining a sugar rich final stream, subjecting the final stream to a fermenting yeast, and obtaining ethanol.    USE - Enzymatic hydrolysis of cellulosic biomass e.g. corncob, corn stover and sugarcane/beet bagasse for producing ethanol used as fuel.    ADVANTAGE - The method enables improved and efficient enzymatic hydrolysis of cellulosic biomass, without loss of lignin and sugars, by economical process.    DETAILED DESCRIPTION - Enzymatic hydrolysis of cellulosic biomass involves providing lignocellulosic material, preparing mixture of lignocellulosic material in water, pretreating mixture with one or more acids at a desired temperature for a desired time period, obtaining stream (a), adjusting pH of the stream (a) with a base, obtaining a stream (b), treating the stream (b) with sodium sulfite at a desired temperature for a desired time period, obtaining stream (c), contacting stream (c) with one or more cellulolytic enzymes at desired temperature for a desired time period, obtaining a sugar rich final stream, subjecting the final stream to a fermenting yeast, and obtaining ethanol.
NOVELTY - Manufacture of biodiesel involves mixing organic solvent, microalgae lipid and methanol, esterifying the mixture, adding catalyst to the esterified product, esterifying the mixture and recovering microalgae oil.    USE - Manufacture of biodiesel (claimed).
NOVELTY - The method involves combusting mixture of methane synthesis gas (1), blowing gas (2), processing mixed coal (3), and processing hot air in a three-waste combustion furnace (4). Obtained hot gas is passed through a temperature dust remover (5) and a smoke desulfurizing tower (13). Ash is produced and transferred to a base slag (23) through a belt machine (21). A lime base (33) and a liquid alkali (34) are desulfurized and transmitted to a liquid alkali desulfurizing regeneration pool (32). Regeneration liquid is received by smoke desulfurizing tower through the regeneration pool.    USE - Three-waste mixed gas burning furnace production method.    ADVANTAGE - The method enables preventing environment from being polluted by flue gas, waste water and waste residue.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a three-waste mixed burning furnace production method.    Methane synthesis gas (1)    Blowing gas (2)    Processing mixed coal (3)    Three-waste combustion furnace (4)    Temperature dust remover (5)    Smoke desulfurizing tower (13)    Belt machine (21)    Base slag (23)    Liquid alkali desulfurizing regeneration pool (32)    Lime base (33)    Liquid alkali (34)
NOVELTY - The utility model claims a new a zero liquid discharge device, a marsh gas pool, a marsh gas pool top part formed so as to seal the marsh gas pool top has a biogas from a pool of liquid leakage, the marsh gas pool by the first liquid outlet pipe connected to storage a biogas, a biogas storage pool through the second liquid outlet pipe connected to a sediment, the sediment pool by biogas liquid lifting pipe connected to the liquid storage regulating a biogas, a biogas liquid storing pool by a third liquid outlet pipe connected to irrigation outlet, a biogas lifting pipe is set with upper so as to improve biogas slurry with the water pump. This new utility model is simple structure, reasonable design, a liquid not only can be a liquid, but also can be a sealing marsh gas pool top, effective to prevent air leakage, a biogas liquid storing pool itself has a larger power can, can well realize to crops for long distance without power.
NOVELTY - The method involves cooling biogas in a cooling column (5). The biogas is heated and passed in a cleaning column (1) through activated carbon. An impregnated activated carbon is passed in a biogas filter and a final sedimentation column (3). The biogas is switched to a side part. The biogas is cooled in the cooling column, where the biogas is heated in another cleaning column (2). The biogas is filtered in another final sedimentation column (4). The cleaning columns, the sedimentation columns, an electric valve (8), a blower (6) and a compressor and a safety burner (7) included in a device.    USE - Method for upgrading biogas in a gas conditioner.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gas conditioner.    Cleaning columns (1, 2)    Final sedimentation columns (3, 4)    Cooling column (5)    Blower (6)    Safety burner (7)    Electric valve (8)
NOVELTY - The method involves passing percolate from a reactor through a pneumatic valve (9). A cleaning opening (8) is formed into a main collecting shaft (5), where the percolate is transported into a thick container (3). The percolate is passed into a main percolating vessel (1). Positioned sensors, a percolating pump, an automatic device are utilized for adjusting pH value in a closed conduit system. A flow meter is arranged into an electric pneumatic valve that is actuated by a servomotor and a manifold. A nozzle is utilized for passing sprayed biomass in the reactor.    USE - Method for adjusting percolate in container biogas stations.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for adjusting percolate in container biogas stations.    Main percolating vessel (1)    Fine container (2)    Thick container (3)    Main collecting shaft (5)    Cleaning opening (8)    Pneumatic valve (9)
NOVELTY - Separating and purifying osthol and imperatorin from fructus cnidii comprises crushing common cnidium fruit, soaking in cold anhydrous ethanol, extracting, filtering extraction liquid, vacuum concentrating to obtain extract, dispersing in water, extracting with petroleum ether, combining petroleum ether layers, vacuum distilling, dissolving in methanol, filtering, supercritical fluid chromatography separation, where the mobile phase is supercritical fluid, modifier is methanol, separating, detecting by UV detector, and collecting target component fraction according to the detection signal.    USE - The method is useful for separating and purifying osthol and imperatorin from common cnidium fruit (claimed).    ADVANTAGE - The method: utilizes supercritical carbon dioxide for purification process; does not use organic solvent harmful to environment; and provides product without harmful residues.    DETAILED DESCRIPTION - Separating and purifying osthol and imperatorin from fructus cnidii comprises (a) crushing common cnidium fruit, adding cold anhydrous ethanol, soaking, extracting, filtering extraction liquid, vacuum concentrating to obtain extract, dispersing in water, extracting with petroleum ether, combining petroleum ether layers, and vacuum distilling to obtain fructus cnidii extract, and (b) dissolving fructus cnidii extract in methanol, filtering, carrying out supercritical fluid chromatography separation, with C18 chromatographic column, where the mobile phase is supercritical fluid, modifier is methanol, separating, detecting by UV detector, and collecting target component fraction according to the detection signal.
NOVELTY - Preparing pymetrozine, comprises (i) taking acetamido triazinone, carrying out acid hydrolyses using acid solution to generate aminotriazinone acid, (ii) immediately condensing with nicotinaldehyde solution to generate pymetrozine salt, and (iii) carrying out neutralizing treatment with qualified alkali and processing.    USE - The method is useful for preparing pymetrozine (claimed).    ADVANTAGE - The method: reduces generation of impurities, improves conversion of raw materials, pymetrozine production of 95-97 %, yield of 2-5 %; is environmentally friendly and suitable for industrial production.
NOVELTY - The device has shaft (3) which is connected to motor (2). The speed of the motor is adjusted by governor (1). An excitation light source (6) is arranged above photoelectric rotary drum anode (5). A platinum cathode (12) is placed in cathode region (9). The photoelectric rotary drum anode is immersed in the anolyte (10). A catholyte solution (11) is acidic solution. The platinum cathode is connected with the carbon brush through an external circuit. The platinum cathode is connected to the catholyte within the cathode region which is sealed in a nitrogen atmosphere.    USE - Photochemical cell device for treating alcohol-containing waste water using high chroma hydrogen-electricity generation.    ADVANTAGE - The simultaneous power generation and hydrogen production are realized, the necessity of adding voltage is prevented. The efficiency of the catalytic hydrogen production is ensured and the cost of platinum plate is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the photochemical cell device for treating alcohol-containing waste water.    Governor (1)    Motor (2)    Shaft (3)    Brush (4)    Photoelectric rotary drum anode (5)    Excitation light source (6)    Cathode region (9)    Anolyte (10)    Catholyte solution (11)    Platinum cathode (12)
NOVELTY - The system has deploy pool that is connected with medium sand removing pool. The deploy pool is set with stirring device. A substance removing sand pool is set with uniform quality in the sand device. The deploy pool is connected with medium sand removing pool. An anaerobic fermentation unit comprises a multi-anaerobic reactor connected with sand pool. A separating unit comprises sediment pool and solid-liquid separating machine. A precipitate pool is connected with anaerobic reactor and solid-liquid separating machine by the pipeline liquid.    USE - System for continuously processing livestock organic waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for continuously processing livestock organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the system for continuously processing livestock organic waste.(Drawing includes non-English language text)
NOVELTY - Producing alcohol involves adding solid food waste products in storage tank for separation. The separated mixture is distilled and then added into mixer for crushing. The crushed mixture is added to tank for hydrolysis. The hydrolyzed mixture is added into cooking tank, which is controlled by power panel that includes a boiler for saccharification to obtain glucose. The obtained glucose is transferred to rest tank, which is added with yeast for saccharifying glucose. The saccharified mixture is added to chamber for de-distillation, where the chamber is equipped with pump.    USE - Method for producing alcohol used as fuel and food product, and in pharmaceuticals (claimed) and cosmetics.    ADVANTAGE - The method enables to increase production of alcohol, and recycle waste food products.    DETAILED DESCRIPTION - Producing alcohol involves adding solid food waste products in storage tank for separation. The separated mixture is distilled and then added into mixer for crushing. The crushed mixture is added to tank for hydrolysis. The hydrolyzed mixture is added into cooking tank, which is controlled by power panel that includes a boiler for saccharification to obtain glucose. The obtained glucose is transferred to rest tank, which is added with yeast for saccharifying glucose. The saccharified mixture is added to chamber for de-distillation, where the chamber is equipped with pump. The de-distilled mixture under pressure and thermal intensity, gets converted to alcohol. The alcohol is removed from the chamber by pipe, which is controlled by a valve under the influence of pump. The alcohol is stored in reservoir and the distilled residue is transferred to waste tank.
NOVELTY - The utility model belongs to a fuel production equipment area, especially relates to a kind of a biomass fuel production molding device, wherein a. the first transport platform guide rail is located on the first cut and, the first pouring a wheel mounted on the other end a cutting platform of the first, the first cutter and the first cutter air cylinder connection, a first pressing plate and a pressing plate air cylinder connect the first, the second sliding guide rail is located on the transporting guide rail and the first, the second transport guide rail is located on the cutting platform and the first, the second transport guide rail is located on the cutting platform and a second end, the second pouring a wheel mounted on the other end a cutting platform and the second, the second cutter and the second cutter connected air cylinder, the second pressure plate and the second pressing plate air cylinder connection, a rolling wheel and a rolling cylinder connected, the collecting box installed on the sliding guide rail of the third.
NOVELTY - The utility model claims a new a kind of biological diesel oil water washing tower, a tube part provided with rough biologic diesel oil import, a part provided with biologic diesel oil outlet and bottom equipped with water washing water outlet, top equipped with gas phase outlet, a cylinder wall of a to a uniformly formed with a water washing water of import, a water washing water import and a water washing water import pipe connect. Import the biology diesel oil outlet tube and separation chamber connected, top part of separation chamber provided with a side separating biological diesel oil outlet chamber, separating biological diesel oil outlet chamber and separation chamber import a separation chamber is located on the top part of separating room separating chamber equipped with gas phase outlet, bottom of separating room provided with separated water outlet, water outlet installed with separated water separated valve. The lower part tube installed with video mirror tube and liquid level surface sensor can detect oil water separation surface of the cylinder bottom and a water washing water outlet installed with controlled for adjusting the liquid level surface sensor. The biological diesel oil water washing tower floor area a, water washing effect is good, consume low power, can realize continuous production.
NOVELTY - This new utility model claims of a kind of biology diesel oil continuous recycling one de-acidifying device, comprising oil tank, a plate type heat exchanger, constant temperature between lye tank, static state mixer and reaction kettle, crude oil tank and plate type heat exchanger connected with transporting pump, constant temperature slot and plate-type heat exchanger connected in common import and static state mixer, import and plate-type heat exchanger and outlet of constant temperature slot are installed with flow meter, static state mixer outlet and the reaction kettle is between import connected with transporting pump, a reaction kettle top end installed with output shaft of electrical machine, electrical machine connected with the inside of the reaction kettle stirring shaft, stirring shaft installed with stirring paddle, on the outside of the reaction kettle wall is set with outlet of the bottom heating set, a reaction kettle through transporting pump orderly connected with separator and salt groove. Continuous supply of this utility new model for biological diesel oil by continuous, and can make and de-acidifying process is continuous and removing water, the ester exchange reaction of biological diesel oil is raw material, increase yield of biological diesel oil.
NOVELTY - The utility model claims a new fungus plant capsule group type sewage treatment device, comprising a suspension and a suspension component fixed on the floating piece micelle, the micelle floating part comprises matrix and cover of a matrix of micelle layer; said suspension component comprises column-shaped suspension in and around the suspending cavity is hollow steady ring, inner side of the hollow steady ring through a wall of a swing arm and a suspension in a column, one end the swing arm and the column is in a suspension, the other end and the hollow steady ring a, a swing arm and a part set with elastic section, a diameter ratio of the column-shaped suspension cavity is 5: 1-10: 1. The hollow circle and stable suspension in the columnar structure can maintain stable in a water body, not easy to swing. A water flow when a columnar suspension cavity, a swinging arm connected with hollow ring can maintain stable static state, suspension in swing producing a torque conversion for elastic segment that absorb.
NOVELTY - Biomass gasification-anaerobic digestion combined production of high-grade fuel gas comprises e.g. establishing regional biomass utilization park, building biomass gasification system and biomass anaerobic digestion system, in the biomass gasification system, collecting biodegradable biomass, carrying out gasification process, producing synthesis gas, in the biomass anaerobic digestion system, collecting biodegradable biomass for anaerobic digestion process, generating marsh gas, adding synthesis gas in anaerobic digestion system, realizing biological methanation of synthesis gas.    USE - The method is useful for biomass gasification-anaerobic digestion combined production of high-grade fuel gas (claimed).    ADVANTAGE - The method realizes biological methanation of synthesis gas, realizes regional biomass utilization, overcomes complex catalytic methanation and traditional chemical method of biogas purification technology operations, and high investment operation cost.    DETAILED DESCRIPTION - Biomass gasification-anaerobic digestion combined production of high-grade fuel gas comprises (i) establishing regional biomass utilization park, and building biomass gasification system and biomass anaerobic digestion system, (ii) in the biomass gasification system, collecting biodegradable biomass, carrying out gasification process, producing synthesis gas, in the biomass anaerobic digestion system, collecting biodegradable biomass for anaerobic digestion process, generating marsh gas, and (iii) adding synthesis gas in anaerobic digestion system, realizing biological methanation of synthesis gas, using synthesis gas and adding hydrogen gas for purifying, at last preparing into high grade fuel gas.
NOVELTY - The method involves collecting the floating garbage in the garbage collection container provided on water surface. The mud extracted from water bottom sludge, is cleaned. The acid alkali agent is supplied to the bottom of water portion according to the mud acid alkaline. The light catalyze cell, microorganism reaction area and aquatic plant purification zone are formed in water portion in vertical and downward direction. The microorganism reaction area is set in a certain proportion of aerobic bacteria and anaerobic bacteria to purify the water portion.    USE - Sewage treatment method.    ADVANTAGE - The purification of the water portion is increased. The self-purification capacity is recovered. The time pollute of the water portion is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the sewage treatment process.    Container main portion (1.1)    Garbage collecting port (1.2)    U-type retainer ring (1.4)    Water inlet (1.6)    Water supply pump (2)
NOVELTY - The utility model claims an annular marsh gas fermentation system of multi-circulation biogas stirring flow, a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate,... in a top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe and fermentation feedstock a position... feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and a discharging blocking plate formed with at least one between a plate, between the adjacent blocking plate forming one of ferment cell, ferment cell top part set with mutually independent and gas-guide tube, the gas-guide tube is set with with a valve, a discharge pipe of water pipe is set with arrange in a discharge tube with liquid one-way flow into the one-way valve in water pressure. A feedstock arrange water pipe set with a control water pressure in a biogas liquid one-way flow into feedstock tube and one-way valve, fermentation efficiency of a fermentation of a different, cause different production rate, a gas pressure of different fermentation are a, promoting a biogas slurry flow stirring in the fermentation system to promote a uniform distribution of strain fermentation system, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. ferment, the ferment cell in forming enough air pressure a and to promote flow of liquid.
NOVELTY - This new utility model claims of can type detachable combined novel energy generating device, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline ferment is ferment annular pipe, set annular fermentation pipe on top, annular pipe of fermentation formed with opening, centre position of the opening position is set with extending two side with insert clapboard to separator, feedstock pipe and discharging pipe and annular pipe bottom respectively vertical and fermentation of the feedstock pipe and side wall of discharging pipe extending to biogas liquid face of annular fermentation pipe below seat; between water pressure and feedstock pipe connected with feedstock pipe drain pipe, water discharging pipe and connected with discharging pipe between pipe, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper with valve; the utility model adopt new annular fermentation system, fermentation line longer, which ensures full fermentation, by multi-plate for the whole fermentation system divided into more of ferment cell. Using pressure difference, promoting biogas fungus, flow of fermentation raw material, increase fermentation efficiency.
NOVELTY - This new utility model claims of multiple annular area beyond efficient marsh gas ferment system lifting strain uniform distribution of device, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline ferment is ferment annular pipe, set annular fermentation pipe on top, annular pipe of fermentation set with opening, the opening center position is set up with extending to two side insert clapboard to separator, feedstock pipe and discharging pipe and annular pipe bottom respectively vertical and fermentation of the feedstock pipe and side wall of discharging pipe extending to biogas liquid face of annular fermentation pipe below seat; between water pressure and feedstock pipe connected with feedstock pipe drain pipe, water discharging pipe and connected with discharging pipe between pipe, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve with the fermentation system also comprises cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure in connection. Brucella pipe is circular pipe fixed on annular ferment bacteria distributing pipe in side wall, Brucella and pipe shape is annular pipeline phase, ferment bacteria distributing pipe set with multiple of one vertical direction of the cloth fungus through hole.
NOVELTY - This new utility model claims of biogas liquid turbulent flow beyond efficient stirring marsh gas ferment system, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline ferment is ferment annular pipe, set annular fermentation pipe on top, annular pipe of fermentation set with opening, the opening center position is set up with extending to two side insert clapboard to separator, feedstock pipe and discharging pipe and annular pipe bottom respectively vertical and fermentation of the feedstock pipe and side wall of discharging pipe extending to biogas liquid face of annular fermentation pipe below seat; between water pressure and feedstock pipe connected with feedstock pipe drain pipe, water discharging pipe and connected with discharging pipe between pipe, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve with the fermentation system also comprises cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure in connecting, bacteria distributing pipe is annular; Pipeline fixed on annular ferment bacteria distributing pipe in side wall, Brucella and pipe shape is annular pipeline phase, ferment bacteria distributing pipe set with multiple of one vertical direction of the cloth fungus through hole.
NOVELTY - This new utility model claims of multi-area biogas liquid turbulent flow driving fungus uniformly distributed beyond the high-efficient ferment system, comprising the feedstock tube, discharging tube, fermentation pipeline, hydraulic pipeline ferment is ferment annular pipe, set annular fermentation pipe on top, annular pipe of fermentation set with opening, the opening center position is set up with extending to two side insert clapboard to separator, feedstock pipe and discharging pipe and annular pipe bottom respectively vertical and fermentation of the feedstock pipe and side wall of discharging pipe extending to biogas liquid face of annular fermentation pipe below seat; between water pressure and feedstock pipe connected with feedstock pipe drain pipe, water discharging pipe and connected with discharging pipe between pipe, inner annular fermentation pipe at least set with one of plate, and between adjacent blocking plate forming one of fermentation area, top part of fermentation area is set with independent with the gas-guide tube, the gas-guide tube is set with upper valve with the fermentation system also comprises cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure in connection. Brucella pipe is circular pipe fixed on annular ferment bacteria distributing pipe in side wall, Brucella and pipe shape is annular pipeline phase, ferment bacteria distributing pipe set with multiple of one vertical direction of the cloth fungus through hole.
NOVELTY - The utility model claims a multi-region bacteria distribution efficient marsh gas fermentation system, wherein a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe and fermentation feedstock a position... feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and a discharging blocking plate formed with at least one between a plate, between the adjacent blocking plate forming one of ferment cell of marsh gas ferment system also comprises annular cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and water pressure in connection. Brucella pipe is circular pipe fixed on annular ferment bacteria distributing pipe in a wall, Brucella and pipe shape is annular pipe. fermentation, bacteria distributing pipe is set with a with a vertical upper direction of the cloth through a fungus, ferment efficiency of a fermentation of a different, cause different production rate, a gas pressure of different fermentation are a, promoting a biogas slurry flow stirring in the fermentation system to promote a uniform distribution of strain fermentation system, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. fermentation, the fermentation zone forming in the enough air pressure a and promote flow of liquid.
NOVELTY - The utility model claims a barometric disturbance biogas liquid convection system, comprising a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and a discharge tube of a vertical extending to ferment pipe bottom of clapboard separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe and fermentation feedstock a position... feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking plate and a discharging blocking plate formed with at least one between a plate, between the adjacent blocking plate forming one of ferment cell of marsh gas ferment system also comprises annular cloth device fungus, bacteria distributing device comprises a drain pipe, pipe cloth bacteria, fungus cloth hole, a drain pipe and a water in a, bacteria distributing pipe is annular; Pipeline fixed on annular ferment bacteria distributing pipe in a wall, Brucella and pipe shape is annular pipe. fermentation, bacteria distributing pipe is set with a with a vertical upper direction of the cloth through a fungus, ferment efficiency of a fermentation of a different, cause different production rate, a gas pressure of different fermentation are a, promoting a biogas slurry flow stirring in the fermentation system to promote a uniform distribution of strain fermentation system, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. fermentation, the fermentation zone forming in the enough air pressure a and promote flow of liquid.
NOVELTY - The utility model claims a pressure disturbance super high efficient biogas liquid convection stirring marsh gas generator, comprising a material inlet and outlet cylinder, annular fermentation pipe, a marsh gas ferment system main body, a vertical cylinder connected with annular fermentation pipeline, a cylinder between a feedstock tube and discharging tube, a feedstock and discharging pipe by separate a separate, mounted in annular fermentation pipe top, a feedstock tube between a feedstock with a drain pipe, a discharging pipe connected with the discharging tube between drain pipe, annular pipe and fermentation feedstock a position... feedstock with a plate, annular pipe and discharging pipe connected with ferment site to set with a discharging plate, a feedstock-blocking board and a discharging board between set with blocking plate, between the adjacent blocking plate forming ferment cell of marsh gas ferment system also comprises annular bacteria distributing device, is provided with a top part and a fermented independently and gas-guide tube, can be each of the cell a. ferment, the ferment cell in forming enough air pressure a and, Promoting flow of biogas.
NOVELTY - Unilateral moving stirring method comprises e.g. adding fermentation feedstock in a biogas fermentation system, fermenting to produce methane gas, accumulating the methane gas in a inner plate. Increasing gas pressure, pushing the gas in a upper part of a gas board via moving pneumatic piston. The pneumatic piston stimulates upward movement of the movable stirring network via connecting rod, and other end of the movable stirring network is connected by bottom mobile of the fermentation system, so as to deflect the movable stirring network, and stirring the movable stirring network and biogas.    USE - Used as unilateral moving stirring method.    DETAILED DESCRIPTION - Unilateral moving stirring method comprises adding fermentation feedstock in a biogas fermentation system, fermenting to produce methane gas, accumulating the methane gas in a inner plate. increasing gas pressure, pushing the gas in the upper part of a gas board via moving pneumatic piston, the pneumatic piston stimulates upward movement of the movable stirring network via connecting rod, other end of the movable stirring network is connected by bottom mobile of the fermentation system, so as to deflect the movable stirring network, then stirring the movable stirring network and biogas, passing biogas on the top of the gas board, then dropping the gas pressure in the gas board, then placing a counterweight block on the top of the pneumatic piston under the action of gravity. The counterweight block pushes the pneumatic piston in downward, then resetting driven of the movable stirring network, and again stirring the biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the unilateral moving stirring method.
NOVELTY - Pneumatic stirring and biogas collecting using multipurpose gas storage plate, comprises providing multiple baffles in the inner gas storage plate, and dividing the gas storage plate into multiple fermentation zone, unevenly distributing the fermentation raw materials and other bacteria in the biogas system, so as to cause different fermentation efficiency and inconsistent pressure in the adjacent fermentation area; maintaining constant pressure, and stirring; and when the pressure difference across the fermentation area is equal or cannot overcome the spring force, collecting the biogas.    USE - The method is useful for pneumatic stirring and biogas collecting using multipurpose gas storage plate (claimed).
NOVELTY - This new utility model claims of one of zoology pigsty, aiming at providing a kind of one can effective realize zoology pigsty excrement solid and liquid separation. It comprises setting floor of closed form rail in the square region, and is set on the fence door, the floor in the fence along one diagonal inclined rail bar is set, and to the corner of the lower end is set with diagonal with drain pipe of floor, the two edge floor and lower diagonal adjacent in the end enclosure is set with with drainage ditch. The utility model new implement of liquid and solid excrement separated, effective to prevent solid waste by wet fermentation but growing bacteria and smell, improving effective cultivation environment, for fast fattening pig provide proper living environment.
NOVELTY - The utility model claims a of a kind of a composite type flushing-free water treatment system, the system mainly comprises the first water pump, the second water pump, a timing automatic switch, a sealing cabin chamber and a gas pump, a water pump and a sewage processing connected mutually, the other end and the sealing chamber connected, air pump and sealing chamber connected, working state of pump and the second water pump timing switch automatically change.... Sewage entering into a chamber of a water impurity and pollutant to obtain effective and eliminate a decomposing and filtering and, to make a water quality purification, the process not using disinfectant additive equal, it will not cause a second time. . continuously removing impurities and a purification of a circle, to reach without change of a water-saving and better processing effect. The sleeve system may need to process sewage according to the weight number is set with device scale, suitable flexible, can be widely applied in each area aquarium, zoology, aquatic product cultivation and landscape water body equal, with good application prospect.
NOVELTY - This new utility model provide a kind of artificial wetland microorganism immobilized a filler device, which solves the problem is: aiming at some compare a biodegradability, nutrition material ratio not matching the sewage, waste water and only depend on artificial wetland technology convention processing technology compare to reach the expected effect, using artificial wetland technology application can has a certain limitation, the utility model of new technology point is: in in a rectangular box body is set with top with immobilized microorganism filler, side wall and bottom of the rectangular box with topless; the immobilized microorganism filler divided of the third type, a microorganism and a 6-8 cm, 3-6 cm, 2-3 cm a fixed filler. And artificial wetland microorganism flora adjusting device matching use can increase effective internal wetland sewage purification of microorganism content; and a wetland unit a processing function fusogenic.. The utility model also has a simple structure, a simple operation, notable effect equal character.
NOVELTY - A marsh gas pool temperature control system using solar energy water heater, the structure is: a marsh gas pool set with warm water pipe. Temperature control water pipe one end of a water pump connection, the other end of the first water pump joint and the first three-way pipe is connected, the first three-way pipe and the other three joint respectively through a water inlet of the first hot water valve and the first cold water valve and hot water tank and cold water tank connect, the other end temperature.... and the second three-way pipe and the first joint connection, the second three-way pipe and the other three joint respectively through a second hot water valve and cold water valve and the second solar energy water heater and hot water tank and the cold water tank outlet connection. Cold water valve and hot water valve is a electromagnetic valve. A water tank, cold water tank and a marsh gas pool are set with temperature sensor. Water pump, all the electromagnetic valve and temperature sensor are connected with a central control unit electric. ... that of marsh gas pool temperature due to a cause of yield is not a problem, and according to user requirement may increase or reduce yield, and low cost.
NOVELTY - A biogas biological desulfurization device comprises tank body (1) provided with bottom air separation plates (11), air distributor (2) and air inlet (3), desulfurization liquid circulating pump (10), air discharge pipe (12), desulfurization liquid conduit (15), desulfurization liquid inlet and outlet (9), desulfurization liquid pipe (13), gas distributor (4) provided with biofilm attached to filler layer (6), biogas inlet (5) connected to gas distributor, desulfurization liquid distributor (7) connected to tank body through liquid circulation pipe (8), and biogas outlet (14).    USE - Biogas biological desulfurization device.    ADVANTAGE - The device is energy-saving, can avoid mixing of biogas and air, increases hydrogen removing rate, and has reasonable design, good stability, and high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biogas biological desulfurization device.    Tank body (1)    Air distributor (2)    Air inlet (3)    Gas distributor (4)    Biogas inlet (5)    Filler layer (6)    Desulfurization liquid distributor (7)    Liquid circulation pipe (8)    Desulfurization liquid inlet and outlet (9)    Desulfurization liquid circulating pump (10)    Bottom air separation plates (11)    Air discharge pipe (12)    Desulfurization liquid pipe (13)    Biogas outlet (14)    Desulfurization liquid conduit (15)
NOVELTY - The device has an anode electrode (1) that is set with an anode. A cathode electrode (4) is set with cathode. A connection portion is provided between anode electrode and cathode electrode. Electric conduction acid solution is provided inside cathode. The top of cathode chamber is connected with a gas collection device. The anode electrode is formed of light catalyze layer. A biological compatible composite layer is formed by a composite electrode. A biologic compatible layer surface is covered using electric fungus biological film.    USE - Bio-electrochemical device used for hydrogen production by solar energy.    ADVANTAGE - Since anode electrode that is formed of light catalyze layer, the corrosion solution and fatal flaw are avoided. The hydrogen is produced efficiently and the generation of dirt is reduced. Since electronic driver is realized by the sunlight, the need for other energy input is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the bio-electrochemical device. (Drawing includes non-English language text)    Anode electrode (1)    Anode chamber (2)    Ion-exchange membrane (3)    Cathode electrode (4)    Cathode chamber (5)
NOVELTY - Preparation of biofertilizer involves (a) drying cattle manure and apple pomace, crushing dried material, mixing powder with corn flour and Bacillus mucilaginosus, fermenting mixture and drying, (b) mixing apple pomace and bagasse, crushing, sterilizing powder, inoculating powder with B. megaterium, fermenting mixture and drying, and (c) mixing products obtained in steps (a) and (b), adding photosynthetic bacteria, Lactobacillales and Aspergillus niger, fermenting mixture and drying.    USE - The method is useful for preparing biofertilizer for improving soil structure of potato (claimed).    ADVANTAGE - The method prepares biofertilizer with high yield and quality.    DETAILED DESCRIPTION - Preparation of biofertilizer involves (a) drying cattle manure and apple pomace, crushing dried cattle manure and apple pomace to obtain 40 mesh size powder, mixing obtained powder with corn flour and Bacillus mucilaginosus, fermenting mixture and drying, (b) mixing apple pomace and bagasse, crushing mixture to obtain 40 mesh size powder, sterilizing mixture at 121 degrees C, inoculating mixture with B. megaterium, fermenting mixture and drying, and (c) mixing products obtained in steps (a) and (b), adding photosynthetic bacteria, Lactobacillales and Aspergillus niger, fermenting mixture and drying.
NOVELTY - Preparation of fertilizer involves (a) preparing Saccharina japonica broth by performing enzymolysis, (b) fermenting cattle and sheep manure to obtained fermented manure, (c) mixing soybean and corn stover and fermenting, (d) mixing S. japonica broth, fermented manure and fermented soybean and corn stover and fermenting mixture, and (e) drying fermented mixture, crushing, sealing and storing.    USE - The method is useful for preparing fertilizer for Fuji apple (claimed).    ADVANTAGE - The prepared fertilizer improves flavor and quality of apple, increases taste, yield and aroma of apple, and is easy and convenient to use.
NOVELTY - Biogas fermentation system includes fermentation tank (10). The fermentation tank is provided with inlet (12) and outlet (14) from both ends. The middle of the fermentation tank is provided with fermentation chamber (16), which is connected to inlet and outlet. The fermentation tank is provided with gas plate, which is equipped with support unit present at top of the fermentation tank. Gas storage plate is present at the lower end of the side wall of the fermentation tank near the inlet. The fermentation tank also includes rod (80) i.e. crossbar and vertical rod.    USE - Biogas fermentation system.    ADVANTAGE - The biogas fermentation system is highly efficient.    DETAILED DESCRIPTION - Biogas fermentation system includes fermentation tank. The fermentation tank is provided with inlet and outlet from both ends. The middle of the fermentation tank is provided with fermentation chamber, which is connected to inlet and outlet. The fermentation tank is provided with gas plate, which is equipped with support unit present at top of the fermentation tank. Gas storage plate is present at the lower end of the side wall of the fermentation tank near the inlet. The fermentation tank also includes rod i.e. crossbar and vertical rod. One end of the crossbar is connected to vertical rod. The fermentation tank near inlet is provided with feed inlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas fermentation system.    Fermentation tank (10)    Inlet (12)    Outlet (14)    Fermentation chamber (16)    Rod (80)
NOVELTY - Three-level anaerobic device has anaerobic chamber, which is designed in tunnel shape. The three-level anaerobic device comprises level-I anaerobic chamber (1), level-II anaerobic chamber (2) and level-III anaerobic chamber (3) for anaerobic reaction, where fermented biogas is collected through a tunnel type vault.    USE - Three-level anaerobic device used for collecting biogas.    ADVANTAGE - The three-level anaerobic device has adequate fermentation, gas production rate, long service life and effective conservation of surface area.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of three-level anaerobic device    Level-I anaerobic chamber (1)    Level-II anaerobic chamber (2)    Level-III anaerobic chamber (3)    Feedstock (4)    Gas-guide tube (12)
NOVELTY - Stirring device comprises biogas fermentation system and stirring sleeve (430). The biogas fermentation system comprises biogas storage plate, where dampers are arranged in the biogas storage plate to separate the biogas storage plate into fermentation areas. The upper end of the damper is fixed into stirring sleeve with two symmetrical ends. The stirring sleeve is a flexible sleeved with a pneumatic piston (450). The two ends of the pneumatic piston are connected to an outer sleeve through a piston rod, respectively.    USE - Stirring device.    DETAILED DESCRIPTION - Stirring device comprises biogas fermentation system and stirring sleeve. The biogas fermentation system comprises biogas storage plate, where dampers are arranged in the biogas storage plate to separate the biogas storage plate into fermentation areas. The upper end of the damper is fixed into stirring sleeve with two symmetrical ends. The stirring sleeve is a flexible sleeved with a pneumatic piston. The two ends of the pneumatic piston are connected to an outer sleeve through a piston rod, respectively. The external walls provided at two ends of the stirring sleeve is sleeved with a spring, respectively. The outer sleeve is provided with cavity and the outer wall of the stirring sleeve. A hole is provided, which connects the fermentation area and the cavity. The outer sleeve is connected to a stirring net.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of stirring device.    Baffle plate (26)    Stirring sleeve (430)    Spring (440a and 440b)    Pneumatic piston (450)
NOVELTY - System comprises gas cylinder (310), plate (330), gas piston (340) and upper piston rod. The gas cylinder is internally provided with the plate to separate cavity of the gas cylinder into a left area and a right area, which are interconnected to up and down. The gas piston is flexibly sleeved between internal wall of the gas cylinder and the plate. The gas piston divides the left area into left upper area and left lower area. The upper end of the gas piston is connected to upper piston rod. The upper part of the upper piston rod is provided with a ring-shaped gas groove (370).    USE - System used for collecting excessive gas.    DETAILED DESCRIPTION - System comprises gas cylinder, plate, gas piston and upper piston rod. The gas cylinder is internally provided with the plate to separate cavity of the gas cylinder into a left area and a right area, which are interconnected to up and down. The gas piston is flexibly sleeved between internal wall of the gas cylinder and the plate. The gas piston divides the left area into left upper area and left lower area. The upper end of the gas piston is connected to upper piston rod. The upper part of the upper piston rod is provided with a ring-shaped gas groove. The gas cylinder is provided with a gas inlet. The effective area S1, which is provided at the lower end of the piston is larger than S2 at the upper end. The gas inlet is connected to biogas storage plate of biogas fermentation system. The upper piston rod is externally sleeved with a fixed block. The gas bag are sleeved and fixed on the fixed block, which is fixed in the left area. The left area is a limiting bench, which is fixed on the inner wall of the gas cylinder and the plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system.    Gas cylinder (310)    Gas inlet (320)    Plate (330)    Gas piston (340)    Ring-shaped gas groove (370)
NOVELTY - Biogas fermentation system includes cylinder (310), plate (330), piston (340) and piston rod (350). The piston rod is set within the cylinder. The cylinder is provided with cavity plate divided into left and right regions. The piston slides in the cylinder wall. The lower end of the piston rod is connected to air guide on the upper surface of the piston. The piston rod is provided with annular intermediate position gas guide groove. The top of the piston rod has socket with fixed block (380), which is provided with upper air bag with air inlet passage (360).    USE - Biogas fermentation system.    ADVANTAGE - The biogas fermentation system is energy efficient.    DETAILED DESCRIPTION - Biogas fermentation system includes cylinder, plate, piston and piston rod. The piston rod is set within the cylinder. The cylinder is provided with cavity plate divided into left and right regions. The piston slides in the cylinder wall. The lower end of the piston rod is connected to air guide on the upper surface of the piston. The piston rod is provided with annular intermediate position gas guide groove. The top of the piston rod has socket with fixed block, which is provided with upper air bag with air inlet passage. The piston rod is located between top block and gas spring guide, which is provided on the cylinder inlet. The biogas fermentation system also includes fermentation tank body, gas plate and partition plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas fermentation system.    Cylinder (310)    Plate (330)    Piston (340)    Piston rod (350)    Air inlet passage (360)    Fixed block (380)
NOVELTY - The method involves extrusion plate under the marsh gas storage air outflow plate. The biogas is returned to fermentation area. Biogas fermentation gathered in multiple fermentation chambers. An inlet/discharge port is formed in fermentation zone between air resistance plate and adjacent baffle. A support device is fixed above the fermentation chamber. Methane gas is stored within pressure plate is gradually increased. The fermentation pool biogas is returned to fermentation area.    USE - Marsh gas fermentation method.    ADVANTAGE - The fermentation efficiency in fermentation area is improved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the marsh gas fermentation system.    Ferment pool portions (10-40)
NOVELTY - The utility model claims a mixed flow type U-shaped beyond efficient marsh gas generating system, which is composed of a feedstock tube, a discharge pipe, a fermentation pipeline, a feedstock material and a detachable tube and a U type pipe. terminal a fermentation feedstock and a side wall and a side wall extended U-type discharge pipe in fermentation, of between a U-type fermentation pipe on top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, a U-shaped pipe is set with fermentation with gas-guide tube, the fermented line a, liquid flow stirring notable effect, and promotes a uniform strain distribution.
NOVELTY - The utility model claims a anaerobic fermentation system for promoting uniform distribution of strain through several section convection disturbance, composed of a feedstock tube, a discharge pipe, a fermentation pipeline, composed of, a feedstock material and a detachable tube and a U type pipe. terminal a fermentation feedstock and a side wall and a side wall extended U-type discharge pipe in fermentation, of between a U-type fermentation pipe on top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, a U-shaped pipe is set with fermentation with gas-guide tube, the fermented line a, liquid flow stirring notable effect, and promotes a uniform strain distribution.
NOVELTY - The utility model claims a high efficient Anaerobic fermentation system of pneumatic pushing marsh liquid disorder flow, which is composed of a feedstock tube, a discharge pipe, a fermentation pipeline, the feedstock material and a detachable tube and U type pipe. terminal a fermentation feedstock and a side wall and a side wall extended U-type discharge pipe in fermentation, between a U-type fermentation pipe on top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, a U-shaped pipe of fermentation set with gas-guide tube, the fermented line, liquid flow stirring notable effect, and promotes uniform strain distribution.
NOVELTY - The utility model claims a high efficient methane generating system connecting with fermentation zone to promote flow stirring, wherein it comprises a feedstock tube, a discharging tube, a pipe ferment, the ferment pipe is straight pipe, fermentation pipe two end side top part equipped with open mouth and a detachably connected with a biogas liquid face with a feedstock tube and discharging tube, a feedstock side wall and a side wall extending to the discharge pipe in the fermentation, installed on fermentation pipeline between top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharge tube and drain in fermentation pipeline also is set with multi-number between the feedstock has a side wall and a side wall and between the discharging plate, a feedstock/discharging pipe side wall and adjacent blocking plate and forming a space of fermentation area or a space between adjacent blocking plate forming one of fermentation area, a top of a fermentation zone is connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and it promots the fermentation raw material into a fermentation system, fermentation system and increase the gas production system.
NOVELTY - The utility model claims a new type burdock several section beyond efficient cloth fungus of marsh gas ferment system, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device and fermentation line a. .... a a and one-way valve, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims a new hydraulic pneumatic promoting uniform strain distribution and methane generating system, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device. Fermentation line a, a water pressure and a one-way valve and a, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims a new hydraulic biogas bend flow stirring is beyond efficient methane generating system, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device. Fermentation line a, a water pressure and a one-way valve and a, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - The utility model claims a methane generating device is a bent long fermentation path, wherein comprising: a feedstock, a discharge pipe, a fermentation pipe, a fermentation level pipe set, a feedstock material and a vertical U-type fermentation pipeline connected with a terminal a, a fermentation pipe of a hydraulic part, a feedstock tube connecting seat for feedstock a drainage hole, a discharging pipe and a position for discharging a drainage hole, a pipeline and fermentation feedstock pipe connecting seat is set with a feedstock to a baffle, a fermentation pipe and discharging pipe connecting seat is set with a discharging pipe to plate, discharging tube between blocking board and a feedstock-blocking plate is set with at least a one with a plate, a disc feeding/discharging pipe and between adjacent blocking plate or between the adjacent blocking plate forming one of fermentation area, top part of each fermentation area is set with two independent with the gas collecting pipe, each fermentation area of top part and connecting with the independent gas collecting pipe, a gas collecting tube is set with with a valve, a U-shaped channel type fermentation device and fermentation line a. .... a a and one-way valve, biogas slurry realize full flow within a system, and a uniform distribution of strain, a preventing crust, high yield, suitable for large scale production.
NOVELTY - Cultivation of enoki mushroom involves taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 52-56 wt.% 3-5 mm corn cob, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, fermenting naturally, turning once a day for 5-6 days, adding 3-4 wt.% lime for first turn and 1 wt.% light calcium carbonate for second turn, controlling moisture content to 63-65%, cooling to obtain cultivation material, adding to enoki mushroom, covering mycelium with 1-2 cm thick loam soil and spraying with dried shiitake stem solution at 3-5 kg/m2.    USE - Method for cultivating enoki mushroom (claimed).    ADVANTAGE - The method is environment-friendly, saves manpower and coal resources, improves bacterial resistance and growth performance of mushroom, and has high biological conversion rate.    DETAILED DESCRIPTION - Cultivation of enoki mushroom comprises taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 52-56 wt.% 3-5 mm corn cob, 12-16 wt.% wood chips and 22-26 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days, adding 3-4 wt.% lime for first turn and 1 wt.% light calcium carbonate for second turn, controlling moisture content to 63-65%, cooling to obtain cultivation material, adding to enoki mushroom, covering mycelium with 1-2 cm thick loam soil, adding 20 times water to dried shiitake stem, soaking for 18-24 hours, filtering, diluting to obtain 0.01-0.02 g/mL dried shiitake stem solution and spraying to loam soil covered mycelium at 3-5 kg/m2.
NOVELTY - Cultivation of Pleurotus citrinopileatus involves taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 24-34 wt.% cotton seed hull and 12-14 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hour and turning once a day for 5-6 days, adding 2-3 wt.% lime for first turn, 1 wt.% gypsum for second turn and 1 wt.% calcium superphosphate for third turn.    USE - Method for cultivating Pleurotus citrinopileatus (claimed).    ADVANTAGE - The method is environment-friendly, saves manpower and coal resources, improves bacterial resistance and growth performance of mushroom, and has high biological conversion rate.    DETAILED DESCRIPTION - Cultivation of Pleurotus citrinopileatus comprises taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 45-55 wt.% 3-5 mm corn cob, 24-34 wt.% cotton seed hull and 12-14 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days, adding 2-3 wt.% lime for first turn, 1 wt.% gypsum for second turn and 1 wt.% calcium superphosphate for third turn, controlling moisture content to 63-65%, cooling to obtain cultivation material, adding to Pleurotus citrinopileatus, covering mycelium with 1-2 cm thick loam soil, adding 20 times water to dried shiitake stem, soaking for 18-24 hours, filtering, diluting to obtain 0.01-0.02 g/mL dried shiitake stem solution and spraying to loam soil covered mycelium at 4-6 kg/m2.
NOVELTY - Cultivation of Pleurotus citrinopileatus involves taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 21-31 wt.% 3-5 mm corn cob and 14-16 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days and adding 3-4 wt.% lime for first turn, 1 wt.% gypsum for second turn and 1 wt.% calcium superphosphate for third turn.    USE - Method for cultivating Pleurotus citrinopileatus (claimed).    ADVANTAGE - The method is environment-friendly, saves manpower and coal resources, improves bacterial resistance and growth performance of mushroom, and has high biological conversion rate.    DETAILED DESCRIPTION - Cultivation of Pleurotus citrinopileatus comprises taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 45-55 wt.% bagasse, 21-31 wt.% 3-5 mm corn cob and 14-16 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days, adding 3-4 wt.% lime for first turn, 1 wt.% gypsum for second turn and 1 wt.% calcium superphosphate for third turn, controlling moisture content to 63-65%, cooling to obtain cultivation material, adding to Pleurotus citrinopileatus, covering mycelium with 1-2 cm thick loam soil, adding 20 times water to dried shiitake stem, soaking for 18-24 hours, filtering, diluting to obtain 0.01-0.02 g/mL dried shiitake stem solution and spraying to loam soil covered mycelium at 4-6 kg/m2.
NOVELTY - An axillary bud culture medium comprises 30000 mg/l sugar, 700 mg/l agar, 2.0-5.0 mg/l 6-benzylaminopurine, 0.2-0.5 mg/l naphthalene acetic acid, 40-60 mg/l penicillin and 50-70 mg/l carbendazim at a pH of 5-6.    USE - Axillary bud culture medium for breeding vetiver grass (claimed).    ADVANTAGE - The medium has reduced pollution rate, increased incidence rate of sterile axillary buds, reduced axillary buds occurrence time, improved proliferation medium formulations, reduced pollution rate, improved bud proliferation rate and improved survival rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for breeding vetiver grass.
