NOVELTY - The new type utility claims anti-seismic full-automatic slag-discharge biomass pool, in orderly set with deslagging, filtering room and pressure in a fermentation pool top, a discharging room and a filtering room adjacent and provided with a first filter plate, filter room and a pressure in adjacent and provided with a filter plate, a filter of the first filter plate diameter greater than a diameter of the second filter filtering plate, provided with anti-vibration beam in a fermentation pool, a shock-proof beam comprises main beam and secondary beam, the secondary beam provided with a pair. The utility model is new type would make old biogas residue from slag discharging pipe and a marsh gas production process, biogas residue entering into deslagging discharged, through a side wall filter room on a filter network and a biogas residue and biogas residue filtering out solid, liquid in flow enter water pressure, is generated marsh gas to rising storage sum room of fermentation pool on part, than the existing marsh gas pool gas quantity multi-30%. The utility model is new type shock resistance, thus can be suitable for mountain area, geological active, earthquake frequent equal area.
NOVELTY - Bio-organic fertilizer comprises 30-40 wt.% fermented product of sludge and garbage, 20-30 wt.% human and animal excreta, 15-20 wt.% fallen leaves, 5-10 wt.% fermentation agent, 2.5-5 wt.% matrine, and 3-5 wt.% abamectin.    USE - The fertilizer is useful for preventing pests (claimed).    ADVANTAGE - The fertilizer: save energy; can be recycled to make energy; provides nutrients to crops; protects the environment; prevents breeding and growth of various pests; and does not cause harm to crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-organic fertilizer, comprising stacking the fermented product of sludge and garbage, human and animal excreta and fallen leaves in a cellar, then adding the fermentation agent, fermenting at 20-30 degrees C environment for 2-3 months under sealed condition, air-drying, and finally adding matrine and abamectin, and granulating into particles.
NOVELTY - Microbial soil conditioner comprises 15-50 wt.% Bacillus mucilaginosus (CICC No.21699), 5-25 wt.% Bacillus stearothermophilus (ATCC No.25177), 10-35 wt.% Lactobacillus plantarum (ATCC No.8014), 10-40 wt.% Streptococcus lactis (ATCC No.19435) and 5-30 wt.% Streptomyces flavoretus (ACCC No.40046).    USE - The microbial soil conditioner is useful for improving soil compaction (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing microbial soil conditioner, comprising: (a) preparing solid culture medium for different strains, sterilizing, aseptically transferring into inclined surface flat plates, inoculating strains and culturing at 27 degrees C for two days; (b) picking the single colony from above culture, then inoculating aseptically into a 50 ml conical flask containing liquid culture medium, culturing at 30 degrees C under 130 rotations/minute for 24-48 hours to obtain primary seed culture; (c) aseptically inoculating primary seed culture into a 500 ml conical flask containing liquid culture medium, culturing at 30 degrees C under 130 rotations/minute for 36-48 hours to obtain secondary seed culture; and (d) mixing the secondary seed culture of different strains, then inoculating 1-5% mixed culture into a fermenter containing fermentation culture medium, culturing at 30 degrees C for 4-7 days until the viable count in fermentation broth reaches 10-15x 108 cells/ml, where the fermentation culture medium comprises 50-100 g/l glucose, 20-100 g/l sucrose, 1-5 g/l cheese peptone, 1-5 g/l potassium dihydrogen phosphate, 1-5 g/l urea, 5-20 g/l dipotassium hydrogen phosphate, 5-20 g/l magnesium sulfate heptahydrate, 15-20 g/l sodium chloride, 5-20 g/l ammonium sulfate and balance of distilled water with a pH of 6-8.