NOVELTY - Extracting volatile oil involves extracting resveratrol and eudesmol from Chrysanthemum. Chrysanthemum is distilled with water. Obtained volatile oil-water mixture is extracted, and then dehydrated by rotary evaporator at 40-45 degrees C, and concentrated to obtain the final product.    USE - Method for extracting volatile oil used for preventing mites such as twospotted spider mite (claimed).    ADVANTAGE - The method enables to extract volatile oil which is eco-friendly, simple to prepare, and suitable for industrial production, and does not cause drug resistance.
NOVELTY - A near natural river ecological restoration method comprises maintenance, rainwater drain preprocessing cleaning, and water quality control treatment and maintenance comprising organic matter sludge locking process, river micropore aeration technology, beneficial fungus water body biological repairing technique, manual plant floating island technology and submerged plant ecological restoration technology.    USE - Near natural river ecological restoration method (claimed).    ADVANTAGE - The method reduces pollutants, enhances organic matter microbial decomposition, maintains self-cleaning function, constructs complete aquatic food chain, inhibits algae growth, and maintains and improves water quality.
NOVELTY - Processing dairy manure involves separating barn and cow dung dry solids from manure, and then treating solid waste. Cow urine and cow dung are collected by underground pipe, and then filtered by filter device. Obtained sewage is transferred to anaerobic tank through underground pipe. Treated sewage is transferred to aerobic tank, and mixed with deodorant, deaminase and water. Obtained product is utilized in farming, or transferred to biological purification and storage pond in non-irrigation season.    USE - Method for processing dairy manure (claimed).    ADVANTAGE - The method enables to process dairy manure used in agriculture.
NOVELTY - Loosening agent comprises 25-35 wt.% starch, 10-15 wt.% calcium carbonate, 25-30 wt.% ammonium hydrogen carbonate, 5-15 wt.% anhydrous potassium aluminum sulfate and 15-25 wt.% calcium biphosphate. Loosening agent is prepared by drying raw materials and then crushed through 120 meshes sieve screen into powder. Powders are mixed and stirred uniformly by using a stirrer for 20-30 minutes, and then packaged.    USE - Loosening agent used for fermenting organic fertilizer (claimed).    ADVANTAGE - The loosening agent increases organic fertilizer stacking fermentation temperature, shortens fermentation time and material decomposed period, and reduces machine turning energy consumption.
NOVELTY - Anti-sintering type biomass fuel comprises 25-50 wt.% rice straw, 15-25 wt.% corn straw, 5-10 wt.% walnut shell, 5-13 wt.% tree bark and 0.5-2 wt.% anti-sintering agent.    USE - Anti-sintering type biomass fuel.    ADVANTAGE - The anti-sintering type biomass fuel reduces emission of harmful gases.
NOVELTY - Biogas fermentation system includes fermentation tank (10) and gas plate (30). The fermentation tank is provided with fermentation chamber (16), and inlet (12) and outlet (14) on right and left side walls. The fermentation chamber is provided with support device, and is placed in fermentation tank, where gas plate is fixed on side wall of the fermentation tank. The gas plate is present near the inlet, which is provided with inlet-air resistance plate (32). The gas plate near outlet is also provided with outlet-air resistance plate.    USE - Biogas fermentation system.    ADVANTAGE - The biogas fermentation system is highly efficient.    DETAILED DESCRIPTION - Biogas fermentation system includes fermentation tank and gas plate. The fermentation tank is provided with fermentation chamber, and inlet and outlet on right and left side walls. The fermentation chamber is provided with support device, and is placed in fermentation tank, where gas plate is fixed on side wall of the fermentation tank. The gas plate is present near the inlet, which is provided with inlet-air resistance plate. The gas plate near outlet is also provided with outlet-air resistance plate. The inlet side wall is provided with feed inlet drain pipe and outlet side wall is provided with feed outlet drain pipe. The biogas fermentation system further includes rod (40) i.e. vertical rod and cross-rod, where one end of the cross-rod is connected to the vertical rod.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas fermentation system.    Fermentation tank (10)    Inlet (12)    Outlet (14)    Fermentation chamber (16)    Gas plate (30)    Inlet-air resistance plate (32)    Rod (40)
NOVELTY - Solid feedstock biogas fermentation device comprises an outer tank (1) and an inner tank (2). The inner tank is provided with a biogas storage chamber (9) and expansion branch tube. The expansion branch tube is connected to air outlet through a vent valve (8). The inner tank is provided with a spray nozzle (7). The spray nozzle is connected to a fluid makeup valve and a circulating valve (4) through an extension pipe and a spray valve (5). The fluid make up valve is connected to a fluid inlet.    USE - Solid feedstock biogas fermentation device.    ADVANTAGE - The solid feedstock biogas fermentation device is easy to operate, and has high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of solid feedstock biogas fermentation device.    Outer tank (1)    Inner tank (2)    Circulating valve (4)    Spray valve (5)    Spray nozzle (7)    Vent valve (8)    Biogas storage chamber (9)
NOVELTY - Microbial agent comprises Bacillus amyloliquefaciens (CGMCC No 1.769) fermented powder and Saccharomyces cerevisiae (CGMCC No 2.3853) fermented powder.    USE - Microbial agent used in sewage treatment or aerobic tank for in-situ reduction of sludge (all claimed).    ADVANTAGE - The microbial agent is highly efficient, cost-effective and simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial agent, which involves:    (A) freeze-drying fermented broths of Bacillus amyloliquefaciens and Saccharomyces cerevisiae separately to obtain fermented powders; and    (B) mixing fermented powders in appropriate ratio to obtain microbial agent.
NOVELTY - Environment-friendly preparation of 2,2'-dibenzamidodiphenyl disulfide (DBD) rubber peptizer includes adding water and sodium hydroxide into reaction vessel, stirring, adding benzothiazole, heating, and cooling; adding water, controlling temperature, and oxidizing with hydrogen peroxide solution to obtain diphenylamine disulfide-containing reaction solution; and adding toluene, controlling reaction temperature, dropping benzoyl chloride, stirring, filtering, washing filter cake with water, and drying.    USE - Method for environment-friendly preparation of 2,2'-dibenzamidodiphenyl disulfide rubber peptizer (claimed).    ADVANTAGE - The method is easy to control, does not need purification step which simplifies the process and reduces yield loss, recycles toluene, sodium bicarbonate and water, and has almost no gas emissions, greatly reduced cost and energy consumption, and high yield.    DETAILED DESCRIPTION - Environment-friendly preparation of 2,2'-dibenzamidodiphenyl disulfide (DBD) rubber peptizer comprises:    (A) adding water and sodium hydroxide into reaction vessel, stirring to dissolve, adding benzothiazole, heating to 70-80 degrees C for 2.5-3.5 hours, and cooling to room temperature;    (B) adding water, controlling temperature to 10-45 degrees C, and oxidizing with hydrogen peroxide solution to obtain diphenylamine disulfide-containing reaction solution; and    (C) adding toluene, controlling reaction temperature to 40-50 degrees C, dropping benzoyl chloride, stirring, filtering, washing filter cake with water, and drying to obtain DBD rubber peptizer while stratifying filtrate, recycling toluene upper layer, and separating lower aqueous phase into sodium bicarbonate and sodium chloride.
NOVELTY - A high acid vegetable oil biodiesel and glycerin synchronization method comprises taking vegetable oil, adding acid, putting into esterification reactor, adding p-toluenesulfonic acid and methanol, carrying out esterification reaction, steaming, stirring, distilling, collecting distillate, putting into ester exchange reactor, adding sodium hydroxide, carrying out transesterification reaction, stirring, raising temperature to remove unreacted methanol, recycling methanol, and removing reaction liquid.    USE - High acid vegetable oil biodiesel and glycerin synchronization method (claimed).    ADVANTAGE - The method is energy efficient. It has biodiesel product yield of 99% and glycerin product purity of 95%.
NOVELTY - The high-concentration anaerobic reactor device has a tank housing (1) which is provided with a water inlet pipe (2) at an upper portion and a manhole (10) on a top portion. An upper portion of the water inlet pipe is provided with a three-phase separator (3) which is connected to a gas collecting pipe (4).    USE - High-concentration anaerobic reactor device for producing a biogas.    ADVANTAGE - The high-concentration anaerobic reactor device is featured with a novel structure, beautiful appearance, a stable operation, easy utilization, low operation cost, and high biogas production. The problem of environment pollution caused by straw burning and free discharge of biomass waste is eliminated by producing the biogas from the biomass wastes such as comprising crop straw, livestock manure, industrial organic waste and municipal solid organic garbage. Hence the living quality of the environment is increased effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the high-concentration anaerobic reactor device.    Tank housing (1)    Water inlet pipe (2)    Three-phase separator (3)    Gas collecting pipe (4)    Manhole (10)
NOVELTY - Extracting agent comprises 0.5-2 wt.% citric and/or malic acid in ratio of 1:1, 0.1-1 wt.% vitamin C, 0.01-0.5 wt.% sodium bisulfite and balance is water.    USE - Extracting agent used for extracting subcritical water and polyphenol from lotus seed solid waste.    ADVANTAGE - The extracting agent is quick, eco-friendly and easy to industrialize.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for extracting subcritical water and polyphenol from lotus seed solid waste, which involves:    (A) extracting raw materials and adding to the extracting agent for 10-20 minutes;    (B) filling with nitrogen and sealing at 5-20 MPa and 120-180 degrees C for 10-30 minutes;    (C) extracting and cooling to 25-35 degrees C;    (D) centrifuging the extract, collecting and cooling the supernatant;    (E) passing the supernatant through the resin column at a constant flow rate;    (F) washing with water to remove the impurities and adding 70% aqueous ethanol to resin column;    (G) collecting the eluent at 35-45 degrees C and recovering ethanol to obtain concentrated liquid; and    (H) drying the concentrate by freeze drying or spray drying to obtain polyphenol from lotus solid waste.
NOVELTY - A Cynanchum paniculatum C21 steroid conversion product is prepared by drying Cynanchum paniculatum root and rhizome, crushing, alcohol extracting, filtering, combining, recovering alcohol, dissolving into water, filling into macroporous resin column D101 chromatography, eluting with water and alcohol, discarding eluent, filling into decolorization resin D941 column chromatography, eluting with alcohol, collecting eluent, concentrating, drying, adding sulfur acid solution, water bath heating, taking out, cooling, shaking with ethyl acetate, combining, and recovering ethyl.    USE - Method for preparing Cynanchum paniculatum C21 steroid conversion product used for preparing gastric cancer multi-drug resistant cell 5-fluorouracil reversal agent, colon cancer multi-drug resistant cell 5-fluorouracil reversal agent, colon cancer multi-drug resistant cell adriamycin reversal agent, colon cancer multi-medicine drug-resistant cell cisplatin reversal agent, lung cancer multi-medicine drug-resistant cell paclitaxel reversal agent, and gastric cancer multi-drug resistant cell cisplatin reversal agent (all claimed).    ADVANTAGE - The product increases radiotherapy and chemotherapy effect.    DETAILED DESCRIPTION - A Cynanchum paniculatum C21 steroid conversion product is prepared by drying Cynanchum paniculatum root and rhizome, crushing, 90% alcohol extracting for 3 times for 2 hours, filtering, combining, recovering alcohol under reduced pressure, dissolving into water, filling into macroporous resin column D101 chromatography, eluting with water and 30% alcohol to colorless, discarding eluent, filling into decolorization resin D941 column chromatography, eluting with 90% alcohol, collecting eluent, concentrating under pressure, drying, adding 2% sulfur acid solution, water bath heating at 80 degrees C for 5 hours, taking out, cooling, shaking with ethyl acetate for 5 times, combining, and recovering ethyl.
NOVELTY - The method involves providing built-in microwave reactor in which microwave digestion temperature is set to specific value and microwave digestion sludge with anaerobic bacteria is added. The microwave digestion process is performed by methane gas collected in methane collecting tower (10). A sludge dewatering tank (5) is arranged for dewatering the sludge. A sludge fermentation gas is entered into deodorization tower (12) in which sodium hydroxide and sodium bicarbonate solutions are added. The sludge dewatering tank extrusion liquid is entered into sludge fermentation tank (6).    USE - Sludge treatment method of sewage plant.    ADVANTAGE - The sludge treatment process of sewage plant is performed effectively with high flexible operation reliability, long service life, improved treatment effect, small usage area, reduced noise and reduced atmospheric pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sludge treatment method of sewage plant. (Drawing includes non-English language text)    Sludge screening equipment (1)    Sludge dewatering tank (5)    Sludge fermentation tank (6)    Methane collecting tower (10)    Deodorization tower (12)
NOVELTY - Preparation of sludge mixture involves deodorizing 70-80 pts. wt. renewable sludge, sterilizing, adding 1-3 wt.% biomass vinegar liquid, placing for 2-3 hours to obtain treated sludge, adding 3-5 pts. wt. sodium carbonate, 1-5 pts. wt. strong oxidizing catalyst, 1-5 pts. wt. sodium chloride and 1-5 pts. wt. detergent, spraying 20-30 pts. wt. limestone, placing for 1-2 hours, subjecting the obtained mixture to high-temperature sterilization at 100-300 degrees C, drying with moisture content of 15-45%, filtering and molding.    USE - Preparation of sludge mixture used for renewable fuels (claimed).    ADVANTAGE - The method enables preparation of sludge mixture having high calorific value and low coal ignition point.    DETAILED DESCRIPTION - Preparation of sludge mixture involves deodorizing 70-80 pts. wt. renewable sludge, sterilizing, adding 1-3 wt.% biomass vinegar liquid, placing for 2-3 hours to obtain treated sludge, crushing 3-5 pts. wt. sodium carbonate, 1-5 pts. wt. strong oxidizing catalyst, 1-5 pts. wt. sodium chloride and 1-5 pts. wt. detergent, spraying 20-30 pts. wt. limestone, placing for 1-2 hours, subjecting the obtained mixture to high-temperature sterilization at 100-300 degrees C, drying with moisture content of 15-45%, filtering to remove impurities with particle size of 6 mm or more and molding.
NOVELTY - Producing methane involves mixing tourmaline powder, activated carbon powder or graphite as additive, Cyanobacteria or straw as fermentation substrate in fermenter to carry out anaerobic fermentation to produce methane.    USE - Method for producing methane (claimed).    ADVANTAGE - The method enables to produce methane with improved efficiency.
NOVELTY - The wastewater is subjected to ultrasonic-biological-denitrification treatment using nitrification bacteria, and activity of nitrifying bacteria is inhibited.    USE - Ultrasonic-biological-denitrification treatment of wastewater in aeration tank and sludge return pipe (claimed).    ADVANTAGE - The method enables stable and efficient ultrasonic-biological-denitrification treatment of wastewater.
NOVELTY - The stirrer has a geared motor (1) provided with a shaft (2), which is fitted with a scraping element (6), a breaking unit (5) and mixing elements (3, 4). A rigid structure (10) is connected with the geared motor, which is connected with the mixing elements that are removably attached with a breaking unit. A coupler unit (9) is connected with a lower end of the scraping element, which is provided with a coupler part (7) and a thrust bearing (8).    USE - Stirrer i.e. micro biogas fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a stirrer.    Geared motor (1)    Shaft (2)    Mixing elements (3, 4)    Breaking unit (5)    Scraping element (6)    Coupler part (7)    Thrust bearing (8)    Coupler unit (9)    Rigid structure (10)
NOVELTY - Slow-release organic fertilizer comprises 55-75 wt.% crushed branches, 25-45 wt.% animal manure, 2-5 wt.% phosphate fertilizer, 1-3 wt.% iron fertilizer and 1.5-3 wt.% cellulolytic bacteria.    USE - As slow-release organic fertilizer.    ADVANTAGE - The organic fertilizer is easy to obtain and rich in nutrients, activates soil nutrients, improves soil texture, enhances plant absorption of nutrients, and reduces pest diseases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned organic fertilizer, which involves (a) collecting willow branches, and crushing branches, (b) adding other raw materials into the crushed branches, and uniformly mixing materials, (c) stacking the mixture, maintaining the moisture content of the mixture to 58-62%, and piling mixture, (d) controlling pile height of the mixture to 1-1.5 m, (e) turning the compost mixture, and (f) controlling temperature and volume of the compost mixture, and preparing fertilizer.
NOVELTY - Preparation of zoledronate sodium salt involves reacting imidazol-1-yl-acetic acid hydrochloride as raw material in ionic liquid as reaction medium, condensing by phosphoric acid and phosphorus trichloride, hydrolyzing, obtaining zoledronic acid monohydrate and reacting with sodium hydroxide. Ionic liquid is 1-butyl-3-methylimidazolium tetrafluoroborate, N-ethylpyridinium tetrafluoroborate, 1-n-butyl-3-methylimidazolium hexafluorophosphate, 1-hydroxyethyl-2,3-dimethylimidazolium chloride, 1-propylronitrile-3-methylimidazolium chloride or 1-carboxyethyl-3-methylimidazolium chloride.    USE - Preparation of zoledronate sodium salt used for preparing drug.    ADVANTAGE - The method provides zoledronate sodium salt with high yield and purity, by simple and environmentally-friendly process.
NOVELTY - Preparing 10% carbofuran controlled-release pesticide granule, involves mixing soft water and film-forming agent, sequentially adding dispersing agent, coloring agent, defoaming agent, oil and kaolin, to mixture, stirring added materials, sequentially adding carbofuran and cross-linking agent, stirring added materials to obtain mixed solution, performing wet grinding of the mixed solution to obtain paste, dehydrating river sand, mixing dried river sand and the paste, granulating mixture, and drying granules.    USE - The method is useful for preparing 10% carbofuran controlled-release pesticide granule (claimed).    ADVANTAGE - The method prepares pesticide granule that provides pesticide effect for long period of time, and causes only minimal effects on environment.    DETAILED DESCRIPTION - Method for preparing 10% carbofuran controlled-release pesticide granule, involves mixing soft water and film-forming agent at 50-60 degrees C for 40 minutes, sequentially adding dispersing agent, coloring agent, defoaming agent, oil and kaolin, to mixture, stirring added materials for 15 minutes, sequentially adding carbofuran and cross-linking agent, stirring added materials for 15 minutes to obtain mixed solution, performing wet grinding of the mixed solution to obtain paste, dehydrating river sand to obtain dried river sand, mixing dried river sand and the paste, granulating mixture, and drying granules.
NOVELTY - A fuel reformer (10) comprises inner cylinder (11) with combustor (14) inside, outer cylinder (12) which accommodates inner cylinder inside, space dividing outer peripheral surface of inner cylinder and internal peripheral surface of outer cylinder, evaporation part (21) for heating supplied water to produce water vapor for reformation, and cylindrical-shaped water absorbing component (22), in which helical flow path is formed beforehand, positioned at the evaporation part.    USE - A fuel reformer for steam-reforming to-be-modified gas to produce fuel gas to be supplied to fuel cell (claimed).    ADVANTAGE - Fuel reformer can improve freedom degree of formation position of a flow path while suppressing manufacturing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a vertical cross-sectional diagram of a fuel reformer. (Drawing includes non-English language text).    Fuel reformer (10)    Inner cylinder (11)    Outer cylinder (12)    Combustor (14)    Evaporation part (21)    Water absorbing component (22)
NOVELTY - A modifier (20) comprises hydrogen-containing gas production line (K) which circulates fluid containing hydrogen-containing fuel and produces hydrogen-containing gas and recycle gas line (R) which circulates hydrogen-containing gas upstream of modifier through hydrogen-containing gas production line as recycle gas. Recycle gas line is arranged so that recycle gas to circulate may heat-exchange with fluid of hydrogen-containing gas production line.    USE - A modifier for fuel cell system (claimed).    ADVANTAGE - The modifier can suppress the generating efficiency fall of a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a plane cross-sectional diagram of the modifier. (Drawing includes non-English language text).    Modifier (20)    Modification catalyst (24)    Shift catalyst (27)    Hydrogen-containing gas production line (K)    Recycle gas line (R)
NOVELTY - The hydrogen and oxygen gas manufacturing, storage and transportation system has a deep sealed production chamber (10) capable of withstanding high pressure, and an electrolyzing device which is positioned at the bottom of the production chamber for producing hydrogen and oxygen gas under pressure, and an oxygen escape pipe (18) extending from the exterior to bottom of chamber. The anode of the electrolyzing device is provided at the bottom (20) of oxygen escape pipe, for generating oxygen within the pipe with the electrolyzing device.    USE - Manufacturing, storage and transportation system of hydrogen and oxygen gas used for electric power generation, fuel for hydrogen-powered vehicles.    ADVANTAGE - Provides a production chamber which maintains adequate pressure of the hydrogen and oxygen gases produced, but does not require extension of production chamber downwardly to great depths, thus reducing production costs for building the system. The waste product of the system is clean water which flows by gravity back into the water source, without requiring pumps to move the water in and out of the chambers, and compressors to pressurize and move the hydrogen and oxygen gases from the storage structures, to the power plant or another consuming use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a manufacturing, storage and transportation method of hydrogen and oxygen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the manufacture, storage and transportation system of hydrogen and oxygen gas.    Production chamber (10)    Water source (11)    Water (16)    Oxygen escape pipe (18)    Escape pipe bottom (20)
NOVELTY - Preparation of methanation catalyst involves contacting nickel-aluminum alloy and alkali in water.    USE - Preparation of methanation catalyst used for removing traces of carbon oxide and hydrogen (all claimed).    ADVANTAGE - The method provides catalyst having high mechanical strength, and excellent low-temperature high selectivity methanation performance, using reduced amount of alkali.
NOVELTY - An environmentally-friendly biodiesel comprises 0.04 wt.% No. 120 solvent oil, 0.016 wt.% fatty acid methyl ester, 0.014 wt.% ethylhexyl nitrate, 0.02 wt.% copper naphthenate, 0.012 wt.% manganese naphthenate, 0.012 wt.% barium naphthenate, 0.012 wt.% alkanolamine triacetate, 0.05 wt.% ethyl acetate, 3.8 wt.% barium sulfonate and 0.024 wt.% dioctyl sodium sulfosuccinate as additives. Also claimed is the production method of the biodiesel.    USE - Environmentally-friendly biodiesel used for vehicles, ships, and all types of diesel engines.    ADVANTAGE - The environmentally-friendly biodiesel has excellent low-temperature resistance, improved quality, excellent solubility, water resistance, contributes to energy saving, and is manufactured by a simple process.
NOVELTY - The method involves converting nitrogen component in wastewater into nitrate nitrogen or nitrite nitrogen, and calculating oxygen demand from amount of total oxygen consumed in measuring time. A value is converted into oxygen demand of reducing agent, based on relationship between activated-sludge mixing liquid quantity and amount of addition reducing agents. BODact is made as parameter of oxygen consumption coefficient in case of disassembly of soluble easily decomposable organic substance in activated-sludge liquid mixture and reducing agent liquid.    USE - Operating method of biotic denitrifying processing apparatus used for processing waste water.    ADVANTAGE - Since the amount of reducing agents to the denitrifying process is controlled appropriately, the untreated BOD load of the denitrifying process processing water is reduced, and the denitrifying reducing agent expense is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biotic denitrifying processing apparatus. (Drawing includes non-English language text)    Biological denitrification apparatus (1)    Nitrification tank (2)    Denitrifying tank (3)    Sedimentation tank (5)    Return-sludge line (5a)
NOVELTY - A reactor cartridge comprises body (11, 12, 13) enclosing, core in containment vessel having exit nozzle, greater than or equal to 1 elastomeric winding (25) surrounding the containment vessel, water line (100) which delivers fluid to core, and expanded PTFE tube having sealed end and open end fluidly connected to valve in which fluid delivered to core via water line urges the core to produce hydrogen via reaction and hydrogen permeates the expanded PTFE tube and is delivered to the valve.    USE - A reactor cartridge for production of hydrogen (claimed).    ADVANTAGE - Hydrogen and other products produced by reactor are filtered with clog-less filter and pure hydrogen is output.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) production of hydrogen from cartridge with elastomeric reactor and clog-less filter which involves placing fuel pellet in containment wound with elastomeric windings (25) inside a wrapping in sealed fuel cartridge (10), adding water to fuel pellet in containment, generating hydrogen gas and other products from water and fuel pellet reaction, filtering the produced product with clog-less filter connected to expanded PTFE tube containing desiccant, and outputting hydrogen post filtration from expanded PTFE tube unit (200); and    (2) fuel for cartridge comprising solid portion containing 70% sodium borohydride and 30% oxalic acid and liquid portion containing 98% distilled water and 2% cobalt chloride hexahydrate.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the elastomeric hydrogen reactor device and system.    Fuel cartridge (10)    Body (11, 12, 13)    Elastomeric winding (25)    Water line (100)    Expanded PTFE tube unit (200)
NOVELTY - The utility model claims a... catalyze gasification system, relating to catalyze gasification technology area. For solving the technology of catalyze gasification system of high energy consumption, low efficiency, equipment investment is large and the carbon conversion rate is low but a problem. The utility model is a catalyze gasification system, comprising a reactor entrance and the first slag ash, the ash outlet of the reactor and said first hopper connected, the gas outlet of the reactor and between gas entrance and the first slag provided with heat exchanger, inside the reactor and a product gas through the heat exchanger after entering into the first hopper, wherein the first slag and ash in a later a product outlet and a first slag discharging. This utility model new catalyze gasification system for generating methane gas.
NOVELTY - The utility model claims a a a a kind of biological diesel oil distillation tower, distillation tower comprises a tower body, a left film heater and the tower top condenser, a finished product cooling device, and right film heater and circulation pump, left and right tower distillation tower lower part two side respectively connected a left reducing film heater and right film heater and, left film heater and a pipeline and a connected feedstock, plant asphalt circle a distillation tower and a tower through pipeline and circulation pump connected, and right film heater top through pipeline and circulation pump connected, bottom and right film heater and provided with plant asphalt discharging port, tower top condenser connected with distillation tower body and tower top gas phase outlet part, finished product cooling device and tower top condenser connected with. The utility model using a falling film method using material staying a short in a heater, reducing of material coking and heat to resolve a risk. Reducing right film heater bottom equipped with a asphalt, reducing a material residue in tower is a circulation times, reducing of material coking and heat to resolve a risk.
NOVELTY - This new utility model claims a reaction device for manufacturing biological diesel oil, comprises reactor, circulation pump, a condenser, a heater and distributor, top part of said reactor equipped with feedstock port and vent, the bottom reactor equipped with discharging port, upper end of reactor equipped with distributor, distributor through pipeline and circulation pump connected with the circulation pump respectively connected with and lipid feeding port and discharging port, upper is connected with distributor and pipeline circulation pump set with heater, vent and condenser connected with emptying. This new utility model structure is simple, the cost is low, operation is simple, production energy consumption low, it is suitable for waste animal and vegetable lipid (such as channel of oil, hogwash oil, animal and plant oil foot, comprising palm acidification oil of each of acidified oil) and microorganism lipid manufacturing biological diesel oil.
NOVELTY - This utility model refers to a methyl alcohol gasoline special for vaporizing reaction mchine, comprising distiller and a condenser, between the distiller and the condenser by pipeline connected with, in the condensing set with exhauster to pump, and pipeline connected with the working efficiency high, purifying precision high, suitable can quickly remove residue, convenient maintenance, saving of cost.
NOVELTY - Of the new utility model claims of a kind of a biomass pyrolysis device based on the microwave, a microwave reaction tank, a microwave reaction tank is set with with a microwave generator, microwave reaction tank and upper end part and side wall are installed with a hollow stop tube, internal bottom of microwave reaction tank is set with with isolating plate, isolation pad plate mounted with exit of the reactor, reactor connected with gas-guide tube, a gas tube and a condensation collector. This utility model through a reactor using a e microwave reaction tank, a biomass can be under a function of microwave heating, and can be a condensation device for a pyrolysis product, at the same time can prevent the microwave leakage.
NOVELTY - The utility model claims a new simple a biological coal preparation device, comprising a cover (1), a device main body (11) and pedestal (10) are equal, wherein the main body (11) comprises the third layer, from outside to inside is a metal shell (3), insulating layer (4) and pyrolysis reaction container (5). The utility model is a new design, reasonable design, suitable use, convenient carry, can meet scientific research process at a small amount of biological coal, has large practicability.
NOVELTY - The utility model claims a a a a kind of energy saving biomass gasification furnace, a bracket, a bracket mounted with a furnace body, a top furnace body is provided with an air outlet, a furnace body top end and side wall mounted with a discharge end into to extruding and pelletizing device of internal furnace body, a furnace material combustion producing the fuel gas and heat rising to furnace body top, extruding the material to a granulating device for heating in a high temperature material by extruding and granulating device and extrusion forming a push to. , a material discharging end of the extrusion granulating device into a body inside, extruding and granulating device via extrusion material generating a large amount of heat and increase temperature of the material, the heat generation is complete using, at the same time the utility model use a gas carry and continue to heat material by heating, realize a waste heat use, increase of original gasification temperature of a block, which greatly increase of gasification efficiency, this utility new type extruding and granulating device and furnace body sealing matching, can realize no leakage continuous feedstock, which ensures a safe production.
NOVELTY - The utility model claims a of a production of biomass granule fuel for drying machine, comprising a machine box, a hopper, a electromagnet, pulverizer, transporting belt, air-blowing drier, suction wind remove wet machine and discharging port, a hopper is set with is set with on the drier tank inside for a hopper in a machine top box, the electromagnet plate, the pulverizer is set with electromagnet at a low, the transporting belt is set with a pulverizer, the air-blowing drier is set with a drier box bottom, a suction wind remove wet machine is set with transporting belt at upper part, a discharge port formed in a machine box. This new utility model is reasonable structure, each step for processing raw material of collective on one platform machine inside, reduce production cost and increase production efficiency.
NOVELTY - Biofuel production vehicle comprises a vehicle body which is set on a traveling crane system, a waste processing system and a biofuel production system. The vehicle body is provided with storage containers (12) set on a feeding device. The feeding device comprises a feeding interface (14) which is connected to a magnetic selection device (15). The upper part of the magnetic selection device is set with a selection fan (16). The one side of the selection fan is provided with a rake feeder (17).    USE - The vehicle is useful for treating waste (claimed).    ADVANTAGE - The vehicle easily stores, and transports waste; is economical; and saves labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biofuel production vehicle for treating waste.    Storage containers (12)    Feeding interface (14)    Magnetic selection device (15)    Selection fan (16)    Rake feeder (17)
NOVELTY - A bottom of the utility model is a new supply of a kind of a portable hydrogen-enriched water electrolytic device, the electrolytic rod (1), a battery (2), control circuit (3), a starting key (4), a shell (5), battery base (6), the electrolytic rod (1) installed in the sealing shell (5), a battery (2), control circuit (3) is respectively mounted on the battery seat (6), a battery seat (6) installed on the shell (5), a starting key (4) installed in the shell (5), a control circuit (3) respectively and the electrolytic rod (1), a battery (2) connected with power, the starting key (4) start up the control circuit (3) controlling the electrolytic bar (1) electrolytic water hydrogen manufacture. The portable hydrogen-enriched water electrolytic device has simple structure, convenient carry, low cost, closed direct use, suitable cleaning, electrolytic efficiency is high, no precipitate and fouling product.
NOVELTY - The device has the feeding port (1) and discharging port that are set corresponding to inlet end cover (2) and discharging port end cover. A pipe type heat exchanger (7) is fixed in carbonization furnace. A heating carrier import is located correspond to heating carrier outlet located at left end of a lower end enclosure (10). The heating carrier import is symmetrical distributed on the lower end enclosure. The left and right sides of upper end enclosure (5) are set with catalyst import (4) connected to catalyst guide pipe (6).    USE - Organic biomass coal preparation device.    ADVANTAGE - Effective control of the carbonization furnace temperature and reaction time is ensured. Implementation of organic biomass coal is ensured. The process for preparation of the biomass organic coal is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic biomass coal preparation device.    Feeding port (1)    Inlet end cover (2)    Catalyst import (4)    Upper end enclosure (5)    Catalyst guide pipe (6)    Pipe type heat exchanger (7)    Lower end enclosure (10)
NOVELTY - The device has a pyrolysis reactor (1) that is connected to an oxidation reactor (2). The middle portion of oxidation reactor is connected to oxygen outlet of regeneration reactor (3). A stated unit (3a) is connected with smoke gas outlet (3c) of regeneration reactor. The feedstock port of oxidation reactor is connected with top of gasification reactor (4). A reaction tube is set vertical to regeneration reactor. A coke/bed material outlet of pyrolysis reactor is connected to gasification reactor and regeneration reactor.    USE - Device for performing biomass grading gasification for producing enriching hydrogen gas.    ADVANTAGE - The tar carbon conversion process is avoided. The condensation of pyrolysis gas and tar caused by downstream device failure is avoided. The carbon di oxide is collected easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for performing biomass grading gasification for producing enriching hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device for performing biomass grading gasification for producing enriching hydrogen gas.    Pyrolysis reactor (1)    Oxidation reactor (2)    Regeneration reactor (3)    Stated unit (3a)    Smoke gas outlet (3c)    Gasification reactor (4)
NOVELTY - The apparatus has a remove glue kettle (3) whose upper end is respectively provided with feedstock. A discharging port is connected to raw material oil feedstock port which is connected with upper end of first reaction kettle (7). A second reaction kettle (8) is equipped with upper end port and feedstock gas phase outlet. A third reaction kettle (9) is equipped with upper end port and feedstock gas phase outlet. The discharging pipe is connected to a first flash evaporation remove alcohol unit (12). A sedimentation pool or centrifugal machine is connected to a second alcohol unit (15).    USE - Apparatus for performing continuous gas phase catalytic esterification of biodiesel.    ADVANTAGE - The methanol circulation amount is reduced. The manufacturing cost is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing continuous gas phase catalyzed biologic diesel oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the apparatus for performing continuous gas phase catalytic esterification of biodiesel.    Remove glue kettle (3)    First reaction kettle (7)    Second reaction kettle (8)    Third reaction kettle (9)    First flash evaporation remove alcohol unit (12)    Second flash evaporation remove alcohol unit (15)
NOVELTY - The generator has an outer portion with a set of main conversion splitter (101), a set of front converter splitter (15) and a set of rear converter splitter (17). The front converter splitter is connected to the alternating current (AC) adapter for converting power from alternating current into direct current. The front converter splitter is connected to input electrode plates (111) of the power cable. A transformer (16) and shunt units manufacture mass and rapid hydrogen gas using front and rear converter splitters and multi-group diverter assembly cell, after the conversion.    USE - Hydrogen generator.    ADVANTAGE - Mass production of rapid hydrogen gas is attained by hydrogen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen generator.    Front converter splitter (15)    Transformer (16)    Rear converter splitter (17)    Main conversion splitter (101)    Electrode plate (111)
NOVELTY - The apparatus has a mixing tank that is communicated with an electrolysis unit and gas supply unit. The interior portion is filled with liquid catalyst mixing tank. Hydrogen and oxygen are contained in the electrolysis cell output and air supply unit output. The air is contacted with the liquid catalyst in order to produce combustible gas after output to burner. The burner is used to detect flammable gas consumption size, so as to control the change of electrolysis unit.    USE - Oxygen-containing gaseous fuel production apparatus.    ADVANTAGE - The electrolytic generation of oxygen and hydrogen amount is achieved, such that the safety of oxygen-containing gaseous fuel production apparatus is increased reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oxygen-containing gaseous fuel production apparatus.    Electrode (264)    Power supply unit (266)    Check valve (282)    Flow control valve (284)    Gas-liquid separator (366)
NOVELTY - The device has an aerobic treatment device (1) that is provided for degradation and adsorption of sewage. A sediment device is provided for performing adsorption and sedimentation treatment of sewage. The aerobic treatment device is filled with a multi-microorganism ball element (3). Multiple clapboards (4,5) are arranged vertically in aerobic treatment device. The blocking effect of sewage in the aerobic treatment device is provided by the clapboards. The microorganism ball element is extended to the sewage compound.    USE - Device for removing sewage compound.    ADVANTAGE - The degradation and precipitation treatment of sewage is performed, and the supernatant water is treated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for removing sewage compound.    Aerobic treatment device (1)    Microorganism ball element (3)    Clapboards (4,5)    Fan (6)    Carrier separator (8)
NOVELTY - The device has a fermentation pool (10,20,30) that is connected with a water pressure pipe comprising a feedstock (40) and a discharge pipe. The middle portion of fermentation pool is provided with a fermentation chamber connected with a feeding port and discharging port. A gas feedstock port is arranged close to the side wall of gas baffle plate. The side surface of fermentation pool is provided with a pull rod. A transverse rod is connected with one end side of a vertical rod. The side surface of fermentation pool is fixed with a gas-guide tube.    USE - Large multistage interaction biogas fermentation device.    ADVANTAGE - The block in fermentation device is avoided, and fermentation efficiency is improved. Since the expensive membrane portion is replaced, the cost is reduced. The device structure is reasonable with reduced manufacturing difficulty.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the large multistage interaction biogas fermentation device.    Fermentation pools (10,20,30)    Feedstock (40)    Water inlet (50)
NOVELTY - The system has first fermentation tank (10) that is provided with a rod. The rod includes rails and stanchions. A vertical rod is connected with a gas fermentation chamber wall through a sidewall lower plate. The gas fermentation chamber is fixedly connected with an air plate. A first pipe is connected with discharging port of sub fermentation tank drain pipe. A water pipe is arranged with biogas slurry. The drain pipe is located on same point of horizontal plane.    USE - Parallel type ultra-efficient biogas fermentation system.    ADVANTAGE - The uniform distribution of strains is improved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the parallel type ultra-efficient biogas fermentation system.    Fermentation tanks (10,20,30)    Hydraulic pressure (40)    Storage unit (50)    Pull rod (60)    Aqueduct (70)
NOVELTY - Generating biogas by fermentation using S-shaped fermentation tank, comprises pouring fermentation raw materials into feed inside mouth, pulling supporting rod, fixing first connecting rod in upward movement on bottom supporting rod, promoting uniform distribution of fermentation; removing blocking in fermentation tank by pressing supporting rod, pushing and rotating first connecting rod and second connecting rod with baffle to downward deflection so that rotation baffle tend to horizontal state; generating biogas, accumulating in gas storage plate and discharging.    USE - The method is useful for generating biogas by fermentation using S-shaped fermentation tank (claimed).    DETAILED DESCRIPTION - Generating biogas by fermentation using S-shaped fermentation tank, comprises (a) pouring fermentation raw materials into feed inside the mouth, pulling the supporting rod, fixing first connecting rod in upward movement on the bottom supporting rod, pulling active connection of first connecting rod and second connecting rod at the bottom of the support bar of rotating baffle upward deflection, fixing upper supporting rod and lower supporting rod using bolt or screw, pulling the supporting rod back and forth and driving vertically the rotating baffle, swinging back and forth, promoting uniform distribution of fermentation; (b) removing blocking in fermentation tank by pressing supporting rod, moving first connecting rod fixed on the bottom of supporting rod to downward movement, pushing and rotating the first connecting rod and the second connecting rod with baffle to downward deflection so that rotation baffle tend to horizontal state, pulling the supporting rod back and forth and driving horizontally rotating baffle, swinging back and forth; and (c) generating biogas, accumulating in the gas storage plate, passing via gas storage plate through external airway to output biogas.
NOVELTY - The system has fermentation tank portion (10) that is provided with a fermentation chamber provided with separating plate (30). The fermentation chamber is fixed with biogas storage plate (20) provided with biogas guide tube (22). The feed inlet (12) and outlet (14) are arranged on spaces between the ends of biogas storage plate and fermentation tank. A stirring groove (16) is arranged between the side walls of biogas storage plate and fermentation tank and between the side walls of biogas storage plate and separating plate. The stirring groove is arranged inside stirring device (40).    USE - Long path fermentation system for fermentation of animal manure slurry.    ADVANTAGE - The stable gas flow is guaranteed to increase the stability of the equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the long path fermentation system.    Fermentation tank portion (10)    Feed inlet (12)    Outlet (14)    Stirring groove (16)    Biogas storage plate (20)    Biogas guide tube (22)    Separating plate (30)    Stirring device (40)
NOVELTY - The method involves fixing a stirring sleeve in a fermentation system and connecting a terminal of sleeve with a pneumatic piston. The left outside sleeve is fixed with a left spring contacted with the stirring sleeve. The left sleeve is connected with an air discharging pipe. The left sleeve is moved to left side and the right side sleeve is moved to right side, under the action of air pressure. The pneumatic piston reset, for performing fixed and a mobile stirring except the outer region of left sleeve and right sleeve.    USE - Biogas slurry stirring method for automatic circulation stirring device.    ADVANTAGE - Since the biogas storage plate drives pneumatic piston in the stirring sleeve, the biogas slurry is stirred with the stirring net. Hence, the uniform distribution of the fermentation material and the strains is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic circulation stirring device.    Gas storage (20)    Baffle plates (26,28)    Automatic circulation stirring device (400)    Stirring net (410)
NOVELTY - The system has a biogas slurry processing unit that includes a marsh liquid pool, an aerobic fermentation pool, a sediment pool and a harmless treatment pool connected with a storage unit. A nutrition liquid storing pool and a harmless treatment pool are connected with a mixing distribution pool. The nutrient liquid storage pool and irrigation water storing pool are respectively connected with a mixing distribution pool. A first end of irrigation system is connected with a mixing distribution pool and second end is distributed to field.    USE - Biogas slurry application system used in livestock and poultry industry.    ADVANTAGE - The heavy metal, harmful microbe and other impurities in biogas slurry are removed effectively. The biogas slurry harmness is eliminated. The biogas slurry is fully utilized for efficient irrigation.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the operation of biogas slurry application system. (Drawing includes non-English language text)
NOVELTY - The synthesis method of beta -unsaturated ketones involves adding catalytic calcium hydroxide to low concentrated alcohol solution, uniformly mixing, and carrying out aldol condensation reaction in the presence of aldehydes and ketones.    USE - The method is useful for synthesis of beta -unsaturated ketones (claimed).    ADVANTAGE - The method enables economical synthesis of beta -unsaturated ketones with high yield, and excellent corrosion resistance and durability in an environmentally-friendly manner.
NOVELTY - The portable preparation device has a main outlet (5) that is arranged at a middle portion on an upper cover (4). An air tube (1) is connected with an upper portion of the main outlet, while a lower portion of the main outlet is connected with a side wall of the air tube. A middle portion of the air tube is provided with a handle (2), and the upper cover is uniformly distributed with several outlet channels (3). A bottom of a supporting face (9) is provided with a supporting column (14) which extends between the supporting face and a furnace bottom (11).    USE - Portable preparation device of straw biochar.    ADVANTAGE - The portable preparation device of straw biochar is featured portability, uniform temperature distribution effect, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for straw biochar preparation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of the portable preparation device of straw biochar.    Air tube (1)    Handle (2)    Outlet channel (3)    Upper cover (4)    Main outlet (5)    Supporting face (9)    Furnace bottom (11)    Supporting column (14)
NOVELTY - The hydrogen-oxygen generating device has a cylindrical tube (1) that is provided with a sealing plate (2) to which a round hole is provided. The round hole is welded to a small cylinder (3) to form an electrolytic groove (4). An upper end of the small cylinder is provided with a turbine generator (5) to which an electrolysis cathode (6) and an electrolysis anode (7) are connected. The electrolytic groove is provided with a cone gas collection cover (8) to which a tube (9) is connected.    USE - Hydrogen-oxygen generating device.    ADVANTAGE - The electrolytic generation of hydrogen and oxygen is efficient. The material cost for generating hydrogen-oxygen is reduced. The time for generation of hydrogen and oxygen is saved, without pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing hydrogen-oxygen generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen-oxygen generating device.    Cylindrical tube (1)    Sealing plate (2)    Small cylinder (3)    Electrolytic groove (4)    Turbine generator (5)    Electrolysis cathode (6)    Electrolysis anode (7)    Cone gas collection cover (8)    Tube (9)
NOVELTY - Depressant composition comprises 2.5-10 pts. wt. isodecyl methacrylate, 2.5-10 pts. wt. ethyl acetoacetate and 2.5-10 pts. wt. isooctyl acrylate.    USE - Depressant composition for biological diesel oil (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing depressant composition, which involves using isodecyl methacrylate, ethyl acetoacetate and isooctyl acrylate.
NOVELTY - Fuel oil composition comprises 60 wt.% light diesel oil, 38.5 wt.% tap water, 2 wt.% toner, 0.16 wt.% fusion agent, peregal, alkanolamide, p-(1-methylheptyl)phenol, sorbitol esters, acetic anhydride, cyclohexanol, isopropylamine, cyclohexane and methyl phenyl carbinol.    USE - Fuel oil composition.    ADVANTAGE - The fuel oil composition ensures good quality.