NOVELTY - Waste oil production biodiesel oil continuous esterification technique comprises e.g. taking waste oil, catalyst, and methanol, passing through metering pump into continuous esterification reactor (1) and carrying out continuous esterification reaction, discharging, entering material into water-containing methanol separator (2), separating excess amount of methanol and water generated in material, entering into methyl alcohol rectifying tower (3), continuously entering material into a continuous catalyst separator (4), and separating catalyst and carrying out trans-esterification.    USE - The method is useful for waste oil production biodiesel oil continuous esterification (claimed).    ADVANTAGE - The method can make acid value reach about 2 mg potassium hydroxide (KOH)/g, is easy to manage, and implements continuous production.    DETAILED DESCRIPTION - Waste oil production biodiesel oil continuous esterification technique comprises (i) taking waste oil, catalyst, and methanol, passing through metering pump into continuous esterification reactor (1) and carrying out continuous esterification reaction, and discharging, and (ii) continuously entering step (i) resulting material into aqueous methanol separator (2), separating excess amount of methanol and water generated in material, then entering into methyl alcohol rectifying tower (3), continuously entering material into a continuous catalyst separator (4), and separating as catalyst and carrying out tran-sesterification reaction to obtain trans-esterification material.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the waste oil production biodiesel oil continuous esterification technique (Drawing includes non-English language text).    Esterification reactor (1)    Aqueous methanol separator (2)    Methyl alcohol rectifying tower (3)    Continuous catalyst separator (4)    Sewage workshop (5)
NOVELTY - The method involves collecting combustible solid particle. The gas is conveyed. The solid particles with conveying combustible gas is separated. The combustible solid particles are combusted. The non-oxidizing gas or gas mixture is conveyed. The nitrogen gas, carbon dioxide, oxygen, carbon monoxide, hydrogen, methane and sulfur are set to preset range.    USE - Flammable solid particle combustion method.    ADVANTAGE - The non-oxidizing gas or gas mixture is conveyed, so that efficient transport of particulate matter is achieved, operating cost is reduced and the safety is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the flammable solid particle combustion process. (Drawing includes non-English language text)
NOVELTY - Inorganic filler suspension comprises montmorillonite powder, fly ash, activated carbon, biological bacterial sludge, sodium silicate, foaming agent, titanium dioxide sol, and water.    USE - The inorganic filler suspension is useful for processing sewage (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the inorganic filler suspension, which involves taking montmorillonite powder, fly ash and activated coal in stirrer, adding water to the stirrer, stirring added materials, slowly adding sodium silicate, uniformly stirring added materials, adding titanium dioxide sol, foaming agent and biological bacterium sludge to obtained mixture, uniformly stirring the materials, and incubating mixture for 24 hours.
NOVELTY - Stiff silkworm excrement bio-organic fertilizer comprises 60-80 pts. wt. stiff silkworm excrement fermentation product, 10-20 pts. wt. leaves leavening product, 30-50 pts. wt. rice bran leavening product, 1-3 pts. wt. animal excrement fermentation product, and 15-20 pts. wt. rice water.    USE - Used as stiff silkworm excrement bio-organic fertilizer.    ADVANTAGE - The bio-organic fertilizer: has simple preparation process, low cost and high fertilizer efficiency; is suitable for soil conditioning; activates soil microorganisms to overcome soil compaction; increases soil air permeability; reduces water loss and evaporation; reduces stress and drought; reducing salinity damage; reduces fertilizer dosage; can achieve the large requirement of crop nutrients; and achieves high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the stiff silkworm excrement bio-organic fertilizer, comprising stirring uniformly the above mentioned components, subjecting to high-temperature sterilization at 60-80 degrees C environment, and then granulating into particles to obtain the finished product.
NOVELTY - Special organic fertilizer comprises 20-40 wt.% wheat straw, 40-50 wt.% corn stalk, 35-40 wt.% chicken manure, 5-15 wt.% eggshell, 5-15 wt.% rice water, and balance kelp.    USE - Special organic fertilizer used for plant (claimed) development and growth.    ADVANTAGE - The fertilizer has high organic matter content and abundant nutrients, and makes soil more fertile and ventilation to plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of special organic fertilizer comprising taking wheat straw and corn stalk, cutting, adding remaining raw materials, mixing, placing in sealed environment, maintaining temperature at 30-38 degrees C, reacting for 15-20 days, and drying.