NOVELTY - Preparation of synthetic natural gas involves taking crude gas, removing hydrogen sulfide in first absorber (A1) to obtain purified gas, dividing into two, transferring first purified gas to adiabatic methanation reactor (R03) and second purified gas to isothermal methanation reactor (R02) with catalytic agents, adding superheated steam to adjust carbon monoxide and hydrogen gas at molar ratio of 1:2.95-3.05, transferring first reaction gas to recycle gas compressor (K01), recycling compressed gas to adiabatic methanation reactor (R03), cooling second reaction gas and separating condensate.    USE - Method for preparing synthetic natural gas.    ADVANTAGE - The method is simple and short, has low operating and investment costs, and has centralized heat recovery.    DETAILED DESCRIPTION - Preparation of synthetic natural gas comprises taking crude gas, removing hydrogen sulfide with Rectisol (RTM: acid gas removal solvent) in first absorber (A1) to obtain purified gas, dividing into two, transferring first purified gas to adiabatic methanation reactor (R03) with steam superheater (E03) and second purified gas to isothermal methanation reactor (R02) with upper layer and lower layer catalytic agents, adding superheated steam to adjust carbon monoxide and hydrogen gas at molar ratio of 1:2.95-3.05, transferring first reaction gas to recycle gas compressor (K01), recycling compressed gas to adiabatic methanation reactor (R03), cooling second reaction gas, separating condensate and removing carbon dioxide with Rectisol (RTM: acid gas removal solvent) in second absorber (A2).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of system for preparing synthetic natural gas.    First absorber (A1)    Second absorber (A2)    Steam superheater (E03)    Recycle gas compressor (K01)    Isothermal methanation reactor (R02)    Adiabatic methanation reactor (R03)
NOVELTY - The device has a red mud plastic film (1) that is sealed with an adhesive layer. The inlet end of a fermentation tank is provided with a feeding tube (3). A discharging pipe (4) is inserted into a discharge opening portion formed in other side of the fermentation tank. A slag discharging pipe (5) is connected with the discharging pipe.    USE - Full-molded soft plastic type anaerobic device used in bio-gas production industry.    ADVANTAGE - The structure of anaerobic device can be simplified. The pressure of water inside fermentation tank can be adjusted automatically. The anaerobic device can be operated and carried easily. The anaerobic device can be installed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the full-molded soft plastic type anaerobic device.    Red mud plastic film (1)    Feeding tube (3)    Discharging pipe (4)    Slag discharging pipe (5)    Hook hole (7)
NOVELTY - Preparing traditional Chinese medicine involves weighing chicken bone extract (50-60 parts), antler glue (100-110 parts), ootheca mantidis (50-60 parts), calcined oyster (30-50 parts), cuttlebone (50-60 parts), ginseng (100-110 parts), Astragalus (20-30 parts), Angelica (120-130 parts), white peony root (100-110 parts), Cyperus vinegar (100-110 parts), aspartame (50-60 parts), licorice (20-30 parts), radix Rehmannia (200-220 parts), rhizome Rehmannia (200-220 parts), and Ligusticum chuanxiong hort (50-60 parts).    USE - Preparing traditional Chinese medicine used for treating inflammation and spasm (claimed).    DETAILED DESCRIPTION - Preparing traditional Chinese medicine involves weighing chicken bone extract (50-60 parts), antler glue (100-110 parts), ootheca mantidis (50-60 parts), calcined oyster (30-50 parts), cuttlebone (50-60 parts), ginseng (100-110 parts), Astragalus (20-30 parts), Angelica (120-130 parts), white peony root (100-110 parts), Cyperus vinegar (100-110 parts), aspartame (50-60 parts), licorice (20-30 parts), radix Rehmannia (200-220 parts), rhizome Rehmannia (200-220 parts), Ligusticum chuanxiong hort (50-60 parts), Bupleurum (20-30 parts), Salvia (100-110 parts), yam (100-110 parts), gordon euryale seed (50-60 parts), and Aspidium cornu cervi (30-50 parts). Astragalus, white peony root, aspartame, ginseng, Bupleurum, and licorice are extracted in ethanol to obtain filtrate. Obtained filtrate is dried under reduced pressure to obtain a dry product. Cuttlebone, ootheca mantidis, radix Rehmannia, Ligusticum chuanxiong hort, Salvia, calcined oyster, Angelica, Cyperus, rhizome Rehmannia, gordon euryale seed, yam and Aspidium cornu cervi are extracted with water to obtain filtrate. Obtained filtrate is concentrated under reduced pressure to obtain another dry product. Obtained products are mixed with chicken extract to obtain final product.
NOVELTY - A methane-bacteria activator comprises 5-50 pts. wt. methane-bacteria growth regulator, 1-10 pts. wt. nitrogen, 100 pts. wt. water, 1-5 pts. wt. phosphorus, 0.1-1 pts. wt. sulfur, 0.5-5 pts. wt. metal material and 100 pts. wt. refined alcohol which is obtained by refining waste alcohol having concentration of 10-80 wt.%.    USE - Activator is used for methane-bacteria used in unit for processing industrial wastewater (claimed) during production of biogas.    ADVANTAGE - The activator has excellent fermentation efficiency. The biogas is produced economically during industrial wastewater processing.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of methane-bacteria activator; and    (2) industrial wastewater processing unit.
NOVELTY - Insect biocontrol storage method involves harvesting grains, full drying, finely selecting grains, preparing pithos, cleaning sacks, sterilizing warehouse, packaging chamber, sealing cover and ventilating warehouse.    USE - Insect biocontrol storage method for grains (claimed).    ADVANTAGE - The insect biocontrol storage method is simple, environment friendly and has good anti-bacterial effect of pest control.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an insect biocontrol storage method for grains, which involves:    (A) removing impurities from the mature grains to ensure uniform heating;    (B) exposing the grains to the sun for 6-8 days to a moisture content of 6% -8%;    (C) detecting the imperfect particles and impurities of the grains to ensure the quality of grains storage and to prevent mildew fever;    (D) cutting yellow-green skin of grapefruit by a knife and keeping under sun for 4-6 days;    (E) keeping fresh cedrela sinensis tree leaf and peach tree leaves in the ratio of 1:1 under the sun to a moisture content of 2% -4% for future use;    (F) preparing pithos by spraying pesticide and keeping in sun exposure for a long time and covering the bottom of the container with 5-6 cm thick rice bran and the top with an oil cloth for future use;    (G) cleaning sacks by adding pepper to the boiling water in the mass ratio of 1:50,boiling for 10-20 minutes,cooling the solution to 60-70 degrees C,soaking the sack in the obtained solution for 20-30 minutes and drying naturally;    (H) sterilizing warehouse by spraying pesticide and ventilating for 1-3 hours;    (I) selecting fully dried grains and keeping in the cleaned pithos;    (J) sealing the pihos filled with grains with a pressure tight solid precast concrete and closing the warehouse; and    (K) ventilating the warehouse once at every 2-4 months and significantly cooling the warehouse to enhance grain storage.
NOVELTY - Screening nitrifying bacteria involves dividing stacked fertilizer into two equal parts and preparing compost in laboratory, respectively. Content, pH value, organic matter, ammonia nitrogen, nitrite and nitrate of the fertilizer are measured at different stage. The compost samples are heated, and rotten, screened fro circular projection, edge, yellow and smooth surface of bacterial strain. The strain is screened by using enriched culture to obtain conversion into nitrate and nitrite bacterial strain. The bacterial strain is spore bacteria of Bacillus strain N7.    USE - Method for screening nitrifying bacteria (claimed).    ADVANTAGE - The method enables to screen nitrifying bacteria in which new bacterial strain is obtained, which effectively promotes conversion of nitrogen to reduce ammonia emissions in composting process, improves environment pollute and increases nitrogen content in compost, which improves the quality of compost.
NOVELTY - Method for preparing cultivation material for cultivating Ganoderma lucidum, involves extracting shiitake mushroom using purified water, mixing extract with sawdust and soybean cake, maintaining obtained mixture at 60 degrees C for 24 hours, adding lime and gypsum, turning and fermenting the mixture, maintaining moisture content of fermented product at 63-65%, cooling fermented product, adding the product to polypropylene plastic bag, inoculating the G.lucidum into the bag, and cultivating the G.lucidum at 20-22 degrees C for 26-28 days.    USE - The method is useful for preparing cultivation material which is used for cultivating G.lucidum (claimed).    ADVANTAGE - The method improves growth of G.lucidum, saves labor, and is performed environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing cultivation material for cultivating Ganoderma lucidum, involves (a) obtaining 72-80% sawdust, 16-20% soybean cake, 3-4% shiitake mushroom, 1.5% lime and 1% gypsum, where particle diameter of the sawdust is 3-5 mm, and the shiitake mushroom is dried and crushed to obtain powder having particle diameter of 2-3 mm, (b) immersing the shiitake mushroom in 20-30 times purified water at low temperature for 18-24 hours, extracting obtained mixture, and uniformly mixing extract with the sawdust and soybean cake, (c) maintaining obtained mixture at 60 degrees C for 24 hours, adding lime and gypsum to the mixture, turning the mixture, fermenting the mixture for 5-6 days, and maintaining moisture content of fermented product at 63-65%, and (d) cooling fermented product, adding the product to polypropylene plastic bag, inoculating the G.lucidum into the bag, cultivating the G.lucidum at 20-22 degrees C for 26-28 days, and maintaining humidity at 60-75% during cultivating process.
NOVELTY - Preparation of everolimus intermediate (I-a) comprises dissolving rapamycin, methylamine, sodium bicarbonate and 2-((tert-butyldiphenylsilyl)oxy)ethyl trifluoromethanesulfonate in dichloromethane, treating and concentrating.    USE - Method for preparing everolimus intermediate used for preparing everolimus (claimed).    ADVANTAGE - The method is simple, ensures high yield, does not need column chromatography, and fits industrial application.    DETAILED DESCRIPTION - Preparation of everolimus intermediate of formula (I-a) comprises dissolving rapamycin, methylamine, sodium bicarbonate and 2-((tert-butyldiphenylsilyl)oxy)ethyl trifluoromethanesulfonate in dichloromethane, treating and concentrating.    INDEPENDENT CLAIMS are included for:    (1) preparation of everolimus of formula (II) comprising reacting (I-a) with hydrogen fluoride solution in organic solvent; and    (2) preparation of everolimus ethyl impurity of formula (I) comprising taking (II), acid and anhydrous ethanol, placing in reaction flask, heating, monitoring reaction, washing, and drying.
NOVELTY - The method involves acquiring water for performing an indirect heat exchange process. Waste heat generated is recycled by high pressure steam external supply. Biomass synthesis gas is obtained by a cyclone dust removal treatment. A cooling process is performed by flowing synthesis gas to an indirect heat exchanging process. A de-dusting cooling process is performed by using washing liquid. Dust content and tar content are obtained. A judgment is made whether temperature sensible heat recovery rate is greater than purification of biomass synthesis gas.    USE - Biomass synthesis gas pressure cooling purification method.    ADVANTAGE - The method enables cooling and purifying the biomass synthesis gas in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass synthesis gas pressure cooling purification device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass synthesis gas pressure cooling purification device.
NOVELTY - The high temperature heat insulating material includes a radiant heat shielding material which is formed of silicon carbide and tin oxide. A reinforcing material consists of inorganic fiber which is formed of glass fiber, carbon fiber and aluminum fiber. A core material consists of diatomite and fumed silica.    USE - High temperature heat insulating material for generating station, oil facility, equipment for steel manufacture and solid fuel cell.    ADVANTAGE - The manufacturing cost of the high temperature heat insulating material is reduced. The excellent mechanical strength of the high temperature heat insulating material can be secured. The high heat insulation property is achieved. The material which is harmful to the human body and the environment is suppressed.
NOVELTY - The method involves producing exhaust gas during a combustion process in a combustion chamber (10) of a combustion system (2), and treating the exhaust gas with a reducing agent, where constituent i.e. hydrogen, of fuel medium is used as a constituent of the reducing agent. The reducing agent is formed as a mixture of hydrogen and ammonia. The constituent of the fuel medium is produced by water electrolysis. A catalytic converter (22) for executing selective catalytic reduction of the exhaust gas is arranged in a reducing chamber (20).    USE - Method for aftertreatment of exhaust gas produced during combustion of fuel medium in an industrial system e.g. power plant and motor vehicle.    ADVANTAGE - The method enables the treating of the exhaust gas with the reducing agent, where constituent i.e. hydrogen, of fuel medium is used as the constituent of the reducing agent, thus achieving simple and inexpensive aftertreatment of the exhaust gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a combustion system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a combustion system with a gas turbine and an electrolyzer.    Combustion system (2)    Expander (6)    Combustion chamber (10)    Reducing chamber (20)    Catalytic converter (22)
NOVELTY - The method involves stacking a separator (40) and a thermoplastic resin frame (20) and creating a battery assembly (100). The separator and the resin frame are positioned in a case of a stack based on a first reference. The stack is arranged about the battery assembly. The battery assembly is positioned in the stack based on the second reference. The shape of the second reference is different from the first reference.    USE - Manufacturing method for fuel cell stack.    ADVANTAGE - The assembly accuracy of the fuel cell stack is improved by preventing the reference from being deformed.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the manufacturing method for the fuel cell stack. (Drawing includes non-English language texts).    Electric power generation body (10)    Resin frame (20)    Separator (40)    Battery assembly (100)
NOVELTY - The furnace has a hearth (1) connected with another hearth (2). The former hearth is fixed to a feedstock device (3). A bottom part of the hearth is connected to a reciprocating fire grate (11). The reciprocating fire grate is provided with a cooler (12) and an air chamber (13). Left and right side of the air chamber are provided with a front arch part (14) and a rear arch part (15) respectively. A flame baffling wall (16) is mounted on the rear arch part along longitudinal direction. Another flame baffling wall (21) is divided into two top parts by a cavity body (18).    USE - Reciprocating grate biomass multi-time gasification furnace.    ADVANTAGE - The furnace can improve combustion efficiency and utilize less space at time of combustion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reciprocating grate biomass multi-time gasification furnace.    Hearths (1,2)    Feedstock device (3)    Reciprocating fire grate (11)    Cooler (12)    Air chamber (13)    Front arch part (14)    Rear arch part (15)    Flame baffling walls (16,21)    Cavity body (18)
NOVELTY - A garbage fuel bar comprises 28-32 pts. wt. domestic garbage powder, 38-42 pts. wt. straw powder, 28-32 pts. wt. building garbage powder, and 7-9 pts. wt. high-efficiency plant particles.    USE - Garbage fuel bar (claimed).    ADVANTAGE - The garbage fuel bar saves cost by effectively using agricultural waste materials and has excellent thermal efficiency. The plant particles and straw powder serve as combustion improver.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of garbage fuel bar, which involves stirring all components, molding the mixture into product, and drying.
NOVELTY - The utility model claims a of a kind of a biomass fuel combustion system and again. Biomass fuel combustion system comprises boiler main body. the biomass storage bin, a biomass pyrolysis furnace, a gas-solid separator, main burner, burner and semi-coke. combustion gas burner, boiler noumenon comprises hearth, main burner, burner and semi-coke. combustion gas burner are set on main body of boiler, the main the main burn burner, combustion gas burner.. the burn, the semi-coke burner upstream of the combustion zone again, biomass entrance and exit biomass pyrolysis furnace of the biomass storage bin connected with the pyrolysis product pyrolysis product entrance and exit gas solid separator of biomass pyrolysis furnace is connected with the gas outlet of gas-solid separator and combustion gas burner.., semi coke exit of gas-solid separator and semi-coke burner.. The utility model can avoid a biomass and coal powder directly mixed, increase utilization rate of biomass can at the same time.
NOVELTY - Soil activator comprises lignosulfonate and at least one microorganism.    USE - The soil activator is useful for: stimulating the growth of a plant or crop by strengthening the structure and developing the root system and shoot of the plant or crop root system and increasing the chlorophyll content of the plant, where the plant or crop is for arugula, lettuce, radish, spinach, carrots, broccoli, cabbage, cauliflower, cucumbers, onion, garlic, tomatoes, fruit trees, strawberries, maize, wheat, cereal, sorgho, canola, tea, potatoes, potting soil, soya, turf or ornamental plants; and stimulating the growth of a tree, where the tree is a bamboo tree or a redbud tree (all claimed). The ability of soil activator (comprised of 83% ammonium lignosulfonate, and 10% microorganism comprising Bacillus subtilis, Bacillus licheniformis, or Pseudomonas putida) to stimulate plant growth was tested in carrots field by measuring biomass production. The results showed that the soil activator exhibited 14.68 plus minus 1.27 kg vegetable harvested/plot as compare to control of 8.98 plus minus 0.47 kg vegetable harvested/plot.    ADVANTAGE - The soil activator: produces natural enzymes when applied to soil, which increases nutrients bioavailability in the soil generating a surplus of available micronutrients that the roots take in; nourishes the plant while boosting the roots strength and absorption; and helps plants to develop stronger, bigger, denser, and healthier root systems for better overall growth and stronger plants that are more resistant to unfavorable environmental conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a soil activator comprising a lignosulfonate, nitrogen, phosphorus, soluble potash, Bacillus subtilis, Bacillus amyloliquefaciens, and Pseudomonas monteilii.
NOVELTY - Substance comprises either: effective microorganisms, water and at least one disinfectant and/or odor-neutralizing chemical; or effective microorganisms, water and at least one disinfectant and/or odor-neutralizing chemical first substance, and water glass, preferably sodium water glass as second substance.    USE - The substance is useful for processing sewage sludge (claimed).    ADVANTAGE - The substance improves utilization of sewage sludge as fertilizer.
NOVELTY - This new utility model claims of one of biomass pyrolysis gasification combustion section conversion biological coal/steam cogeneration device, comprises fluidization bed pyrolysis gasification furnace, low heat value fuel gas combustion chamber, one level separating device, second level cyclone separator, air pre-heater, a steam generating device and smoke treatment device equal device. This new utility model by using and generating pyrolysis of biomass raw material in fluidization bed pyrolysis gasification furnace, gasification reaction product material coal and high temperature low heat value biomass fuel gas, using two level separating device realize biological coal and gas is separated, to obtain high quality biological coal, generation of the high temperature steam can use for outside supply steam, can effective reduce production cost, increase production benefit.
NOVELTY - Nutrient salts derived from urine are recovered from used absorbent article by immersing used absorbent article in calcium-compound-containing aqueous solution, inactivating super-absorbent polymer, separating liquid containing calcium compound and nutrient-salt-containing constituent material of absorbent article from solid, and collecting nutrient salts.    USE - Recovery of nutrient salts derived from urine from used absorbent article containing urine for recycle of used paper diaper.    ADVANTAGE - Wastewater treatment burden can be decreased, and process cost reduction and environmental load reduction are attained.
NOVELTY - Manufacture of highly-purified hydrogen involves supplying hydrogen-containing-gas containing impurity gas into container filled with hydrogen-storage material obtained by carrying out mechanical milling of a mixture with catalyst chosen from metal hydride, niobium pentoxide, vanadium pentoxide and titanium oxide, discharging impurity gas from sealed container, and discharging hydrogen occluded by heating the hydrogen storage material in sealed container.    USE - Manufacture of highly-purified hydrogen used as fuel in petroleum refinery, semiconductor industry and chemical industry.    ADVANTAGE - The method efficiently and economically provides highly-purified hydrogen with purity of more than 99% and yield of 90% or more. The whole quantity of impurity gas is discharged by a simple method without discharging the hydrogen occluded into hydrogen-storage material by using vacuum state directly. Since cooling of hydrogen-storage material is not necessary, the hydrogen-storage portion is enlarged.
NOVELTY - The utility model claims a new a hydrogen preparing device, comprising electrolytic groove, electrolytic groove through pipeline and a hydrogen cooling device and cooling device connected with oxygen, hydrogen cooling device via a hydrogen pipeline connected with separator, hydrogen separator by pipeline and washer connected with hydrogen, hydrogen scrubber through pipeline and dewatering tank connected with, dehydrating tank via a hydrogen pipeline connected with press, press by hydrogen and molecule sieve connected with pipeline, molecule sieve by pipeline and hydrogen storage tank connected with, wherein, the hydrogen storage tank comprises a tank body, a tank body upper part provided with a valve, a tank body is jacketed structure, a tank body and a valve to contact, provided with a tank body equipped with medium import and medium outlet, a tank body fixed with a device. The utility model structure is simple, a suitable operation, hydrogen purity.... hydrogen efficiency is high, the storage effect is good, the simplified of industrial process and industrial cost.
NOVELTY - The utility model claims a new kind in hydrogen system, especially relates to a kind of a water electrolytic a pure hydrogen system. The utility model comprises a electrolytic groove, liquid hydrogen separator, hydrogen cooling device and hydrogen storage tank, electrolytic groove separately connected and pure water device, alkaline liquor device, a liquid separator and hydrogen separator liquid, pure water device and a replacement machine connected, pure water device top provided with a gas outlet, a liquid separator and collector connected oxygen, hydrogen liquid separator and washer, hydrogen cooling device, 3A molecule sieve purifier, 4A molecule sieve and a hydrogen storage tank connected in turn, bottom of hydrogen separator liquid and electrolytic groove connection, hydrogen cooling device on the pipeline between a 3A molecule sieve purifier equipped with silk screen catcher, a bottom hydrogen liquid separator and silk screen catcher connected, scrubber and lotion collector connected. This new utility model structure is simple, operation is convenient, in a hydrogen of high purity, with high economic benefit.
NOVELTY - The utility model claims a electrolytic water hydrogen oxygen manufacture equipment technology area, specifically claims a kind of.... hydrogen electrolytic device, comprising electrolytic groove, electrolytic groove connected with a hydrogen separator, a separator, hydrogen separator connected with purifier, electrolytic groove connected with pure water tank, a pure water tank set with air inlet and air outlet, a hydrogen separator by hydrogen pipeline orderly connected with the hydrogen pipeline between cooling device with a steam-water separator, a pure water box and air outlet connect hydrogen separator and cooling device, a separator by oxygen pipeline connected with purifier, comprising purifier in turn connected with a remove absorbing agent tank, cooling device, a steam-water separator and molecule sieve adsorption tank, the device can by electrolytic, separating, purifying prepared high pure oxygen and normal hydrogen, can directly use for industrial application, simplify a industrial process and industrial cost.
NOVELTY - This new utility model relates to a novel electrolytic water of hydrogen preparing device, comprising electrolytic groove, electrolytic groove through pipeline and a hydrogen cooling device and cooling device connected with oxygen, hydrogen cooling device via a hydrogen pipeline connected with separator, hydrogen separator by pipeline and washer connected with hydrogen, hydrogen scrubber through pipeline and dewatering tank connected with, dehydrating tank via a hydrogen pipeline connected with press, press by hydrogen and molecule sieve connected with pipeline, molecule sieve by pipeline and a drying device, drying device through pipeline and hydrogen storage tank connected with the electrolytic groove through a pipeline and remove salt water tank and alkaline liquor tank connected with. Hydrogen storage tank comprises a tank body, a tank body upper part provided with a valve, a tank body is jacketed structure, to a control valve contact, provided with a tank body equipped with medium import and medium outlet, a tank body fixed with a device. The utility model structure is simple, a suitable operation, hydrogen purity.... hydrogen efficiency is high, the storage effect is good, the simplified of industrial process and industrial cost.
NOVELTY - The utility model claims a electrolytic water hydrogen oxygen manufacture equipment technology area, specifically claims a kind of electrolytic water... common device hydrogen, comprising electrolytic groove, electrolytic groove connected with a hydrogen separator, a separator, hydrogen separator connected with purifier, electrolytic groove connected with pure water tank, a pure water tank set with air inlet and air outlet, a separator by a pipeline orderly connected with the oxygen pipeline between oxygen with cooling device and steam-water separator, a pure water box and air outlet connect a separator and cooling device, hydrogen separator through pipeline connected with hydrogen purifier, comprising purifier in turn is connected with a glue absorbing tank, deoxidant adsorption tank, cooling device, a steam-water separator and molecule sieve adsorption tank, the device can by electrolytic, separating, purifying prepared high pure hydrogen and normal oxygen, can directly use for industrial application, simplify a industrial process and industrial cost.
NOVELTY - A recombinant methanotrophic bacterium being capable of producing lactic acid from organic waste or biogas or methane and comprising a heterologous nucleic acid or gene which encodes for lactate dehydrogenase (Ldh) enzyme, is new.    USE - The recombinant methanotrophic bacterium is used for producing lactic acid from organic waste or biogas or methane. The lactic acid produced is L-lactic acid or D-lactic acid. The bacterium is chosen from 50 e.g. Methylococcus capsulatus, Methylobacterium extorquens, M.organophilum, M.mesophilicum, M.dichloromethanicum, Methylocella silvestris, Methylosinus trichosporium, Methylobacillus flagellatus KT, M.populi, and M.chloromethanicum, preferably M.capsulatus (Bath) strain (all claimed).    ADVANTAGE - The bacterium enables to produce lactic acid from methane or biogas or organic waste at at least 5 fold higher than that by wild-type strain under similar conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process for producing lactic acid from organic waste using the bacterium; and    (2) process for producing lactic acid from a carbon source using the bacterium.
NOVELTY - Method for upgrading biooil or biooil fraction, involves providing biooil or biooil fraction, providing hydrogen (H2), and reacting the biooil or biooil fraction and hydrogen in the presence of a catalyst at less than 150 degrees C under pressure of less than 100 bar (absolute) to produce a hydrogenated liquid oil at carbon yield of over 75%.    USE - The method is useful for upgrading biooil or biooil fraction (claimed).    ADVANTAGE - The method stabilizes biooil or biooil fraction at low temperature and low pressure.    DETAILED DESCRIPTION - Method for upgrading biooil or biooil fraction, involves (a) providing biooil or biooil fraction, providing hydrogen (H2), and reacting the biooil or biooil fraction and hydrogen in the presence of a catalyst at less than 150 degrees C under pressure of less than 100 bar (absolute) to produce a hydrogenated liquid oil at carbon yield of over 75%, (b) providing biooil or biooil fraction, providing oxygen reducing reaction conditions, and reacting the biooil or biooil fraction under oxygen reducing reaction conditions at low temperature and/or low pressure to produce an upgraded biooil product comprising fewer carbonyl groups than the biooil or biooil fraction, or (c) providing biooil or biooil fraction, providing solution comprising one or more fermentation organisms and sugar source, combining the solution and the biooil or biooil fraction to obtain fermentation mixture, and incubating the fermentation mixture at 15-30 degrees C for 16-72 hours to produce upgraded biooil fermentation product comprising fewer carbonyl groups than the biooil.
NOVELTY - A biomass mash is prepared by subjecting biomass containing less than or equal to 10% lignin and/or neutral detergent fiber (NDF) of less than or equal to 65% with respect to dry matter content to 1st pH adjusting step using a base to achieve a pH of greater than or equal to 7.5 at 1-40 degrees C for 5 minutes, followed by 2nd pH adjusting step using an acid to obtain biomass mash with pH of 1-6.5.    USE - Preparation of biomass mash for production of feed, bio-fuel, and other industrial products (all claimed).    ADVANTAGE - The biomass mash has reduced viscosity. The combination of pH adjusting steps provides a biomass having no microbial activity, which improves stability when stored under anaerobic conditions and the window in time to sustain a high quality feed stock under aerobic conditions. Storage losses are reduced due to improved anaerobic stability and feeding losses due to aerobic stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) biomass mash;    (2) use of liquid fraction in the production of feed, biofuel, and other industrial products; and    (3) use of non-liquid fraction in the production of feed.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of scenarios of an on-farm produced biomass mash and subsequent steps of further use.
NOVELTY - A solid oxide cell (100) consists of a cathode (110) for decomposing water and producing hydrogen gas, an anode (120) facing the cathode for discharging oxygen gas, and an electrolyte (130) provided between the anode and the cathode. The cathode contains alkaline earth metal-transition metal-containing complex oxide (a) (I).    USE - Solid oxide cell is used for producing hydrogen and oxygen.    ADVANTAGE - The solid oxide cell has excellent thermal-chemical stability, and enables efficient production of hydrogen and oxygen, by economical process.    DETAILED DESCRIPTION - A solid oxide cell consists of a cathode for decomposing water and producing hydrogen gas, an anode facing the cathode for discharging oxygen gas, and an electrolyte provided between the anode and the cathode. The cathode contains alkaline earth metal-transition metal-containing complex oxide (a) of formula: RET2O5+d (I), where R is rare-earth metal or lanthanide, E is alkaline earth metal, T is transition metal, and d is 1 or less.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of solid oxide cell.    Solid oxide cell (100)    Cathode (110)    Anode (120)    Electrolyte (130)    External power supply (140)
NOVELTY - Production of biomethane involves providing methanogens to biogas, performing methanation process, carrying out partial purification of biogas, producing partially-purified biogas, introducing the resultant biogas into at least two adsorption vessels, performing adsorption process using adsorbent, separating methane and carbon dioxide in the partially-purified biogas through adsorption-separation membrane and obtaining at least one gaseous methane-rich retentate (biomethane) which can be used as a substitute for natural gas and carbon dioxide-rich permeate gas.    USE - Production of biomethane (claimed).    ADVANTAGE - The method enables efficient and safe production of biomethane.    DETAILED DESCRIPTION - Production of biogas involves providing methanogens to biogas, performing methanation process, carrying out partial purification of biogas by adsorptive removal of hydrogen sulfide and volatile organic compound, producing partially-purified biogas, introducing the resultant biogas into at least two adsorption vessels connected in series, performing adsorption process using adsorbent, separating methane and carbon dioxide in the partially-purified biogas through adsorption-separation membrane and obtaining at least one gaseous methane-rich retentate (biomethane) which can be used as a substitute for natural gas and carbon dioxide-rich permeate gas containing less than 7% methane. All or portion of carbon dioxide-rich permeate gas is used as an inert gas and for inerting digesters during loading/unloading of inputs. An INDEPENDENT CLAIM is included for plant for production of biomethane.
NOVELTY - A halogen compound (II) is reacted with nitrile compound (I) and sulfur at 70 degrees C or more in presence of an ether compound (IV) to obtain isothiazole compound (III).    USE - Production of isothiazole compound e.g. 3,4-dichloro-5-cyano isothiazole used as intermediate in production of pharmaceuticals, agrochemicals, functional dye and electronic material.    ADVANTAGE - The method efficiently provides isothiazole compound without using N,N-dimethylformamide, chlorine, transition metal catalyst and toxic chemicals, and by discharging reduced amount of waste material.    DETAILED DESCRIPTION - A halogen compound of formula (II) is reacted with nitrile compound of formula (I) and sulfur at 70 degrees C or more in presence of an ether compound of formula (IV) to obtain isothiazole compound of formula (III).    R1,R2=alkyl or cycloalkyl;    R=cyano, carboxy or alkoxycarbonyl;and    X=fluoro, chloro, bromo, or iodo.
NOVELTY - A dispersed white ink comprises titanium dioxide comprising particles contained in thermoplastic polymer resin matrix. The particles have maximum interparticle distance of 1 mu m or less and exhibits statistical variance of 0.02 or less.    USE - Dispersed white ink is used for digital printing.    ADVANTAGE - The dispersed white ink is manufactured by economical method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture (400) of dispersed white ink, which involves integrating (405) components for the white ink, reducing (410) particle size and dispersing particles in ink carrier fluid to form semi-solid mixture, and grinding (415) the semi-solid mixture to form the dispersed white ink.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of manufacture of dispersed white ink.    Manufacture process (400)    Integration process (405)    Reduction process (410)    Grinding process (415)
NOVELTY - Preparing anagliptin (I) or its salt comprises: (a) treating 2-methyl-1,2-propane diamine (II), with 2-methylpyrazolo(1,5-a) pyrimidine-6-carboxylic acid (III) and N,N'-carbonyldiimidazole in presence of suitable organic solvent to obtain N-(2-amino-2-methylpropyl)2-methylpyrazolo (1,5-a) pyrimidine-6-carboxamide (IV); (b) condensing (IV) with 1-(2-chloroacetyl)-2S-pynolidine carbonitrile (V) in presence of base and a catalyst in solvent; and (c) isolating anagliptin or its salts from the reaction mixture.    USE - The process is useful for preparing (I) or its salt which is used for treating diabetes. No biological data given.    ADVANTAGE - The process: is economically viable and industrial eco-friendly; and involves simple steps.    DETAILED DESCRIPTION - Preparing anagliptin of formula (I) or its salt comprises: (a) treating 2-methyl-1,2-propane diamine of formula (II), with 2-methylpyrazolo(1,5-a) pyrimidine-6-carboxylic acid of formula (III) and N,N'-carbonyldiimidazole in presence of suitable organic solvent to obtain N-(2-amino-2-methylpropyl)2-methylpyrazolo (1,5-a) pyrimidine-6-carboxamide of formula (IV); (b) condensing (IV) with 1-(2-chloroacetyl)-2S-pynolidine carbonitrile of formula (V) in presence of base and a catalyst in solvent; and (c) isolating anagliptin or its salts from the reaction mixture. An INDEPENDENT CLAIM is also included for a purification process, where the HPLC purity of Anagliptin is 99.5% or more when measured by HPLC is obtained, the process comprising treating Anagliptin with isopropyl acetate.
NOVELTY - Heated titanium oxide is made to contact a silica- containing plant material, to recover silica.    USE - Recovery of silica. Uses include but are not limited to electrodes of lithium-ion battery, eye shadow, cream, milky lotion, polishing component of toothpaste, desiccant, deodorizer, additive for beer, refined sake and soy sauce, raw material of optical fiber, agricultural fertilizer, humidity control agent, polishing agent, heat-resistant instrument, lab ware, enamel, pozzolanic cement, ceramic, liquid-chromatography carrier, electric light bulb, cathode ray tube display and newspaper printing ink, mineral water, health food, and bone porosity prevention therapeutic composition.    ADVANTAGE - The method enables recovery of soluble silica of high purity and high recovery efficiency, at low temperature process of 500 degrees C and low pressure, with suppressed environmental pollution by preventing usage of strong acid.
NOVELTY - Fuel composition comprises a mixture of alkanes comprising pentadecane, hexadecane, and heptadecane. Heptadecane and pentadecane are predominant in the mixture. Portion of the carbon used as raw material of the alkanes in the mixture is inorganic carbon. The fuel composition has a higher ( delta )p than a comparable fuel composition made from fixed atmospheric carbon or plant-derived biomass.    USE - The fuel composition is useful for recombinant biosynthesis of N-alkanes; and for modifying photoautotrophic organisms as hosts, such that the organisms efficiently convert carbon dioxide and light into N-alkanes.    ADVANTAGE - The fuels comply with ASTM standards, for instance, standard specifications for diesel fuel oils D 975-09b, and Jet A, Jet A-1 and Jet B as specified in ASTM Specification D. 1655-68. In addition to some environmental advantages of the fuel composition such as carbon dioxide (CO2) conversion and renewable source, other advantages of the fuel compositions include low sulfur content, low emissions, being free or substantially free of alcohol and having high cetane number.
NOVELTY - Method for producing docosahexaenoic acid (DHA), involves culturing one or more stocks of Aurantiochytrium having genetic identity from at least 92% with respect to a 1210 base pair sequence (SEQ ID NO: 1) fully defined in the specification, in heterotrophic conditions, in chemically definite culture medium having less than 3.5 g/l, preferably less than 1 g/l, more preferably less than 10 mg/l ions of sodium and less than 1 g/l, preferably less than 500 mg/l, more preferably 200 mg/l chloride ions.    USE - The method is useful for producing DHA which is used as product, or ingredient in agroalimentary product or aquiculture (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) use of all or portion of biomass and/or coproduced material obtained from the above-mentioned method as product, or ingredient in agroalimentary product or aquiculture;    (2) culture medium; and    (3) use of the culture medium for preparing culture of protists for production of lipids and pigments.
NOVELTY - Complex microbial agent comprises Bacillus subtilis, Lactobacillus plantarum and Angel yeast. The Bacillus subtilis has preservation number CCTCC M2010260; and the Lactobacillus plantarum has preservation number CCTCC M2010150.    USE - The complex microbial agent is useful for fermenting chicken manure (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing fermented chicken manure, comprising (i) mixing chicken manure and straw powder, adding cornmeal, microbial agents, and deodorants, and controlling moisture to 35-70%; (ii) stirring, stacking to width of 1.5-2 m and height of 0.8-1.5 m, drilling the top of the compost pile for ventilation, then covering the compost pile with rectangular plastic sheet, and fermenting; (iii) turning the compost pile every 1-2 hours, fermenting for 2-4 weeks, and turning once a week to ensure aerobic fermentation; and (iv) heating the compost pile to 55-70 degrees C, so as to Escherichia coli and parasite eggs, when the compost becomes loose and dry, and covered with white mycelium, adding koji flavor, and naturally cooling.
NOVELTY - The horizontal furnace includes an inlet funnel (1) connected to a transport pipe (2) and roller material forwarded by auger (3). The inlet tube (4) access carbonization and evaporation of liquid in carbonization or evaporation oil chamber. The inlet tube is connected internally with carbonizing chamber. A combustion chamber is designed with chimney and filter.    USE - Horizontal furnace for carbonizing biomass for generating coal as fuel for thermal feedback in furnace.    ADVANTAGE - The horizontal furnace reduces volume of biomass fuel and generates a carbon-based material, enables precise control of driving and heating biomass during whole transformation process on carbon, and thus obtains better yield of carbonization without any combustion during carbonization process, and coal with very high thermal efficiency and greater power capacity in burning.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic front general view of the carbonization furnace.    Inlet funnel (1)    Transport pipe (2)    Auger (3)    Inlet tube (4)    Structure (A)
NOVELTY - Preparing residual fuel oil by animal and plant oil acid, comprises (i) carrying out amination reaction of animal and plant oil to obtain a reaction product, (ii) carrying out hydrogenation reaction of the reaction product to obtain layered mixed liquid, (iii) oil separating the layered mixed liquid and taking lower layer heavy oil, (iv) adding a cracking catalyst into the heavy oil and carrying out liquid phase catalytic cracking reaction to obtain mixed fuel oil, and (v) fractionating the mixed fuel oil.    USE - The method is useful for preparing residual fuel oil by animal and plant oil acid (claimed).    ADVANTAGE - The method is simple and suitable for large scale production.
NOVELTY - Tomato fertilizer comprises 100-120 pts. wt. pig manure, 40-50 pts. wt. bagasse, 30-40 pts. wt. wheat bran, 20-30 pts. wt. eggshell, 35-45 pts. wt. weathered coal, 30-50 pts. wt. urea, 50-60 pts. wt. diammonium phosphate, 40-60 pts. wt. potassium chloride, 3-5 pts. wt. trace elements, 4-6 pts. wt. effective microorganism agent, and 10-15 pts. wt. soil conditioner.    USE - Fertilizer is useful for promoting growth of tomato.    ADVANTAGE - The tomato fertilizer has rich in nutrients, can be prepared with high efficiency, and reduces soil heavy metals and toxic substances.
NOVELTY - Preparation of crystalline form propacetamol A hydrochloride involves adding crude propacetamol hydrochloride to a solvent, heating to 55-95 degrees C, dissolving by stirring, filtering, cooling the filtrate at rate of 1-7 degrees C/hour to 12-20 degrees C, crystallizing for 4 hours, filtering, washing the filter cake and drying under vacuum at 50-55 degrees C.    USE - Preparation of crystalline form propacetamol A hydrochloride (claimed).    ADVANTAGE - The method enables simple, safe, economical and environmentally-friendly preparation of crystalline form propacetamol A hydrochloride having high quality and excellent stability and storage stability. The crystalline form propacetamol A hydrochloride does not absorb water.
NOVELTY - Substituted 4-iodo-5-phenyl-3H-furan-2-one compounds (Q) are new.    USE - The new compounds (Q) are useful for preparation of antibacterial, sterilization, antiinflammatory and anti-cancer drugs (claimed).    ADVANTAGE - The compounds (Q) can be easily prepared with high yield of 52-67% in an environmentally-friendly manner.    DETAILED DESCRIPTION - Substituted 4-iodo-5-phenyl-3H-furan-2-one compounds of formula (Q) are new.    R1= aryl or alkyl;and    R2= electron withdrawing group comprising halo or electron donating group comprising alkyl or alkoxy.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of compounds (Q); and    (2) use of compounds (Q) for preparation of antibacterial, sterilization, antiinflammatory, and anticancer drugs.
NOVELTY - Preparation of sofosbuvir polymorphic form 6 involves dissolving sofosbuvir in solvent chosen from cyclopentyl methyl ether, and mixture of cyclopentyl methyl ether and ether, crystallizing, filtering, washing and drying.    USE - Preparation of sofosbuvir polymorphic form 6 (claimed).    ADVANTAGE - The method enables preparation of sofosbuvir polymorphic form 6 having high purity, by simple and environmentally-friendly process.
NOVELTY - This new utility model claims biogas recovery area, especially relates to a kind of one biogas slurry relux ammonia nitrogen stripping recovery device, comprising: remove tank main body, wherein the lower part is set with biogas slurry with container, the container side wall lower part connected with one multi-air inlet pipe, each air inlet pipe are extending blowing remove tank main body and air pump connected, container is set with one upper cover of cover body is opened with two multi-hole, each hole position are installed with one gas spur track, remove tank main body side wall is mounted with one alkali liquid drip tank, acid absorb tank, it is set with biogas slurry container at the upper part, absorb acid tank and side wall of part with is set with main gas path, a gas one end main path and each gas spur track is connected, blowing top part and remove tank main body is provided with an exhaust port, an exhaust port through the air inlet pipeline and air pump connected, a gas main path the other end extending downward to the bottom absorb acid tank. This utility model new supply of one of structure is simple, the operation cost low, can at the same time active relux biogas slurry recycling ammonia nitrogen and ammonia nitrogen stripping recovery device.
NOVELTY - This new utility model claims of one of desulfurized waste water and remove mercury and system, including, impurity removing system, concentration device, electrolytic device and alkaline liquor storage device, waste water via SO42-removing, magnesium ion and removing calcium ion removing equal impurity ion and removing process, the desulfurized waste water after iron removing impurity through depth purification after concentration, concentration via the waste electrolytic water, electrolytic production of chlorine desulfurizing tower and oxidation of mercury, so as to make the mercury removing of smoke. This new utility model not only solves of the desulphurization waste water treatment process water containing salt water quality weight more and issue, then can implement high efficient and demercuration, also at the same time may get applied widely is Cl2, NaOH solution and clean energy H2.
NOVELTY - Microorganism organic fertilizer comprises chicken manure, straw, oil cake, humic acid, vinasse, rice husk, compost bacteria and trace elements. The preparation of microorganism organic fertilizer comprises mixing chicken manure, straw, oil cake, humic acid, vinasse, rice husk and compost bacteria, fermenting and drying, then mixing with the trace elements in a ratio of 1:1 and granulating.    USE - Used as microorganism organic fertilizer.    ADVANTAGE - The organic fertilizer: mainly comprises organic nutrients and adopts inorganic fertilizers, so that the fertilizer can provide crops with comprehensive and reasonable nutrients, improve soil quality comprehensively, and boost soil fertility; can improve soil with lowered quality, e.g. salinized and alkalized soil or acidized and alkalized soil, upon long-term use; is rapid and durable in fertility and free of fertilizer damage; is capable of providing comprehensive and balance nutrients, largely improving crop disease resistance and reducing the production cost, and free of environment pollution in production and using processes; has obvious yield-increasing investment-saving effects and increases economic and social benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the microorganism organic fertilizer, comprising (i) mixing chicken manure, straw, oil cake, humic acid, vinasse, rice husk and compost bacteria in a mixing tank for 1-2 hours; (ii) fermenting the mixed mixture for three days; (iii) mixing the obtained mixture and trace elements in the ratio of 1:1, and transporting into extrusion granulation equipment; (iv) sieving with 2-4 mm powder sieve, and filtering powdery substance; (v) screening particles larger than 4 mm, filtering, crushing, granulating and recycling; (vi) packaging, weighing, and inspecting.
NOVELTY - This utility model claims one new heating at the best position of the methane tank, comprising methane tank main body, said methane tank main body side wall equipped with stir liquid, stirring the liquid through pipe connected with pipe pump, the pipe pump end under methane tank main body and the discharge port pipe connected with, the discharge port pipe one end the bottom center of marsh gas tank, a discharge port pipe the other end connecting with valve, the tank main body to the inner layer along inner wall set with tank pipe, the coil pipe and the water inlet and water outlet of the marsh gas tank main body by thread connection, wherein the coil in the tank body inner layer and the middle part. The beneficial effect: and the existing marsh gas ferment device, average production rate of the fermentation device is higher than the gas speed under 50 temperature, as the temperature of fermentation tank gas speed is 1-2 time, even 2 also more time. In our country in northern cold area and large farm, with wide application prospect.
NOVELTY - A functional between a coal combustion flue gas for preparing methane and device, a coal combustion device (1) and producing methane (2), wherein, the coal device (1) is a discharge port through pipeline and producing methane container (2) bottom is connected, a coal combustion device (1) and producing methane container (2) is set with fan I (3), a dust removing device (4) and valve III (8), a pipe and a methane producing container is set with front end with deflation valve (7), the methane container (2) top part through the pipeline and combustion chamber of combustion coal device (1) connected and set with valve I on a pipeline (18), a fan (5), a gas cabinet I (6) and valve II (19). And the existing technology, this utility new type save of carbon dioxide and methane producing strain and producing hydrogen organic matter fermentation fungus producing the carbon dioxide one link, for power plant discharge the direct contact, generating methane. Not only reducing of carbon dioxide discharge, but also change waste as treasure.
NOVELTY - A kitchen garbage treatment is used for marsh gas system, a kitchen garbage powder crush machine, tank ferment pool, an air storage tank, a fuel gas filter, a marsh gas generation converter, kitchen garbage powder crush machine via liquid pipe and a tank fermentation pool connected, tank ferment. Internal end of a gas pipe and a gas storage tank connected, a part of gas storage tank through gas combustible gas filter filtering supply fuel gas stove using, enter into marsh gas generation converter for power generation and supply domestic electric appliance use. The utility model is a new supply of marsh gas system for a kitchen waste processing structure is simple, can make in a kitchen of a food waste conversion for marsh gas, and is suitable for common family city, with saving energy, clean environment, reducing insect pests disturber equal.
NOVELTY - The utility model claims a straw hydrolysis acidification processing device, which is suitable for producing the straw hydrolysis acidification treatment area before methane gas. The device comprises straw hydrolysis acidification groove internal of the straw hydrolysis acidification treatment chamber, a water collecting slot is located outside of and is set with a solar heating device and a top part, is set with heating element with a straw hydrolysis acidification groove bottom, side part is set with with ultrasonic wave generating device, with inlet at one side is set with groove and straw hydrolysis acidification, with a water-collecting groove is set with mutually connected drainage hole bottom on the straw hydrolysis acidification groove, and bottom of groove and straw hydrolysis acidification tank to inclined side..., set up with a top part and a straw hydrolysis acidification groove, spray head through pipeline, water circulation pump and water collecting groove mutually connected, heating component by a water circulation pump and corresponding pipeline and solar energy heating device connected with each. The utility model can increase a yield of straw Anaerobic fermentation solves the material in Anaerobic fermentation tank in the upper floating phenomenon.
NOVELTY - Use of solid acid catalyst for synthesizing isobornyl acrylate, is calimed. The synthesis of isobornyl acrylate comprises taking acrylic acid and camphene and reacting in presence of the solid acid catalyst to obtain isobornyl acrylate. The preparation of the solid acid catalyst comprises mixing and dissolving metal halide and water, adjusting metal halide solution pH to 8-10 using 5-20% concentration alkaline solution, allowing to stand, aging, washing using deionized water, drying solid in oven, taking ammonium salt and dried solid powder, mixing, placing in muffle furnace and baking.    USE - The solid acid catalyst is useful for synthesizing isobornyl acrylate (claimed).    ADVANTAGE - The method is simple, utilizes raw materials which are readily available and economical. The catalyst has strong acidity, good recycling property and high selectivity for isobornylacrylate.    DETAILED DESCRIPTION - Use of solid acid catalyst for synthesizing isobornyl acrylate, is calimed. The synthesis of isobornyl acrylate comprises taking acrylic acid and camphene of molar ratio 1.2:1-3:1 and reacting in presence of the solid acid catalyst at 30-90 degrees C for 2-10 hours to obtain isobornyl acrylate, where the mass of solid acid catalyst is 1-25% mass of camphene. The preparation of the solid acid catalyst comprises mixing and dissolving metal halide and water in mass ratio of 1:5-1:100, adjusting metal halide solution pH to 8-10 using 5-20% concentration alkaline solution, allowing to stand, aging for 10-30 hours, washing 3-10 times using deionized water, drying solid in oven at 80-120 degrees C for 10-30 hours, taking ammonium salt and dried solid powder in mass ratio of 1:20-1:2, mixing, placing in muffle furnace at 300-600 degrees C and baking for 3-15 hours.
NOVELTY - The synthesis method of borneol involves performing microwave esterification reaction of alpha -pinene and anhydrous oxalic acid in microwave reactor, adding catalyst including 4A-type molecular sieve and aluminum sulfate hexadecahydrate, filtering, washing with hot water to obtain esterified fluid, distilling esterified fluid using naphtha in presence of steam, adding sodium hydroxide solution and then performing saponification reaction, and distilling.    USE - Synthesis of borneol (claimed).    ADVANTAGE - The method enables simple, economical and rapid synthesis of borneol with improved yield using simple raw materials, under mild reaction conditions.    DETAILED DESCRIPTION - The synthesis method of borneol involves performing microwave esterification reaction of alpha -pinene and anhydrous oxalic acid at microwave power of 50-110 Watts for 0.5-3 hours in a microwave reactor, adding 0.01-0.05 times the mass of catalyst including 4A-type molecular sieve and aluminum sulfate hexadecahydrate in a mass ratio of 1:10-15, filtering esterified product, washing with hot water at 70-90 degrees C for 30-60 minutes to obtain an esterified fluid, distilling esterified fluid using naphtha in the presence of steam, adding 30-35% sodium hydroxide solution and then performing saponification reaction, and distilling.
NOVELTY - The method of separating and purifying physcion and emodin from Polygonum cuspidatum involves crushing Polygonum cuspidatum herb, soaking in ethanol and then extracting, filtering and then concentrating, adding mixed solution of methanol, water, ethyl acetate and petroleum ether, distilling, dissolving extract in methanol, filtering, performing supercritical fluid chromatography using supercritical fluid and modifier including methanol in liquid chromatography column, detecting organic volatile substances using UV detector, and collecting fractions.    USE - The method is useful for separating and purifying physcion and emodin from Polygonum cuspidatum (claimed).    ADVANTAGE - The method enables environmentally-friendly separation and purification of physcion and emodin from Polygonum cuspidatum without using harmful organic solvents and producing harmful residues.    DETAILED DESCRIPTION - The method of separating and purifying physcion and emodin from Polygonum cuspidatum involves crushing Polygonum cuspidatum herb, soaking powder in ethanol and then extracting, filtering and then concentrating under reduced pressure, adding mixed solution of methanol, water, ethyl acetate and petroleum ether to extract, distilling under vacuum to obtain Polygonum cuspidatum extract, dissolving Polygonum cuspidatum extract in methanol, filtering, performing supercritical fluid chromatography using supercritical fluid as mobile phase and methanol as modifier, detecting organic volatile substances in the extract using UV detector, and collecting fractions. The mass ratio of methanol, water, ethyl acetate and petroleum ether is 6:10:5:2.
NOVELTY - Rhizosphere growth-promoting bacterium i.e. Enterobacter cancerogenus N10 strain with the preservation number CGMCC No. 1.14969, is new.    USE - The strain is useful as inoculant (growth-promoting agent) or microbial fertilizer for promoting plant growth, preferably wheat (all claimed).    ADVANTAGE - The strain has nitrogen fixation and phosphate-solubilizing property, promotes production of indole acetic acid, increases soil nutrients and promotes plant to absorb soil nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also claimed for use method of the stain as inoculant or microbial fertilizer for promoting wheat growth, comprising culturing Enterobacter cancerogenus, spraying 1 ml solution of (optical density at 600 is 0.8) in lysogeny broth medium as an inoculant or microbial fertilizer on the surface of sprouted wheat seed and cultivating under green house, where the wheat seeds are planted in sterile broth mixed with low nitrogen and calcium phosphate, after soaking and incubation for germination.
NOVELTY - Preparation of enzalutamide, involves adding 4-(3-(4-cyano-3-(trifluoromethyl)phenyl)-5,5-dimethyl-4-oxo-2-thioxoimidazolidin-1-yl)-2-fluorobenzoic acid derivative (I) to a solvent, reacting with methylamine, and collecting enzalutamide (II).    USE - Preparation of enzalutamide (claimed).    ADVANTAGE - The method enables simple and convenient post-treatment, reduces reaction time, is economical and suitable for industrial scale, and is carried out under mild conditions without using time-consuming column chromatography operations and highly toxic methyl iodide reagents.    DETAILED DESCRIPTION - Preparation of enzalutamide, involves adding 4-(3-(4-cyano-3-(trifluoromethyl)phenyl)-5,5-dimethyl-4-oxo-2-thioxoimidazolidin-1-yl)-2-fluorobenzoic acid derivative of formula (I) to a solvent, reacting with methylamine, and collecting enzalutamide of formula (II).    R1=methyl, ethyl or isopropyl.
NOVELTY - Synthesis of high-purity quinocetone involves adding petroleum ether, maquindox, pyridine and benzaldehyde to reactor, stirring, heating to 60-90 degrees C, refluxing for 6-8 hours, cooling, suction-filtering, and drying. The reactor has water distributor, water knockout vessel and condensation pipe.    USE - Synthesis of high-purity quinocetone used for veterinary drug.    ADVANTAGE - The method enables economical, simple and quick synthesis of high-purity quinocetone with high yield, and reduced waste contamination.
NOVELTY - An preparation of alogliptin benzoate drug substance involves adding mixed solvent and crude alogliptin benzoate to a reactor, heating to reflux until the solution is clear, cooling, adding seed crystals, cooling-crystallizing, centrifuging and drying.    USE - Preparation of alogliptin benzoate drug substance (claimed).    ADVANTAGE - The method enables simple, economical and environmentally-friendly preparation of alogliptin benzoate drug substance having purity of 99.8%, single impurity content of 0.05% or less, and low ethanol content of 0.1% or less, with high yield using nontoxic solvent.
NOVELTY - The utility model claims an efficient marsh gas pool of hydraulic shoe type biogas liquid circulation flow, a feedstock tube, a discharge pipe, a fermentation pipeline, composed of, a feedstock material and a detachable tube and a U type pipe. terminal a fermentation feedstock and a side wall and a side wall extended U-type discharge pipe in fermentation, between a U-type fermentation pipe on top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, a U type pipe is set with fermentation with gas-guide tube, the fermented line a, liquid flow stirring notable effect, and promotes a uniform strain distribution.
NOVELTY - The utility model claims a device for pipe type marsh gas fermentation system lifting biogas turbulence effect, wherein it comprises a feedstock tube, a discharging tube and a pipe ferment, wherein the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position... feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system. It increases the fermentation system and system.
NOVELTY - The utility model claims a high-efficient methane generating system of straight pressure extrusion biogas stirring convection, wherein it comprises a feedstock tube, a discharging tube and a pipe ferment, wherein the ferment pipe is straight pipe, fermentation pipe two end side top part equipped with open mouth and a detachably connected with a biogas liquid face with a feedstock tube and discharging tube, a feedstock side wall and a side wall extending to the discharge pipe in the fermentation, installed on fermentation pipeline between top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharge tube and drain in fermentation pipeline also is set with multi-number between the feedstock has a side wall and a side wall and between the discharging plate, a feedstock/discharging pipe side wall and adjacent blocking plate and forming a space of fermentation area or a space between adjacent blocking plate forming one of fermentation area, a top of a fermentation zone is connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, In using biogas liquid flow stirring promoting uniform distribution of strain, and promote the fermentation material into fermentation system, fermentation system and increase the gas production system.
NOVELTY - This new utility model claims a methane generating system for prompting uniform strain distribution by one-way circulation flow stirring, wherein a feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position... feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone... connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain. and it promots the fermentation raw material into a fermentation system, fermentation system and increase the gas production system.
NOVELTY - This new utility model claims of double pipe channel beyond efficient biogas liquid convection stir the methane generating device, comprising the feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, fermentation pipe two side top part equipped with open end and respectively can detachably connected with the following biogas liquid side with feedstock tube and discharging tube, feedstock pipe side wall and discharge tube side wall extending to ferment in the pipe, installed on fermentation pipeline between top, and feedstock pipe connected with level set between the feedstock tube drain pipe, water discharging pipe and connected with horizontal place of discharge pipe. in fermentation pipeline also set with multi-number between the feedstock tube side wall and discharge pipe side wall and between baffle, feedstock pipe feeding/discharging pipe side wall and the adjacent blocking plate and form one space of fermentation area or the space between the adjacent blocking plate forming one of fermentation area, respectively the top of ferment cell connected with each independent and gas-guide tube, the gas-guide tube is set with upper valve with the liquid circulation flow stirring performance strong. In using biogas liquid flow stirring promoting uniform distribution of strain, and promote the fermentation material into fermentation system, fermentation system and increase the gas production system.
NOVELTY - This new utility model claims of separated type methane generator promote the marsh liquid turbulent flow effect and device, comprising the feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, fermentation pipe two side top part equipped with open end and respectively can detachably connected with the following biogas liquid side with feedstock tube and discharging tube, feedstock pipe side wall and discharge tube side wall extending to ferment in the pipe, installed on fermentation pipeline between top, and feedstock pipe connected with level set between the feedstock tube drain pipe, water discharging pipe and connected with horizontal place of discharge pipe. in fermentation pipeline also set with multi-number between the feedstock tube side wall and discharge pipe side wall and between baffle, feedstock pipe feeding/discharging pipe side wall and the adjacent blocking plate and form one space of fermentation area or the space between the adjacent blocking plate forming one of fermentation area, respectively the top of ferment cell connected with each independent and gas-guide tube, the gas-guide tube is set with upper valve with a biogas circulation stirring performance strong flow, using biogas liquid flow stirring to promote uniform distribution of strain. and it promots the fermentation raw material into a fermentation system, fermentation system and increase the gas production system.
NOVELTY - The invention claims a methane generating system for prompting uniform strain distribution by using high pressure, wherein a feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position... feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone... connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system, It increases the fermentation system and system.
NOVELTY - The utility model claims a have a high air pressure to promote turbulence of biogas methane generating system, wherein a feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, pipe respectively connected with fermentation feedstock tube and discharge tube with two end side, between installed on fermentation pipe top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, pipeline and fermentation feedstock a position... feedstock with a plate, fermented pipe and discharging pipe connecting seat to set with a discharging blocking plate, a fermentation pipeline also is set with multi-number between the feedstock has a blocking plate and a blocking plate and a discharging plate, the space between the adjacent blocking plate forming one of fermentation area, a top of a fermentation zone... connected with gas-guide tube, the gas-guide pipe is set with a valve with a biogas circulation stirring a strong flow, a biogas liquid flow stirring to promote uniform distribution of strain, and promote the fermentation raw material into a fermentation system, Increase the fermentation system and system.
NOVELTY - This new utility model claims of using air pressure pushing biogas slurry circulation flow stirring of methane generating bacteria distributing system, comprising the feedstock tube, discharging tube, pipe ferment, the ferment pipe is straight pipe, fermentation pipe two side top part equipped with open end and respectively can detachably connected with the following biogas liquid side with feedstock tube and discharging tube, feedstock pipe side wall and discharge tube side wall extending to ferment in the pipe, installed on fermentation pipeline between top, and feedstock pipe connected with level set between the feedstock tube drain pipe, water discharging pipe and connected with horizontal place of discharge pipe. in fermentation pipeline also set with multi-number between the feedstock tube side wall and discharge pipe side wall and between baffle, feedstock pipe feeding/discharging pipe side wall and the adjacent blocking plate and form one space of fermentation area or the space between the adjacent blocking plate forming one of fermentation area, respectively the top of ferment cell connected with each independent and gas-guide tube, the gas-guide tube is set with upper valve with the liquid circulation flow stirring performance strong. In using biogas liquid flow stirring promoting uniform distribution of strain, and promote the fermentation material into fermentation system, fermentation system and increase the gas production system.
NOVELTY - Method of preserving timber or wood products, involves providing timber or wood products, and applying preservative composition comprising bifenthrin to the timber or wood product, where the bifenthrin has retention in the timber or wood product of 0.5-4 g/m.    USE - The method is useful for preserving timber or wood products from insect, preferably termite e.g. Coptotermes acinaciformis, bacterial or fungal attack which is useful as building material used in housing as timber framing, trussing or particle board (all claimed).    ADVANTAGE - The method is cost-effective, rapid, and environmentally-friendly.
NOVELTY - The device has casing (630) whose inside portion is set with optical anode (110) and optical cathode (120). Upper cover plate (620) is provided in upper portion of casing. Lower cover plate (610) is provided in lower portion of casing. Optical anode is connected with upper cover plate, and optical cathode is connected with lower cover plate. Upper cover plate and lower cover plate are tightly contacted with casing. Anode concentric ring element (111) is set at lower surface of anode wafer (112). Cathode concentric ring element (121) is set at upper surface of cathode wafer (122).    USE - Photo-catalytic water reaction hydrogen production device.    ADVANTAGE - The photo-catalytic water reaction hydrogen production device is provided with improved hydrogen production efficiency and high reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the photo-catalytic water reaction hydrogen production device.    Optical anode (110)    Anode concentric ring element (111)    Anode wafer (112)    Optical cathode (120)    Cathode concentric ring element (121)    Cathode wafer (122)    Lower cover plate (610)    Upper cover plate (620)    Casing (630)
NOVELTY - Cultivation of Pleurotus citrinopileatus involves taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 45-55 wt.% 3-5 mm bagasse and 13-15 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days and adding 2-3 wt.% lime for first turn, 1 wt.% gypsum for second turn and 1 wt.% calcium superphosphate for third turn.    USE - Method for cultivating Pleurotus citrinopileatus (claimed).    ADVANTAGE - The method is environment-friendly, saves manpower and coal resources, improves bacterial resistance and growth performance of mushroom, and has high biological conversion rate.    DETAILED DESCRIPTION - Cultivation of Pleurotus citrinopileatus comprises taking 3-4 wt.% 2-3 mm dried shiitake stem, adding 20-30 times water, soaking for 18-24 hours, adding 45-55 wt.% 3-5 mm bagasse, 23-33 wt.% cotton seed hull and 13-15 wt.% rice bran, material piling at 1.0-1.2 m high, 2-3 m wide and 300-500 kg dry weight, inserting stick to form hole with 10-15 cm diameter, fermenting naturally at 1 stomata/m3 stomatal density until it reaches 60 degrees C, insulating for 24 hours, turning once a day for 5-6 days, adding 2-3 wt.% lime for first turn, 1 wt.% gypsum for second turn and 1 wt.% calcium superphosphate for third turn, controlling moisture content to 63-65%, cooling to obtain cultivation material, adding to Pleurotus citrinopileatus, covering mycelium with 1-2 cm thick loam soil, adding 20 times water to dried shiitake stem, soaking for 18-24 hours, filtering, diluting to obtain 0.01-0.02 g/mL dried shiitake stem solution and spraying to loam soil covered mycelium at 4-6 kg/m2.
NOVELTY - The device has mixing pump (1) that is connected with nozzle (7) through pipeline. Insulation sleeve and reaction tube (6) are connected with screw thread. Strengthening pipe (10) is provided with pressure spring electrode (9). Connecting element (12) is connected with each separating room entrance (13) through pipeline. Heavy phase outlet valve (18) and plant tank (19) are connected with pipeline. Pressure spring electrode and high voltage electrode group (5) are connected with high pressure electrostatic generator (11) through lead.    USE - Device for producing bio-diesel.    ADVANTAGE - The device is simple in structure, and having safe operation. Response time is short. The charging process of the device method is simple. The device consumes low energy. Full transesterification is achieved. Lipid conversion rate is high.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing bio-diesel.    Mixing pump (1)    High voltage electrode group (5)    Reaction tube (6)    Nozzle (7)    Pressure spring electrode (9)    Strengthening pipe (10)    High pressure electrostatic generator (11)    Connecting element (12)    Separating room entrance (13)    Heavy phase outlet valve (18)    Plant tank (19)
NOVELTY - A long-acting nitrogen and phosphorus fertilizer comprises 20-30 pts. wt. urea, 20-25 pts. wt. monoammonium phosphate, 15-22 pts. wt. ammonium sulfate, 8-14 pts. wt. diatomaceous earth, 6-10 pts. wt. ammonium bicarbonate, and 3-5 pts. wt. boric acid.    USE - Long-acting nitrogen and phosphorus fertilizer.    ADVANTAGE - The fertilizer provides persistent high fertility.
NOVELTY - Device comprises biological garbage pulverizer, pump (8), pipeline (1), anaerobic digestion pool (6), a discharging device, biogas treatment and utilization apparatus with electrical equipment. The biological garbage (2) is transferred to the anaerobic digestion pool through the pipeline where the fermentation pool is set with a detecting device (5).    USE - Device used for fermenting biological garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Pipeline (1)    Biological garbage (2)    Detecting device (5)    Anaerobic digestion pool (6)    Pump (8)
NOVELTY - Micro Bacillus XR001 strain is preserved at China General Microbiological Culture Collection Center (CGMCC No: 10237), and is new.    USE - Micro Bacillus XR001 strain used for degrading oil from the waste water.    ADVANTAGE - The micro Bacillus XR001 strain degrades oil from waste water in mild reaction conditions with low energy consumption and with high efficiency where the degradation efficiency is more than 80%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of screening degrading bacteria, which involves:    (A) adding waste water sludge (0.08g/mL) to sterile water and incubating in dark at a shaker for 24 hours to obtain bacterial suspension;    (B) sterilizing the inoculated bacterial suspension (5 vol.%) in inorganic salt medium and placing at a shaker in dark for 7 days to obtain bacteria;    (C) adding glucose (5 vol.%) to the obtained bacteria in an oil paint with waste water and sub-culturing for 7 days in dark at a to obtain broth of degradation strains with oil-based paint;    (D) reducing the subculture generation to 1/5 and increasing (5 vol.%) the volume ratio of oil-based paint generation;    (E) adding inorganic salt agar, sterile water and inorganic medium for dilution, placing for solidification and spreading evenly at 30 degrees C for 7 days;    (F) picking up the transparent rings around the colonies and performing repeated inoculations to obtain purified oil paint degradation strains; and    (G) inoculating the purified oil paint degradation strains in Luria-Bertani (LB) medium to obtain colonies of bacteria at a concentration of 1 at an optical density of 600nm.
NOVELTY - A feeding composition comprises Agrocybe aegerita substrate, and fermented cow manure at volume ratio of 1:5.    USE - Feeding composition used for earthworms (claimed).    ADVANTAGE - The feeding composition is non-polluting, and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the feeding composition comprising pulverizing cow manure, sieving to remove debris, adjusting humidity to 60-65%, stacking to width of 2-3 m, and height of 1 m, fermenting for 25-28 days for 5-7 days, turning, fermenting for 11-12 days, turning, fermenting for 15 days, turning, fermenting for 20 days, turning, adjusting pH value to 6.8-7.6, and mixing with Agrocybe aegerita substrate.
NOVELTY - Functional microbial fermented fertilizer comprises 30-70 wt.% starfish and 30-70 wt.% stratum. The fertilizer further comprises 5-30 pts. wt. molasses and 5-20 pts. wt. microorganism based on 100 pts. wt. mixture of starfish and stratum.    USE - The fertilizer is useful as plant growth hormone for promoting plant growth.    ADVANTAGE - The fertilizer provides nitrogen, phosphorus and potassium to plant, and improves quality and functionality of soil, and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing functional microbial fermented fertilizer, comprising (a) mixing and pulverizing starfish and stratum to produce first mixture, (b) mixing mixture of starfish and stratum with molasses and microorganism to produce second mixture, (c) mixing the second mixture with salt water, and (d) fermenting the mixture; (i) mixing 30-70 wt.% starfish, 5-20 wt.% seaweed, 5-20 wt.% Saccharina japonica, 5-20 wt.% hijiki, 5-20 wt.% sargassum, 5-20 wt.% stratum to produce first mixture, (ii) mixing 100 pts. wt. mixture of starfish and stratum with 5-30 pts. wt. molasses and 5-20 pts. wt. microorganism to produce second mixture, (iii) mixing the second mixture with salt water, and (iv) fermenting the mixture.
NOVELTY - Fertilizer comprises 38 wt.% plant straw, 20 wt.% animal waste, 2 wt.% beer yeast, 20 wt.% urea, 10 wt.% monoammonium phosphate and 10 wt.% potassium sulfate.    USE - The fertilizer is useful for conditioning soil and improving soil activity.    ADVANTAGE - The fertilizer is cost-effective, required in minimal quantity, and increases yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of fertilizer, which involves (a) mixing 30% of plant straw, animal waste, urea, monoammonium phosphate and potassium sulfate, grinding mixture, granulating ground mixture into granules, cooling and drying granules, (b) grinding remaining plant straw, adding beer yeast, and molasses to ground plant straw, mixing mixture until moisture content reaches 50-60% and 30% carbon nitrogen ratio, stacking mixture, and fermenting mixture at 20-30 degrees C for 8-12 days, (c) dissolving fermented product obtained in the step (b) in water at 60 degrees C, spraying dissolved solution on granules obtained in the step (a), and packing granules into capsule.
NOVELTY - Purifying terlipressin involves dissolving terlipressin coarse peptide liquid solution in water and then adding the dissolved material with 5% ammonia water. The obtained material is stirred and then the pH value is regulated to 7-8 to obtain terlipressin coarse peptide liquid alkaline solution. The obtained solution is added with 1.5% hydrogen peroxide aqueous solution at pH 7-8 and then the obtained material is filtered to obtain oxidized coarse terlipressin peptide liquid. The octadecyl silane bonding silicon glue is selected as mobile phase A and aqueous solution of phosphoric acid.    USE - Method for purifying terlipressin (claimed).    ADVANTAGE - The method enables to purify terlipressin in cost-effective and environment-friendly manner, and with high efficiency and purity, and mild reaction conditions.    DETAILED DESCRIPTION - Purifying terlipressin involves dissolving terlipressin coarse peptide liquid solution in water and then adding the dissolved material with 5% ammonia water. The obtained material is stirred and then the pH value is regulated to 7-8 to obtain terlipressin coarse peptide liquid alkaline solution. The obtained solution is added with 1.5% hydrogen peroxide aqueous solution at pH 7-8 and then the obtained material is filtered to obtain oxidized coarse terlipressin peptide liquid. The octadecyl silane bonding silicon glue is selected as mobile phase A and aqueous solution of phosphoric acid, triethylamine and diethylamine acetate as B phase. The oxidized coarse terlipressin peptide liquid is eluted with acetonitrile and then the pH value of the eluted material is adjusted to 4.5 to obtain the purified desired material.
NOVELTY - Purifying and preparing triptorelin involves dissolving triptorelin crude peptide in warm water and then selecting octadecylsilane bonded silica gel as stationary phase and 0.2% aqueous solution of phosphoric acid and tetrabutyl ammonium phosphate as mobile phase. The dissolved material is purified with 12-15% mobile phase, where the 0.2% aqueous solution of phosphoric acid is prepared by adding 1 liter of pure water with 2 milliliters of phosphoric acid and 1 milliliter tetrabutyl ammonium phosphate.    USE - Method for purifying and preparing triptorelin (claimed).    ADVANTAGE - The method enables to purify and prepare triptorelin in cost-effective and eco-friendly manner, and with high yield and purity, and mild reaction conditions.
NOVELTY - Performing protein affinity-purification involves cloning M protein in an expression vector, and then performing purification of cloned M protein in order to obtain purified soluble M protein. The protein affinity-purification is performed, where the obtained purified soluble M protein is conjugated with anti-chicken immunoglobulin Y antibodies in a molar ratio of 1:1. The resulted conjugated immunoglobulin mixture is then subjected to N-Hydroxysuccinimidyl-activated Sepharose (RTM: Pre-activated agarose matrix) 4 fast flow to obtain immunoglobulin Y antibodies as primary products.    USE - Method for performing protein affinity-purification used for obtaining purified immunoglobulin Y antibodies (claimed).    ADVANTAGE - The 95% efficient protein affinity-purification enables to obtain highly purified immunoglobulin Y antibodies, in a simple and environment-friendly manner.    DETAILED DESCRIPTION - Performing protein affinity-purification involves cloning M protein in an expression vector, and then performing purification of cloned M protein in order to obtain purified soluble M protein. The protein affinity-purification is performed, where the obtained purified soluble M protein is conjugated with anti-chicken immunoglobulin Y antibodies in a molar ratio of 1:1. The resulted conjugated immunoglobulin mixture is then subjected to N-Hydroxysuccinimidyl-activated Sepharose (RTM: Pre-activated agarose matrix) 4 fast flow to obtain immunoglobulin Y antibodies as primary products. The immunoglobulin Y antibodies are obtained from egg yolks. The resulting immunoglobulin Y antibodies, after purification, is dissolved in phosphate buffered saline (pH 7.0 to 7.4), where the prepared immunoglobulin Y antibodies-containing solution is dialyzed in dialysis bag under overnight condition at 4 degrees C, for collecting highly purified immunoglobulin Y antibodies as the finished product.
NOVELTY - A soil improver contains 60-65 pts. wt. yellow mud, 4-6 pts. wt. biological coal, 6-8 pts. wt. bentonite, 0.5-0.8 pt. wt. polyacrylamide, 8-10 pts. wt. leather mud pit, 3-5 pts. wt. old pit mud, 3-5 pts. wt. pond sludge, 2-4 pts. wt. peat, 3-5 pts. wt. soybean meal, 3-5 pts. wt. fresh fermented grains, 3-5 pts. wt. yeast powder, 10-12 pts. wt. composite mud functional broth, 10-12 pts. wt. yellow water, 7-9 pts. wt. wine tail and 8-10 pts. wt. inorganic nutrient solution. The biological coal, bentonite and polyacrylamide are added as soil additives.    USE - Soil improver (claimed).    ADVANTAGE - The soil improver has excellent soil improvement characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of soil improver.
NOVELTY - Microbial inoculum comprises Clostridium strain DSM19732, Flavobacterium multrivorum strain DSM22681, Coprothermobacter proteolyticus strain DSM5265, Thermoanaerobacter tengcongensis strain DSM14523, Thermus aquaticus strain DSM8682, thermophiles strain DSM21630, Syntrophomonas strain DSM4212, Methanothermobacter thermautotrophicus strain DSM1053, Methanosarcina strain DSM1825, methanogenic bacteria strain DSM25720 and Methanobacterium strain DSM3637.    USE - Microbial inoculum used for digesting kitchen garbage in anaerobic condition (claimed).    ADVANTAGE - The microbial inoculum enables to digest kitchen garbage in a rapid and efficient manner.
NOVELTY - Using microorganism electrolytic pool for alcohol conversion as acetic acid for producing methane comprises using proton exchange film, separating electrolytic pool as anode room and cathode room, respectively placing anode electrode and cathode electrode, and connecting through high potential terminal of voltage-stabilizing power supply and low potential terminal. The acetic acid fungus is Geobacter metallireducens. The cathode electrode surface is attached to a single electroactive methane or mixture with electro-active methane-producing fungus.    USE - Method for using microorganism electrolytic pool for alcohol conversion as acetic acid for producing methane for wastewater treatment (claimed).    ADVANTAGE - The method is energy-saving and has reduced emission.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for alcohol conversion and producing methane.
NOVELTY - The hydropower station has a pumping pipe (5) that is arranged on a groove portion of upper water tube. A concrete retaining wall (4) is surrounded on the upper reservoir (3), and set with a solar energy electric plate (13). A power storage battery is mounted at inside the concrete retaining wall, and connected with wind power generator (12) and composite water pump (6). A solar energy battery is connected with the composite water pump and solar energy electric plate. The power storage battery and solar energy storage battery are mutually connected in series.    USE - Ecological reservoir pumped-storage hydropower station.    ADVANTAGE - The energy conversion in the hydropower station is improved. The water quality of the hydropower station is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sewage treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ecological reservoir pumped-storage hydropower station.    Upper reservoir (3)    Concrete retaining wall (4)    Pumping pipe (5)    Composite water pump (6)    Wind power generator (12)    Solar energy electric plate (13)
NOVELTY - Preparing cultivation material involves pulverizing wood powder (58-62%), cotton seed hull (23-26%), soybean cake (8-10%), mushroom (3-4%), lime (2%) and light calcium carbonate (1%) to obtain material having size of 3-5mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, cotton seed hull and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin.    USE - Method for preparing cultivation material used for Hypsizygus marmoreus (claimed).    ADVANTAGE - The method is eco-friendly, and ensures increased catalytic decomposition and growth of Hypsizygus marmoreus.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (58-62%), cotton seed hull (23-26%), soybean cake (8-10%), mushroom (3-4%), lime (2%) and light calcium carbonate (1%) to obtain material having size of 3-5 mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, cotton seed hull and soybean powder are added to soaked product. Obtained mixture (300-500 kg) is piled in heap having height of 1-1.2 m and diameter of 10-15 cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Light calcium carbonate is added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product id kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 24-25 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing wood powder (42-48%), corn cob (38-40%), bean cake (8-10%), mushroom (3-4%), lime (2.5%) and light calcium carbonate (1%) to obtain material having size of 3-5mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, cotton seed hull and bean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented.    USE - Method for preparing cultivation material used for Hypsizygus marmoreus (claimed).    ADVANTAGE - The method is eco-friendly, and ensures increased catalytic decomposition and growth of Hypsizygus marmoreus.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (42-48%), corn cob (38-40%), bean cake (8-10%), mushroom (3-4%), lime (2.5%) and light calcium carbonate (1%) to obtain material having size of 3-5mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, cotton seed hull and bean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Light calcium carbonate is added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product id kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 24-25 days to obtain the final product.
NOVELTY - Fertilizer comprises organic fertilizer, which is obtained by culturing tobacco leaves with Hermetia illucens larvae, and inorganic fertilizer, and microbial powder comprising nitrogen-fixing bacteria, Bacillus mucilaginosus, and Enterobacter cloacae.    USE - Fertilizer used for cultivating soybean (claimed).    ADVANTAGE - The fertilizer is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer used for cultivating soybean, which involves:    (A) obtaining organic fertilizer by cultivating tobacco leaves with Hermetia illucens larvae;    (B) mixing superphosphate, calcium magnesium phosphate, potassium sulfate, potassium dihydrogen phosphate, calcium sulfate, zinc sulfate, molybdate, ferric chloride, clay, and borax to obtain a mixture;    (C) adding microbial powder to obtained mixture, which is dried to obtain moisture content 5%; and    (D) mixing dried product with organic fertilizer to obtain another mixture, which is granulated to obtain final product.
NOVELTY - Preparing cultivation material involves crushing 52-58% sawdust, 25-28% corn core, 10-12% soybean, 3-4% mushroom, 3% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2 m, and width 2-3 m to obtain ladder-shaped stack (300-500 kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room.    USE - Method for preparing cultivation material used for Auricularia polytricha (claimed).    ADVANTAGE - The method is eco-friendly and saves labor cost, and enables to prepare cultivation material that produce highly active metabolite product of Auricularia polytricha, and ensures Auricularia polytricha growth.    DETAILED DESCRIPTION - Preparing cultivation material involves crushing 52-58% sawdust, 25-28% corn core, 10-12% soybean, 3-4% mushroom, 3% lime and 1% gypsum into powder with particle diameter of 3-5 mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2 m, and width 2-3m to obtain ladder-shaped stack (300-500 kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room and cultured at 18-20 degrees C for 36-38 days.
NOVELTY - Preparing cultivation material involves crushing 58-62% sawdust, 12-16% corn core, 16-18% soybean, 4-5% mushroom, 3-4% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room.    USE - Method for preparing cultivation material used for black fungus (claimed).    ADVANTAGE - The method is eco-friendly and saves labor cost, and enables to prepare cultivation material that produce highly active metabolite product of black fungus, and ensures its rapid growth.    DETAILED DESCRIPTION - Preparing cultivation material involves crushing 58-62% sawdust, 12-16% corn core, 16-18% soybean, 4-5% mushroom, 3-4% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room and cultured at 18-20 degrees C for 36-38 days.
NOVELTY - Producing 1-naphthol-4-sulfonic acid comprises adding water into sodium 4-aminonaphthalene-1-sulfonic acid, heating, adding caustic soda liquid, completely stirring, conveying into enamel reaction pot, circulation in sealing system, heating, introducing sulfur dioxide for hydrolysis reaction, and measuring after sometime, taking caustic soda liquid into ammonia concentration pot, heating, adding the hydrolyzate, heating to remove ammonia, precipitating, concentrating and filtering, steam blowing filtrate, adding hydrochloric acid, filtering when hot, and blow drying filter cake.    USE - The method is useful for producing 1-naphthol-4-sulfonic acid (claimed).    ADVANTAGE - The method: is environmentally friendly (claimed); utilizes sulfur dioxide, which increases 4-sodium sulfamate conversion rate up to 100%; saves sulfur resource to about 50%; and reduces production cost.    DETAILED DESCRIPTION - Producing 1-naphthol-4-sulfonic acid comprises (a) taking sodium 4-aminonaphthalene-1-sulfonic acid into a dissolution pot, adding water, heating to 95 degrees C, adding caustic soda liquid, completely stirring the whole solution, conveying into 3000 l enamel reaction pot, circulation in sealing system, heating to 100 degrees C, introducing sulfur dioxide for hydrolysis reaction, and measuring after sometime, (b) taking caustic soda liquid into ammonia concentration pot, heating to 100 degrees C, adding the hydrolyzate, adjusting the pH of the solution, heating to remove ammonia, carrying out acid precipitation in one batch, concentrating and filtering to remove impurities, and (c) steam blowing the filtrate, conveying into acid precipitation kettle, adding hydrochloric acid to adjust pH of the solution, filtering when hot, blow drying filter cake and packing.
NOVELTY - Microbial inoculant is prepared by mixing tomato skin residue, rice hull, wheat bran and microorganism composite fermentation raw liquid to obtain fermentation preparation.    USE - Microbial inoculant used for decomposing organic material and improving soil organic matter and soil structure (all claimed).    ADVANTAGE - The microbial inoculants quickly decomposes cellulose, hemicelluloses and lignin in soil structure, restrains growth of pathogen, and increases performance, disease resistance and immune force of plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microorganism composite fermentation raw liquid, which involves:    (A) switching culture strain, rejuvenating after purifying, and shaking culture medium;    (B) switching culture medium to small tank (120 l) for seed culture, where culture medium comprises 1.2 kg corn flour, 1.2 kg bran, 0.5 kg molasses and 0.05 kg zinc phosphate;    (C) fermenting the culture medium at 30 degrees C with rotating speed of 120 revolutions per minute for 18 hours;    (D) placing fermentation liquid as seed to fermentation tank (10 ton), and adding bacterial culture medium, which comprises 7 ton water, 110 kg corn flour, 120 kg wheat bran, 75 kg molasses and inorganic salt and growth factor, where inorganic salt comprises 0.2 wt.% copper sulfate and prompting growth factor comprises 0.01 wt.% riboflavin and 0.01 wt.% pantothenic acid;    (E) fermenting the culture medium at 121 degrees C for 30 minutes, and then cooling at 33 degrees C; and    (F) fermenting the product 30 degrees C with rotating speed of 150 revolutions per minute for 18-22 hours to obtain final product.
NOVELTY - Selenium rich vegetable planting enriched soil comprises dry farmland soil, peat soil, selenium enriched mixture and loam soil at a weight ratio of 1:1:0.4:0.2-1.2:1:0.8:0.4. The dry farmland soil is 3-6 months dried paddy field soil taken during seeding of crops. The loam soil comprises rice straw, branch leaves, burned weed ash and woodland soil at a weight ratio of 1:2-3. The selenium enriched mixture comprises 4 kg manure, 0.8 kg lime, 4 kg poultry and livestock manure, 0.5 kg cake fertilizer and 5-10 g sodium selenite, prepared by mixing and composting.    USE - Selenium rich enriched soil used for planting vegetable, particularly Osmunda japonica (claimed).    ADVANTAGE - The soil has lasting fertilizer effect and increase yield Osmunda japonica.    DETAILED DESCRIPTION - Selenium rich vegetable planting enriched soil comprises dry farmland soil, peat soil, selenium enriched mixture and loam at a weight ratio of 1:1:0.4:0.2-1.2:1:0.8:0.4. The dry farmland soil is 3-6 months dried paddy field soil taken during seeding of crops. The loam comprises rice straw, branch leaves, burned weed ash and woodland soil at a weight ratio of 1:2-3. The selenium enriched mixture comprises 4 kg manure, 0.8 kg lime, 4 kg poultry and livestock manure, 0.5 kg cake fertilizer and 5-10 g sodium selenite, prepared by mixing and composting. The poultry and livestock manure is prepared by taking sorghum, wheat, and soybean at a weight ratio of 6:3:1, crushing, mixing into fermentation substrate, mixing selenium yeast and fermentation substrate at a ratio of 1:5, adding water, fermenting for 70 days at 28 degrees C, feeding to livestock and poultry, and collecting livestock and poultry manure.
NOVELTY - The device has a connecting pole (6) connected with a transparent shell (2) by a cover plate (3). An upper part of an outer bearing drug box (8) is provided with an inner connecting rod (6). The outer bearing drug box and an inner bearing drug box (9) are respectively formed with an external through hole (81) and an inner through hole (91). A motor (4) is connected with a stirring shaft (5). A fan (10) is connected with a smoke pipe (11) and a filter pipe (12). An end of the smoke pipe is fixed on the shell. A middle part of the filter tube is formed with a water flow hole.    USE - Plaster manufacturing device for a home and a small industry.    ADVANTAGE - The device has high automation range so as to reduce labor force and processing time, and reduces environment pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a plastic manufacturing device.    Transparent shell (2)    Cover plate (3)    Motor (4)    Stirring shaft (5)    Connecting pole (6)    Outer bearing drug box (8)    Inner bearing drug box (9)    Fan (10)    Smoke pipe (11)    Filter pipe (12)    External through hole (81)    Inner through hole (91)
NOVELTY - Carbon steel reinforced concrete structure-based anaerobic power generation gas station comprises an anaerobic device, a temperature increasing pressure pump, a power generation unit, and a four portion-based purifier.    USE - The gas station is useful in biogas production.    ADVANTAGE - The gas station increases biogas yield; is economical, and suitable in rural construction using local materials from farms and livestock farms; has environment purification property; saves energy, and raw materials resources; removes overflowing from pipe and overspills of device; and completely utilizes feed liquid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the carbon steel reinforced concrete structure-based anaerobic power generation gas station.
NOVELTY - Inactivating tobacco virus involves pre-treating tobacco waste by placing into pretreatment unit. The pre-treated product is transferred to anaerobic digestion unit and processed at 35-55 degrees C for more than 20 days to obtain biogas which is transferred into the biogas purification storage unit, and then transferring the biogas in utilization unit.    USE - Method for inactivating tobacco virus for preventing and treating viral diseases (claimed).    ADVANTAGE - The method enables to inactivate tobacco virus with high efficiency.
NOVELTY - Preparing trilobatin involves treating grapefruit agricultural waste with 60-95% aqueous ethanol to obtain grapefruit flavonoid extract, which is basified with sodium hydroxide and subjected to palladium carbon catalytic hydrogenation at low pressure at room temperature to obtain hydrogenated product. The obtained hydrogenated product is hydrolyzed by rhamnosidase enzyme to obtain product, which is cooled to obtain trilobatin.    USE - Method for preparing trilobatin (claimed).    ADVANTAGE - The method enables to prepare trilobatin in eco-friendly manner, and is suitable for industrial applications.
NOVELTY - Biological humic acid liquid fertilizer comprises 100-1000 pts. wt. maifanite powder, 5-50 pts. wt. composite microorganism microbial inoculums, 3-30 pts. wt. photosynthetic bacteria, 2-20 pts. wt. honey, 200-2000 pts. wt. water and solid raw material granules are obtained through 240-400 meshes.    USE - Biological humic acid liquid fertilizer used for stimulating plant growth.    ADVANTAGE - The biological humic acid liquid fertilizer is eco-friendly, increases yield, nutrient quality and appearance quality of crops, improves soil structure, enhances fertilizer effect and pesticidal effect, and promotes sustainable development of agriculture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological humic acid liquid fertilizer, which involves:    (A) mixing and fermenting straw, composite microorganism microbial inoculum, photosynthetic bacteria, honey, and water in a fermentation tank at 25-35 degrees C for 7-10 days; and    (B) fermenting the obtained fermented product after mixing remaining components in another fermentation tank at 25-35 degrees C for 7-10 days.
NOVELTY - N-Cyclohexyl-2-benzothiazolesulfenamide preparation involves mixing crude 2-mercaptobenzothiazole thiazole and 25% cyclohexylamine into a reactor with stirring in a mass ratio of 1: 2.5. The formed solution is heating at 45 degrees C, and then sodium hypochlorite is added dropwise for 1.5 hours. The resulting mixture is cooled, filtered and washed with cyclohexylamine solution, and then dried to form N-cyclohexyl-2-benzothiazolesulfenamide.    USE - Method for preparing N-cyclohexyl-2-benzothiazolesulfenamide as rubber accelerator (claimed).    ADVANTAGE - The method prepares N-cyclohexyl-2-benzothiazolesulfenamide in a simple, cost-effective and eco-friendly manner with increased product yield on industrial scale.
NOVELTY - Improving biomass fuel gas exhaust gas comprises feeding biomass fuel into biomass gasifier; gasifying clean hot gas using burner; introducing hot air into heat exchanger and combusting at 500-900 degrees C; mixing biomass hot gas and hot air and combusting at 1500-1700 degrees C; and introducing air into kiln exhaust air heat exchanger at 600-900 degrees C, mixing with hot air, heating to 500-900 degrees C, cooling to 150-200 degrees C, and discharging to atmosphere.    USE - Method for improving biomass fuel gas exhaust gas (claimed) used for glass, ceramic, casting, and food industries.    ADVANTAGE - The method is energy-saving and avoids thermal pollution.
NOVELTY - Method of extracting total flavonoids from jasmine by response surface methodology, involves respectively crushing jasmine flower, stem and leaves to obtain powders, adding solvent to the powders, performing ultrasonic extraction at 85-92 degrees C for 2-3 times for 20-30 minutes (each time), filtering extracts, mixing filtrates, subjecting mixture to chromatographic separation for 0.5-1 hour, adding the product to purification tank, and performing chromatography, filtration or vacuum distillation to obtain purified product.    USE - The method is useful for extracting total flavonoids from jasmine by response surface methodology (claimed).    ADVANTAGE - The method simply and cost-effectively extracts flavonoids from jasmine, is environmentally-friendly, consumes less time, saves energy, and prevents loss of solvent. The production rate of product reaches 98.6%.    DETAILED DESCRIPTION - Method of extracting total flavonoids from jasmine by response surface methodology, involves (a) using design expert software based on Box-Behnken design for extraction, (b) respectively crushing jasmine flower, stem and leaves to obtain powders, (b) adding the powders to extracting tank, and then adding solvent to the tank for immersing the powders in solvent for 10-20 minutes, where liquid-solid ratio of solvent and the powders is 15-20:1, (c) subjecting immersed mixture obtained in step (b) to ultrasonic extraction at 85-92 degrees C for 2-3 times for 20-30 minutes (each time), filtering extracts, and mixing filtrates, (d) subjecting mixture obtained in step (c) to chromatographic separation for 0.5-1 hour, and (e) adding the product to purification tank, and performing chromatography, filtration or vacuum distillation to obtain purified product.
NOVELTY - Syzygium samarangense fertilizer comprises 18-22 pts. wt. cow manure, 15-18 pts. wt. chicken manure, 20-40 pts. wt. straw, 10-20 pts. wt. soybean meal, 10-20 pts. wt. bagasse, 40-50 pts. wt. urea, 30-40 pts. wt. superphosphate, 30-40 pts. wt. potassium sulfate, 2-5 pts. wt. trace elements, 3-5 pts. wt. amino acid, 15-25 pts. wt. herbal extract, 1-2 pts. wt. Bacillus subtilis and 0.6-1 pt. wt. Chaetomium.    USE - Syzygium samarangense fertilizer used for preventing plant disease and insect pests.
NOVELTY - A bacterial strain, preferably Clostridium beijerinckii strain SE-2 (CCTCC NO: M2014384) capable of producing alcohol (butanol and ethanol) fuels by synchronously utilizing glucose and xylose in lignocellulose hydrolyzate, is new. The alcohol fuel is produced by inoculating strain into seed medium, culturing medium, transferring the seed culture broth into secondary seed medium, culturing medium, adding the culture into secondary fermentation medium, performing anaerobic batch fermentation of the medium, controlling pH, and fermenting medium.    USE - The bacterial strain, preferably C.beijerinckii strain SE-2 is useful for producing alcohol (butanol and ethanol) fuels (claimed).    DETAILED DESCRIPTION - A bacterial strain, preferably Clostridium beijerinckii strain SE-2 (CCTCC NO: M2014384) capable of producing alcohol (butanol and ethanol) fuels by synchronously utilizing glucose and xylose in lignocellulose hydrolyzate, is new. The alcohol fuel is produced by (a) preparing seed culture medium and fermentation culture medium, (b) inoculating C.beijerinckii strain SE-2 into seed medium, and culturing medium at 37 degrees C for 16 hours to obtain seed culture broth, (c) transferring the seed culture broth into secondary seed medium, and culturing medium at 30 degrees C for 20 hours, and (d) adding the obtained culture into secondary fermentation medium containing corncob hydrolyzate, performing anaerobic batch fermentation of the medium at 37 degrees C, controlling pH of the medium using 10 M sodium hydroxide, and fermenting medium for 72 hours.