NOVELTY - Leachate collecting device of organic solid waste film type compost fermentation, comprises a main pipe (1) and a timing blower and a leachate collection tank connected with the main pipe. The top portion rows of the main pipe are axially spaced with multiple discharge guide grooves (2). The top of the discharge guide groove is provided with a top closure plate (3). Top closure plate has a width of less than discharge guide groove. Top closure plate is formed with an aperture (4).    USE - Used as leachate collecting device of organic solid waste film type compost fermentation.    ADVANTAGE - The device has simple structure, and is economical, easy to maintain and assemble.    DETAILED DESCRIPTION - Leachate collecting device of organic solid waste film type compost fermentation, comprises a main pipe (1) and a timing blower and a leachate collection tank connected with the main pipe. The top portion rows of the main pipe are axially spaced with multiple discharge guide grooves (2). The top of the discharge guide groove is provided with a top closure plate (3). Top closure plate has a width of less than discharge guide groove. Top closure plate is formed with an aperture (4). Both the sides of the top closure plate are provided with curved side plates (5). The top closure plate is connected with side plate by the main pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the leachate collecting device of organic solid waste film type compost fermentation.    Main pipe (1)    Discharge guide groove (2)    Top closure plate (3)    Aperture (4)    Side plate (5)
NOVELTY - Special compound fertilizer comprises clay, calcium superphosphate, rice bran fermented material, magnesium sulfate, and potassium dihydrogen phosphate.    USE - Special compound fertilizer used for rice (claimed).    ADVANTAGE - The method is simple, has fast fertilizer efficiency and low cost, and increases rice yield to 20-30%. The fertilizer is rich in nutrient and organic matter and can be quickly absorbed by soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fertilizer comprising taking clay, calcium superphosphate, rice bran fermented material, magnesium sulfate, and potassium dihydrogen phosphate at weight ratio of 20:13:12:5:3, air drying, mixing, crushing, sterilizing at 90-150 degrees C, granulating, and processing.
NOVELTY - The method involves arranging an air resistance plate between the adjacent fermentation areas to produce biogas and accumulating in the inlet/outlet pipes. The methane fermentation is carried out inside a drain pipe (52) when stored. The pressure is stored within a primary fermentation biogas inflow conduit through a front conduit (32) and a rear conduit (34). The pressure stored within the primary conduit is flowed into a secondary fermentation biogas inflow conduit. The methane is produced using biogas.    USE - Method of promoting multistage pressure disturbance fermentation device for producing methane.    ADVANTAGE - The biogas fermentation efficiency is high, the convection effect is improved, and the fermentation raw material is used at a lower rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the primary fermentation system.    Primary fermentation system (10)    Front conduit (32)    Rear conduit (34)    Secondary fermentation system (40)    Drain pipe (52)
NOVELTY - Method for preprocessing and performing anaerobic fermentation of corn straw, involves selecting corn straw, natural drying obtained corn straw, crushing the corn straw using crusher to obtain powder having 20 mesh size, adding 2 wt.% sodium hydroxide and 2-10 wt.% ammonia to the powder, preprocessing obtained mixture at -20 degrees C to 20 degrees C, sealing the mixture for 3 days, adding water and ammonium hydroxide to obtained mixture, adding 6 times water to the mixture, stirring and sealing the mixture, and performing anaerobic fermentation at -20 degrees C for 3 days.    USE - The method is useful for preprocessing and performing anaerobic fermentation of corn straw (claimed).    ADVANTAGE - The method is environmentally-friendly to perform.    DETAILED DESCRIPTION - Method for preprocessing and performing anaerobic fermentation of corn straw, involves selecting corn straw, natural drying obtained corn straw, crushing the corn straw using crusher to obtain powder having 20 mesh size, adding 2 wt.% sodium hydroxide and 2-10 wt.% ammonia to the powder, preprocessing obtained mixture at -20 degrees C to 20 degrees C, sealing the mixture for 3 days, adding water and ammonium hydroxide to obtained mixture, adding 6 times water to the mixture, stirring and sealing the mixture, and storing the mixture and performing anaerobic fermentation at -20 degrees C for 3 days. The anaerobic fermentation is performed by adding the mixture to apparatus charged with nitrogen, sealing the apparatus with rubber stopper, and shaking obtained product at 35 plus minus 2 degrees C.