NOVELTY - The water treatment type garbage treatment device has a cylindrical hopper (11), which has the diameter, in which the upper part is broad and the lower part is narrow for injecting the food waste. A pulverizing device (12) is provided for pulverizing the food waste. A sensor and a check valve are equipped between the pulverizing device and a biofilter. The pulverizing device is configured to detach and attach in the garbage treatment device.    USE - Water treatment type garbage treatment device.    ADVANTAGE - The water treatment type garbage treatment device has a cylindrical hopper, which has the diameter, in which the upper part is broad and the lower part is narrow for injecting the food waste, and hence ensures cost effective water treatment type garbage treatment device, and prevents environmental contamination.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a water treatment type garbage treatment device. (Drawing includes non-English language text).    Hopper (11)    Pulverizing device (12)    Biofilter (13)    Water purifier (14)    Drain (17)
NOVELTY - Liquid organic fertilizer comprises 30-40 pts. wt. animal manure fermentation product, 20-30 pts. wt. corn straw powder, 10-15 pts. wt. egg shell, 5-10 pts. wt. rice, 15-20 pts. wt. water, 3-5 pts. wt. sewage sludge and vinegar (a bottle).    USE - Used as liquid organic fertilizer.    ADVANTAGE - The fertilizer has simple preparation procedure (claimed); rapidly increases the soil fertility; can be prepared at home easily using animal excrement and domestic waste, where the animal excrement contains various active enzymes produced by gastrointestinal secretion, and various enzymes produced by microorganisms; improves the soil enzyme activity, and physical, chemical and biological properties of soil; increases soil water retention capacity, fertilizer preservation, and ventilation performances; promotes the growth of plants; and is not only rich in nutrients, but also protects the environment, and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing liquid organic fertilizer, comprising uniformly stirring all the above mentioned raw materials, placing into a large cylinder, fermenting for 3-5 months under sealing conditions, and obtaining a layer of yellow liquid on the surface of the cylinder, once there is slight odor of alcohol, and finally obtaining the product.
NOVELTY - Method for cultivating cucumber, involves soaking cucumber seeds in warm water, further soaking the seeds in potassium permanganate solution, washing seeds with water, uniformly spreading seeds on clean gauze, placing seeds in incubator, preparing nursery matrix using peat and straw, adding e.g. lactic acid bacteria and adhesive mixed cucumber seed to the matrix, adding water, fertilizing, transplanting the seedlings with 4-5 leaves into ditch, preventing plants from bird, and controlling weeds by spraying hybrid strain.    USE - The method is useful for cultivating cucumber (claimed).    ADVANTAGE - The method is simple, cost-effective and environmentally-friendly, and produces high yield.    DETAILED DESCRIPTION - Method for cultivating cucumber, involves (a) selecting soil with deep, fertile and well-drained soil, (b) soaking cucumber seeds in warm water of 50-55 degrees C for 15-17 minutes, further soaking the seeds in 550 times potassium permanganate solution for 15-18 minutes, washing seeds with water, uniformly spreading seeds on clean gauze, and placing seeds in incubator at 28-32 degrees C for germination, (c) preparing nursery matrix using peat and straw, steaming matrix at 82 degrees C for 30-40 minutes, adding 55 ml/160 l lactic acid bacteria into nursery matrix, further adding 0.03-0.05% wettable powder, 1.5-3% copper sulfate and 1-1.5% adhesive mixed cucumber seed to the matrix, and adding water, (d) adding 20-30 kg/m2 manure, 5-7 kg/m2 calcium phosphate, 5-7 kg/m2 potassium sulfate, and 6-8 kg/m2 urea into the matrix, (e) preparing solution containing iodine and dried seaweed, and adding the solution into matrix, (f) transplanting the seedlings with 4-5 leaves into ditch, where the ditch has width of 14-16 cm, and groove depth of 3-4 cm, (g) preventing plants from bird, and (h) controlling weeds by spraying hybrid strain.
NOVELTY - Preparing special nutritional liquid, by (a) mixing milk vetch seeds, okra seeds, corn seeds, and selenium-rich pig manure, mixing with water-soluble activated selenium, germinating, drying, and milling to obtain selenium-rich germ powder, and (b) mixing biogas, animal blood, chicken manure, starch, selenium-rich germ powder, potassium sulfate, and phosphoric acid or potassium dihydrogen phosphate, inoculating mixed yeast, lactic acid bacteria, Bacillus subtilis and methane bacteria, fermenting, mixing with water, filtering, and storing in dark containers.    USE - The method is used for preparing special nutritional liquid for blueberry rhizospheric microorganism activation (claimed).    DETAILED DESCRIPTION - Method for preparing special nutritional liquid, involves (a) mixing 2400-2600 kg 40% milk vetch seeds, 30% okra seeds, 30% corn seeds, and selenium-rich pig manure, mixing with 0.2-0.5% water-soluble activated selenium, germinating, when shoot length reaches 2-5 cm drying the germinated seeds at low temperature until moisture content reaches less than or equal to 14%, and milling to obtain selenium-rich germ powder, and (b) mixing 28-32 pts. wt. biogas, 18-22 pts. wt. animal blood, 6-8 pts. wt. chicken manure, 32-34 pts. wt. starch, 4-6 pts. wt. selenium-rich germ powder, 3.3-3.8 pts. wt. potassium sulfate, and 1.4-1.6 pts. wt. phosphoric acid or potassium dihydrogen phosphate, inoculating mixed yeast, lactic acid bacteria, Bacillus subtilis and methane bacteria, fermenting under dark conditions at 25-34 degrees C for 15 days, mixing with water using mixer, filtering the mixture, and storing the filtrate in dark containers in cool environment.
NOVELTY - Fertilizer is prepared by mixing organic fertilizer, inorganic fertilizer comprising nitrogen, phosphorus, potassium and trace elements comprising inorganic zinc, boron, molybdenum and manganese, and microbial inoculum, where the fertilizer increases nitrogen fixation ability and absorption capacity of ginger plant root.    USE - As fertilizer for ginger (claimed).    ADVANTAGE - The fertilizer improves absorbability of the root of ginger plant, is rich in minerals and trace elements, and improves ginger yield and quality to more than 50%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves (a) mixing the edible fungi residue and chicken manure, subjecting the mixture to aerobic fermentation to obtain organic fertilizer, (b) mixing the above-mentioned nitrogen, phosphorus, potassium and trace elements comprising inorganic zinc, boron, molybdenum and manganese to obtain inorganic fertilizer, and (c) mixing the products obtained in the steps (a)-(b) and microbial inoculum, fermenting the mixture, crushing the mixture, spray drying the mixture at room temperature and pelletizing the mixture.
NOVELTY - A chromium complex contaminated soil microbial remediation agent comprises greater than or equal to 1 chemical reducing agent and active bacteria e.g. thermophilic carboxydotrophic Streptomyces.    USE - A chromium complex contaminated soil microbial remediation agent (claimed).    ADVANTAGE - The remediation agent effectively reduces hexavalent chromium concentration in soil and is fast, safe, inexpensive, and environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of chromium complex contaminated soil microbial remediation agent which involves mixing chemical reducing agent, active bacteria, carrier, and nutrients.
NOVELTY - A Clostridium butyricum UCN-12 bacterial strain having preservation number CGMCC No. 9652 is new.    USE - A Clostridium butyricum UCN-12 bacterial strain having preservation number CGMCC No. 9652 for composition used as livestock and/or poultry feed additive to prevent Clostridium welchii disease, and livestock and poultry deodorizing and veterinary medicine (all claimed).    ADVANTAGE - Clostridium welchii disease is treated or prevented without the need to add antibiotic which may leave antibiotic residuals that pollute the environment. Egg flavor is enhanced, and egg cholesterol and fat are reduced. Egg fishy smell is removed, and livestock and/or poultry production performance is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) composition for feed additive which is prepared by taking an effective amount of Clostridium butyricum UCN-12 bacterial strain, placing in bacterial strain fermentation culture, centrifuging fermentation culture liquid, and using resulting fermented bacterial culture, nutrient solution, or its dried product as active component in feed additive; and (2) Clostridium butyricum UCN-12 bacterial strain, its fermentation culture, nutrient solution, or dried product form for livestock and/or poultry feed additive.
NOVELTY - Bacillus amyloliquefaciens SQR-7 strain is new, which is preserved in China general microbiological culture collection with preservation number CGMCC NO: 7497.    USE - Bacillus amyloliquefaciens SQR-7 strain used for producing organic fertilizer for preventing and treating bacterial wilt disease in tobacco (all claimed) and promoting growth of tobacco.    ADVANTAGE - The Bacillus amyloliquefaciens SQR-7 strain has tobacco bacterial wilt prevention rate of 80%, and increases disease resistance ability of tobacco.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing organic fertilizer, which involves (a) culturing Bacillus in fermentation medium at 30 degrees C to obtain fermentation liquid inoculum, (b) inoculating fermentation liquid inoculum into rotten cattle manure compost and vegetable and then fermenting 30-50 degrees C for 5-7 days to obtain fermentation product; and (c) drying fermentation product at 60 degrees C to obtain the product, and    (2) preventing and controlling tobacco plant from bacterial wilt disease of continuous in continuously cropped soil comprises uniformyl spreading 325 kg/hectare ammonium bicarbonate and 750kg/hectare quicklime on the soil surface layer, watering, covering the soil with agricultural film, preprocessing the soil for 10 days, ploughing the soil and drying.
NOVELTY - Preparation of hydroquinone intermediate material involves mixing 863 mL water and 1 g ethylparaben, adding 5 g sodium hydrogen sulfite, 1 g ethylene diamine tetraacetic acid disodium, 90 g glycerin, 10 g vitamin C and 30 g hydroquinone, stirring, sterilizing and bottling in 97 mL bottle.    USE - Method for preparing hydroquinone intermediate material (claimed) used for preparing hydroquinone lotion.    ADVANTAGE - The method is environmental-friendly, inexpensive, economical and has high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for (1) preparation of hydroquinone with 99% yield comprising taking aniline in sulfuric acid medium and oxidizing with iron and pyrolusite powder containing 60-65% manganese dioxide, (2) preparation of hydroquinone with 85% yield comprising reducing p-benzoquinone to hydroquinone in water with iron, concentrating, bleaching, crystallizing and drying; and (3) preparation of hydroquinone with 80% yield comprising taking dicumyl peroxide, diisopropyl peroxide and acid catalyst, preferably sulfuric acid, adding hydroquinone and acetone, neutralizing, centrifuging, purifying and vacuum drying.
NOVELTY - A M85 methanol gasoline oil comprises 85 wt.% methanol, 3-5 wt.% gasoline, 1.2-2 wt.% sodium methoxide, 0.7-0.9 wt.% pine oil, 3-7 wt.% waste oil, 1-3 wt.% glycerol, 0.3-0.9 wt.% acetone and 0.3-0.7 wt.% polyoxyethylene ether.    USE - M85 Methanol gasoline oil (claimed).    ADVANTAGE - The M85 methanol gasoline oil has high quality, and excellent water resistance, shelf life and storage stability, and moisture content of 3%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of M85 methanol gasoline oil.
NOVELTY - The system has a semi-coke combustor (12) and a reburning gas burner (11) provided on boiler. A main burner (13) is located in main combustion zone and reburning gas burner is located in reburn zone. Semi-coke combustor is located upstream of reburning zone. A biomass inlet of a biomass silo (1) is connected to outlet of a biomass pyrolysis furnace (3). The outlet of pyrolysis furnace is connected to pyrolysis product inlet of a gas-solid separator (5). The gas outlet of gas-solid separator is connected to reburning gas burner and to semi-coke outet of semi-coke combustor.    USE - Biomass fuel reburn system.    ADVANTAGE - The biomass fuel reburn system avoids direct coal and biomass co-firing, while improving the utilization of biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biomass fuel combustion method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass fuel reburn system.    Biomass silo (1)    Biomass pyrolysis furnace (3)    Gas-solid separator (5)    Reburning gas burner (11)    Semi-coke combustor (12)    Main burner (13)
NOVELTY - The utility model claims a new automatic feeding of sheep grain gasification furnace, comprising stove body and storage hopper, and between the stove body and a material transporting mechanism connected; the between of a stove shell and stove body linear form, with the third arrange air inlet is set with a parallel and, from bottom to top in turn... a air inlet in the upper stove is linear, the second grade and the third grade air inlet air inlet. This new utility model is advantages as the second level air inlet is formed, which greatly increase of combustion-supporting efficiency, and the third level is set with an air inlet, a combustion gas in a compare the fuel, insufficient of quadratic air inlet quantity, a biomass raw material and burning is more uniform, eliminating second time smoke dust and discharge. At the same time also can be a standardization industrial production, reduce a cost, which is good for product to popularize.
NOVELTY - Synthesize biomass boiler device, relates to biomass energy conversion technology area. A hearth, the hearth combustion chamber connected with universally used for the smoke exhaust pipe, hearth set with draught fan, a bottom end is set with hearth with furnace cover, a hearth set heat absorbing plate a hearth for dividing into the first combustion chamber and the second combustion chamber, a heat absorbing plate connected with hearth bottom; a is set with exhaust pipe, exhaust pipe through transverse pipe is connected with a hearth and a second combustion chamber connected below the hearth side is set with a first combustion chamber connected with the furnace door, hearth and exhaust pipe side wall is interlayer and a discharge interlayer is an interlayer structure, the connected hearth, a interlayer filling with superconducting liquid type water, discharge pipe on a side provided with a interlayer connected with the water outlet side is set with hearth and interlayer connected with the water inlet. It solves the lack of some a biomass conversion and energy device, and the existing biomass energy conversion device not capable of full combustion, heat absorbing slow, no environmental protection problem equal.
NOVELTY - A morphine, heroin alkali standard product is prepared by taking sample heroin, acid hydrolyzing to obtain morphine crude product, purifying by silica gel column chromatography, re-crystallizing with methanol to obtain morphine standard product, gas chromatography mass spectrometry analysis detecting to heroin purity of greater than or equal to 97.8%, acetylating, re-crystallizing to obtain heroin alkali standard product, and gas chromatography mass spectrometry analysis detecting to heroin purity of greater than or equal to 98.4%.    USE - Method for preparing morphine, heroin alkali standard product (claimed).    ADVANTAGE - The method is safe and environment-friendly, has low cost, and performs at low temperature and pressure.
NOVELTY - The structure has a blower (560) and an integrated dilute chamber (550) formed in hydrogen gas separator (512). A vent valve (551) is set in upper outlet (512a) of separator, to eject hydrogen to dilute chamber. A water pump (514) is set for injecting electrolyzed water separated from hydrogen gas. A main ballast line supplies seawater for electrolysis from feeding unit. A blast line (511) of electrolyzer (510) injects the electrolyzed water to main ballast line. An air-blowing pipe (561) which infuses the air for dilute into dilute chamber, is extended from outlet of blower.    USE - Hydrogen gas exhausting structure of electrolyzer unit of vessel equilibrium water processing unit.    ADVANTAGE - The air-blowing pipe which infuses the air for dilute into dilute chamber, is extended from outlet of blower, so that the danger of the explosion is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of hydrogen gas exhausting structure. (Drawing includes non-English language text)    Electrolyzer (510)    Blast line (511)    Hydrogen gas separator (512)    Upper outlet (512a)    Water pump (514)    Dilute chamber (550)    Vent valve (551)    Blower (560)    Air-blowing pipe (561)
NOVELTY - Producing carbon source using biodiesel by-product, comprises (a) introducing air and coagulants on a deoxygenated waste by-product generated from oil purification process of biodiesel raw materials, and performing pressure floatation process to separate particulate matter present in the deoxygenated waste, and (b) mixing the deoxygenated waste with biodiesel waste by-product generated from biodiesel production process to obtain carbon source.    USE - The carbon source is useful as external carbon source for wastewater processing (claimed).    ADVANTAGE - The method is economical and environmentally friendly.
NOVELTY - The system (100) has a pocket cell comprising two plates that are enclosed within housing. One of the two plates comprises a cathode and anode, where electrolytic solution is placed within the cell housing. Electrical leads are electrically coupled to the cathode and the anode. An envelope unit encompasses one of the two plates. An electrolyte storage unit is coupled to the pocket cell through an electrolyte inlet line. A hydrogen collector is coupled to the pocket cell through a hydrogen line. An oxygen collector is coupled to the pocket cell through an oxygen line.    USE - System for making hydrogen and oxygen for an engine e.g. diesel engine, petrol engine and natural gas engine, for electrolysis application.    ADVANTAGE - The system controls rate of electrolysis and amperage and minimizes temperature and degradation in an efficient manner. The system minimizes or eliminates unwanted electrolysis, maximizes efficiency of desired electrolysis and reduces erosion of materials. The system eliminates a need for a separate cooler and all accompanying equipment, thus reducing capital cost and footprint.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for making hydrogen and oxygen gas for an engine for electrolysis application.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of system for making hydrogen and oxygen for an engine for electrolysis application.    System for making hydrogen and oxygen for engine for electrolysis application (100)    Power source (102)    Chamber outlet (105)    Pump (108)    Gas outlet (133)
NOVELTY - The system has an inlet that is provided for solid and liquid reagent addition. The aqueous alkaline waste solution is consumed. The regenerated aqueous alkaline solution comprising reduced amount of dissolved hydroxide ions of metal is produced. A regenerated aqueous alkaline solution free of dissolved hydroxide ions of metal is produced. The metal is aluminum and the dissolved hydroxide ions of metal are aluminate ions.    USE - System for treatment of aqueous alkaline waste solution such as spent electrolyte solution and alkaline electrolyte solution used in metal/air battery or in hydrogen generator for on-board vehicle and off-board vehicle (all claimed) such as electric vehicle and unmanned aerial vehicle (UAV). Can also be used for reserve and emergency power supply and other application.    ADVANTAGE - Since the amount of hydroxide contaminants is reduced, and the desired alkaline compound is reformed, the electrolyte is re-used. Thus, the operation of metal-air batteries is more efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for the treatment of aqueous alkaline waste solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustatring the process for treatment of aqueous alkaline waste solution.    Step for performing electro chemical reaction (11.1)    Step for performing hydrolysis (11.4)    Step for performing co-solvent distillation (11.5)    Step for performing separation (11.6)    Step for performing re-concentration (11.12)
NOVELTY - The method involves cooling a natural gas stream in an ethylene refrigeration cycle (50) to produce a cooled gas stream. The cooled gas stream is cooled in a first chiller of a methane refrigeration cycle (70) and a first core (402) of a second chiller of methane cycle. A refrigerant of a refrigerant recycle stream separate from cooled natural gas stream is cooled in a second core of the second chiller of second refrigeration cycle such that the recycle stream enters second chiller at a second pressure lower than a first pressure of cooled gas stream.    USE - Method for liquefying natural gas stream in liquefied natural gas facility such as cascade-type LNG facility.    ADVANTAGE - The reduction in the feed rate is combined with the increased nitrogen concentration in the feed stream to the nitrogen rejection unit (NRU) which reduces the size and cost of the NRU. The impact of fluctuations in feed gas flow and composition on the NRU operation is lessened thus resulting in improved controllability and operability of the NRD.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for liquefying natural gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of a cascade-type LNG facility.    Chillers (32A,32B,34,35,53,55)    Treatment system (40)    Ethylene refrigeration cycle (50)    Methane refrigeration cycle (70)    Chiller core (402)
NOVELTY - The system (100) has an exhaust system (120) in exhaust gas in communication with an internal combustion engine (110). A turbocharger is provided with a turbine (160) co-rotatably coupled with a compressor (140), where the turbine being in exhaust gas receives communication with the internal combustion engine and exhaust gas providing communication with a methane oxidation catalyst. The compressor being in air is in communication with an air intake, and charges air in communication with the engine, where an exhaust gas recirculation line is positioned upstream of the turbine.    USE - Internal combustion engine system.    ADVANTAGE - The system increases brake thermal efficiency, thus achieving resultant increase in a load carrying ability and power density of the engine by reducing combustion temperatures. The system induces backpressure in a main exhaust line to effectively increase the pressure of the exhaust gas in the main exhaust line, thus creating necessary pressure differential by closing exhaust flow regulating device to allow less exhaust gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an exhaust system for use with a spark-ignited gaseous fuel internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an internal combustion engine system with an exhaust system.    Internal combustion engine system (100)    Internal combustion engine (110)    Exhaust system (120)    Compressor (140)    Turbine (160)
NOVELTY - Production of methane-containing gas mixture involves passing a feed gas mixture (26) through bed of methanation catalyst (30) to react portion of hydrogen with portion of carbon dioxide and form a methane-containing gas mixture containing residual hydrogen (32), adding oxygen-containing gas to methane-containing gas mixture containing residual hydrogen to form feed gas mixture (40), and passing the feed gas mixture (40) through bed of oxidation catalyst to react residual hydrogen and oxygen to form hydrogen depleted methane-containing gas mixture (46).    USE - Production of methane-containing gas mixture (claimed).    ADVANTAGE - The method enables efficient production of methane-containing gas mixture with high yield, and reduced hydrogen concentration in methane-containing gas mixture.    DETAILED DESCRIPTION - Production of methane-containing gas mixture involves passing a feed gas mixture (26) comprising hydrogen and carbon dioxide through a bed of methanation catalyst to react a portion of the hydrogen with portion of the carbon dioxide and form a methane-containing gas mixture containing residual hydrogen, adding an oxygen-containing gas to the methane-containing gas mixture containing residual hydrogen to form feed gas mixture (40), and passing the feed gas mixture (40) through a bed of an oxidation catalyst to react the residual hydrogen and oxygen to form hydrogen depleted methane-containing gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining production of methane-containing gas mixture.    Carbon dioxide-containing gas mixture (10)    Heat exchanger (14)    Hydrogen-containing gas mixture (20)    Feed gas mixture (26,40)    Methanation vessel (28)    Methanation catalyst (30)    Residual hydrogen (32)    Hydrogen depleted methane-containing gas mixture (46)
NOVELTY - The utility model claims a... down feeding the biomass fuel gasification furnace, it from above to below a. divide the head hearth (6), hearth (7) and hearth (7) bottom is equipped with hearth feedstock passage, the upper belt (3), hearth bottom belt (8) and lower belt (9) composed of biomass gasification furnace ignition air inlet device, or ignition air inlet device provided with a channel for a wind belt (27), the outlet fire damper band (1) and hearth bottom belt 8 composed of biomass gasification furnace combustion air inlet device. The utility model a feedstock inlet and flame stable ignition and combustion success.
NOVELTY - The cell (2) has hydrogen electrode chamber (21) that includes electrolyte aqueous solution while supporting hydrogen electrode (22). Oxygen electrode chamber (23) includes electrolyte aqueous solution while supporting oxygen electrode (24). Cell generates hydrogen from chamber (21), and generates oxygen from chamber (23) by electrolyzing electrolyte aqueous solution. Amount of negative charges stored in hydrogen electrode chamber interior at time of hydrogen production is 1 to 2 times the amount of positive charges stored in oxygen electrode chamber interior at time of oxygen generation.    USE - Water electrolysis cell for electrolyzing alkaline electrolyte solution.    ADVANTAGE - The high durability water electrolysis cell is provided with respect to the electric power source with a sharp fluctuation of output electric power such as renewable energy. The water electrolysis cell suppresses deterioration of oxygen electrode, while suppressing decline in the conversion efficiency of power energy even in a case where the fluctuation of output electric power uses the intense electric power source. The oxygen and hydrogen are manufactured stably while reducing the oxygen generation electric potential of oxygen electrode and showing high energy conversion efficiency, even if using the big electric power of fluctuation using natural energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the bipole type element provided with oxygen electrode for alkaline water electrolysis.    Water electrolysis cell (2)    Hydrogen electrode chamber (21)    Hydrogen electrode (22)    Oxygen electrode chamber (23)    Oxygen electrode (24)
NOVELTY - The method involves operating a cooling device i.e. blower (13), such that temperature of a fuel gas generation apparatus (R) is relatively-reduced to stop process completion temperature during a short time cooling control process. Prolonged cooling control process is switched and performed to operate the cooling device such that the temperature of the fuel gas generation apparatus is relatively-reduced to the stop process completion temperature during a long time cooling process, where processing time of the long time cooling process is higher than setting determination period.    USE - Method for operating a fuel cell system.    ADVANTAGE - The method enables switching and performing the prolonged cooling control process to operate the cooling device such that the temperature of the fuel gas generation apparatus is relatively-reduced to the stop process completion temperature during the long time cooling process, where the processing time of the long time cooling process is higher than the setting determination period so as to perform a serial process when stopping operation of the fuel gas generation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system. '(Drawing includes non-English language text)'    Fuel gas generation apparatus (R)    Flow volume detection part (1)    Raw fuel gas supply path (2)    Gas-leakage detection apparatus (3)    Blower (13)
NOVELTY - A fuel cell system comprises fuel-supply path (21) in which fuel circulates, modification part (12) which generates reformed gas which a fuel is introduced from fuel-supply path, reforms fuel using water vapor and contains hydrogen, fuel cell (14) which produces electric power by making oxygen in oxidizing agent gas, and hydrogen in reformed gas from modification part react, branch path (45) which branches from fuel-supply path, and on-off valve (50) which opens and closes branch path.    USE - A fuel cell system.    ADVANTAGE - Durability of fuel cell is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text).    Modification part (12)    Fuel cell (14)    Fuel-supply path (21)    Branch path (45)    On-off valve (50)
NOVELTY - A fuel cell (100) comprises fuel cell main body (2) which contains anode and cathode, desulfurizer (8) for desulfurizing fuel gas, gas flow channel (4) where fuel gas flows, and open valve (10). Fuel cell main body generates electric power by using fuel gas supplied to anode and cathode, respectively, and oxidizing agent gas. Fuel gas flow channel connects desulfurizer to anode. Open valve is connected to fuel gas flow channel. Fuel cell main body is operated by supplying fuel gas to anode through desulfurizer and fuel gas flow channel. Open valve is maintained in closed state.    USE - A fuel cell.    ADVANTAGE - The fuel cell can suppress performance deterioration of desulfurizer during emergency shut down of operation of fuel cell main body.    DETAILED DESCRIPTION - A fuel cell (100) comprises fuel cell main body (2) which contains anode and cathode, desulfurizer (8) for desulfurizing fuel gas, gas flow channel (4) where fuel gas flows, and open valve (10). Fuel cell main body generates electric power by using fuel gas supplied to anode and cathode, respectively, and oxidizing agent gas. Fuel gas flow channel connects desulfurizer to anode. Open valve is connected to fuel gas flow channel. Fuel cell main body is operated by supplying fuel gas to anode through desulfurizer and fuel gas flow channel. Open valve is maintained in closed state. When emergency shut down of operation of fuel cell main body is carried out, open valve is opened. Fluid which flows backward toward desulfurizer through fuel gas flow channel is discharged to exterior of fuel gas flow channel through open valve.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel cell.    Fuel cell main body (2)    Fuel gas flow channel (4)    Desulfurizer (8)    Open valve (10)    Fuel cell (100)
NOVELTY - A raw material processing apparatus comprises container (11) which circulates raw material (F) and accommodates catalyst layer containing catalyst for processing raw material, and boundary component (15) which is provided in container to allow movement in forward/reverse direction (Db) which is a direction through which raw material flows, or its reverse direction, and has raw material passage division part which allows raw material to pass through without allowing solid catalyst to pass through, and guide part (15a) which guides movement of boundary component in forward/reverse direction.    USE - A raw material processing apparatus for fuel cell system (claimed).    ADVANTAGE - The fuel system suppresses the inclination of the catalyst layer with respect to the flow of a raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system comprising desulfurizer (10) which de-sulfurizes raw material, modification part which produces hydrogen-containing fuel gas for reforming raw material desulfurized with desulfurizer, and fuel cell which introduces and electric-power-generates the fuel gas and oxygen-containing oxidizing agent gas in which desulfurizer and/or modification part have raw material processing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional diagram of the desulfurizer.    Desulfurizer (10)    Container (11)    Boundary component (15)    Guide part (15a)    Forward/reverse direction (Db)    Raw material (F)
NOVELTY - This new utility model provide a biomass gasification furnace of contact type sealing feeder, comprising a part provided with entrance, a part provided with the outlet housing, a centre shaft housing is equipped with a at least 10 of circumferential direction evenly distributed blade form a center impeller, impeller center a a a a has impeller, blade and impeller plate centre of the impeller are provided with a housing end wall circle contact of elastic soft contact metal piece, the centre of the impeller is soft elastic contact metal piece and a relative a center impeller in the rotating direction as a micro-bending process, a center impeller and impeller plate and elastic soft contact metal piece rotate to a housing side and a common housing form of a sealed chamber filled with the raw material, each side always has at least three adjacent blade form a number of continuous and sealed chamber. The utility model a sealing feeding machine suitable for feeding the biomass gasification furnace and gasification furnace, it can form complete seal feeding, avoids the air leakage and result in gas explosion in the furnace chamber.
NOVELTY - The device has a power supply unit connected with an upper part of a socket (1). An end of the upper part of the socket is connected with an air cleaner (2). Another end of the upper part of the socket is connected with multiple gas detection machines (3) that are provided with a data processing unit and a feedback control unit. Each gas detection machine is provided with an ozone detecting machine (31) and a methane detecting machine (32). The data processing unit and the feedback control unit are connected with a rubbish room air purification system.    USE - Rubbish room deodorant sterilization control device.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a rubbish room deodorant sterilization control device. '(Drawing includes non-English language text)'    Socket (1)    Air cleaner (2)    Gas detection machines (3)    Ozone detecting machine (31)    Methane detecting machine (32)
NOVELTY - The system has a fuel heater (20) for pre-heating liquefied natural gas in a fuel tank (10). A steam generator (40) heats water supply supplied from a water supply tank and generates steam. A reformer (50) produces hydrogen using the steam of the steam generator. A fuel cell system (60) receives the hydrogen from the reformer and produces electricity using the hydrogen. A battery (63) stores surplus power produced from a polymer electrolyte film fuel cell (PEMFC) (62). A waste heat recovering system (70) is arranged in a molten carbonate fuel cell (61).    USE - Waste heat recovery system for different types of a ship (claimed). Uses include but are not limited to a merchant ship, a carrier, a passenger carrying ship, a transport ship and a marine structure.    ADVANTAGE - The system operates a ship in an environment-friendly manner and effectively utilizes waste heat generated from a molten carbonate fuel cell and a main engine, so that efficiency of the system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a waste heat recovery system.    Fuel tank (10)    Fuel heater (20)    Steam generator (40)    Reformer (50)    Fuel cell system (60)    Molten carbonate fuel cell (61)    PEMFC (62)    Battery (63)    Waste heat recovering system (70)
NOVELTY - A recombinant methanotrophic bacterium comprising one or more exogenous nucleic acids or genes encoding for a first group of enzymes consisting at least one of malate dehydrogenase, pyruvate carboxylase, phosphoenol pyruvate carboxylase, phosphofructokinase, citryl-CoA lyase, isocitrate lyase, fumarate reductase, malate synthase, aspartate transaminase, succinyl CoA synthetase, and pyruvate kinase, is new.    USE - The recombinant methanotrophic bacterium is useful for producing succinic acid from organic waste or biogas or methane (claimed).    ADVANTAGE - The recombinant methanotrophic bacterium efficiently converts organic waste to a useful chemical and thus providing an environmentally-friendly and commercially viable solution for waste management.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process (P1) for producing succinic acid from a carbon source using recombinant methanotrophic bacterium involves receiving at least one carbon source chosen from biogas or methane as input, culturing the bacterium in the input and thus converting the input into succinic acid, and optionally, purifying or separating the succinic acid produced from the culture for obtaining the succinic acid; and    (2) process (P2) for producing succinic acid from organic waste using recombinant methanotrophic bacterium involves receiving organic waste as input, anaerobically digesting the organic waste to biogas, culturing the bacterium in the biogas so generated and thus converting the biogas to the succinic acid, where temperature of 35-50 degrees C, preferably 45 degrees C is maintained throughout the act of converting the input to succinic acid, pH is maintained at 4-7, preferably 5.8 during the act of converting the input to succinic acid, and oxygen concentration of not greater than 20, and optionally, purifying the succinic acid produced from the culture for obtaining the succinic acid.
NOVELTY - Degrading a cellulosic material or xylan-containing material comprises treating cellulosic material or xylan-containing material with an enzyme composition comprising polypeptide having xylanase activity selected from: (a) a polypeptide having at least 95% sequence identity amino acids 20-335 of fully defined 335 amino acids (SEQ ID NO: 4) given in the specification; (b) variant of mature polypeptide of amino acids 20-335 of SEQ ID NO: 4 comprising substitution, deletion, and/or insertion at one or more positions; and (c) fragment of polypeptide of (a) or (b) that has xylanase activity.    USE - The method is useful for degrading cellulosic material or xylan-containing material (claimed); for saccharifying cellulosic material or xylan-containing material to fermentable sugars; and for converting fermentable sugars to useful fermentation products, e.g. fuel, potable ethanol, and/or platform chemicals (e.g. acids, alcohols, ketones, and gases).    ADVANTAGE - Provided are improved cellulolytic and hemicellulolytic enzyme compositions through supplementation with additional enzymes to increase efficiency and to provide cost-effective enzyme solutions for degradation of lignocellulose.
NOVELTY - A transformant produced by introducing, into a host coryneform bacterium, a gene coding for an enzyme having chorismate-pyruvate lyase activity, is new.    USE - The transformant is useful for producing 4-hydroxybenzoic acid or its salt (claimed) which is used as biofuel and chemical substance utilized as a polymer raw material of a liquid crystal.    ADVANTAGE - The transformant produces product efficiently with reduced cytotoxicity when cultured aerobically and in conditions when the transformant does not proliferate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing 4-hydroxybenzoic acid or its salt, which involves culturing the transformant in a culture medium comprising at least one starting compound chosen from saccharides, chorismic acid, and their salts, and recovering product.
NOVELTY - The utility model claims a.... hydrogen production by reforming methanol fuel cell a submarine, a methyl alcohol water hydrogen production by reforming fuel cell power generation system, a methanol water hydrogen production by reforming power generation, which avoids the danger of carrying high pressure hydrogen, carrying turn safety of methanol water, and the same quality condition below, is carrying more and more hydrogen, which solves the existing technology of high pressure hydrogen storage not only dangerous hydrogen storage then no more a problem, mainly in a submarine application area.
NOVELTY - A cleaning agent comprises 10-22 pts. wt. potassium soap, 2-5 pts. wt. triethanolamine oleate soap, 1.5-5 pts. wt. 1,2-propanediol, 3-8 pts. wt. deionized water, 2-5 pts. wt. glucose triacetate, 14-25 pts. wt. fatty alcohol ethoxylate, 30-50 pts. wt. diethylene glycol, 0.2-0.5 pt. wt. brightening agent, 1-4 pts. wt. butane, 5-10 pts. wt. sodium carbonate, 5-10 pts. wt. zeolite, 0.5-1.2 pts. wt. sodium benzoate, 0.02-0.05 pt. wt. lemon flavor and 15-24 pts. wt. clay.    USE - Agent is used for cleaning cotton-based coat collar stain.    ADVANTAGE - The agent has excellent stain-removing effect within short period of time. The clothes cleaned using the agent has suppressed damage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cleaning agent.
NOVELTY - A ternary catalyst comprises ruthenium and platinum which are carried to inorganic oxide carrier which has monoclinic crystal zirconium oxide as main component, and combustion air with respect to fuel generated by combustion of gas adjusted to theoretical air fuel ratio. Ternary catalyst performs reduction removal of nitrogen oxide by making methane into reducing power in ternary-catalyst reaction process of methane containing gas containing carbon monoxide, nitrogen oxide, and methane.    USE - A ternary catalyst used for purification of methane containing gas (claimed).    ADVANTAGE - Methane removal performance is excellent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a purification of methane containing gas which involves making ternary catalyst contact methane containing gas in which methane in methane containing gas is used as reducing power and removing carbon monoxide, nitrogen oxide and methane in methane containing gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the purification performance of the ternary catalyst. (Drawing includes non-English language text).
NOVELTY - The system has a gas source (1) connected with a gas generator (2) through a signal cable wire and a gas pipe. An oil gas detector (6) is connected with the gas generator through an air pipe. An oil generator (4) is connected with a matched oil source (3) through the signal cable wire and an oil tube. A small booster pump (5) is connected with the oil gas detector through an air tube. A temperature sensor is connected with a heater. A microprocessor is connected with a pressure sensor, the temperature sensor and the heater through the signal cable wire.    USE - Gas detection instrument precision dissolution demarcating system.    ADVANTAGE - The system is convenient to maintain, and has high demarcating accuracy, and can reduce detection period and avoid influence of normal operation of a monitoring circuit.    DETAILED DESCRIPTION - The system contains transformer insulation oil that contains hydrogen, carbon monoxide, carbon dioxide, methane gas, acetylene gas, ethylene gas and ethane gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a gas detection instrument precision dissolution demarcating system. '(Drawing includes non-English language text)'    Gas source (1)    Gas generator (2)    Matched oil source (3)    Oil generator (4)    Small booster pump (5)    Oil gas detector (6)
NOVELTY - Method for producing astaxanthin, involves culturing microalga, incubating culture to produce astaxanthin in alga cells, and irradiating the alga cells using combination of blue LEDs having peak wavelength of 420-500 nm and red LEDs having peak wavelength of 620-690 nm.    USE - The method is useful for producing astaxanthin which is useful in cosmetics, health food, and pharmaceutical.    ADVANTAGE - The method produces 100 mg/l or more, preferably 300 mg/l or more astaxanthin which has antioxidant property, and consumes minimal energy.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) culture solution of the microalga, comprising 300 mg/l or more astaxanthin-containing content; and    (2) alga culture comprising 7 wt.% or more astaxanthin-containing content.
NOVELTY - A metal complex has a structure in which terephthalic acid is coordinated to aluminum ion cluster, and has Fd-3m space group.    USE - Metal complex for catalyst and adsorption agent of hydrogen, carbon dioxide, nitrogen, methane and propane.    ADVANTAGE - The metal complex has excellent thermal resistance and high specific surface area.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of metal complex, which involves reacting a raw material mixture containing an aluminum source, terephthalic acid and an aprotic solvent, and setting molar ratio of water with respect to aluminum of raw material mixture to 1 or less.
NOVELTY - This new utility model belongs to biomass energy use area, relating to a forming fuel is a kind of flat-die forming mould. The forming mould present tube, the upper end is a feeding port, lower end is discharging port, a feed port present, the inner diameter of upper to lower is reduced and a forming mould inner wall sliding transition. The utility model is a model forming fuel flat-die forming mould structure is novel, suitable process, production efficiency high, the energy consumption is low, small wear, stable running, suitable for biomass forming fuel flat-die production device use, can generate the good economic and social benefit in a forming fuel production process.
NOVELTY - This new utility model claims of one plant based on solar energy and sea water battery and drive the photoelectric degrading organic pollutant preparing hydrogen and device, the device comprises chamber and degradation and degradation chamber connect is set hydrogen device, top of the degradation room with light transparent window, and the degradation chamber equipped with vertical light catalyze electrode pair, the catalyze electrode pair and light anode on the cathode, and positive electrode is visible light response type, the cathode is hydrogen-producing electrode; the periphery of degradation room equipped with buoyancy plate, also comprises sea water battery, light catalyze electrode through sea water battery for power supply. This utility new type photoelectric catalyze degrading pollutants for preparing hydrogen and electrolytic water hydrogen manufacture two of hydrogen preparing method mutually combined, sea water battery using light to catalyze degradation offshore pollutant and electrolytic water supply stable voltage, the pollutant in degrading sea water and produce hydrogen can, realize to realize high efficient hydrogen production, remove pollute, increase economical efficiency equal multi-target weight.
NOVELTY - Producing combustible gases involve pre-treating lignocellulose containing biomass by heterogeneous photocatalytic degradation under solar radiations. The pre-treated biomass is subjected to co-digestion with manure to obtain combustible gases.    USE - Method for producing combustible gases (claimed).
NOVELTY - A photocatalyst electrode (100) consists of p-type-semiconductor layer (20), a functional layer (30), a n-type-semiconductor layer (40) and a reaction co-catalyst (50) in an order on a collector electrode (10). The functional layer is a semiconductor layer, where the potential (VBMp in eV) of the valence band upper end of the p-type-semiconductor layer with respect to a vacuum level is more than potential (VBMf in eV) of the valence band upper end of the functional layer with respect to a vacuum level.    USE - Photocatalyst electrode is used in photolysis of water during production of hydrogen (claimed).    ADVANTAGE - The photocatalyst electrode has high photoelectric current value and can accelerate water-splitting reaction with high efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of photocatalyst electrode, which involves laminating the p-type-semiconductor layer on the collector electrode, laminating the functional layer on the p-type-semiconductor layer, laminating the n-type-semiconductor layer on the functional layer, and providing the reaction co-catalyst on the n-type-semiconductor layer; and    (2) photolysis of water, which involves immersing the photocatalyst electrode in an aqueous Solution and irradiating light.    DESCRIPTION OF DRAWING(S) - The drawing shows a conceptual view of lamination constitution of the photocatalyst electrode.    Collector electrode (10)    P-type-semiconductor layer (20)    Functional layer (30)    N-type-semiconductor layer (40)    Reaction co-catalyst (50)    Photocatalyst electrode (100)
NOVELTY - The gasifier (100) has a controller (114) adatped to receive a first signal, a second signal and a sensor signal, where the first signal is indicative of rate of fuel-gas extraction, the second signal is indicative of physical parameter of base-fuel and the sensor signal is received from a sensor unit (112). The controller is adapted to generate a thermodynamic indicator based on the first signal and the second signal and monitor the sensor signal and trigger one of a feeder (102), an extractor and an outlet (108) according to the thermodynamic indicator and the sensor signal.    USE - Gasifier for producing fuel-gases from bio-mass and waste substances in cooking and food industries.    ADVANTAGE - The reactor is adapted to cause slowpyrolysis of base-fuel for causing heat exchange among base fuel through convection and produce char with carbon content to enable employing char as coking coal grade fuel and/or as reducing agent in smelting iron ore. The gasifier can employ air as sole gasifying agent in gasification reactions and eliminate requirement of introducing steam into the reactor. The gasifier is inexpensive, and ensures ease and optimal operation, increases operating efficiency and reduces waste resources.    DETAILED DESCRIPTION - The sensor signal is indicative of thermodynamic parameters within a reactor (104). The physical parameter is a parameter corresponding to base-fuel defining quality, content and/or of base-fuel. An INDEPENDENT CLAIM is also included for a method for manufacturing a controller.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gasifier.    Gasifier (100)    Feeder (102)    Outlet (108)    Sensor unit (112)    Controller (114)
NOVELTY - The utility model claims a reboiler of biologic diesel oil rectifying tower, comprising of a heating pipeline, wherein a heating inner pipe each one a. stainless steel silk, the stainless steel silk on a set up of a stainless steel disk. After the utility model is set with steel wire and a round disc, a reducing each. heating pipe in through the material, material heating pipe inner wall along a flow, a material and a full wall contact, ensure heating effect as the traditional boiler is 1.3 time, a stainless steel disk a reducing material through space, a material production 4kg/cm2 pressure in internal heater, thoroughly solving a coking and reboiler;
NOVELTY - The utility model claims a new high efficient environmental protection of biological diesel oil preparing device, comprising: mixing tank, a reaction kettle, the reaction kettle is connected with mixing tank, mixing tank and stirring tank and finished product tank connected with, the stirring tank and finished product tank also equipped with a connection between the pulse mechanism, ultrasonic generator and magnetic tank, a pulse mechanism and a stirring tank connected with, a magnetic tank and finished product tank connected with, said reaction kettle comprises kettle body, stirring device, heating device and cooling forming device, a kettle body provided with a , on installed with stirring device, kettle body external mounting heating device, a side provided with a feedstock, bottom kettle body provided with a discharge port, a kettle body. cooling device. The utility model structure is simple, a suitable installation, suitable range is wide, maintenance cost is low, using life long, which greatly increase a response speed and can effect a biomass gas of a diesel oil, at the same time that of agriculture and forestry waste is a problem, energy saving environmental protection.
NOVELTY - Fuel additive for biodiesel and diesel fuel, comprises: leaf extract as ignition booster, alcohol as oxygenate and citric acid as stabilizer.    USE - Fuel additive for biodiesel and diesel fuel (claimed).    ADVANTAGE - The fuel additive can suppress smoke and improve the combustion properties of biodiesel. The additive will also have an impact on the oxidation stability of the biofuel and its blend with biodiesel.
NOVELTY - The ship has a driving motor connected with a reforming methanol fuel cell power generation system that performs methyl alcohol water hydrogen production operation. The driving motor generates electric energy. The reforming methanol fuel cell power generation system is provided with a methanol water storage tank for performing hydrogen production process, where the methanol water storage tank is connected with a reforming device that is equipped with a fuel cell. A hydrogen purifying device is connected with the fuel cell and a storage battery.    USE - Methyl alcohol water hydrogen production by reforming fuel cell electric motor car ship.    ADVANTAGE - The ship reduces water pressure range and increases product safety and quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methyl alcohol water hydrogen production by reforming fuel cell electric motor car ship.
NOVELTY - The submarine has a methyl alcohol water hydrogen production reforming fuel cell power generation system connected with a driving motor to provide electrical energy. The methyl alcohol water hydrogen production reforming fuel cell power generation system is provided with a methyl alcohol water storage tank, a hydrogen production reforming device and a fuel cell. The methanol water storage tank is connected with the hydrogen production reforming device. The hydrogen production reforming device is connected with the fuel cell.    USE - Water hydrogen production reforming methanol fuel cell electric motor car submarine.    ADVANTAGE - The submarine avoids danger of high pressure hydrogen and improves safety of carrying methanol and water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a water hydrogen production reforming methanol fuel cell electric motor car submarine.
NOVELTY - Tomato compound fertilizer comprises ammonium molybdate, diammonium phosphate, potassium chloride, zinc borate, sulfuric acid, potassium-magnesium fertilizer, manganese sulfate, zinc amino acid chelate, iron amino acid chelate, copper amino acid chelate, molybdenum amino acid chelate, pond sludge, corn cakes, rapeseed cake, kraal manure, borax, peat, attapulgite nanopowder, sand, rock phosphate, naphthalene acetic acid, gibberellin, yeast, and soil bacteria.    USE - Tomato compound fertilizer (claimed).    ADVANTAGE - The tomato compound fertilizer has rich in nutrients and excellent slow release effect, can improve soil, and is environmentally-friendly.    DETAILED DESCRIPTION - Tomato compound fertilizer comprises 10-15 pts. wt. ammonium molybdate, 20-25 pts. wt. diammonium phosphate, 20-30 pts. wt. potassium chloride, 1-4 pts. wt. zinc borate, 5-10 pts. wt. sulfuric acid, 1-2 pts. wt. potassium-magnesium fertilizer, 1-3 pts. wt. manganese sulfate, 1-2 pts. wt. zinc amino acid chelate, 1-3 pts. wt. iron amino acid chelate, 1-4 pts. wt. copper amino acid chelate, 2-3 pts. wt. molybdenum amino acid chelate, 30-40 pts. wt. pond sludge, 15-20 pts. wt. corn cake, 20-25 pts. wt. rapeseed cake, 30-40 pts. wt. kraal manure, 1-2 pts. wt. borax, 10-15 pts. wt. peat, 2-5 pts. wt. attapulgite nanopowder, 2-3 pts. wt. sand, 2-5 pts. wt. rock phosphate, 0.5-0.8 pts. wt. naphthalene acetic acid, 0.05-0.1 pts. wt. gibberellin, 1-2 pts. wt. yeast, and 2-4 pts. wt. soil bacteria.
NOVELTY - The utility model claims a new garbage of a processing device. .. a garbage recycling device, comprising a waste filtering pool, a garbage transport belt, a garbage lifting to the transporting belt travelling crane grab bucket, with tail end provided with a garbage transporting the garbage pulverizer, and a garbage pulverizer is set with discharging port and extrusion molding machine, a discharging end of the extrusion forming machine with fuel block is set with transporting belt, a a fuel block transport belt provided with a temporary storage bin, storage bin discharging port connected with a feeding port, wherein the biomass feedstock and biomass combustion machine is set with spiral feedstock with packing auger, a feedstock material a temporary storage bin and a spiral packing auger and a connected feedstock. The utility model is a model for a process of garbage reasonable technique, a process after the garbage not only can directly carry out combustion application, a surplus of fuel block also can carry out packing converying, as a fuel.
NOVELTY - This new utility model claims one kind of biology diesel oil continuous automatic glycerin soap separator, comprising tube and support leg, the vertical tube fixed in support of, one tube end is equipped with feedstock wherein, upper part and lower part of the other end respectively provided with rough methyl ester and glycerin soap outlet collecting hopper, wherein glycerin soap collecting hopper bottom is equipped with continuous out glycerol, in inner cavity of said tube set with multiple block vertical arranged baffle plate. This utility model new realization of continuous separation, reducing of the manual operation is not controllability, thus separating out the glycerol and the fatty acid methyl ester, content of rough glycerol can reach 80% left and right, then the glycerine and fatty acid methyl ester can control implementation of continuous production in 0.05%, content can control at 0.1%, of convenient rough methyl ester tower, than the same reaction rate of rough fatty acid methyl ester distillation yield is high to 2-3 %, and.
NOVELTY - A kind of high efficiency and is one of groove oil recycling processing device, belonging to food sanitary apparatus technology area, to include collecting processing and collection processing side surface lower edge fixedly connected with the mixing reagent box, wherein said collecting processing box at the top end surface set with upper cover, the upper cover of the top surface centre fixedly connected with motor, the lower cover top surface of internal circle fixedly connected with stirring paddle, and the electric machine and the stirring paddle connected mutually, the lower cover of the top end surface of internal angle to direction of left lower corner fixedly connected with filter screen, collecting the processing internal lower end surface fixedly connected with temperature control heating pipe, a ground groove for primary esterification pre-processing supply oil biological diesel oil production use, accurate quantitative adding castor oil and methanol, vitriol is equal key of the device, at the same time needed to fix temperature heating and constant stirring.
NOVELTY - The utility model claims a... biomass coal heating manufacture device, comprising insulating shell, the insulating shell top equipped with feedstock port and discharge port, a bottom heat preservation shell body set with discharge port and n hot air import, inside the insulating shell equipped with a vertical stirring axis., the stirring shaft from up to below a set with a stirring impeller, between the stirring impeller horizontal arrangement with a clapboard, the clapboard bottom are arranged with a heating tube, the upper clapboard connected with a vibration motor. A current phase comparison device, this utility new type has simple structure, using suitable, low investment cost low, high combustion efficiency, uniform combustion, easy cleaning and not easy to slag.
NOVELTY - This new utility model relates to one of biomass thermal cracking reaction kettle, wherein it comprises: one present and cylindrical kettle body with the semi-spherical bottom, one via flange fixedly connected on cover of the kettle body top part, one is set with the discharge tube in seal upper cover, is set with one centre on heat guide pipe and the internal kettle body, and multiple uniformly arranged the periphery of heat guide pipe on the center heat guide pipe, wherein the upper end of the centre guide heat pipe closed, lower end fixedly connected close in centre of the kettle body bottom, upper end of periphery of the heat guide pipe, lower end fixedly connected at bottom of the kettle body. The utility model can be widely applied in new biomass energy using system.
NOVELTY - The utility model claims a of a kind of a manufacturing device of carbonizing straw biological coal, comprising device shell, a device shell provided with a straw cutting device, a feeding device and carbonizing furnace, at a device shell provided with a straw cutting device is connected a feedstock, a carbonization furnace connected to the discharging port, the straw cutting device is a feedstock, the feeding device for cutting the straw transporting to carbonizing in furnace, the carbide furnace for microwave carbonization, carbonization furnace bottom provided with a tar collecting pipe, carbonization furnace top provided with smoke. And the carbonizing device phase comparison, this utility new type has simple structure, using suitable, suitable for rural popularization use, at the same time in a reducing environment caused by burning of the straw, as people biological carbon as a supply of energy.
NOVELTY - The utility model claims a new biomass straw synthesize a cogeneration plant production line, a carbonizing kiln, primary purification device, a level purification recycling device, a draught fan and gas purification recycling using device, exit the primary purification device through pipeline connected with one level purification recycling device, an air outlet and a purification recovery device by a pipe connected with draught fan, an air outlet connected with combustion gas purification recycling device and a draught fan. The production line is using various raw material mixed with the combustion destructive distillation, carbonizing, change of single use of biomass raw material, expanding a biomass raw material and using range, compared with the traditional of production period, increase of yield and quality, but also can obtain other industrial raw material.
NOVELTY - The utility model claims a biological diesel blending fuel production device, comprises diesel oil tank of biological diesel manufacturing device,additive tank, regulator tank,reaction kettle,material metering table, valve, pipeline and pump,reaction kettle includes premixing finished product tank, tank set with outside reinforcing stirring circulation pipeline between premixing tank and finished product tank, outside the tank strengthening in turn provided with pulse device, ultrasonic generator and stirring circulation pipeline of magnetizer, wherein the magnetizer by flange of metal shell,metal shell two end, the iron core set on metal tube shell, wherein the super-conducting coil winding on iron core and high frequency power supply composed of, ultrasonic generator by electric signal conversion for sound chemistry ultrasonic generator of machine vibration. The structure design is reasonable, use reliability and overcomes biology diesel oil production device for refining the material, the magnetization effect ideal and no problem, reach aim of full stirring material, increase product performance, reducing oil consumption and clean environmental protection.
NOVELTY - The utility model claims a... continuous esterification reactor, a tube, bracket and heating device, a tube fixed on a bracket, bottom part and top of the tube provided with a feedstock and a discharging port, a tube of inner cavity from bottom to top in turn a mixing section as material, heating a material a and material staying reaction section, the heating device is set with a material heating a section of a tube. The utility model is a new type of material can mix in a material for full mixing, then a heating and carrying out reaction at a material heating, then enter into material staying reaction section, at last discharging from a continuous discharging, realize a biological diesel oil production continuous, fat acid reaction rate reach to 98%.
NOVELTY - Method of composting and fermenting basal fertilizer involves (a) weighing manure, (b) adding water and stirring composting formulation, blending the weighed raw materials obtained in step (a) to obtain mixed raw material and adding the composting formulation obtained in step (b) to obtain a mixture and blending the mixture continuously, (d) constructing a cement pit and covering the inner layer with plastic film, filling the cement pit with mixture obtained in step (c) and covering the top layer of the pit with plastic film and discharging the air and (e) fermenting.    USE - The method is useful for composting and fermenting basal fertilizer which is useful for fruit trees (claimed).    ADVANTAGE - The method enables to compost and ferment the basal fertilizer in short period. The basal fertilizer is easily absorbed by roots and lays a solid foundation for the later growth fruit trees and has short fermenting time and conserves nutrition.    DETAILED DESCRIPTION - Method of composting and fermenting basal fertilizer involves (a) weighing manure, loose material and nitrogen preserving materials, (b) taking and mixing composting formulation with water and stirring, (c) blending the weighed raw materials obtained in step (a) using mixer for 5 minutes to obtain mixed raw material and adding the composting formulation obtained in step (b) to obtain a mixture, and continuing to blend the mixture for 10 minutes, (d) construction a cement pit and covering the inner layer of the cement pit with plastic film, filling the cement pit with mixture obtained in step (c), compacting the mixture within the pit and covering the top layer of the pit with plastic film and discharging the air, (e) fermenting the mixture inside the cement pit for 6-10 days at 40-50 degrees C.
NOVELTY - Trichosanthes kirilowii Maxim. special organic-inorganic complex fertilizer comprises 15-17 pts. wt. urea, 13-15 pts. wt. ammonium, 20-22 pts. wt. potassium sulfate, 35-38 pts. wt. biological organic fertilizer, 8-10 pts. wt. humic acid and 5 pts. wt. magnesium-zinc-boron fertilizer.    USE - Used as Trichosanthes kirilowii Maxim. special organic-inorganic complex fertilizer.    ADVANTAGE - The fertilizer has moderate cost, and is suitable for planting Trichosanthes kirilowii Maxim.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing Trichosanthes kirilowii Maxim. special organic-inorganic complex fertilizer comprising (i) taking 70% rape seed pulp, 29.8% edible fungus slag, and 0.2% ferment strain composed fermentation raw material, fermenting, regulating water content to 40%, mixing uniformly and stacking under high temperature of 60-65 degrees C, preparing biologic organic fertilizer, and (ii) using urea, ammonium, potassium sulfate, humic acid, magnesium-zinc-boron fertilizer and prepared biologic organic fertilizer, mixing, stirring uniformly, extrusion granulating to obtain granular complex fertilizer.
NOVELTY - Fertilizer comprises soybean bean pulp, duck manure, urea, ammonium chloride, calcium nitrate, diammonium phosphate, potassium chloride, magnesium sulfate, zinc sulfate, sodium selenate, ammonium molybdate, copper sulfate, zeolite, vermiculite, fly ash, malic acid, tartaric acid, sodium humate, phosphorus solubilizing bacteria, dicyandiamide, N-(n-butyl) thiophosphoric triamide, polyacrylamide, brassinolide and gibberellin.    USE - The fertilizer is useful for increasing yield of drought- and disease- resistant peach (claimed).    ADVANTAGE - The fertilizer has various nutrient components.    DETAILED DESCRIPTION - Fertilizer comprises 30-60 pts. wt. soybean bean pulp, 50-80 pts. wt. duck manure, 25-40 pts. wt. urea, 5-10 pts. wt. ammonium chloride, 2-6 pts. wt. calcium nitrate, 8-15 pts. wt. diammonium phosphate, 20-40 pts. wt. potassium chloride, 4-8 pts. wt. magnesium sulfate, 0.5-1.5 pts. wt. zinc sulfate, 2-5 pts. wt. sodium selenate, 1-3 pts. wt. ammonium molybdate, 1-2.5 pts. wt. copper sulfate, 30-60 pts. wt. zeolite, 10-25 pts. wt. vermiculite, 2-10 pts. wt. fly ash, 2-5 pts. wt. malic acid, 1-5 pts. wt. tartaric acid, 2-5 pts. wt. sodium humate, 1-3.5 pts. wt. phosphorus solubilizing bacteria, 0.3-1 pts. wt. dicyandiamide, 0.1-0.8 pts. wt. N-(n-butyl) thiophosphoric triamide, 4-10 pts. wt. polyacrylamide, 0.1-0.7 pts. wt. brassinolide and 0.3-1.5 pts. wt. gibberellin.
NOVELTY - Manufacture of electrocatalyst involves preparing solution containing metal-ion buffer, nickel precursor and copper precursor, applying an electric potential to the solution and electroplating nickel-copper alloy on a substrate. The electrochemical surface area of nickel in the nickel-copper alloy is 3.8-18 m2/g.    USE - Manufacture of electrocatalyst (claimed) used in alkaline water electrolysis for hydrogen production.    ADVANTAGE - The method provides electrocatalyst with high yield and catalytic activity and excellent durability and stability, by simple and economical process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for controlling electrocatalyst composition by changing electrolysis condition; and    (2) electrocatalyst, which comprises nickel-copper alloy of formula: NixCuy, where x is 16-59 and y is 41-84.
NOVELTY - The utility model claims a new a kind of underwater respiratory device, at least a respiratory cover, upper cover equipped with a respiratory gas pipe and air suction pipe, electrolytic device a for sealing the electrolytic chamber, hydrogen chamber and oxygen chamber, an air outlet pipe and air suction pipe respectively and oxygen chamber via hole, provided with a storage battery and electrolytic rooms, top of electrolytic chamber equipped with a cathode chamber and anode chamber, cathode chamber and hydrogen chamber connection, anode of storage battery and the first conductor connected with the cathode and the second conductor is connected with storage battery, and electrolytic chamber installed with water a mixture of dilute sulfur acid, hydrogen chamber and out electrolytic device through top part of air outlet connection pipeline, an air outlet pipeline provided with waterproof cap, a simple structure, a light weight, and can automatically generate oxygen supply a low in human respiratory water, at the same time when people need to pay water and can help people automatically returns to the water surface, saving of labour and swimming in the floating process of people to prevent of a floating in the air and consume the process caused by the not safe factor.
NOVELTY - This new utility model claims of one of marsh gas septic tank, comprising the first level fermentation tank, and the second level fermentation tank, third level fermentation tank and feedstock pipe. Of the first level fermentation tank equipped with feedstock port and discharge port, lower part equipped with waste material removing port, and the side wall is opened with the first outlet, the second level of fermentation tank provided with an air outlet, lower part equipped with waste material removing port, and the side wall is opened with the second entrance and the second outlet of the third grade of fermentation tank equipped with an exhaust port and a discharge port, lower part equipped with waste material removing port, the upper side wall is provided with the third entrance. Feedstock pipe comprises vertical and connected on vertical pipe upper end is S shape bent, the vertical pipe lower end through feed inlet extends into the internal box of the first level fermentation tank. This new utility model through to feedstock tube, pipeline and discharging port height of reasonable design, using excrement sewage processing Anaerobic fermentation in the following environment of hypoxia, generated biogas, biogas slurry and biogas residue can collect use. At the same time this new utility model small volume, simple structure, easy installation, cleaning, increase of space utilization rate.
NOVELTY - Preparing biodiesel catalyst, comprises (i) crushing egg shells, passing over 160-180 meshes to obtain solid powder; (ii) dissolving sodium silicate powder in deionized water to prepare sodium silicate solution; (iii) according to mass ratio of sodium silicate and egg shell powder of 1.5-4.4, adding sodium silicate solution into the egg shell powder, stirring to obtain suspension; (iv) drying the suspension overnight in a vacuum oven, to obtain solid powder; and (v) calcining the solid powder under nitrogen protection in a muffle furnace to obtain powdery catalyst, and storing in vacuum oven.    USE - The method is useful for preparing biodiesel catalyst (claimed).    ADVANTAGE - The biodiesel catalyst: includes environment-friendly, inexpensive and renewable raw materials; has strong catalytic activity for biodiesel, and has yield of 85%; has better stability; can be used repeatedly 8 times; and achieves fatty acid conversion rate of more than 80%.
NOVELTY - The air cleaner (800) has electrolysis device (200) which separates the water into oxygen and hydrogen. The first and second electrical discharge rooms (300,500) are installed at the movement route of the air. The oxygen plasma in first electrical discharge room is made to react with oxygen gas supplied from electrolysis device, so as burn the fine dust in the air. The hydro plasma in second electrical discharge room is made to react with hydrogen gas supplied from electrolysis device, so as to perform deodorization and sterilization of harmful component in the air.    USE - Air cleaner.    ADVANTAGE - The deodorization and sterilization of the air can be performed efficiently in a rapid manner, so that the bacteria or fine dust contained in the air can be removed reliably without using the filter. Hence, simplification and miniaturization of the air cleaner can be ensured. The deodorization and sterilization speed can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for air conditioning method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the air cleaner. (Drawing includes non-English language text)    Water supply unit (100)    Electrolysis device (200)    Electrical discharge rooms (300,500)    Electric dust collection column (400)    Air cleaner (800)
NOVELTY - Angelica dahurica is crushed and extracted with petroleum ether. The obtained extract is decompressed and concentrated, and mixed with methanol. The obtained extract is filtered and subjected to supercritical fluid chromatographic separation using 18C chromatographic column and methanol modifier as fluid phase. The separated product is detected using a UV detector.    USE - Separation and purification of isoimperatorin or imperatorin from A.dahurica (claimed).    ADVANTAGE - The method is environmentally-friendly, economical and carried out with reduced energy consumption, and does not produce toxic residue. The carbon dioxide used in the process can be recycled efficiently.
NOVELTY - The utility model claims a new biomass energy biogas system, belonging to marsh gas engineering technique area, comprising gas generating system, a marsh gas generating system input end connected with a feedstock, the feedstock pool connected with a straw pre-processing system and fecal sewage pre-processing system, a marsh gas generating system output end in turn connected with one gas storage cabinet, a gas system, one path is in sequence connected with a discharging pool, slag recycling device. The utility model is suitable for a large-scale marsh gas engineering system, can to a biomass can carry out a kind of reasonable use, high conversion rate, high efficiency, a biogas residue and biogas liquid can effective improvement soil, increase crop yield.
NOVELTY - The utility model belongs to the biogas production device field, especially relates to a solar internal heating type biogas device , comprising a marsh gas tank and a solar energy water heater, a marsh gas tank top are each feeding port, one side is set with biogas outlet, biogas tank top feedstock in mounting a feedstock tube, a feedstock tube are connected with feedstock tank, a marsh gas outlet install marsh gas output pipe and marsh gas output pipe are connected marsh gas output pipe, a solar energy water heater water outlet connected with a marsh gas inlet pipe, a marsh gas inlet pipe is set with water pump, water inlet pipe through marsh gas tank is set with tank, a solar energy water heater and water inlet end. The marsh gas generating device a reasonable, connecting is simple, material enter, using the gas and water circulation, a can increase production efficiency, reduce cost and production process.
NOVELTY - The system has a main body bracket fixed at a middle part of a vegetable planting system main body. A dairy manure layer is located on a right side of a main body bracket. A seeding bed is fixed on a left side of the main body bracket. A plastic film layer is fixed on an outer side of the vegetable planting system main body. The main body bracket is provided with a PVC transverse pipe, a first elbow, a tee joint and a three-way valve. A reducing pipe is connected to the first elbow. The transverse pipe is fixed to a second elbow. The three-way valve is connected with a third elbow.    USE - Cow dung fermentation heat pumpkin, muskmelon and watermelon cultivation system.    ADVANTAGE - The system has better heating effect, easy usage, convenient management, low manufacturing cost and high resource utilization rate, and ensures better environmental protection effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cow dung fermentation heat vegetable cultivation system. '(Drawing includes non-English language text)'
NOVELTY - Device comprises raw water regulating tank (2), anaerobic sequencing batch reactor (3), carbon removing sequencing batch reactor (15) and nitrogen removing sequencing batch reactor (21). Anaerobic sequencing batch reactor upper part is provided with an air storage tank. Anaerobic sequencing batch reactor water outlet is connected with middle water tank. The middle water tank and carbon removing sequencing batch reactor are connected to water inlet. Carbon removing sequencing batch reactor and nitrogen removing sequencing batch reactor are connected to pH detecting instrument (9).    USE - Device used for denitrifying high nitrogen organic waste water (claimed).    ADVANTAGE - The device enables to reduce chemical oxygen demand of waste water by 95%, and removes ammonia by 99% and total nitrogen by 95%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of denitrifying device.    Raw water regulating tank (2)    Anaerobic sequencing batch reactor (3)    PH detecting instrument (9)    Carbon removing sequencing batch reactor (15)    Nitrogen removing sequencing batch reactor (21)
NOVELTY - The new type utility claims have one kind animal corpse biology compost process system, comprising tube, tube wall at the tube set with feed inlet, on feed inlet mounted with one used for sealing feedstock wherein the door plate, tube far away from end part of feedstock wherein set with discharging mouth, when discharging mouth mounted to cylinder body with positive rotate limit compost, time for discharging the discharging reversing plate, tube set with multiple used for internal animal body to carry out the cutting blade, tube set on bottom frame on the two transmission roller of upper, one side bottom frame is mounted with drive transmission roller rotate for the power device.
NOVELTY - Method for producing rice seedling matrix involves drying cow dung until moisture reaches 35-45%, grinding dried cow dung, fermenting ground cow dung at 70-80 degrees C for 10-15 days and humidity content of 35-45%, adding 5 wt.% Equisetum ramosissimum and 4 wt.% organic fertilizer to 40% fermented cow dung powder, adding 2% of nitrogen, phosphorus, and potassium to fermented cow dung powder, and adjusting pH of mixture to 4.5-5.5.    USE - The method is useful for producing rice seedling matrix (claimed).    ADVANTAGE - The method improves seedling quality, causes minimal disease and pest attack, replaces soil for seeding, and is cost-effective, and environment-friendly.
NOVELTY - Extracting resveratrol from Polygonum cuspidatum Sieb. et Zucc, comprises (i) drying, and crushing root of Polygonum cuspidatum Sieb. et Zucc into powder form; (ii) adding ethanol to Polygonum cuspidatum Sieb. et Zucc powder, and filtering; (iii) adding ethanol to first extraction liquid, extracting under ultrasonic condition, and filtering, to obtain filter liquor; (iv) mixing the filter liquor twice, and recovering ethanol by distillation; (v) fermenting the extract to remove harmful substances; and (vi) inactivating, and concentrating, to obtain the product.    USE - The method is useful for extracting resveratrol from Polygonum cuspidatum Sieb. et Zucc (claimed).    ADVANTAGE - The method is simple, and easy; shortens the extraction time; has high extraction efficiency up to 3.4959%; does not utilize anhydrous ethanol as solvent while extracting; and utilizes low ethanol concentration.    DETAILED DESCRIPTION - Extracting resveratrol from Polygonum cuspidatum Sieb. et Zucc, comprises (i) drying, and crushing the root of Polygonum cuspidatum Sieb. et Zucc into powder form; (ii) adding 60-80% ethanol into Polygonum cuspidatum Sieb. et Zucc powder, where the solid-liquid ratio is 1:10-1:20, and extracting under ultrasonic condition at 30-50 degrees C for 20-50 minutes, where the ultrasonic wave power is 65-75 Watt (W), and then filtering, to obtain filter liquor; (iii) adding 60-80% ethanol to first extraction liquid, where the solid-liquid ratio is 1:10-1:20, and again extracting under ultrasonic condition, at 30-50 degrees C for 20-50 minutes, where the ultrasonic wave power is 65-75 W, and then filtering, to obtain filter liquor; (iv) mixing the filter liquor twice, and recovering ethanol by distillation; (v) fermenting the extract to remove harmful substances; and (vi) inactivating, and concentrating, to obtain the product.
NOVELTY - Automatic broken shell biogas digester comprises multiple plenum chambers and multiple septic chambers disposed in the lower side of plenum chamber. The bottom part of septic chamber is a bucket-shaped structure. The septic chamber is set with a feed port. The lower side-side wall of the septic chamber is provided with a finished product slag outlet, set with valves. The plenum chamber is set with a discharge port. The upper part of plenum chamber is set with a biogas outlet. An isolated diaphragm body is set between the plenum chamber and septic chamber through crust for curing feed solution.    USE - Used as an automatic broken shell biogas digester.    ADVANTAGE - The digester is economical, achieves automatic feed solution crust fermentation process, has high fermentation efficiency, prevents secondary pollution and suitable for large-scale industrialization.    DETAILED DESCRIPTION - Automatic broken shell biogas digester comprises multiple plenum chambers and multiple septic chambers disposed in the lower side of plenum chamber. The bottom part of septic chamber is a bucket-shaped structure. The septic chamber is set with a feed port. The lower side-side wall of the septic chamber is provided with a finished product slag outlet, set with valves. The plenum chamber is set with a discharge port. The upper part of plenum chamber is provided with a biogas outlet. An isolated diaphragm body is set between the plenum chamber and septic chamber through crust for curing feed solution. The diaphragm body is set with discharge port in obliquely upward direction. A ventilation channel is set between diaphragm body and digester.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the automatic broken shell biogas digester.
NOVELTY - Treating starch waste water involves taking starch waste water and then regulating pH value of starch waste water. Starch waste water is added into reactor and then sealed it. Hydrogen gas is produced in sealed reactor and microalgae are added into starch waste water to obtain mixture. The mixture is stirred and then cultured it.    USE - Method for treating starch waste water (claimed). The method enables to treat starch waste water with increased efficiency of 170%.    ADVANTAGE - The method enables to treat starch waste water with efficiency by 170%.
NOVELTY - A room temperature methane sensor comprises a quartz crystal microbalance electrode in which surface is covered with noble metal/cerium oxide/ mesoporous silicon composite material with thickness of 1415-5400 ng composites, where the composite material is mesoporous silica as a carrier loaded with precious metals and oxidation cerium complex, and mass ratio of the noble metal oxide and mesoporous silicon oxidation is 0.053: 0.949: (1-10).    USE - Room temperature methane sensor for detecting natural gas, shale gas, biogas and methane gas.    ADVANTAGE - The sensor detects methane with excellent selectivity and high sensitivity, and can be prepared in simple and cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing room temperature methane sensor.
NOVELTY - A composite type flush-free water processing system comprises first water pump (1) and second water pump (2) used for pumping and draining, timing automatic switch (3) used for switching the first water pump (1) and the second water pump (2) working state, sealing chamber (4) set with filter material fungus bed for aerobic fungus attachment, and pump (5) used for taking external air pressing into internal sealing chamber.    USE - Composite type flush-free water processing system used for aquarium, ecological fish tank, aquatic product cultivation and landscape water body.    ADVANTAGE - The system eliminates pollution and impurity by filtering and decomposing, does not use disinfectant additive to purify, circulates water obtain from filtration and purification, and saves labor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage treatment using composite type flush-free water processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of composite type flush-free water processing system.    First water pump (1)    Second water pump (2)    Timing automatic switch (3)    Sealing chamber (4)    Pump (5)
NOVELTY - Microbial electrolysis cell with anaerobic/aerobic coupling device comprises anode chamber (1), cathode chamber (2), precipitation tank (3), anode chamber inlet (4), sludge port (5), fender (6), anode chamber outlet (7), exhaust port (8), electrode socket (9), gas collecting device (10), cathode chamber inlet (11), air pump (14), aeration head (15), power supply (17), sedimentation tank sludge outlet (19) and sludge pump (24). The fender (6) is provided with anode chamber side wall outlet (7), anode chamber exhaust port (8) and electrode socket (9).    USE - Microbial electrolysis cell with anaerobic/aerobic coupling device used for treating dye-containing wastewater.    ADVANTAGE - The microbial electrolysis cell with anaerobic/aerobic coupling device is inexpensive and has stable operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of microbial electrolysis cell with anaerobic/aerobic coupling device.    Anode chamber (1)    Cathode chamber (2)    Precipitation tank (3)    Anode chamber inlet (4)    Sludge port (5)    Fender (6)    Anode chamber outlet (7)    Exhaust port (8)    Electrode socket (9)    Gas collecting device (10)    Cathode chamber inlet (11)    Air pump (14)    Aeration head (15)    Power supply (17)    Sedimentation tank sludge outlet (19)    Sludge pump (24)
NOVELTY - Culture soil composition comprises peat moss, wood residue, pine sawdust, arrowroot pulverized powder, zeolite, effective microorganism, pH adjusting agent, cation exchange capacity enhancer, and microelement fertilizer, where the pine sawdust and arrowroot pulverized powder are mixed together, and dry mass rate of the arrowroot pulverized powder is 30-60%.    USE - The culture soil composition is useful for cultivation of crops (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) jiffy pots comprising the culture soil composition;    (2) green wall unit comprising the culture soil composition;    (3) pellet type or powdery organic fertilizer comprising the culture soil composition;    (4) fuel pellets comprising the culture soil composition;    (5) method for preparing the jiffy pots, involves growing crop culture soil composition using timber-product, and multiplying the crop material; and    (6) cultivation method of the seed using the culture soil composition, involves preparing mixture of natural soil and culture soil, culturing seed with the mixture, and growing crops.
NOVELTY - The new type utility claims have one kind using the excrement sewage of urbanization manure pool in organic fertilizer and device, belonging to organic fertilizer in device technology field, the technology point comprises manure, comprising manure side edge provided with the quantitative stirring bucket, provided with stirrer inside at quantitative stirring bucket, provided with complement hopper quantitative stirring bucket on the top of complement hopper connected with auxiliary material transport belt, auxiliary material transport belt connected with auxiliary material transport motor, provided with orderly connected with the transport groove and transmission belt at the lower part complement hopper, provided with mutually connected with the spiral stirring machine and spiral transport mechanism in transport in groove, spiral stirring position for transport groove and close to the stirring bucket one side inside, the stirring bucket and a discharging mouth and complement hopper are the transport slot close to the stirring bucket one end near end part, the utility model is new type aims to provide one kind structure is reasonable, operation is simple and using effect is good and the excrement sewage and use urbanization manure pool in organic fertilizer and device, used for manufacture of organic fertilizer.
NOVELTY - A one inclined bottom air inlet type aerobic fermentation reactor, fermentation tank with circular inner tank, end cover and sleeve, inner tank and two end cover composed of space is one of closeness fermentation, upper part of fermentation tank provided with feedstock mouth and discharge mouth, the lower part of fermentation tank lower end cover set with discharging mouth, length of fermentation tank more than or equal to diameter, fermentation tank at fixed in one with height difference of the substrate is inclined state, in fermentation tank mounted have one of several group of tangential plate or tangential spiral composite plate, radial pole, stirring and stirring shaft connected with one pole and can saving type stirrer, fermentation tank and inner tank bottom is provided with multiple group outside air room, air room is set inside jacket, air room side in the inner tank is provided with multiple aeration nozzle, the utility model is new type square meter floor space small, low power consumption, high efficiency, fermentation reactor inner wall no scale formation, easy discharging, no second time pollute, water-containing rate low, organic waste is harmless and recycling treatment and environmental protection effect is good.
NOVELTY - The utility model is new type supply have one kind indoor Anaerobic aerobic compost bucket, comprising bucket main body and fertilizer bucket cover, wherein the bucket cover comprises outer cover, bottom of the outer cover set with outer cover and fixedly connected with the insect, part of the outer cover is set with outer cover and moving connected with the inner cover. The utility model is new type of indoor Anaerobic aerobic compost bucket, for Anaerobic aerobic combined, wherein the aerobic fermentation time can prevent insects entering into, which greatly shortens have fermentation time.
NOVELTY - The utility model is new type supply one kind organic material heating transport device, comprising heating device and transport device, transport device and heating device and semi seal producing hot air through pipe connected with the heating device generating the heat transport to transport device internal sum, using the material in transport device in heating process in the converying; another end transport device comprises bottom is connected with pipe-shaped groove the riser device is connected input convey device of pipe-shaped level is set, the lower part of conveying device convey several fermentation groove set with heating device comprises hot air furnace, a hot air furnace connected with pressurizing device, check valve through the hot air into the hot air bag, hot bag by several pipeline connection equipped with several vent hole on the output device and lifting up and convey. The utility model is new type can realize heating and conveying to the organic material convey in winter season, effective solves have fermentation process is difficult to process the problem, the whole structure is simple and reasonable, the material pre-heating and in process of spiral converying heated uniformly and heat transfer efficiency high.
NOVELTY - Apparatus comprises a mixing unit (110) for mixing and discharging livestock manure with moisture controlling agent, located on ground, a transferring unit (120) for transferring the discharged manure mixture upwardly, a fermenting unit (130) for fermenting the manure mixture at upper part, and discharging into the lower part, an aging unit (140) for aging the fermented manure mixture, and discharging the obtained compost to lower part, an extracting unit (150) for extracting the aged compost, disposed on lower side of the aging unit, and located on ground, and an exhaust unit to exhaust gas.    USE - The apparatus is useful for processing livestock manure (claimed).    ADVANTAGE - The apparatus prevents soil and ground water contamination, and is convenient to operate.    DETAILED DESCRIPTION - Apparatus comprises a mixing unit (110) for mixing and discharging livestock manure with moisture controlling agent, located on ground, a transferring unit (120) for transferring the discharged manure mixture upwardly, a fermenting unit (130) for fermenting the manure mixture at upper part, and discharging into the lower part, an aging unit (140) for aging the fermented manure mixture, and discharging the obtained compost to lower part, an extracting unit (150) for extracting the aged compost, disposed on lower side of the aging unit, and located on the ground, an exhaust unit for exhausting gas generated from the aging unit and the fermenting unit, and a purifying unit for purifying the exhausted gas with deodorizer and dust collector.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the apparatus for processing livestock manure.    Mixing unit (110)    Transferring unit (120)    Fermenting unit (130)    Aging unit (140)    Extracting unit (150)
NOVELTY - A plant for processing domestic garbage in severe cold region and aerobic compost reactor, relating to one kind aerobic compost reactor. The utility model is new type to solve the compost reactor heating and heat preservation effect is good, no ventilating oxygen supply not be uniform, resulting in domestic garbage compost finished product rate not high, processing amount is small and the problem. The utility model is new type of motor and cylindrical reactor tank body are mounted on rotating bracket on the reactor temperature control box and cylindrical reactor tank body connected with the shaft in an axial direction is set in the columnar reactor tank body, outside shaft is sleeved in shaft on the motor and shaft connected with outside, said inner shaft and outside shaft are set on the whole multi-small hole, two more annular agitator blade mounted at outside shaft on the air compressor through gas flow meter and in shaft connection, two block plate electrode mounted on at two end surface of columnar reactor tank body and the insulating layer mounted on at two end face of column-shaped reactor tank body and outside wall. The utility model is new type used for treatment in northern cold area domestic garbage.
NOVELTY - The new type utility claims have one plant fruit and vegetable organic garbage disposer, comprising in turn connected with the feedstock unit, pre processing unit, transport unit, fermentation unit, a discharging unit, pre processing unit adopt vertical structure comprises the spiral transport tube, smashing unit, extrusion unit, fermentation unit comprises fermentation bin, wherein the fermentation chamber to feedstock provided with microbial inoculum, under part of fermentation chamber set with heating device inside the fermentation chamber provided with sensor, fan, spray device, stirring device, outside wall of the fermentation chamber provided with insulating layer, the discharging unit comprises incline plate channel, fermentation cabin lower part is discharging mouth and incline plate channel connected with the lower part of incline plate channel set with packaging bag. Structure is simple, integrated degree high, can realize and produce the garbage source treatment.
NOVELTY - The new type utility claims have one turn A polishing wheel, comprising wheel disc and mounted on wheel disc on the multiple polishing cutter turn plate and . Using said structure of the utility model is new type through at the same time turn polishing cutter plate and equipped with blade can realize to organic fertilizer for the efficient, than single equipped with blade effect is better.
NOVELTY - Fertilizer composition comprises 15-19 pts. wt. buffalo milk, 12-13 pts. wt. leech, 20-22 pts. wt. coriander, 15-22 pts. wt. scorpion, 10-12 pts. wt. Salvia seed, 1 pt. wt. pectin lyase, 1 pt. wt. pectinesterase, 1 pt. wt. aspartic protease, and 1 pt. wt. cellulase.    USE - As fertilizer composition for Indian strawberry (claimed).    ADVANTAGE - The fertilizer composition increases yield of Indian strawberry, is cost-effective, and prevents soil salinization.
NOVELTY - Energy-saving biomass gasification furnace comprises a support and a furnace mounted on the support. The bottom part of the furnace is installed with an ash tray. The top part of the ash tray extends into a blast system at the bottom part. The top end of the furnace is provided with an air outlet. The side wall of the top end of the furnace body is provided with a discharge end which extends into an extrusion granulating device inside the furnace body. The furnace side portion is provided with feeding device to supply feed into the granulating device.    USE - Used as energy-saving biomass gasification furnace.    ADVANTAGE - The biomass gasification furnace: utilizes the extrusion granulating device for generating heat by material extrusion and enhances the temperature of the material; completely utilizes the heat generated by granulation process; utilizes the heat carried by the combustible gas to continuously heat the material; utilizes waste heat; enhances the gasification initial temperature of the material block and greatly enhances the gasification efficiency; adopts the sealed combination of the extrusion granulator and furnace body for implementing no-leakage continuous feeding process and ensuring the production safety.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the energy-saving biomass gasification furnace.
NOVELTY - The application of methyl jasmonate for improving quality of microalgae biodiesel, is claimed.    USE - Application of methyl jasmonate for improving quality of microalgae biodiesel (claimed).    ADVANTAGE - The method provides biodiesel with high cetane number and quality.
NOVELTY - Replacing petroleum diesel oil with biodiesel oil involves utilizing 50-75 wt.% biodiesel oil, 10-20 wt.% petroleum diesel oil, 10-30 wt.% base oil and 1-10 wt.% additive, where the additive comprises 10 wt.% nitric acid ethyl ester, 60 wt.% ethylhexyl nitrate, 30 wt.% isoamyl nitrate and 2 wt.% blending liquid, 1.5 wt.% ethylene acrylic acid, 1 wt.% 2,6-di-tert-butyl-p-cresol, 0.5 wt.% alkyl amine phosphate, 1.5 wt.% turkey oil, 1.5 wt.% mixed liquid of petroleum sulfonate, alkyl phenate and salicylate and 1 wt.% heavy oil.    USE - Method for replacing petroleum diesel oil with biodiesel oil (claimed).    ADVANTAGE - The method enables to replace petroleum diesel oil in simple, environmental-friendly and stable manner, and with biodiesel oil with high oil replacement rate and good power performance, and has reduced carbon dioxide emissions to prevent global warming, and prevented suffocation of petroleum aromatic hydrocarbons to produced highly carcinogenic pollution, bronchitis and allergic diseases of the human.    DETAILED DESCRIPTION - Replacing petroleum diesel oil with biodiesel oil involves utilizing 50-75 wt.% biodiesel oil, 10-20 wt.% petroleum diesel oil, 10-30 wt.% base oil and 1-10 wt.% additive, where the additive comprises 10 wt.% nitric acid ethyl ester, 60 wt.% ethylhexyl nitrate, 30 wt.% isoamyl nitrate and 2 wt.% blending liquid, 1.5 wt.% ethylene acrylic acid, 1 wt.% 2,6-di-tert-butyl-p-cresol, 0.5 wt.% alkyl amine phosphate, 1.5 wt.% turkey oil, 1.5 wt.% mixed liquid of petroleum sulfonate, alkyl phenate and salicylate, 1 wt.% heavy oil, 1 wt.% mixture of ethylene glycol diethyl ether, ethylene glycol monomethyl ether and isopropyl alcohol, and 1-10 wt.% mixed liquid additive.
NOVELTY - Improving biodiesel oil yield involves taking lipid and 1-6C monohydric alcohol mixture as raw material and then reacting the selected material with organic accelerator and solvent at 140-350 degrees C temperature and 1-12 megapascal pressure. The fatty acid monoester is collected, where the organic accelerator is selected from phospholipid, phosphate, 1-6C organic acid or alkyl ammonium hydroxide, and the weight ratio of lipid and organic accelerator is 1:0.0001-0.1.    USE - Method for improving biodiesel oil yield (claimed).    ADVANTAGE - The method enables to improve biodiesel oil yield without the addition of other inorganic acid catalyst.
NOVELTY - Fermented organic fertilizer comprises straw (1000-1500 pts. wt.), chicken manure (1000-1300 pts. wt.), cow dung (1000-1500 pts. wt.), pig manure (800-1200 pts. wt.), soybean meal (1200-1800 pts. wt.), microbial agents (35-50 pts. wt.), humic acid (10-20 pts. wt.), corn flour (50-80 pts. wt.), enzyme complex (60-90 pts. wt.), and microbial composite (30-60 pts. wt.).    USE - Fermented organic fertilizer.    ADVANTAGE - The fermented organic fertilizer is cost-effective and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fermented organic fertilizer, which involves:    (A) crushing straw and soybean and mixing them with chicken manure, cow dung, pig manure, humic acid, and enzyme complex to obtain a mixture;    (B) adding water to obtained mixture to obtain a product of water content 55-78%;    (C) fermenting the obtained product for 5-10 days;    (D) mixing corn flour, microbial composite, and water to obtain a product of concentration 85-95%;    (E) mixing obtained products to obtain an another mixture, and adding water to obtained product to adjust water content to 60-80%; and    (F) fermenting the obtained product for 7-14 days to obtain final product.
NOVELTY - Vertical multi-layered aerobic biological composting device comprises vertical cylinder (1) set with top cover (2). The top cover is set with hopper (3). The vertical cylinder is set with the multiple separator board (4) that is set with discharging door at the upper vertical cylinder. The upper vertical cylinder is set with sealing cover and outer end part of rotary shaft (6) that is set with driving motor (7), stirrer (8) and multiple layers of blast pipe (9) and air pipe (10).    USE - Vertical multi-layered aerobic biological composting device.    ADVANTAGE - The vertical multi-layered aerobic biological composting device reduces organic solid waste, ensures low space requirement and reduced municipal environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a vertical multi-layered aerobic biological composting device.    Vertical cylinder (1)    Top cover (2)    Hopper (3)    Multiple separator board (4)    Rotary shaft (6)    Driving motor (7)    Stirrer (8)    Blast pipe (9)    Air pipe (10)
NOVELTY - Preparing fertilizer involves mixing cow dung (25-30 pts. wt.) with water (70-75 pts. wt.) to obtain precipitate in a sewage mixing device. Fiber pulp is prepared by mixing coarse fiber (80-90 pts. wt.), ammonium sulfate (8-9 pts. wt.), and ferrous sulfate (2-3 pts. wt.) to obtain a mixture. Obtained mixture is steamed at 6 megapascals for 8-10 hours, and steamed product is filtered to obtain filtrate. Purifying agent is added to obtained precipitate slurry (2/10000 wt.%) to obtain purified product. Purified product (80 pts. wt.) is mixed with obtained filtrate (30 pts. wt.).    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method is simple and enables to utilize waste.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing cow dung (25-30 pts. wt.) with water (70-75 pts. wt.) to obtain precipitate in a sewage mixing device. Fiber pulp is prepared by mixing coarse fiber (80-90 pts. wt.), ammonium sulfate (8-9 pts. wt.), and ferrous sulfate (2-3 pts. wt.) to obtain a mixture. Obtained mixture is steamed at 6 megapascals for 8-10 hours, and steamed product is filtered to obtain filtrate. Purifying agent is added to obtained precipitate slurry (2/10000 wt.%) to obtain purified product. Purified product (80 pts. wt.) is mixed with obtained filtrate (30 pts. wt.), monoammonium phosphate (2-3 pts. wt.), ammonium sulfate (2 pts. wt.), and urea (1 pts. wt.) to obtain a mixture, which is granulated to obtain organic fertilizer.
NOVELTY - Preparing culture medium involves mixing mulberry branch with water. Composite enzyme is added in the mixture and stirred uniformly to carry out fermentation and enzymolysis at room temperature. Obtained mulberry is mixed with cotton seed hull, cassava alcohol residue, wheat bran, lime, gypsum and calcium phosphate.    USE - Method for preparing culture medium for edible fungus (claimed).    ADVANTAGE - The method enables to prepare improved quality culture medium with quick growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for cultivating edible fungus, which involves:    (A) mixing nutrient liquid with culture medium and wrapping in a plastic bag, and then sterilizing; and    (B) placing edible fungus in the mixture and cultivating at 30 degrees C and regulating pH.
NOVELTY - Preparing cultivation material involves taking sawdust (36-40%), bagasse (42-46%), soybean (10-12%), fungus (3-4%), lime (2.5%), and calcium carbonate (1%), where particle size of sawdust is 3-5mm, and baggase is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Piled material is fermented at 60 degrees C. Obtained material is mixed with calcium carbonate.    USE - Method for preparing cultivation material Hypsizygus marmoreus (claimed).    ADVANTAGE - The method is eco-friendly.    DETAILED DESCRIPTION - Preparing cultivation material involves taking sawdust (36-40%), bagasse (42-46%), soybean (10-12%), fungus (3-4%), lime (2.5%), and calcium carbonate (1%), where particle size of sawdust is 3-5mm, and baggase is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with calcium carbonate, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is maintained to 63%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (60-64%), wood powder (18-22%), soybean (10-12%), mushroom (3-4%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, cotton seed hull and bean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented.    USE - Method for preparing cultivation material used for Pleurotus nebrodensis (claimed).    ADVANTAGE - The method is eco-friendly, and ensures increased catalytic decomposition and growth of Pleurotus nebrodensis.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (60-64%), wood powder (18-22%), soybean (10-12%), mushroom (3-4%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, cotton seed hull and bean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum is added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 26-28 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing corn cob (46-50%), wood powder (28-32%), soybean (12-14%), mushroom (3-4%), lime (4-5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn cob and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours.    USE - Method for preparing cultivation material used for Pleurotus nebrodensis (claimed).    ADVANTAGE - The method is eco-friendly, and ensures increased catalytic decomposition and growth of Pleurotus nebrodensis.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing corn cob (46-50%), wood powder (28-32%), soybean (12-14%), mushroom (3-4%), lime (4-5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum is added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 28-30 days to obtain the final product.
NOVELTY - Preparing cultivation material involves crushing 58-62% sawdust, 18-22% bagasse, 12-14% bean cake, 3-4% mushroom, 2.5% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room.    USE - Method for preparing cultivation material used for Auricularia polytricha (claimed).    ADVANTAGE - The method is eco-friendly and saves labor cost, and enables to prepare cultivation material that produce highly active metabolite product of Auricularia polytricha, and ensures its rapid growth.    DETAILED DESCRIPTION - Preparing cultivation material involves crushing 58-62% sawdust, 18-22% bagasse, 12-14% bean cake, 3-4% mushroom, 2.5% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room and cultured at 18-20 degrees C for 36-38 days.