NOVELTY - The utility model is new type relates to fertilizer production device, specifically relates to one plant for urea formaldehyde slow-controlled release fertilizer production of reactor. Including in reaction chamber, reaction chamber set with formaldehyde solution, urea inlet and discharging mouth is set with stirring device, middle shell and the reaction chamber provided with heat exchange jacket, inside said heat exchange jacket provided with spiral shape of rising channel; the stirring device comprises stirring shaft and power shaft transmission is connected with the motor and blade deflection direction is mounted on stirring shaft on the upper agitator blade, lower agitator blade, the agitator blade and upper blade and lower agitator blade opposite the top part of said reaction chamber set with reaction chamber and each lumen connected the air outlet, the air outlet through pipeline connected with condenser; The utility model is new type reactor can recovery the steam in formaldehyde in production process, reducing to pollute the environment in production process, and process stirring reaction is more complete, uniform, the raw material using rate high, low energy consumption.
NOVELTY - A fungi residue treating method involves mixing 60-80 wt.% mushroom, 10-30 wt.% poultry manure, 10 wt.% EM fungus liquid to obtain mixture. The mixture is naturally fermented for 10-15 days. The water content of the fermented mixture is regulated to 60-70% to obtain bait material. The bait material is paved on an earthworm bed, followed by planting 1 kg seedling in every square meter of earthworm bed, feeding earthworm with one time, maintaining the thickness of the bait material at 0.15-0.2 m after every time, collecting the earthworm manure, adding bait material, and catching earthworms.    USE - Method for treating fungi residue for planting organic agricultural products.    ADVANTAGE - The method enables treating fungi residue with improved vigor and fertility of earthworm, and effect of degrading bacteria slag.    DETAILED DESCRIPTION - A fungi residue treating method involves mixing 60-80 wt.% mushroom, 10-30 wt.% poultry manure, 10 wt.% EM fungus liquid to obtain mixture. The mixture is naturally fermented for 10-15 days. The water content of the fermented mixture is regulated to 60-70% to obtain bait material. The bait material is paved on an earthworm bed, followed by planting 1 kg seedling in every square meter of earthworm bed, feeding earthworm once in every 15-20 days with one time, maintaining the thickness of the bait material at 0.15-0.2 m after every time, collecting the earthworm manure, adding bait material for 10 times, and catching earthworms.
NOVELTY - A feed comprises 49.5-52.5 wt.% corn, 13-12 wt.% soybean meal, 15-6 wt.% konjac, 13-17 wt.% bagasse, 6-9 wt.% Jerusalem artichokes, 1.5 wt.% microbial additives, and 2 wt.% premix. The microbial additives are Bacillus natto, Bacillus coagulans, Lactobacillus, Bacillus subtilis, and Enterococcus faecalis at weight ratio of 1:6-8:1-5:3-7:1-2. The content of each strain is greater than 1x 108 cfu/g.    USE - Feed used for deodorizing pig manure (claimed).    ADVANTAGE - The feed increases ability to regulate pig large intestine flora and activity of liver enzymes, reduces large intestine skatole production, promotes liver skatole degradation, improves quality of pork, and reduces in vitro pollution of skatole.    DETAILED DESCRIPTION - A feed comprises 49.5-52.5 wt.% corn, 13-12 wt.% soybean meal, 15-6 wt.% konjac, 13-17 wt.% bagasse, 6-9 wt.% Jerusalem artichokes, 1.5 wt.% microbial additives, and 2 wt.% premix. The microbial additives are Bacillus natto, Bacillus coagulans, Lactobacillus, Bacillus subtilis, and Enterococcus faecalis at weight ratio of 1:6-8:1-5:3-7:1-2. The content of each strain is greater than 1x 108 cfu/g. The feed is prepared by mixing soybean meal, bagasse, Jerusalem artichokes, 1.5% corn, and 1% microbial additive, mixing, adding water until moisture content is 40%, sealing, fermenting for 5-8 days, adding premix and remaining corn and microbial additive, and mixing.
NOVELTY - Coal gangue selenium activation comprises crushing coal gangue mineral sample, sieving over 80-100 mesh sieve, and grinding unscreened gangue to obtain coal gangue powder; drying coal gangue powder at 60-70 degrees C; making mass volume ratio of coal gangue powder to solution of nitric acid at 1:40 g/ml-1:5 g/ml; adding the dried coal gangue powder to 15-20 vol.% nitric acid solution, and stirring into the reaction vessel, sealing the reaction vessel and controlling the reaction vessel at 80-85 degrees C, reacting for 1.5-3.5 hours, and cooling to room temperature.    USE - Method for coal gangue selenium activation (claimed).    ADVANTAGE - The method is simple, energy-saving, and environment-friendly, and has low cost.
NOVELTY - A composting system comprises feeding robot, breaking roller, permanent magnetic separator, winnowing machine, pulverizer, steam ejection type organic garbage disposer, roller type dryer cylinder scalping sieve, and organic fertilizer production device. The steam-type organic garbage processor comprises system frame, pressure ejection device, feeding lifting device, discharge guide tube, and superheated separator.    USE - Composting system.    ADVANTAGE - The system has high garbage processing amount and strong operability. It is green and environment-friendly.    DETAILED DESCRIPTION - Composting system comprises feeding robot, breaking roller, permanent magnetic separator, winnowing machine, pulverizer, steam ejection type organic garbage disposer, roller type dryer cylinder scalping sieve, and organic fertilizer production device. The feeding robot is connected with breaking roller sieving machine inlet. A bag-breaking sieving machine exit roller is connected with permanent magnetic separator inlet. A permanent magnetic separator outlet is connected with machine inlet. The winnowing machine is connected with steam-type organic garbage disposer. The steam-type organic garbage disposal machine is connected with roller type drier inlet. The roller type drier outlet is connected with cylinder scalping sieve inlet. The cylinder scalping sieve is connected with organic fertilizer production device. The steam-type organic garbage processor comprises system frame, pressure ejection device, feeding lifting device, discharge guide tube, and superheated separator.
NOVELTY - Organic fertilizer is prepared by taking organic phosphate fertilizer as phosphate mineral powder raw material and Polygonum cuspidatum as organic acid raw material at 90-120:1 weight ratio.    USE - Organic fertilizer used for organic and green agriculture production.    ADVANTAGE - The organic fertilizer uses natural plant as raw material, does not add chemical synthetic substances, and has simple preparation using less equipment requirements and with no waste discharge.
NOVELTY - Dewatered sludge increased rotten degree biological electrochemical auxiliary anaerobic composting device comprises anaerobic compost chamber (1), electrochemical electrode chamber (2) and electric appliance (3). The anaerobic compost chamber is installed with inner shell (1-1) at center position, graphite brush electrode (1-2), reference electrode (1-3), temperature measuring probe (1-4) and collecting opening (1-5). The electrochemical electrode chamber has inner shell (2-1) and second graphite brush electrode (2-2) as electrochemical electrode.    USE - Dewatered sludge increased rotten degree biological electrochemical auxiliary anaerobic composting device.    ADVANTAGE - The device achieves compost maturity for 35-40 days and 28-30% increase of rotten degree than the prior art.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operation of dewatered sludge increased rotten degree biological electrochemical auxiliary anaerobic composting device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of dewatered sludge increased rotten degree biological electrochemical auxiliary anaerobic composting device.    Anaerobic compost chamber (1)    Inner shell of anaerobic compost chamber (1-1)    Graphite brush electrode (1-2)    Reference electrode (1-3)    Temperature measuring probe (1-4)    Collecting opening (1-5)    Electrochemical electrode chamber (2)    Inner shell of electrochemical electrode chamber (2-1)    Second graphite brush electrode (2-2)    Electric appliance (3)