NOVELTY - Preparing cultivation material involves pulverizing wood powder (58-62%), bagasse (10-14%), soybean (18-20 pts. wt.), mushroom (3-4%), lime (4-5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, bagasse and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours.    USE - Method for preparing cultivation material used for mushroom (claimed).    ADVANTAGE - The method is eco-friendly, and saves labor, and ensures increased catalytic decomposition.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (58-62%), bagasse (10-14%), soybean (18-20 pts. wt.), mushroom (3-4%), lime (4-5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn cob and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum and lime are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polyethylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 38-40 days to obtain the final product.
NOVELTY - Preparing cultivation material involves crushing and drying 54-58% sawdust, 18-24% cottonseed hull, 14-16% bean cake, 4-5% mushroom, 2-3% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag.    USE - Method for preparing cultivation material used for black fungus (claimed).    ADVANTAGE - The method is eco-friendly and saves labor cost, and enables to prepare cultivation material that produce highly active metabolite product of black fungus, and ensures its rapid growth.    DETAILED DESCRIPTION - Preparing cultivation material involves crushing and drying 54-58% sawdust, 18-24% cottonseed hull, 14-16% bean cake, 4-5% mushroom, 2-3% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene cylindrical bag, and inoculated in dark cultivating bacterium room and cultured at 18-20 degrees C for 36-38 days.
NOVELTY - Preparing cultivation material involves taking sawdust (60-64%), bagasse (8-12%), soybean (18-20%), fungus (4-5%), lime (3-4%), and gypsum (1%), where particle size of sawdust and baggase is 3-5mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-2m and diameter of 2-3mm. Vertical hole is created on upper stack of pile by stick. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum to obtain a mixture.    USE - Method for preparing cultivation material used for cultivating black fungus (claimed).    ADVANTAGE - The method is eco-friendly.    DETAILED DESCRIPTION - Preparing cultivation material involves taking sawdust (60-64%), bagasse (8-12%), soybean (18-20%), fungus (4-5%), lime (3-4%), and gypsum (1%), where particle size of sawdust and baggase is 3-5mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-2m and diameter of 2-3mm. Vertical hole is created on upper stack of pile by stick. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is maintained to 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing wood powder (50-54%), cotton seed hull (14-16%), soybean (14-16%), mushroom (4-5%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented.    USE - Method for preparing cultivation material used for mushroom (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (50-54%), cotton seed hull (14-16%), soybean (14-16%), mushroom (4-5%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum and lime are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polyethylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 36-38 days to obtain the final product.
NOVELTY - Preparing cultivation material involves taking cottonseed hull (50-54%), bagasse (12-14%), soybean meal (12-14%), mushroom (3-4%), lime (2-3%), and gypsum (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C. Obtained material is mixed with gypsum to obtain a mixture.    USE - Method for preparing cultivation material used for Ganoderma lucidum (claimed).    ADVANTAGE - The method is eco-friendly.    DETAILED DESCRIPTION - Preparing cultivation material involves taking cottonseed hull (50-54%), bagasse (12-14%), soybean meal (12-14%), mushroom (3-4%), lime (2-3%), and gypsum (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing wood powder (52-58%), corn cob (20-24%), soybean (14-16%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented.    USE - Method for preparing cultivation material used for Ganoderma lucidum (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of Ganoderma lucidum.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (52-58%), corn cob (20-24%), soybean (14-16%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum and lime are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 24-26 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing wood powder (58-64%), bagasse (12-16%), soybean (16-18%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C.    USE - Method for preparing cultivation material used for Ganoderma lucidum (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood powder (58-64%), bagasse (12-16%), soybean (16-18%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then wood powder, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum and lime are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 24-26 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (38-42%), corn cob (34-40%), soybean (14-16%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented.    USE - Method for preparing cultivation material used for abalone mushroom (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of abalone mushroom.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (38-42%), corn cob (34-40%), soybean (14-16%), mushroom (3-4%), lime (3-4%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, corn powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum and lime are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (42-48%), wood powder (28-34%), soybean (16-18%), mushroom (3-4%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, wood powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and fermented.    USE - Method for preparing cultivation material used for abalone mushroom (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of abalone mushroom.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (42-48%), wood powder (28-34%), soybean (16-18%), mushroom (3-4%), lime (2-3%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, wood powder and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Gypsum and lime are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Preparing cultivation material involves taking cottonseed hull (48-52%), bagasse (20-26%), soybean meal (18-20%), mushroom (3-4%), lime (3-4%), and gypsum (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days.    USE - Method for preparing cultivation material used for cultivating Pleurotus eryngii (claimed).    ADVANTAGE - The method is eco-friendly.    DETAILED DESCRIPTION - Preparing cultivation material involves taking cottonseed hull (48-52%), bagasse (20-26%), soybean meal (18-20%), mushroom (3-4%), lime (3-4%), and gypsum (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, bagasse, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 20-22 days to obtain the final product.
NOVELTY - Preparing cultivation material involves taking corn cob (48-52%), bagasse (26-30%), soybean meal (18-20%), mushroom (3-4%), lime (3-4%), and calcium carbonate (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then corn cob, bagasse, soybean meal, mushroom, and lime are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented.    USE - Method for preparing cultivation material used for cultivating Flammulina velutipes (claimed).    ADVANTAGE - The method is eco-friendly, and enables to prepare cultivation material, which ensures improved Flammulina velutipes growth.    DETAILED DESCRIPTION - Preparing cultivation material involves taking corn cob (48-52%), bagasse (26-30%), soybean meal (18-20%), mushroom (3-4%), lime (3-4%), and calcium carbonate (1%), where particle size of bagasse is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then corn cob, bagasse, soybean meal, mushroom, and lime are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Matrix comprises 40-60 pts. wt. soil, 5-10 pts. wt. traditional Chinese medicine slag, 4-8 pts. wt. grass ash, 3-5 pts. wt. wooden meal, 4-6 pts. wt. fermented vegetable liquid, 5-10 pts. wt. fish bone meal, 6-10 pts. wt. bamboo coal powder, 3-9 pts. wt. silt sludge, 5-10 pts. wt. Sorghum shell powder and 4-9 pts. wt. shrimp powder.    USE - Matrix used in Jiangsu-Zhejiang region.    ADVANTAGE - The matrix ensures is economic and environment-friendly, and ensures comprehensive nutrition.
NOVELTY - Preparation of ticagrelor intermediate (i) involves taking N,N-diethylaniline hydrochloride in organic solvent A solution, adding reductant in organic solvent B solution dropwise, insulating at 0-50 degrees C for 4-20 hours, adding (S)-diphenyl prolinol in organic solvent A solution and 2-chloro-1-(3,4-difluorophenyl)ethanone in organic solvent A solution, performing reduction to obtain (S)-2-chloro-1-(3,4-difluorophenyl)ethanol, adding triethyl phosphonoacetate, organic solvent C and alkali, performing ring-closure reaction to obtain ethyl 2-phenylcyclopropanecarboxylate derivative (ii) and washing.    USE - Method for preparing ticagrelor intermediate.    ADVANTAGE - The method has inexpensive, environment-friendly, non-toxic and recyclable reagents, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of ticagrelor intermediate of formula (i) comprises taking N,N-diethylaniline hydrochloride in organic solvent A solution, adding reductant in organic solvent B solution dropwise, insulating at 0-50 degrees C for 4-20 hours, adding (S)-diphenyl prolinol in organic solvent A solution and 2-chloro-1-(3,4-difluorophenyl)ethanone in organic solvent A solution, performing reduction to obtain (S)-2-chloro-1-(3,4-difluorophenyl)ethanol, adding triethyl phosphonoacetate, organic solvent C and alkali, performing ring-closure reaction for 5-30 hours to obtain ethyl 2-phenylcyclopropanecarboxylate derivative of formula (ii), washing, adding inorganic alkali aqueous solution and/or water-alcohol solution, hydrolyzing to obtain (1R,2R)-2-(3,4-difluorophenyl)cyclopropanecarboxylic acid, mixing with organic solvent D, reacting with thionyl chloride, reacting with aqueous ammonia to obtain 1,2-difluorobenzene derivative of formula (iii), adding alkali metal hydroxide aqueous solution and sodium hypochlorite aqueous solution and reacting.
NOVELTY - Preparing sulbenicillin sodium intermediate involves dissolving alpha-chlorophenylacetic acid in alkali solution and then adding the dissolved material with sodium sulfite solution. The obtained material is heated to reflux and then the heated material is added with acid solution to obtain the desired product.    USE - Method for preparing sulbenicillin sodium intermediate (claimed).    ADVANTAGE - The method enables to prepare sulbenicillin sodium intermediate in simple and environment-friendly manner, and with low toxicity.
NOVELTY - An alpha -hydroxy thioether derivative (I) is new.    USE - Hydroxy thioether derivative used as active component of pesticidal composition (claimed).    ADVANTAGE - The method uses inexpensive copper metal and simple organic acid, has high efficiency, and is environment-friendly and simple. The compound is easy to purify.    DETAILED DESCRIPTION - An alpha -hydroxy thioether derivative of formula (I) is new.    R1-R2=1-10C alkyl, 1-10C ester, aryl, or heteroaryl; and    R3=H, 1-10C alkyl, acyl, alkenyl, or alkoxy, hydroxy, amino, halo, or 1-20C aryl.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Caulerpin preparation involves smashing feather shaped algae and then extracting by using microwave auxiliary extraction to obtain crude extract. The obtained crude extract is loaded in high speed counter current chromatography (HSCCC) solvent system. The obtained crude extract is concentrated into a paste, and then dissolved in lower phase solvent system to obtain high-speed countercurrent chromatography sample solution fractions. The obtained fractions are collected for purifying by using high performance liquid chromatography.    USE - Method for preparing caulerpin (claimed).    ADVANTAGE - The method prepares the caulerpin in a simple, precise and eco-friendly manner on industrial scale.
NOVELTY - The disposable medical device substrate comprises 100 parts biodegradable polymer ingredients. The biodegradable polymer ingredient is polylactic acid having molecular weight of 2000000.    USE - Disposable medical device substrate used for manufacturing disposable medical devices such as disposable cervical dilator, disposable uterine probe, disposable uterine curette, disposable vaginal dilator, disposable intrauterine device, disposable tubal extraction and extraction plate, disposable cervical sampler vivo, disposable umbilical cord clip, disposable tongue depressor, disposable mouthpieces, disposable oropharyngeal airway, disposable anesthesia laryngoscope, disposable rectum, sigmoid vivo sampling forceps, disposable nasopharyngeal live sampling clamp, disposable washing and flushing head, disposable surgical knife handle and disposable dental impression trays.    ADVANTAGE - The disposable medical device substrate is degraded by microorganisms completely, prevents pollution of the environment, and thus improves safety and health.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing disposable medical device substrate, which involves:    (A) drying biodegradable polymer having molecular weight of 2000000 in vacuum at 45-55 degrees C for 3-6 hours to form dried pellets; and    (B) placing the dried pellets into injection molding machine hopper at 150-170 degrees C for 4-6 seconds.
NOVELTY - The thermal insulation material comprises 3-9 pts. wt. hydroxypropylmethylcellulose, 20-35 pts. wt. polystyrene, 5-10 pts. wt. sodium lauryl sulfate, 25-40 pts. wt. bentonite, 20-30 pts. wt. water, 10-23 pts. wt. stearic acid, and 30-46 pts. wt. rigid polyurethane.    USE - Thermal insulation material used for preparing pharmaceutical incubator (claimed).    ADVANTAGE - The thermal insulation material ensures good heat conductive coefficient, and can be prepared in a simple and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing thermal insulation material, which involves:    (A) mixing 3-9 pts. wt. hydroxypropylmethylcellulose, 20-35 pts. wt. polystyrene, 5-10 pts. wt. sodium lauryl sulfate, 25-40 pts. wt. bentonite, 20-30 pts. wt. water, 10-23 pts. wt. stearic acid, and 30-46 pts. wt. rigid polyurethane to form a mixture;    (B) heating the formed mixture in a reaction vessel at 40-55 degrees C under reduced pressure for 20-30 minutes;    (C) stirring the mixture at normal temperature for 30 minutes to obtain a slurry;    (D) loading the resulting slurry into mold in an automatic molding drying room at room temperature; and    (E) cooling the finished naturally to form the thermal insulation material.
NOVELTY - Marsh gas pool comprises fermentation room (1) and firedamp with a height greater than fermentation room. The biomass and fermentation room are connected by a pipe (4). The top part is set with feedstock and the fermentation bottom is set with discharging opening (11). The fermentation room is connected with a storage chamber (2) and the upper part of storage chamber is provided with an air outlet (21).    USE - Marsh gas pool.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas pool.    Fermentation room (1)    Storage chamber (2)    Pipe (4)    Discharging opening (11)    Air outlet (21)
NOVELTY - Fertilizer comprises 65-85 wt.% humus organic fertilizer, 15-25 wt.% soil improvement material, 6-12 wt.% quick acting fertilizer and 6-12 wt.% quick-acting nitrogen fertilizer.    USE - Fertilizer used for planting and improving saline -alkali soil plate structure (claimed).    ADVANTAGE - The fertilizer is cost-effective and eco-friendly, and improves multifunctional composite microorganism flora in soil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing fertilizer, which involves mixing quick-acting nitrogen fertilizer and fresh man and animal excreta in ratio of 10:3, adding crop straw and animal manure, adding remaining components uniformly, and then decomposing; and    (2) a method for applying fertilizer, which involves ploughing soil through rotary cultivator and applying fertilizer (2-6 kg) on saline -alkali soil plate pit bottom in depth flat hole of 8-20cm.
NOVELTY - Fertilizer synergistic agent comprises 70-85 pts. wt. starch, 6-7 pts. wt. bacteria, 5-10 pts. wt. carbon source, 3-5 pts. wt. nitrogen source, 30-50 pts. wt. water, 1.6-1.8 pts. wt. trace element, 6-8 pts. wt. sodium alginate hydrolysate, 3-4 pts. wt. nutrient solution bacteriophage and 2-4 pts. wt. root promoting agent.    USE - Fertilizer synergistic agent.    ADVANTAGE - The fertilizer synergistic agent promotes plant absorption, prevents soil caking, reduces incidence of pests disease and increases apparent utilization rate of nutrient fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer synergistic agent, which involves:    (A) mixing and grinding peanut starch, rice flour and water to obtain slurry;    (B) enzymolyzing mixture of sodium carbonate, sodium hydroxide and starch powder with polyphenol oxidase and trypsin at 38-42 degrees C for 5-6 hours;    (C) fermenting obtained mixture with bacteria, carbon source, nitrogen source, water and trace element for 15-18 days;    (D) chelating fermented materials with acetic acid bacteria at 45-50 degrees C for 12-14 hours;    (E) stirring sodium carbonate, sodium hydroxide according and alkaline extracting agent at 65-75 degrees C for 7-9 hours;    (F) pressing and filtering obtained materials to obtain filtered liquid that is mixed with boric acid and acetic acid;    (G) evaporating obtained mixture to obtain solid;    (H) hydrolysing obtained materials seaweed, cellulose and alpha amylase at 35-37 degrees C for 4-5 hours;    (I) filtering hydrolyzed material;    (J) homogenizing filtrate with cross-linked polysaccharide acetate, artemisinin, locust bean gum and water retention agent; and    (K) stirring obtained mixture with root promoting agent uniformly to obtain product.
NOVELTY - The new type utility claims have one kind organic fertilizer in the subcritical water reaction system, comprising a reaction kettle, the reaction kettle with feedstock mouth of the control valve and a discharging mouth of valve control is along the length direction set with rotation shaft in reaction kettle, rotating shaft is double-layer hollow structure, and is provided with the stirring part is through hole, double-layer hollow structure and one inner side, between outside layer formed with a steam entrance, at wall outside layer is set with steam outlet, also comprising A and stirring component interaction and connecting rod, connecting rod is set at rotating shaft of hollow part, one end part of connecting pole by one cam mechanism driving the stirring part in at the same time along with the rotating of rotating shaft also is connecting rod drive then relative rotation axis; also comprises one negative pressure device, a negative pressure device and a reaction kettle seal connected. The utility model is new type with simple operation, automatic degree high, the construction period is short, the organic fertilizer and organic substance content is low and beneficial effect.
NOVELTY - A biological diesel oil magnetic solid acid catalyst comprises iron sulfate, cobalt sulfate, nickel sulfate, ferric chloride, cobalt chloride, nickel chloride, iron phosphate, cobalt phosphate, nickel phosphate, ferric nitrate, cobalt nitrate and/or nickel nitrate.    USE - Biological diesel oil magnetic solid acid catalyst.    ADVANTAGE - The method is simple, can repeatedly recycle catalyst, and has short reaction time, reduced methanol consumption, and no acid slag discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological diesel oil comprising:    (A) adding raw material oil into reaction kettle, heating to 90 degrees C, adding magnetic solid acid catalyst at weight ratio of 200:1, and stirring uniformly;    (B) continuously heating to 100 degrees C, stirring, adding 200 L/hour liquid methanol, vaporizing, feeding methanol steam into rectifying tower, and purifying to recover methanol;    (C) keeping reaction temperature to 100-120 degrees C for 2 hours, and stopping reaction when reaction liquid acid value is reduced to 1 mg potassium hydroxide/g and conversion rate is more than 95%; and    (D) standing to precipitate while electromagnetically absorbing for 30 minutes to absorb magnetic solid acid catalyst, discharging remaining mixture through reaction kettle bottom, adding into crude distillation tank, vacuum-distilling at 10-100 Pa, and collecting 130-180 degrees C fractions.    The raw material oil is waste oil, acidification oil or palm oil.
NOVELTY - A milk cow excrement is anaerobic fermented before pretreated by collecting milk cow excrement in the lagoon every day, placing into mounted mixing device, stirring, uniformly mixing to finish solid and liquid excrement, crushing waste into spiral squeeze type solid-liquid separating machine using SP submersible reamer pump for solid-liquid separation, directly discharging obtained liquid into slurry tank, feeding obtained solid into pulverizer, crushing, falling into discharging mouth to slurry tank, and adding tap water, earth's surface water or biogas slurry.    USE - Method for anaerobic fermenting before milk cow excrement pre-treating (claimed).    ADVANTAGE - The method has long anaerobic digestion time and low raw material utilization rate and raw material gas generation rate, and solves milk cow excrement feedstock equipment and pipeline blockage.    DETAILED DESCRIPTION - A milk cow excrement is anaerobic fermented before pretreated by collecting milk cow excrement in the lagoon every day, placing into mixing device mounting into lagoon, stirring, uniformly mixing to finish solid and liquid excrement, crushing waste into spiral squeeze type solid-liquid separating machine using SP submersible reamer pump for solid-liquid separation, directly discharging obtained liquid into slurry tank, feeding obtained solid into pulverizer, crushing, falling into discharging mouth to slurry tank, adding tap water, earth's surface water or biogas slurry, starting stirrer, regulating concentration to 3-10%, and feedstock pumping into anaerobic digester for anaerobic fermentation production.
NOVELTY - Preparing cultivation material involves pulverizing wood (48-52%), cotton seed hull (32-37%) soybean (8-10%), mushroom (3-4%), lime (2%) and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with cotton seed hull, soybean powder and broadleaf wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin.    USE - Method for preparing cultivation material used for Auricularia polytricha (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing wood (48-52%), cotton seed hull (32-37%) soybean (8-10%), mushroom (3-4%), lime (2%) and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with cotton seed hull, soybean powder and broadleaf wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Obtained material is mixed with gypsum and lime, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is packed in polyethylene bag, and bacteria is inoculated in bag through hole. Obtained material is kept at 18-20 degrees C and 60-75% humidity for 34-36 days to obtain the final product.
NOVELTY - Preparing copper glyphosate comprises heating and reacting glyphosate and copper compound in a solution to obtain copper glyphosate. The copper compound is copper oxide, copper hydroxide and/or basic cupric carbonate.    USE - The method is useful for preparing copper glyphosate (claimed).    ADVANTAGE - The method: does not require a step of generating sodium salt in advance; has simple reaction process; does not need to be treat large amount of wastewater containing sodium; is environmentally friendly; produces mother liquor having low content of glyphosate; and produces copper glyphosate with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for copper glyphosate prepared by the above mentioned method.
NOVELTY - Obtaining bio-ethanol involves soaking cellulosic and hemicellulosic enriched-biomass in sulfuric acid solution for 2-4 hours, where the obtained biomass mixture is then transferred to steam explosion reactor at 1.5-2.2 MegaPascals for 1-15 minutes to obtain sugar hydrolyzate. The resulting sugar hydrolyzate is then filtered to obtain solid cellulosic and hemicellulosic residues. The obtained solid cellulosic and hemicellulosic residues are then mixed with cellulase, water, pH regulated buffers, acids, or bases.    USE - Method for obtaining bio-ethanol from cellulosic and hemicellulosic enriched-biomass (claimed).    ADVANTAGE - The method enables to obtain bio-ethanol from cellulosic and hemicellulosic enriched-biomass, in a cost-effective manner.    DETAILED DESCRIPTION - Obtaining bio-ethanol involves soaking cellulosic and hemicellulosic enriched-biomass in sulfuric acid solution for 2-4 hours, where the obtained biomass mixture is then transferred to steam explosion reactor at 1.5-2.2 MegaPascals for 1-15 minutes to obtain sugar hydrolyzate. The resulting sugar hydrolyzate is then filtered to obtain solid cellulosic and hemicellulosic residues. The obtained solid cellulosic and hemicellulosic residues are then mixed with cellulase, water, pH regulated buffers, acids, or bases, where the prepared system is reacted at 45-55 degrees C for 36 hours or more to obtain enzymatic hydrolyzed solution. The obtained enzymatic hydrolyzed solution is mixed with Rhizopus oryzae, and then subjected to fermentation at 28-30 degrees C for 12-24 hours. The resulting bio-ethanol from cellulosic and hemicellulosic enriched-biomass, after completion of the fermentation, is neutralized to a pH of 6.0-7.0.
NOVELTY - Preparing lysine, comprises adding lysine fermentation strain into a lysine fermentation medium, in presence of carbon sources, and adding ammonium chloride, carrying out fermentation culture, where the initial culture medium has sulfate ion content accounting to 10-16 g/l.    USE - The method is useful for preparing lysine (claimed).    ADVANTAGE - The method does not require to carry out ion exchange process, and deamination process; shortens the extraction process; and reduces the utilization rate of raw materials, and extraction costs; does not produce waste water.
NOVELTY - Method for preparing bioorganic fertilizer, involves mixing wild tung bran, sheep manure, barnyard manure, biogas residue and microbial inoculums, stacking the raw materials, and finally carrying out fermentation.    USE - The method is useful for preparing bioorganic fertilizer (claimed).    ADVANTAGE - The method removes odor, converts organic wastes into high-quality bioorganic fertilizer in short time, increases bioactivity of the bioorganic fertilizer and the soil, and relieves soil deterioration. The bioorganic fertilizer has rapid absorption, high fertilizing performance, is cost-effective and environmentally-friendly, improves physical and chemical properties of soil, and enhances water/fertilizer retention performance of soil.
NOVELTY - Power station comprises anaerobic device, warming pressure pump, power generation unit and four purifier. The anaerobic filter process gas and purified by power machine having fuel or gaseous fuel. The power machine is driven by power generating unit. The power unit generates hot water into hot water tank, which is supplied to anaerobic warming by using pressure pump. The body of the device is cylindrical and gas storage cabinet is hemispherical.    USE - Power station.    ADVANTAGE - The power station increase production efficiency of biogas, cost-effective, eco-friendly, provides clean energy supply, advance and prevents marsh liquid in shell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of power station    Port switch valve (1)    Switch valve (2)    Insulating layer (3)    Wall (4)    Annular corridor (5)
NOVELTY - Brick structured biogas power station comprises a feed port switch valve (1), a discharge port switch valve, and an insulation layer (3). Wall (4) of the brick structured biogas power station is provided with an insulation layer. A corridor (5) is connected to gas cabinets (6) and gas outlet (7). The pores of the corridor leads to biogas outlet (8). Biomass fermenting device (10) is provided with an automatic alarm (9), where the produced biogas is passed through a drainage pipe (39) and then collected to a container. The collected biogas is then ready to be supplied for generating power.    USE - Brick structured biogas power station.    ADVANTAGE - The brick structured biogas power station efficiently utilizes biomass resources to generate biogas in a simple, convenient and cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of brick structured biogas power station.    Feed port switch valve (1)    An insulation layer (3)    Wall (4)    Corridor (5)    Gas cabinets (6)    Gas outlet (7)    To biogas outlet (8)    Automatic alarm (9)    Biomass fermenting device (10)    Drainage pipe (39)
NOVELTY - Brick structured anaerobically biogas producing power station comprises a feed port switch valve (1) and an insulation layer (3). Wall (4) of the brick structured biogas power station is provided with an insulation layer. A corridor (5) is connected to gas cabinets (6) and gas outlet (7). The pores of the corridor leads to biogas outlet (8). Biomass fermenting device (10) is provided with an automatic alarm (9), where the produced biogas is passed through a drainage pipe (39) and then collected to a container. The collected biogas is then ready to be supplied for generating power.    USE - Brick structured anaerobically biogas producing power station.    ADVANTAGE - The brick structured brick structured anaerobically biogas producing power station efficiently utilizes biomass resources to generate biogas in a simple, convenient, cost-effective and environment-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of brick structured brick structured anaerobically biogas producing power station.    Feed port switch valve (1)    An insulation layer (3)    Wall (4)    Corridor (5)    Gas cabinets (6)    Gas outlet (7)    To biogas outlet (8)    Automatic alarm (9)    Biomass fermenting device (10)    Drainage pipe (39)
NOVELTY - Stainless steel reinforced anaerobic power supply station comprises a pressure pump, a power generation unit, a purifier, a feed port switch valve (1), a discharge port switch valve, and an insulation layer (3). Wall (4) of the brick structured biogas power station is provided with an insulation layer. A corridor (5) is connected to gas cabinets (6) and gas outlet (7). The pores of the corridor leads to biogas outlet (8). Biomass fermenting device (10) is provided with an automatic alarm (9), where the produced biogas is passed through a drainage pipe (39) and then collected to a container.    USE - Stainless steel reinforced anaerobic power supply station.    ADVANTAGE - The stainless steel reinforced anaerobic power supply station efficiently utilizes biomass resources to generate biogas in a simple, convenient and cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of stainless steel reinforced anaerobic power supply station.    Feed port switch valve (1)    An insulation layer (3)    Wall (4)    Corridor (5)    Gas cabinets (6)    Gas outlet (7)    To biogas outlet (8)    Automatic alarm (9)    Biomass fermenting device (10)    Drainage pipe (39)
NOVELTY - Anaerobic biogas producing system is cube type and comprises multiple numbers of intermediate permeable apertures. Biogas producing units (1) in the form of circular holes (2), are protruded from the anaerobic biogas producing system. There is a certain gap between stacked each of the biogas producing unit, where the space between them are packed with straw and domestic garbage. Anaerobic fermentation is then carried to produce pure biogas.    USE - Anaerobic biogas producing system used for generating large amount of energy sources and green fertilizer.    ADVANTAGE - The anaerobic biogas system efficiently utilizes straw and domestic garbage resources to generate biogas in a simple, convenient and cost-effective manner. The constructed anaerobic biogas system is capable of creating large amount of biogas sources and green fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of The anaerobic biogas producing system    Biogas producing units (1)    Circular holes (2)
NOVELTY - Constructing high-organic selenium yeast involves first soaking wheat particles in sodium selenite solution for 20-22 hours. The wheat particles are then grown under optimized conditions i.e. relative humidity of 90-95% at 20-25 degrees C for definite duration. Sodium selenate solution is then continued to add to the wheat particles, where pH of the medium is adjusted by calcium sulfate. The grown wheat particles, after completion of the germination, is cleaned with water to obtain wet selenium enriched wheat particles.    USE - Method for constructing high-organic selenium yeast (claimed).    ADVANTAGE - The method enables to construct non-toxic high-organic selenium yeast in a simple, convenient, cost-effective and environment-friendly manner.    DETAILED DESCRIPTION - Constructing high-organic selenium yeast involves first soaking wheat particles in sodium selenite solution for 20-22 hours. The wheat particles are then grown under optimized conditions i.e. relative humidity of 90-95% at 20-25 degrees C for definite duration. Sodium selenate solution is then continued to add to the wheat particles, where pH of the medium is adjusted by calcium sulfate. The grown wheat particles, after completion of the germination, is cleaned with water to obtain wet selenium enriched wheat particles. The obtained wet selenium enriched wheat particles are then sterilized by microwaves, and then crushed into pulp in order to obtain selenium enriched wheat particles syrup. The resulting selenium enriched wheat particles syrup is then incubated at 25-32 degrees C for 10-15 hours to obtain the first generation of high-organic selenium yeast with enhanced conversion rate.
NOVELTY - Biomass is placed in a muffle furnace, and argon is purged and cracking process is carried out under anaerobic or hypoxic condition to obtain biochar. Biochar is sieved in mortar, and sieved biochar is mixed with hydrogen peroxide, and modification treatment is carried out by placing in culture chamber at 28-35 degrees C. The modified biochar is filtered to remove hydrogen peroxide. The resultant material is rinsed using deionized water, and pH of the biochar is adjusted to neutral. The resultant material is then dried to obtain modified biochar.    USE - Modification of biochar (claimed).    ADVANTAGE - The method efficiently and economically provides modified biochar having excellent ammonium-nitrogen adsorption capacity in soil/water components, by simple method.
NOVELTY - Organic compound fertilizer comprises 28-45 pts. wt. chicken manure, 16-25 pts. wt. oil residue cake, 12-17 pts. wt. sauce, 12-21 pts. wt. wheat bran, 16-25 pts. wt. straw, 6-12 pts. wt. beer wastewater sludge, 13-25 pts. wt. phosphorus-nitrogen-potassium compound fertilizer, 5-10 pts. wt. tea dry powder, 8-16 pts. wt. sodium humate, 1-3 pts. wt. ferrous sulfate, 1-3 pts. wt. magnesium sulfate, 0.5-1.2 pts. wt. fermenting agent and 10-15 pts. wt. coal powder ash.    USE - Organic compound fertilizer used for promoting growth of beneficial bacteria in soil.    ADVANTAGE - The organic compound fertilizer improves soil structure for long-term.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic compound fertilizer, which involves:    (A) mixing chicken manure, oil cake sauce residue, bran, corn straw, beer wastewater sludge, phosphorus-nitrogen-potassium compound fertilizer and fermenting agent and stacking to regulating water content to 50-60%;    (B) adding alkali in the mixture to adjust pH value to alkaline, and carrying out fermentation at 45-65 degrees C to obtain first fermentation product;    (C) adding weak alkali in the first fermentation product to adjust pH value, and fermenting at 45 degrees C to obtain second fermentation product;    (D) adding tea powder, sodium humate, ferrous sulfate, magnesium sulfate and coal powder; and    (E) granulating the product in a granulator, and processing in intermittent steam.
NOVELTY - Preparing wine involves pretreating rice before brewing, performing pre-fermentation, fermentation, sterilization and aging for improvement by inoculating lactic acid fungus. The obtained product is fermented to increase the dosage at low temperature, and is ventilated and agitated to inhibit the growth of lactic acid bacteria. The final product is then sterilized using pasteurization.    USE - Method for preparing wine (claimed).    ADVANTAGE - The method enables to prepare wine in a reliable and eco-friendly way with low levels of biogenic amines.
NOVELTY - Composite microbial inoculum comprises 25 wt.% Rhodococcus rhodochrous, 20 wt.% Bacillus subtilis, 15 wt.% Pseudomonas aeruginosa, 10 wt.% Saccharomyces cerevisiae, 10 wt.% European nitrosomonas Aeromonas, 10 wt.% Bacillus cereus spores, 5 wt.% Aspergillus niger and 5 wt.% Paracoccus denitrificans.    USE - Composite microbial inoculum for treating municipal sewage rich in heavy metals (all claimed), and waste water rich in biodegradable, toxic and harmful substances such as arsenic, ammonia, nitrogen and phosphorus.    ADVANTAGE - The composite microbial inoculum has good degradation effect.
NOVELTY - Producing marsh gas involves using solar energy in winter for fermenting marsh gas by adding synergistic agents. Solar fans, solar collector and steam digesters are utilized for solar heat warming in winters. The feed is tree with branches and leaves and then toxic and harmful weeds from tree are collected and disposed. The obtained branches and leaves are crushed. The crushed mixture is mixed with lactic acid bacteria and synergistic agents for fermentation process under vacuum. The obtained fermented mixture is again added with lactic acid bacteria and synergistic agents.    USE - Method for producing marsh gas used for medium and small sized biogas projects (all claimed).    ADVANTAGE - The method enables to improve efficiency and yield of marsh gas production by reducing gas production time and increasing feed conversion rate, and enhance yield, quality and nutrient content of organic fertilizers.    DETAILED DESCRIPTION - Producing marsh gas involves using solar energy in winter for fermenting marsh gas by adding synergistic agents. Solar fans, solar collector and steam digesters are utilized for solar heat warming in winters. The feed is tree with branches and leaves and then toxic and harmful weeds from tree are collected and disposed. The obtained branches and leaves are crushed. The crushed mixture is mixed with lactic acid bacteria and synergistic agents for fermentation process under vacuum. The obtained fermented mixture is again added with lactic acid bacteria and synergistic agents (1/3-1/2 times of the amount of fermented mixture) to increase methane gas production. Gas production time gets shortens in winters as feed conversion rate is improved.
NOVELTY - Biogas system comprises main body, inlet and outlet of material cylinder and annular fermentation pipe (30). The material cylinder is provided between feedstock tube (10) and discharging tube (20). The feedstock tube and discharging tube are separated by fermentation pipe. The feedstock pipe is connected with water pipe. The discharging pipe connected is with discharging tube between drain pipe. The annular fermentation pipe connected to discharging pipe is provided with blocking plate (34). The adjacent blocking plate forms fermentation area between them.    USE - Biogas system.    DETAILED DESCRIPTION - Biogas system comprises main body, inlet and outlet of material cylinder and annular fermentation pipe. The material cylinder is provided between feedstock tube and discharging tube. The feedstock tube and discharging tube are separated by fermentation pipe. The feedstock pipe is connected with water pipe. The discharging pipe connected is with discharging tube between drain pipe. The annular fermentation pipe connected to discharging pipe is provided with blocking plate. The adjacent blocking plate forms fermentation area between them. The biogas system also comprises cloth bacteria device, which includes drain pipe, cloth bacteria pipe, cloth bacteria hole and water pressure. The cloth bacteria pipe is circular pipe fixed to the inner side wall pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas system.    Feedstock tube (10)    Discharging tube (20)    Annular fermentation pipe (30)    Air pipe (36)    Discharging pipe (42)
NOVELTY - Solid-state fermentation tank comprises tanks (1), left bracket (2) and right bracket (3). Top and bottom of the tank are provided with air outlet (4) and lower discharge port (5), which is provided at the top right of the tank. The discharge port imports material in interior (6) of the tank with jacket (7). The discharge port is located at bottom left, lower right on the side of the tank. The side of the tank has three air hammer (8). The tank in central position is provided with interior lateral strain, which is connected to pipe (9). The left bracket and right bracket are coupled.    USE - Solid-state fermentation tank.    ADVANTAGE - The solid-state fermentation tank is water-conservative, energy-conservative, eco-friendly and cost-effective, and doest not produce waste.    DETAILED DESCRIPTION - Solid-state fermentation tank comprises tanks, left bracket and right bracket. Top and bottom of the tank are provided with air outlet and lower discharge port, which is provided at the top right of the tank. The discharge port imports material in interior of the tank with jacket. The discharge port is located at bottom left, lower right on the side of the tank. The side of the tank has three air hammer. The tank in central position is provided with interior lateral strain, which is connected to pipe. The left bracket and right bracket are coupled together by bearing (10) disposed thereon and are provided at both ends of the tank around left supporting shaft (12) and right supporting shaft (13).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid-state fermentation tank.    Tanks (1)    Left bracket (2)    Right bracket (3)    Air outlet (4)    Lower discharge port (5)    Material in interior (6)    Jacket (7)    Hammer (8)    Pipe (9)    Bearing (10)    Left supporting shaft (12)    Right supporting shaft (13)
NOVELTY - Extracting L-tryptophan and feed meal involves culturing Escherichia coli and Corynebacterium glutamicum into culture medium at certain condition to obtain a mixed bacterial suspension. 2% inoculum of the mixed bacterial suspension is inoculated into a fermentation medium to perform fermentation for 30 hours in order to obtain L-tryptophan in the fermentation broth. The fermentation broth is filtered through microfiltration technology to obtain retentate and a filtrate.    USE - Method for extracting L-tryptophan (claimed).    ADVANTAGE - The L-tryptophan extraction method are performed by comprehensive waste treatment technology in a simple and environment-friendly manner. The obtained retentate is effectively utilized for the preparation of feed meal.    DETAILED DESCRIPTION - Extracting L-tryptophan and feed meal involves culturing Escherichia coli and Corynebacterium glutamicum into culture medium at certain condition to obtain a mixed bacterial suspension. 2% inoculum of the mixed bacterial suspension is inoculated into a fermentation medium to perform fermentation for 30 hours in order to obtain L-tryptophan in the fermentation broth. The fermentation broth is filtered through microfiltration technology to obtain retentate and a filtrate. The obtained filtrate is passed through an ion exchange column to obtain high purified L-tryptophan in the eluate. The eluate is then finally passed through ultra-filtration reverse osmosis to obtain concentrated L-tryptophan. The resulting retentate is added to the container comprising waste soybeans, distillers grains, rice straw and wheat bran powder, where the prepared mixture is steam heated at 100 degrees C for 30 minutes to obtain concentrated protein containing solution. The obtained concentrated protein containing solution is then dried and crushed to obtained feed meal.
NOVELTY - Method for preparing microbial fertilizer for preventing and treating multiple pests, involves (a) mixing lactic acid bacteria, Bacillus subtilis and yeast in a mass ratio of 1-2:0.5-1:1-5, (b) mixing corn stalks, chaff and weed in a mass ratio of 20-70:10-20:1-8, and adding water into mixture, and (c) mixing products of steps (a)-(b) in a mass ratio of 0.01-0.1:100, and fermenting the mixture for 2-10 days.    USE - The method is useful for preparing microbial fertilizer for preventing and treating multiple pests for vegetables (claimed).    ADVANTAGE - The microbial fertilizer is cost-effective, and increases multiple nutrients to the soil.
NOVELTY - Bioorganic fertilizer comprises 40-50 pts. wt. livestock manure, 30-40 pts. wt. biogas slurry, 5-10 pts. wt. mushroom residues, 5-10 pts. wt. rice residues, 3-5 pts. wt. cotton and 1-2 pts. wt. fermentation strain which is white rot fungus and Bacillus subtilis.    USE - The bioorganic fertilizer is useful for planting crops, fruit trees, and vegetable.    ADVANTAGE - The fertilizer is simple and convenient to prepare within short period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing bioorganic fertilizer, which involves (a) inoculating 1/asterisk109/ml white rot fungus and B.subtilis in a ratio of 1:1 into slant culture medium, and performing culturing at 25 degrees C for 10 days, (b) mixing the above-mentioned remaining raw materials except biogas slurry, crushing mixture, adding mixture to biogas slurry, turning mixture, until moisture content reaches 60%, (c) mixing products obtained in steps (a) and (b), and spraying water until moisture content reaches 60-80%, and performing fermentation at 60 degrees C for 2-3 days, and 50 degrees C for 7 days.
NOVELTY - The biological spraying apparatus has multi-function device having liquid storage function and propagation function of the biologically active material. The apparatus also has gaseous stream generating and conveying device that generates gaseous stream and supplies the liquid after its propagation. The liquid and gaseous stream form gaseous stream containing ultrafine drug particles to be applied to the target environment by the apparatus.    USE - Biological spraying apparatus for spraying biological active substance in agricultural field.    ADVANTAGE - Achieves cost savings by saving about 30 to 70 percent of agricultural drugs when using the simple, economical and easy to use biological spraying apparatus that can be used widely for agricultural spraying, air humidification, sanitation and air pollution control.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the biological spraying apparatus.    Panel (110)    Switch (111)    Bottom cover (120)    Base (121)    Housing (130)
NOVELTY - A Pseudomonas aeruginosa strain PAO1 (CCTCC M 2014630) capable of degrading pesticides containing ester bonds, is new.    USE - The P.aeruginosa strain PAO1 is useful for degrading pesticides containing ester bonds such as cypermethrin, cyhalothrin, deltamethrin, cypermethrin, fenpropathrin, bifenthrin, kresoxim-methyl, pyraclostrobin and azoxystrobin, and removing pesticide residues in environments such as water bodies and soil (all claimed).    ADVANTAGE - P.aeruginosa strain PAO1 is strong in environmental adaptability, good in degrading effect and convenient in use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pesticide composition, which comprises the strain and other adjuvants.
NOVELTY - Controlling digestion process of anaerobic digestion tank, comprises (a) measuring methane in gas discharged by anaerobic digestion tank, (b) determining increased or decreased flow rate of gas at predetermined measuring time during more methane than predetermined standard, (c) measuring temperature of anaerobic digestion tank during decreased gas flow rate, (d) determining temperature of anaerobic digestion tank in predetermined range, (e) determining pH of sludge in anaerobic digestion tank within predetermined range, and (f) generating alarm when pH of sludge more than predetermined range.    USE - The method is useful for controlling digestion process of anaerobic digestion tank (claimed).    ADVANTAGE - The method controls digestion process automatically.    DETAILED DESCRIPTION - Controlling digestion process of anaerobic digestion tank, comprises (a) measuring a methane content in gas discharged from the anaerobic digestion tank, (b) determining the increased or decreased flow rate of the gas at predetermined measuring time during more methane content than predetermined standards, (c) measuring temperature of the anaerobic digestion tank during decreased flow rate of the gas, (d) determining temperature within a predetermined range of the anaerobic digestion tank, (e) determining pH of sludge in the anaerobic digestion tank within predetermined range, and (f) generating an alarm when pH of the sludge more than the predetermined range. An INDEPENDENT CLAIM is also included for recording media records the controlling method of digestion process, and provided with a controlling device.
NOVELTY - Preparing home-made vegetable organic fertilizer comprises taking 20-30 pts. fallen leaves, 15-20 pts. rotten vegetable leaves, 10-15 pts. soybean residue, 0.5-1 pts. white wine, 5-10 pts. sludge, 3-5 pts. sweet potato seedling and 5-10 pts. chicken manure as raw materials.    USE - The method is useful for preparing home-made vegetable organic fertilizer (claimed).    ADVANTAGE - The fertilizer increases plant yield and promotes photosynthesis of plant.
NOVELTY - Method for preparing organic fertilizer by fermentation, involves preparing zymophyte to mix comprising 1 part mass sugar, 1 part mass starch, 1 part mass traditional Chinese medicine, 1000 parts mass rice bran and/or wheat bran and 1 part mass Bacillus, drying until moisture content reaches 30-50%, turning for 20 days, adding 0.2-0.25 wt.% bacterial mixture to animal excrement, fermenting animal excrement, and performing fermenting management.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method prepares organic fertilizer with high organic matter content and abundant nutrients.
NOVELTY - Biofertilizer comprises agricultural solid waste material fermented by Trichoderma reesei 12 strain and Bacillus subtilis D9 strain.    USE - The biofertilizer is useful for improving growth in saline land (claimed), and improving soil condition.    ADVANTAGE - The biofertilizer improves salt tolerance and survival of plants, and enhances biomass of Suaeda salsa, Cynometra malaccensis and Bassia scoparia by 49.1%, 56.3% and 52.2%, respectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biofertilizer, which involves (a) culturing T.reesei 12 strain in potato dextrose agar (PDA) medium until cell count reaches 1x 108 colony forming unit (cfu)/ml, (b) fermenting solid residue of vinegar using obtained culture of (a), (c) culturing B.subtilis D9 strain in beef peptone culture medium until cell count reaches 2x 108 cfu/ml, (d) fermenting wheat bran using obtained culture of (c) at 37 degrees C for 4 days, and (e) mixing obtained fermentation products of (b) and (d) in a ratio of 5:1 to obtain product, where the product comprises greater than or equal to 0.2x 108 colony forming unit (cfu)/g T.reesei 12 strain, and greater than or equal to 0.5x 108 cfu/g B.subtilis D9 strain.
NOVELTY - Preparation of adenosine triphosphate-competitive small molecule (VI) involves reacting 5-bromo-3-methyl-1H-indazole (I) with amino-protecting reagent, obtaining substituted imidazole intermediate compound (II), coupling with bis(pinacolato)diboron, obtaining substituted 3-methyl-5-(4,4,5,5-tetramethyl-1,3,2-dioxaborolan-2-yl)-1H-indazole (III), coupling resultant with tert-butyl N-((2S)-1-((5-bromopyridin-3-yl)oxy)-3-(1H-indol-3-yl)propan-2-yl)carbamate (IV), obtaining di-tert-butyl dicarbonate-containing indazole compound (V), and removing amino-protecting group of resultant compound.    USE - Preparation of adenosine triphosphate-competitive small molecule used as A443654, preferably inhibiting agent (claimed).    ADVANTAGE - The method enables manufacture of adenosine triphosphate-competitive small molecule with high yield, by environmentally-friendly and economical process, without using toxic hexamethylditin, within short period of time.    DETAILED DESCRIPTION - Preparation of adenosine triphosphate-competitive small molecule of formula (VI) involves reacting 5-bromo-3-methyl-1H-indazole of formula (I) with amino-protecting reagent, obtaining substituted imidazole intermediate compound of formula (II), subjecting resultant compound to Suzuki coupling reaction with bis(pinacolato)diboron in presence of palladium catalyst and base (A), obtaining substituted 3-methyl-5-(4,4,5,5-tetramethyl-1,3,2-dioxaborolan-2-yl)-1H-indazole of formula (III), performing Suzuki coupling reaction of resultant compound with tert-butyl N-((2S)-1-((5-bromopyridin-3-yl)oxy)-3-(1H-indol-3-yl)propan-2-yl)carbamate of formula (IV), obtaining di-tert-butyl dicarbonate-containing indazole compound of formula (V), and removing amino-protecting group of resultant compound. The adenosine triphosphate-competitive small molecule is    R=tetrahydropyranyl, t-butoxycarbonyl, benzyloxycarbonyl, fluorenyl methoxycarbonyl, allyloxycarbonyl or trimethylsilyl ethoxycarbonyl.
NOVELTY - Anaerobic fermentation device has anaerobic bacteria enrichment tank, and anaerobic reactor. The anaerobic bacterium enrichment tank is divided into complete mixing zone, strain enrichment zone and settling zone from bottom to top, where the complete mixing zone is provided with a cyclone water distributor and lateral stirrer, strain enrichment zone is provided with a filler, and the settling zone is provided with three-phase separator, and sludge discharging tube.    USE - The anaerobic fermentation device is useful for performing anaerobic bacterial fermentation (claimed).    ADVANTAGE - The device effectively improves concentration of flora as a microbial carrier, promotes the degradation of the fermentation raw material and increases the volumetric organic load and the volumetric gas productivity.    DETAILED DESCRIPTION - Anaerobic fermentation device has anaerobic bacteria enrichment tank (1), and anaerobic reactor (2). The anaerobic bacterium enrichment tank is divided into complete mixing zone, strain enrichment zone and settling zone from bottom to top, where the complete mixing zone is provided with a cyclone water distributor (4) and lateral stirrer (5), strain enrichment zone is provided with a filler (6), and the settling zone is provided with three-phase separator (7), and sludge discharging tube (8). The mixing zone, strain enrichment zone and settling zone is in a volume ratio of 1:2:1. An INDEPENDENT CLAIM is included for method for using the device for performing anaerobic bacterial fermentation.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of anaerobic fermentation device.    Anaerobic bacteria enrichment tank (1)    Anaerobic reactor (2)    Cyclone water distributor (4)    Lateral stirrer (5)    Filler (6)    Three-phase separator (7)    Sludge discharging tube (8)
NOVELTY - Operating method of multi-zone methane fermentation system involves placing fermentation material into feed tube (10), allowing different amounts of methane to be produced in annular fermentation zones inside the tubes, generating biogas in inner fermentation pipeline (30), allowing biogas to move to feed tube drainage (44) by pressure, using fermentation area at top of airway (36) to discharge biogas, reducing pressure in fermentation zone, returning biogas into fermentation pipe by pressure, using remaining fermentation biogas storage area, and continuously producing biogas.    USE - Operating method of multi-zone methane fermentation system.    ADVANTAGE - Biogas fermentation route is shorted, gas yield is improved, and fermentation efficiency is improved.    DETAILED DESCRIPTION - Operating method of multi-zone methane fermentation system involves placing fermentation material into feed tube (10), allowing different amounts of methane to be produced in annular fermentation zones inside the tubes in which flow pressure in biogas fermentation zone is smaller than flow pressure in fermentation area and when pressure of methane fermentation zone increases, biogas fermentation continues to flow to unfilled fermentation zone, generating biogas in inner fermentation pipeline (30), allowing biogas to move to feed tube drainage (44) by pressure, using fermentation area at top of airway (36) to discharge biogas, reducing pressure in fermentation zone, returning biogas into fermentation pipe by pressure, using remaining fermentation biogas storage area, and continuously producing biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective diagram of the multi-zone methane fermentation system.    Feed tube (10)    Discharge pipe (20)    Fermentation pipe (30)    Airway (36)    Feed tube drainage (44)
NOVELTY - Pressure promoting method of ultra-efficient biogas digester to produce biogas involves successively performing process (A) of placing fermentation raw material into U-shaped fermentation pipe (30) through feed tube (10), allowing biogas to accumulate in entry or exit zone formed between fermentation pipe side wall and adjacent air resistance plate, and allowing biogas to flow between feed tube, discharge pipe (20), and bacteria cloth unit (50) by inflow pressure, and performing process (B) of using biogas fermentation storage area and lowering pressure of biogas fermentation area.    USE - Pressure promoting method of ultra-efficient biogas digester to produce biogas.    ADVANTAGE - Biogas fermentation route is shorted, gas yield is improved, and fermentation efficiency is improved.    DETAILED DESCRIPTION - Pressure promoting method of ultra-efficient biogas digester to produce biogas involves successively performing process (A) of placing fermentation raw material into U-shaped fermentation pipe (30) through feed tube (10), allowing biogas to accumulate in entry or exit zone formed between fermentation pipe side wall and adjacent air resistance plate, and allowing biogas to flow between feed tube, discharge pipe (20), and bacteria cloth unit (50) by inflow pressure, performing process (B) of using biogas fermentation storage area, lowering pressure of biogas fermentation area, allowing biogas to flow to adjacent fermentation zone, returning biogas slurry from feed tube drainage (12) into fermentation pipe by pressure, and completing biogas slurry circulation, and performing process (C) of continuously producing biogas and promoting biogas circulation.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the ultra-efficient biogas digester.    Feed tube (10)    Feed tube drainage (12)    Discharge pipe (20)    Fermentation pipe (30)    Bacteria cloth unit (50)
NOVELTY - A Xylariales strain (Accession No: CCTCC M2014660) is new.    USE - The Xylariales strain is useful for catalytic synthesis of oxysophoridine.    ADVANTAGE - Oxysophoridine can be easily synthesized at low cost. Synthesis method is highly selective and environmentally friendly.
NOVELTY - Method for promoting growth of bay scallop using artificial bait involves cultivating bay scallop via industrial breeding process, and feeding artificial bait substitute for promoting gonadal development, reaching sexual maturity, and discharging mature gamete for reproduction. The artificial bait substitute comprises Spirulina powder, salt, algae powder, starch, egg, yeast powder, photosynthetic bacteria liquid and vitamin B2.    USE - The method is useful for promoting growth of bay scallop using artificial bait (claimed).    ADVANTAGE - The method is safe and inexpensive and reduces the risk of bay scallop cultivation.
NOVELTY - 7-Carbonyl-dehydroabietic acid and selenium dioxide are reacted to obtain dehydroabietate compound (I).    USE - Preparation of dehydroabietate compound (claimed).    ADVANTAGE - The method efficiently and economically provides dehydroabietate compound with high yield by generating reduced amount of by-products.    DETAILED DESCRIPTION - 7-Carbonyl-dehydroabietic acid and selenium dioxide are reacted to obtain dehydroabietate compound of formula (I).
NOVELTY - An iridoid glycoside is used as antiviral, antibacterial, antipyretic, antiinflammatory and antioxidant drug, where drug comprises genipin-1- beta -D gentiobioside glycoside as active ingredient.    USE - Iridoid glycoside in the form of tablet, capsules, granules, water injection, powder, freeze-dried powder, sprays or suppositories used as antiviral, antibacterial, antipyretic, antiinflammatory and antioxidant drug for preventing influenza virus, parainfluenza virus, respiratory tract virus, rhinovirus, adenovirus, hepatitis B virus, coxsackie virus, enteric cytopathic human orphan virus, herpes virus, epstein-barr virus, Staphylococcus aureus, Staphylococcus albus, Staphylococcus epidermidis, Streptococcus B, Klebsiella pneumoniae, Streptococcus pneumoniae, catarrhal cocci, Escherichia coli, Pseudomonas aeruginosa and Candida albicans and treating pneumonia, tracheitis, bronchitis, hepatitis, hepatitis B, myocarditis and keratitis (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of iridoid glycoside comprising taking 1 pt. wt. Gardenia, chopping, adding 5-10 pts. vol. 30-60% ethanol, soaking for 0.5-1 hour, carrying out reflux extraction for 1-2 hours, adding 4-8 pts. vol. 30-60% ethanol, extracting for 0.5-2 hours, filtering, concentrating at 40-80 degrees C with pressure of - 9 Pa to recover ethanol, placing extract in macroporous NKA-2 resin, performing elution with 20-50% ethanol where eluent is S-8 macroporous resin, carrying out vacuum recovery of ethanol and treating concentrated liquid with anhydrous alcohol to obtain genipin-1- beta -D gentiobioside glycoside, geniposide and shanzhiside methyl ester based extract.
NOVELTY - Enhancing the lifetime of a solid oxide electrolysis cell system involves counteracting nitridation of the threads of the in-line electrical heaters of the system. The start-up, shut-down and trip operations are done in a humidified nitrogen atmosphere on the fuel side to achieve a dew point of -70 degrees C to 23 degrees C, and in air on the oxygen side or in carbon dioxide on the oxygen side. The oxidizing conditions are always present across the whole surface of the cells on the oxygen side in the stack.    USE - Enhancing lifetime of solid oxide electrolysis cell system used for the production of hydrogen from surplus electricity generated by e.g. wind turbines.    ADVANTAGE - The method can be carried out with low power consumption.
NOVELTY - Production of final product from wastewater dissolved air flotation sludge involves dewatering of sludge (10), aged sludge (20) or pre-processed sludge to produce sludge filter cake (30) and filtrate (23). The pre-processed is sludge or aged sludge that has undergone additional processing before dewatering and aged sludge is sludge that is stored for a period of time. The dewatering step is a mechanical dewatering step carried out at 30 degrees C which forms sludge filter cake that does not flow under its own mass.    USE - Production of final product e.g. feed and feed supplement for animals, fuel and fuel supplement for energy or heat production, from wastewater dissolved air flotation sludge (all claimed) in dairy or meat industry.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) processing plant; and    (2) final product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the process.    Sludge tank (3)    Sludge (10)    Aged sludge (20)    Filtrate (23)    Sludge filter cake (30)
NOVELTY - The utility model claims a new a uniform combustion of biomass gasification furnace, comprising furnace body and furnace cover, a furnace body of outside cylinder and inside cylinder one, the inner cylinder upper end is provided with a feeding port, a furnace cover for sealing the feeding port, the inner cylinder inner cavity is a cavity, the inner tube outside wall and outside cylinder inner wall set with air in between, the inner cylinder upper end is a week wall set with connected the first out gas in the air hole, a cylinder and a lower end provided with an igniter; the inner cylinder between outside wall and outside cylinder inner wall is set with a separating plate 2 more than block, a partition plate for the air cavity is divided into a partition of 2 more than one, also comprising the air outlet structure, a compartment connected the air outlet structure. And the existing technology, this utility new type is a biomass gasification furnace. air flow flow evenly, to make biomass fuel burning full, a raw fuel gas increase conversion efficiency.
NOVELTY - The method for simultaneously increasing methane yield and methane content involves cutting ryegrass into 1-2 cm pieces, mixing sewage plant remaining sludge with ryegrass pieces, adjusting carbon and nitrogen ratio to 9/1-17/1, controlling initial pH of mixture at 4-13 and performing anaerobic digestion at 35-37 degrees C for 20-30 days to produce methane.    USE - The method is useful for simultaneously increasing methane yield and methane content (claimed) in biogas.
NOVELTY - The treatment equipment has liquid phase advection unit (21) which performs advection of the liquid phase to anaerobic fermenter (3) from the solid-liquid-separation tank (2). A diffuser (25) performs aeration of the anaerobic gas with respect to the aeration direction (D) by providing upper end of the partition wall (W23) in the receiving portion side of the liquid phase advection unit. An inhibition mechanism (C) suppresses the advection of the suspended matter (S) between the aeration region (Z1) of the diffuser and liquid phase flow ON regions (Z2) of the transfer unit (M).    USE - Waste water treatment equipment used in home and apartment.    ADVANTAGE - The load of the aerobic treatment in aerobic-treatment tank is made low and the purity degree of the waste water is improved. Since the deposit is efficiently biogas-ized in anaerobic fermenter, the production amount of biogas is increased. The microorganisms in anaerobic fermenter are reliably held in the tank while maintaining the amount of deposits in anaerobic fermenter, and generation of biogas is maintained favorably.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic views of solid-liquid-separation tank and anaerobic fermenter in waste water treatment equipment.    Solid-liquid-separation tank (2)    Anaerobic fermenter (3)    Liquid phase advection unit (21)    Diffuser (25)    Inhibition mechanism (C)    Aeration direction (D)    Transfer unit (M)    Suspended matter (S)    Partition wall (W23)    Aeration region (Z1)    Liquid phase flow ON region (Z2)
NOVELTY - The control method involves measuring the sunshine degree of sunlight with respect to a hydrolyzing module (3) by a sunshine measure (60) of a solar utilization system (1). The hydrolyzing module decomposes electrolyte solution using the solar energy irradiated to an optical semiconductor catalyst. An electrolyte solution circulation unit (40) circulates the electrolyte solution from the exterior with respect to the hydrolyzing module. The circulating load of the electrolyte solution is controlled according to the sunshine degree of the measured sunlight.    USE - Control method of solar utilization system (claimed).    ADVANTAGE - The circulating load of electrolyte solution is controlled to maintain an optimal state of the electrolyte solution around an electrode.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a solar utilization system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the solar utilization system. (Drawing includes non-English language text).    Solar utilization system (1)    Hydrolyzing module (3)    Fuel cell (20)    Electrolyte solution circulation unit (40)    Sunshine measure (60)
NOVELTY - Method (M1) for fractionating lipid, involves subjecting a microbial biomass to extraction using liquefied dimethyl ether as a solvent and then fractionating the lipid utilizing separation selectivity for the lipid.    USE - The method (M1) is useful for fractionating lipid. The method (M2) is useful for modifying fatty acid composition of lipid. The method (M3) is useful for preparing the lipid (all claimed).    ADVANTAGE - The method enables to produce high quality lipids.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for modifying fatty acid composition of lipid; and    (2) method (M3) for preparing the lipid.
NOVELTY - A recombinant yeast capable of producing ethanol is obtained by introducing gene encoding enzyme that metabolizes xylose into xylulose 5-phosphate and disrupts, delete or inactivate Hansenula polymorpha 4 (HAP4) gene, is new.    USE - The recombinant yeast is useful for producing ethanol. The method (M1) is useful for producing ethanol from xylose. The method (M2) is useful for producing ethanol from sugar mixture of glucose and xylose. The method (M3) is useful for producing ethanol from saccharified liquid prepared from lignocellulosic biomass (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for producing ethanol from xylose;    (2) method (M2) for producing ethanol from sugar mixture of glucose and xylose; and    (3) method (M3) for producing ethanol from saccharified liquid prepared from lignocellulosic biomass.
NOVELTY - A bunker coal is obtained by mixing 80-150 pts. wt. wood flour, 5-30 pts. wt. chaff powder and 100 pts. wt. sewage sludge having moisture content of 70-85%, and drying the mixture using hot air until the moisture content is 0.5-10%.    USE - Bunker coal (claimed).    ADVANTAGE - The bunker coal has high calorific value and suppressed sewage odor.
NOVELTY - The utility model claims a used for agriculture and forestry waste catalyze cracking for preparing biological coal biological diesel oil, the fuel gas device, comprises: add material device, device, cyclone dust collector, purifier, gas collector, the add material device mounted at one side pyrolysis device and pyrolysis device A connected with a cyclone dust collector, a cyclone dust remover connecting purifier, fuel gas collector connected with fuel gas pipe, add material device including a feedstock tube, tube. feedstock in a pyrolysis device is one, the feedstock tube equipped with a piston, a piston fixedly connected with a piston rod, the feedstock tube wall face is set with the feedstock at a, upper part is set with a feeding hopper, a storage hopper installed with turning plate. This new utility model can continuous work, no need, eliminating furnace ash, re-add material, ignition, a high efficiency, and the utility model new... raw material, all the dry and wet plant waste are used as a raw material, raw material source is wide, at the same time that of agriculture and forestry waste is a problem, energy saving environmental protection.
NOVELTY - Use of p-phenylenediamine as additive for Annona squamosa oil biodiesel produced by transesterification or pyrolysis process is claimed.    USE - Use of p-phenylenediamine as additive for Annona squamosa oil biodiesel (claimed) for reducing emission of nitrogen oxide in diesel engine.    ADVANTAGE - The diesel engine reduces the emission of nitrogen oxide using p-phenylenediamine.
NOVELTY - Method for producing methane through acidification pretreatment of hydrogen production of food waste and sludge involves pulverizing food waste and sludge after pretreatment to obtain pretreated feedstock, adding sulfuric acid solution to pretreated feedstock to obtain feedstock mixture, performing hydrolysis, adding hydrolyzed product into fermentation tank, performing fermentation and acidification process, adding methanogenic bacteria to acidified product and fermenting product.    USE - The method is useful for producing methane through acidification pretreatment of hydrogen production of kitchen waste and sludge (claimed).    DETAILED DESCRIPTION - Method for producing methane through acidification pretreatment of hydrogen production of food waste and sludge involves pulverizing food waste and sludge after pretreatment in a mass ratio of 1:1 to obtain pretreated feedstock, adding 1% sulfuric acid solution to pretreated feedstock to obtain 20-30 g/l feedstock mixture, performing hydrolysis at 135 degrees C for 15 minutes, adding 200-500 ml hydrolyzed product into 600 ml fermentation tank, and adjusting pH to 6.4-6.6 using 6 mol/l sodium hydroxide, adding 0.2-0.5 g yeast powder into fermentation tank, performing fermentation at 37 degrees C for 20 minutes, performing acidification of fermented product, adjusting pH of acidified product to 7.9-8.1 using 6 mol/l sodium hydroxide, adding methanogenic bacteria to acidified product and fermenting under anaerobic environment at 37 degrees C.
NOVELTY - Purification of biogas involves injecting air or oxygen to biogas comprising methane, carbon dioxide and hydrogen sulfide, introducing biogas enriched with air or oxygen to adsorber comprising impregnated activated carbon which preferentially adsorbs hydrogen sulfide, adsorbing and recovering hydrogen sulfide depleted biogas.    USE - Purification of biogas (claimed).    ADVANTAGE - The method provides purified biogas having high desulfurization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for plant for purifying biogas, which consists of a biogas source, a source of air or oxygen, an adsorber comprising the impregnated activated carbon, gas duct (a) connecting the biogas source to the adsorber, gas duct (b) connecting the source of air or oxygen to the gas line (l1), flow meter located on the line (l1) of the gases upstream of the point where the gas line (l2) joins the gas line (l1) and a control valve provided on the gas line (l2).
NOVELTY - A methanol fuel corrosion inhibitor is obtained by stirring 18-25 %mass methanol, 10-20 %mass sodium hydroxide, 10-20 %mass benzotriazole, 5-12 %mass ethyleneamine, 25-35 %mass n-butanol, and 2-10 %mass polyvinylpyrrolidone.    USE - Methanol fuel corrosion inhibitor (claimed).    ADVANTAGE - The protective film formed using the methanol fuel corrosion inhibitor provides excellent corrosion resistance.
NOVELTY - An efficient thermoelectric chemical hydrogen-production device includes an electrode and an electrolyte. The electrodes are quantum dot-sensitized titanium oxide nanotube array thin film electrode as anode and foamed nickel electrode as counter electrode. The electrolyte is aqueous solution containing sodium sulfate and sodium sulfide.    USE - Efficient thermoelectric chemical hydrogen-production device (claimed).    ADVANTAGE - The efficient thermoelectric chemical hydrogen-production device produces hydrogen having purity of more than 99.9%, by consuming reduced amount of power.
NOVELTY - The production equipment has a separation film unit (200) which separates the bio methane from the neogenesis gas fuel provided by the pre-processor (100). A control unit (500) controls the throttle valve (700) for controlling amount of air supplied to engine operated power generator (400) and controls the fuel control valve (300) for controlling the base methane concentration gas in the methane content supplied to the power generator from separation film unit.    USE - Production equipment for producing bio-methane using electrolytic copper, from food effluent, garbage water, livestock wastewater, industry wastewater or sludge generated in sewage disposal plant, and organic wastewater.    ADVANTAGE - The high purity methane gas can be separated from neogenesis gas fuel and can be used as liquefied nitrogen gas. The low concentration methane gas separated from high purity methane gas can be supplied to the engine operated generator to produce electric power. Thus, stable power generation can be ensured. The refining efficiency of the neogenesis gas fuel can be enhanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for controlling engine operated generator and membrane separation type refining unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the production equipment for producing bio-methane. (Drawing includes non-English language text)    Pre-processor (100)    Separation film unit (200)    Fuel control valve (300)    Engine operated power generator (400)    Control unit (500)    Throttle valve (700)
NOVELTY - The system (10) has a circulation fluid bed incinerator (200) that provides circularly the fluid yarn circulating in the rapid thermal disintegration reaction device (110). A fluid yarn which spreads to the transporter transferring the biomass is accumulated. A blowing unit (240) is classified into first area and second area. The air is provided to the lower portion of the spreader plate (220). The spreader plate is provided to transfer the fluid yarn transferred from the transporter (150) to second area.    USE - Bio-crude-oil manufacturing system.    ADVANTAGE - The circulation efficiency of the fluid yarn is improved, so as to disperse the fluid yarn into the second area from the transporter. The bubble caps are not arranged, and the flow of air is maintained with the upper direction of the spreader plate. The rising of the fluid yarn is induced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-crude-oil manufacturing system.    Bio-crude-oil manufacturing system (10)    Rapid thermal disintegration reaction device (110)    Transporter (150)    Circulation fluid bed incinerator (200)    Spreader plate (220)    Blowing unit (240)
NOVELTY - The utility model is a new supply of a couple of solar energy light heat of high temperature electrolytic water hydrogen......... a can supply a, preparing hydrogen and separating module and storage module, a supply module includes orderly connected with a light collecting device is collecting, a high temperature heat pipe heat exchanger and a heat exchanger, a water steam and hydrogen mixture heating of water and hydrogen mixture and preparing hydrogen and separating module to 800 degrees C more than a, electrolytic separating hydrogen and oxygen. And the existing technology, this utility new type providing the manufacture hydrogen system, no need fossil energy consumption, production process is green environmental protection, and greatly and decrease of power consumption, the supply stable heat source, which solves a photo-thermal system a weather change but not the stable condition, increase of the availability of system, at the same time increase of electrolytic efficiency of system.
NOVELTY - Biomass microwave cracking system comprises a protective gas tank (1), a pressure reducing valve (2), a connecting hose (3), a microwave cracking reactor (4), a thermoelectric couple (5), a condenser and a microwave controller. The protective gas jar is connected to the pressure reducing valve. The reducing valve is set on the connection hose. The hose is connected with the microwave cracking reactor at right side surface. Microwave power within the microwave cracking reactor can adjusted through stepless adjustment. The cracking temperature is adjusted through a thermocouple contact material.    USE - Used as biomass microwave cracking system.    DETAILED DESCRIPTION - Biomass microwave cracking system comprises a protective gas tank (1), a pressure reducing valve (2), a connecting hose (3), a microwave cracking reactor (4), a thermoelectric couple (5), a condenser and a microwave controller. The protective gas jar is connected to the pressure reducing valve. The pressure reducing valve is set on the connection hose. The hose is connected with the microwave cracking reactor at right side surface. Microwave power within the microwave cracking reactor can adjusted to certain range through stepless adjustment. The cracking temperature is adjusted through a thermocouple contact material. The thermoelectric couple is installed on the microwave cracking reactor. The pyrolysis condenser is connected to the upper part of the microwave cracking reactor through the hose. The pyrolysis reaction controller is installed in the microwave cracking reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass microwave cracking system.    Protective gas tank (1)    Pressure reducing valve (2)    Connecting hose (3)    Microwave cracking reactor (4)    Thermoelectric couple (5)
NOVELTY - Fertilizer comprises manures of cats and dogs.    USE - Fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising pouring raw materials into trough or tank; transferring into centrifuge through pipe and into mixing tank that is connected to reservoir containing water or mineral water with neutral pH, mixing 25 wt.% raw materials and 75 wt.% water; centrifugal crushing, sedimenting, disintegrating solid materials to get aqueous mixture; transferring into digester tank with helix or paddle type mixer, cutting programmable thermostat and screw cap, vertical mixing, anaerobic fermenting, setting pressure at 1 kPa, allowing valve to exhaust excess methane during fermentation process, controlling temperature at not greater than 40 degrees C to speed up fermentation to 30-40 days; cooling, filtering and packaging; and separating fertilizer product from waste by decantation.
NOVELTY - Algae strain SS-B1 (culture collection 7479) preserved at China general microbiological culture collection center is new.    USE - Algae strain SS-B1 used for fixing of carbon dioxide and for producing microalgae lipids (all claimed) and for producing biodiesel.    ADVANTAGE - The algal strain SS-B1 tolerates high concentration of carbon dioxide and sulfur dioxide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for breeding algae, which involves:    (A) obtaining a purified algae strain SS-B1;    (B) performing domestication by passing gas to the algae strain SS-B1, which contains carbon dioxide, increasing content of carbon dioxide from 5-40vol.%;    (C) culturing the domesticated algae to obtain pure algae strains;    (D) growing the pure algae strain to logarithm phase, performing domestication by passing mixed gas, which contains carbon dioxide (20vol.%) and sulfur dioxide, increasing content of sulfur dioxide from 50asterisk10-6v/v to 450asterisk10-6v/v; and    (E) culturing the obtained domesticated algae to obtain the desired algae strain SS-B1.
NOVELTY - The utility model claims a U-shaped several section lifting biogas liquid disorder flow beyond the efficient marsh gas generating system, which is composed of a feedstock tube, a discharge pipe, a fermentation pipeline, a feedstock material and a detachable tube and a U type pipe. terminal a fermentation feedstock and a side wall and a side wall extended U-type discharge pipe in fermentation, between a U-type fermentation pipe on top, a feedstock tube between a horizontal place of feedstock with a drain pipe, a water pressure discharge tube connected with a horizontal discharging pipe and drain pipe, a U type pipe is set with fermentation gas-guide tube with the feedstock pipe arrange water pipe set with a control water pressure in a biogas liquid one-way flow into the one-way valve a feedstock tube, a discharging pipe and a lowest position of the horizontal plane is higher than feedstock. drain pipe at the lowest point; the ferment line a, liquid flow stirring notable effect, and promotes a uniform strain distribution.
NOVELTY - The formation apparatus has hydrogen water generating unit (10) that is set with multiple structures (13). A hydrogen generator (30) is combined to main portion (20). The electrode boards (31) are set between hydrogen water generating unit and main portion. A negative electrode board (32) is set with diaphragm plate (33). The water which is injected to inlet port (11) is ejected to a vent (12).    USE - Formation apparatus for hydrogen water used by human.    ADVANTAGE - The structure of the hydrogen water formation apparatus is simplified and apparatus is manufactured easily. The size of the apparatus is reduced. The installation and maintenance management cost are reduced. The leakage of the apparatus is prevented. The concentration of hydrogen is high in the hydrogen water.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the formation apparatus for hydrogen water.    Hydrogen water generating unit (10)    Inlet port (11)    Vent (12)    Structure (13)    Main portion (20)    Hydrogen generator (30)    Electrode board (31)    Negative electrode board (32)    Diaphragm plate (33)
NOVELTY - The anaerobic digestion system has a piston which is fixed in the outside of an air supply pipe (220). The air supply nozzle is formed in the air supply pipe and connected to inner section of an aerobic fermentation tank (200,300). A blower (221) is connected to an air supply pipe for rapidly injecting air into the aerobic fermentation tank. The aerobic fermentation tank is provided for smoothly performing aerobic fermentation of the solid material. The pre-processor (100) is provided with a pulverizing device (110) for mixing and crushing the organic waste.    USE - Anaerobic digestion system for producing methane gas using bulk organic waste such as livestock excretion, food waste, and agricultural by-products.    ADVANTAGE - The thermal transfer efficiency of the aerobic fermentation tank about the anaerobic digester is improved. The methane gas is produced efficiently by using the aerobic fermentation heat of the aerobic fermentation tank. The energy damping according to the operation of the anaerobic digester is minimized. The aerial pressurizing about the aerobic fermentation tank is effectively performed through the piston. The aerobic fermentation efficiency about the solid material supplied in the aerobic fermentation tank is remarkably enhanced. The production rate of the methane gas is increased by promoting the activity of the anaerobe within the anaerobic digester. The solid-liquid separation of the solid material in the aerobic fermentation tank is made quickly and easily. The biological oxygen demand (BOD) of the waste water ejected to the outside is remarkably decreased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the anaerobic digestion system.    Pre-processor (100)    Pulverizing device (110)    Aerobic fermentation tanks (200,300)    Air supply pipe (220)    Blower (221)
NOVELTY - The system is connected to liquefaction rectifying column (540,560). Liquefied carbon dioxide exhaust line ejects liquefied carbon dioxide in lower portion. Carbon dioxide among source gas is liquefied with carbon dioxide liquefaction mood. Screen (564) for separating liquid and weather is installed at inside of liquefaction rectifying column. Liquefaction rectifying column is connected to refrigerator for cooling source gas compacted in compressor (510). The compressor compresses source gas including carbon dioxide separated from biogas in main component.    USE - High purity carbon dioxide liquefaction recovery system of biogas generated from food waste, livestock excretions, organic waste and landfill.    ADVANTAGE - The energy input is minimized and the carbon dioxide of high purity is refined with liquefaction. The height of the liquefaction rectifying column is minimized. The carbon dioxide liquefying device does not use the re-boiler and re-cooler. The methane gas of high purity and carbon dioxide of high purity are together collected from the biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbon dioxide liquefaction refining portion.    Compressor (510)    Liquefaction rectifying columns (540,560)    Nozzle (561)    Screen (564)    Expansion valve (583)
NOVELTY - Upflow sedimentation hydrolysis and two-stage anoxic/oxic biological treatment system comprises connecting upflow hydrolysis sedimentation tank with 50-60 degrees ramp pool, draft tube and vertical mixer and to anoxic tank, aerobic tanks and transition tank through water outlet pipe (19), inserting draft tube to water inlet pipe, connecting rotary shaft of vertical mixer to draft tube and reflection plate (16), connecting bottom mud bucket (13) to sand washer (21) through suction pipe (20) and connecting sand washer (21) to water inlet pipe through fermented liquid return pipe (24) and pump.    USE - Upflow sedimentation hydrolysis and two-stage anoxic/oxic biological treatment system used for treating sewage (claimed).    ADVANTAGE - The system achieves high concentration of sludge fermentation in bottom pool, produces large amount of volatile fatty acids and enhances anaerobic phosphorus release effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment of sewage comprising feeding sewage to upflow hydrolysis sedimentation tank, mixing low-speed stirring at 2 W/m3 power density or high-speed stirring at 4 W/m3 power density, transferring to secondary sedimentation tank with sludge and water ratio at 0-20%, transferring to 80-100% external reflux sludge to anoxic tank, transferring to first aerobic tank, performing anoxic denitrification if effluent has less than 1 mg/L ammonia and less than 13 mg/L nitrogen or performing nitration reaction if effluent has less than 5 mg/L ammonia in transition tank and transferring to second aerobic tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of upflow sedimentation hydrolysis and two-stage anoxic/oxic biological treatment system.    Bottom mud bucket (13)    Reflection plate (16)    Water outlet pipe (19)    Suction pipe (20)    Sand washer (21)    Fermented liquid return pipe (24)
NOVELTY - Processing cow manure dung involves cleaning cow solid manure and excrement through a cleaning plate in a clearing machine. Water is sprayed on cow solid manure and excrement in summer by using a regulating pool, and then entered into solid-liquid separating machine for solid-liquid separation to obtain stack manure and sewage. Sewage of cow is entered into sewage pump and then in slurry pool. Sewage pH value is maintained at 6.8-8, and then carbon and nitrogen ratio are adjusted to 22-28:1. Sewage is dried, crushed and extruded at room temperature to collect urine in dark tube.    USE - Method for processing cow manure dung uses as organic fertilizer or rotten fertilizer and earthworm breeding or mushroom cultivation matrix (all claimed).    DETAILED DESCRIPTION - Processing cow manure dung involves cleaning cow solid manure and excrement through a cleaning plate in a clearing machine. Water is sprayed on cow solid manure and excrement in summer by using a regulating pool, and then entered into solid-liquid separating machine for solid-liquid separation to obtain stack manure and sewage. Sewage of cow is entered into sewage pump and then in slurry pool. Sewage pH value is maintained at 6.8-8, and then carbon and nitrogen ratio are adjusted to 22-28:1. Sewage is dried, crushed and extruded at room temperature to collect urine in dark tube and placed into grid filtering device for filtering. Sewage pump and slurry pool product is placed into anaerobic reactor to carry out anaerobic reaction to reduce organic substance content in the sewage, The sewage is discharged by using temporary storage pool, and carried out marsh gas purification. Anaerobic product is treated into aerobic pool, where biogas is generated after purification, deodorized the product and ammonia is removed.
NOVELTY - Synchronous implementation of sludge dewatering and biological adsorbent yield increasing comprises taking surfactant and sludge, uniformly mixing, aerobically fermenting, press-filtering by plate and frame filter dewatering, belt dewatering or centrifugal dewatering to obtain filter cake which is dewatered sludge and filtrate which is biological adsorbent, and putting filtrate in refrigerator. The surfactant is anionic surfactant, cationic surfactant, non-ionic surfactant, amphoteric surfactant or biological surfactant.    USE - Method for synchronous implementation of sludge dewatering and biological adsorbent yield increasing (claimed).    ADVANTAGE - The method increases yield of biological adsorbent to 1.8-2.7 times and reduces water of sludge to 7.7-15.8%.    DETAILED DESCRIPTION - Synchronous implementation of sludge dewatering and biological adsorbent yield increasing comprises taking surfactant and sludge at dry weight ratio of 0.01-0.3:1, uniformly mixing, aerobically fermenting at 25-55 degrees C, pH of 5-9 and dissolved oxygen concentration of 0.5-6.5 mg/L for 2-24 hours, press-filtering by plate and frame filter dewatering, belt dewatering or centrifugal dewatering to obtain filter cake which is dewatered sludge and filtrate which is biological adsorbent, and putting filtrate in refrigerator at 0-5 degrees C. The surfactant is anionic surfactant, cationic surfactant, non-ionic surfactant, amphoteric surfactant or biological surfactant.
NOVELTY - Preparing compound fertilizer involves pulverizing garbage, and mixing it with coal gangue. Obtained mixture is combusted in kiln, and then mixed with plant growth elements to obtain compound fertilizer.    USE - Method for preparing compound fertilizer (claimed).    ADVANTAGE - The method enables to prepare compound fertilizer that is economic and has good effect.
NOVELTY - Preparing cultivation material involves pulverizing corn cob (46-54%), wood chips (30-38%), bean cake (8-10%), mushroom (3-4%), lime (2.5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water for 18-24 hours, and then corn powder, wood powder and bean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours.    USE - Method for preparing cultivation material (claimed).    ADVANTAGE - The method is eco-friendly, and ensures increased catalytic decomposition and growth of Grifola frondosa.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing corn cob (46-54%), wood chips (30-38%), bean cake (8-10%), mushroom (3-4%), lime (2.5%) and gypsum (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water for 18-24 hours, and then corn powder, wood powder and bean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Obtained material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Preparing cultivation material involves crushing and drying 54-58% sawdust, 16-20% corn core, 16-18% bean cake, 4-5% mushroom, 3-4% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene plastic bag.    USE - Method for preparing cultivation material used for mushroom (claimed).    ADVANTAGE - The method is eco-friendly and saves labor cost, and enables to prepare cultivation material that produce highly active metabolite product of mushroom, and ensures its rapid growth.    DETAILED DESCRIPTION - Preparing cultivation material involves crushing and drying 54-58% sawdust, 16-20% corn core, 16-18% bean cake, 4-5% mushroom, 3-4% lime and 1% gypsum into powder with particle diameter of 3-5mm. Powder is soaked in clean water (20-30 times) for at low temperature 18-24 hours, and then performed piling of product with height of 1.0-1.2m, and width 2-3m to obtain ladder-shaped stack (300-500kg), and then carried out natural fermentation at 60 degrees C for 24 hours. Fermented product is mixed with lime and gypsum and wrapped in polyethylene plastic bag, and inoculated in dark bacterium room and cultured at 18-20 degrees C for 36-38 days.
NOVELTY - Preparing cultivation material involves pulverizing cotton seed hull (56-60%), bagasse (12-18%), soybean (18-20%), mushroom (3-4%), lime (3-4%) and light calcium carbonate (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, bagasse and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin.    USE - Method for preparing cultivation material used for Pleurotus eryngii (claimed).    ADVANTAGE - The method is eco-friendly, saves labor, and ensures increased catalytic decomposition and growth of Pleurotus eryngii.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing cotton seed hull (56-60%), bagasse (12-18%), soybean (18-20%), mushroom (3-4%), lime (3-4%) and light calcium carbonate (1%) to obtain material having size of 2-3mm. Mushroom powder is soaked in water (20-30 times the quantity of mushroom powder) for 18-24 hours, and then cotton seed hull, bagasse and soybean powder are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height of 1-1.2m and diameter of diameter 10-15cm. Vertical hole is created on upper stack of pile by stick. Pile is covered by tarpaulin, and then fermented at 60 degrees C for 24 hours. Lime and light calcium carbonate are added to obtained material, and fermentation is continued for 5-6 days to obtain fermented product having water content of 63-65%. Fermented product is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Preparing cultivation material involves taking cottonseed hull (48-52%), corn cob (24-30%), soybean meal (8-10%), mushroom (3-4%), lime (3-4%), and gypsum (1%), where particle size of corn cob is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, corn cob, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days.    USE - Method for preparing cultivation material used for cultivating Pleurotus geesteranus (claimed).    ADVANTAGE - The method is eco-friendly.    DETAILED DESCRIPTION - Preparing cultivation material involves taking cottonseed hull (48-52%), corn cob (24-30%), soybean meal (8-10%), mushroom (3-4%), lime (3-4%), and gypsum (1%), where particle size of corn cob is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then cottonseed hull, corn cob, and soybean are added to soaked product. Obtained mixture (300-500kg) is piled in heap having height 1-2m and width 2-3m. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with gypsum, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 24-26 days to obtain the final product.
NOVELTY - Preparing cultivation material involves taking sawdust (50-54%), cottonseed hull (26-30%), tea residue (12-14%), mushroom (3-4%), lime (2-3%), and calcium carbonate (1%), where particle size of sawdust is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, cottonseed hull, tea residue, mushroom, and lime are added to soaked product. Obtained mixture (300-500kg) is piled in heap having diameter 10-15cm. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with calcium carbonate to obtain a mixture.    USE - Method for preparing cultivation material used for cultivating Agrocybe cylindracea (claimed).    ADVANTAGE - The method is eco-friendly.    DETAILED DESCRIPTION - Preparing cultivation material involves taking sawdust (50-54%), cottonseed hull (26-30%), tea residue (12-14%), mushroom (3-4%), lime (2-3%), and calcium carbonate (1%), where particle size of sawdust is 3-5mm, and mushroom is 2-3mm. Mushroom powder is soaked in water (20-30 times) for 18-24 hours, and then sawdust, cottonseed hull, tea residue, mushroom, and lime are added to soaked product. Obtained mixture (300-500kg) is piled in heap having diameter 10-15cm. Piled material is fermented at 60 degrees C for 24 hours. Obtained material is mixed with calcium carbonate, and obtained mixture is fermented for 5-6 days. Moisture content of fermented material is 63-65%. Fermented material is packed in polypropylene bag, and inoculated with fungus. Obtained product is kept in dark environment at 18-20 degrees C and 60-75% relative humidity for 22-24 days to obtain the final product.
NOVELTY - Slow release fertilizer comprises 6-11 pts. wt. sodium nitrate, 5-10 pts. wt. ammonium sulfate, 3-7 pts. wt. animal waste, 4-12 pts. wt. calcium superphosphate, 3-9 pts. wt. potassium sulfate, 4-8 pts. wt. traditional Chinese medicine slag, 2-6 pts. wt. shrimp, 2-7 pts. wt. bamboo coal powder, 4-10 pts. wt. microbial inoculum, 3-8 pts. wt. diatomite, 4-10 pts. wt. rotten cattle and sheep excrement, 4-7 pts. wt. edible fungus residue, 3-8 pts. wt. Typhonium giganteum, 4-8 pts. wt. radix aconiti agrestis, 3-9 pts. wt. Celastrus and 5-8 pts. wt. rhizoma arisaematis.    USE - Slow release fertilizer used for gardening plant (claimed).    ADVANTAGE - The slow release fertilizer supplies nutrient to crops for long time, and increases soil fertility.
NOVELTY - Preparing fertilizer involves crushing tobacco waste. The crushed material and chicken manure are mixed uniformly. The obtained mixture is fermented with Bacillus subtilis at 60-65 degrees C for 5-8 days to obtain product.    USE - Method for preparing fertilizer used for planting konjac (claimed).    ADVANTAGE - The method enables to prepare fertilizer that ensures low cost, and reduces tobacco waste and pollution.
NOVELTY - The obtained diazotized aniline diazonium salt solution is added to 2-(methoxymethyl)aniline, coupled at reaction temperature and pH, to obtain azo compound. Azo compound is hydrogenolyzed in presence of a catalyst, to obtain mixed solution of 2-(methoxymethyl)phenyl-1,4-diamine and aniline substance, and catalyst is removed. Predetermined amount of antioxidant is added to mixed solution, steam-distilled to recover aniline aqueous substance, and remaining liquid is bleached, filtered, cooled and crystallized, to obtain 2-(methoxymethyl)phenyl-1,4-diamine.    USE - Preparation of 2-(methoxymethyl)phenyl-1,4-diamine (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of 2-(methoxymethyl)phenyl-1,4-diamine by simple method, with reduced waste discharge.    DETAILED DESCRIPTION - Nitrobenzyl alcohol is methylation-reacted in an aprotic solvent and in presence of a base at predetermined temperature, and methylation reagent is dripped. After completion of the reaction, the reaction mixture is washed, concentrated and dried, to obtain 2-(methoxymethyl)nitrobenzene. 2-(Methoxymethyl)nitrobenzene is hydrogenated in presence of hydrogenation catalyst, and protic solvent, to obtain 2-(methoxymethyl)aniline. Aniline substance is added to aqueous solution of a inorganic acid and diazotized, to obtain diazotized aniline diazonium salt solution. Diazotized aniline diazonium salt solution is added to 2-(methoxymethyl)aniline, coupled at reaction temperature and pH, to obtain azo compound. Azo compound is hydrogenolyzed in presence of a catalyst, to obtain mixed solution of 2-(methoxymethyl)phenyl-1,4-diamine and aniline substance, and catalyst is removed. Predetermined amount of antioxidant is added to mixed solution, steam-distilled to recover aniline aqueous substance, and remaining liquid is bleached, filtered, cooled and crystallized, to obtain 2-(methoxymethyl)phenyl-1,4-diamine.
NOVELTY - The preparation method of vildagliptin involves: (1) acylating chloroacetyl chloride with L-prolinamide to obtain acylated solution; (2) dripping dehydrating agent into acylated solution obtained in step (1) to obtain dehydrated solution, where the dehydrating agent comprises trifluoroacetic anhydride, cyanuric chloride, phosphorus oxychloride or phosphorus pentoxide; and (3) dripping solution of 3-amino-1-adamantanol into dehydrated solution obtained in step (2), and alkylating reaction mixture.    USE - The method is useful for preparing vildagliptin (claimed).    ADVANTAGE - The method allows for simple preparation of vildagliptin with reduced cost and usage of solvent and high yield in an environmentally-friendly manner.
NOVELTY - Production of environment-friendly, energy-saving, and harmless organic fertilizer comprises mixing dairy manure and Asparagus stalk, stirring, adding 1 kg microorganism microbial inoculum, adding into fermentation tank, turning, stirring, and naturally fermenting; carrying out aerobic biochemical degradation, heating at high temperature, cooling, heat preserving, and carrying out post-fermentation; curing, cooling, depositing, turning, decomposing lignin, heat preserving, stacking for 20 days, and compacting; and spreading, drying, crushing, checking quality, and sub-packaging.    USE - Method for producing environment-friendly, energy-saving, and harmless organic fertilizer (claimed).    DETAILED DESCRIPTION - Production of environment-friendly, energy-saving, and harmless organic fertilizer comprises: (A) mixing dairy manure as main material and Asparagus stalk as additive at ratio of 7:3, stirring, adding 1 kg microorganism microbial inoculum, where water content is 50-60%, adding into fermentation tank, turning, stirring, and naturally fermenting; (B) carrying out aerobic biochemical degradation, heating at high temperature, cooling, heat preserving, and carrying out post-fermentation; (C) curing, cooling, depositing for 5 days, turning once every 12 days, where temperature should not exceed 70 degrees C, decomposing lignin, heat preserving, stacking for 20 days at 2.5-3 m high, and compacting at room temperature to + 5 degrees C or + 10 degrees C during winter; and (D) spreading, drying, crushing, checking quality, and sub-packaging.
NOVELTY - Preparing cultivation material involves pulverizing corn cob (54-60%), wood (22-28%), bean cake (12-14%), mushroom (3-4%), monopotassium phosphate (0.1%), calcium superphosphate (0.4%), and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob and wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick.    USE - Method for preparing cultivation material used for Pholiota nameko (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing corn cob (54-60%), wood (22-28%), bean cake (12-14%), mushroom (3-4%), monopotassium phosphate (0.1%), calcium superphosphate (0.4%), and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob and wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Obtained material is mixed with gypsum, calcium superphosphate, monopotassium phosphate, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is packed in polypropylene bags, and fungus is inoculated in bag through hole. Obtained material is kept at 18-20 degrees C and 60-75% humidity for 26-28 days to obtain the final product.
NOVELTY - Preparing cultivation material involves pulverizing corn cob (52-58%), wood (20-24%), bean cake (14-16%), mushroom (3-4%), lime (3-4%) and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob and broadleaf wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C.    USE - Method for preparing cultivation material used for Pholiota nameko (claimed).    ADVANTAGE - The method is eco-friendly, and ensures accelerated catalytic decomposition, and saves labor.    DETAILED DESCRIPTION - Preparing cultivation material involves pulverizing corn cob (52-58%), wood (20-24%), bean cake (14-16%), mushroom (3-4%), lime (3-4%) and gypsum (1%), and then drying obtained pulverized materials. Mushroom powder is soaked in clean water (20-30 times the quantity of raw materials) for 18-24 hours at low temperature. Soaked product is mixed with corn cob and broadleaf wood powder. Obtained mixture (300-500 kg) is piled in heaps having height and width of 1-1.2m and 2-3m respectively. Vertical hole is made in heaps with stick. Heaps are covered with tarpaulin, and fermented at 60 degrees C for 24 hours. Obtained material is turned once in a day. Obtained material is mixed with gypsum and lime, and fermentation is continued for 5-6 days to obtain fermented product having moisture content of 63-65%. Fermented product is packed in polypropylene bags, and hairy fungus is inoculated in bag through hole. Obtained material is kept at 18-20 degrees C and 60-75% humidity for 26-28 days to obtain the final product.