NOVELTY - A yam cultivation substrate preparation involves mixing calcium superphosphate, diatomaceous earth and medical stone, calcining, grinding, mixing with nutrient solution, immersing, filtering, mixing watermelon rind, wheat bran, potato flour, and black hull, adding water, boiling, adding amylase, adjusting pH value with hydrochloric acid, hydrolyzing, mixing kelp flour and chestnut leaves, crushing, adding water, adding dry poultry manure, egg shell powder, calcium superphosphate, and polyphenols, fermenting, mixing enzyme solution and broth, slowly adding porous filler, and naturally drying.    USE - Method for preparing yam cultivation substrate (claimed).    ADVANTAGE - The method has high product yield. The product increases biological conversion rate, and has strong stress resistance.    DETAILED DESCRIPTION - A yam cultivation substrate is prepared by mixing calcium superphosphate, diatomaceous earth and medical stone at weight ratio of 1:2:5, calcining at 430-460 degrees C 2.5-3 hours, grinding into powder, cooling to room temperature, mixing with nutrient solution, immersing for 2-3 hours, filtering, drying to obtain porous filler, standing, mixing watermelon rind, wheat bran, potato flour, and black hull at weight ratio of 2:3:3:2, adding water at weight ratio of 1:5-6, boiling into thick paste, adding amylase, cooling at 76-78 degrees C, adjusting pH value with hydrochloric acid to 5-6, hydrolyzing at constant temperature for 45-50 minutes to obtain enzyme solution, mixing kelp flour and chestnut leaves at weight ratio of 3:5, crushing, adding water at weight ratio of 1:6-8, stirring, adding 32-34 wt.% dry poultry manure, 8-12 wt.% egg shell powder, 2-3 wt.% calcium superphosphate, and 0.4-0.6 wt.% polyphenols, sealing, fermenting for 7-8 days to obtain broth, mixing enzyme solution and broth at weight ratio of 3:2, slowly adding porous filler, and naturally drying for 2-3 days under humidity of 15-18%.
NOVELTY - A disodium 2,2'-dihydroxy-4,4'-dimethoxy-5,5'-disulfobenzophenone is prepared by taking 1-6C halogenated alkane into sulfonation kettle, adding 2,2'-dihydroxy-4,4'-dimethoxybenzophenone, heating at 70-75 degrees C, slowly dropping amino acid, extracting, adding ammonia, incubating at 70-75 degrees C for 2 hours, insulating, cooling to 15-20 degrees C, slowly dropping sodium hydroxide solution, cooling, precipitating to obtain crystals, cooling to room temperature, centrifuging, adding ethanol, stirring, heating at 40 degrees C for 0.5 hour, cooling, and centrifuging.    USE - Method for preparing disodium 2,2'-dihydroxy-4,4'-dimethoxy-5,5'-disulfobenzophenone (claimed).    ADVANTAGE - The method is easy to control, simple, non-polluting, low-cost, and environment-friendly. The product has high purity.
NOVELTY - Vitamin B6 intermediate 4-methyl-5-alkylsiloxane-based oxazole compound (I) is new.    USE - Compound (I) used for highly-selective preparation of vitamin B6 (claimed).    ADVANTAGE - The method has short process steps, easy operation, little wastewater, good reaction selectivity, low production cost and high product purity, and is safe, environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Vitamin B6 intermediate 4-methyl-5-alkylsiloxane-based oxazole compound of formula (I) is new.    R1-R3=methyl, isopropyl or tert-butyl.    INDEPENDENT CLAIMS are included for:    (1) preparation of compound (I); and    (2) highly-selective preparation of vitamin B6 including subjecting compound (I) and 2-methoxypropyl-1,3-dioxa-5-cycloheptene to addition reaction, hydrolyzing in aqueous alcohol solution, and adding hydrochloride salt to prepare vitamin B6.
NOVELTY - Biomass solid fuel particle comprises 20-50 pts. wt. crop straw, 10-20 pts. wt. mushroom stick, 10-15 pts. wt. pig manure, 10-20 pts. wt. wood chips, 10-20 pts. wt. corn cob, 5-10 pts. wt. carbon rock, 1-2 pts. wt. potassium chloride, and 1-5 pts. wt. combustion improver.    USE - Biomass solid fuel particle.    ADVANTAGE - The biomass solid fuel particle has fuel feedstock reasonable compatibility, thus effectively avoiding problem of single raw material demand that is not easy to collect, while improving molding rate, moisture effect, and durability of fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass solid fuel particle by drying material to moisture content of 15-18%; crushing material into particle size of less than 5 mm; granulating crushed material into certain diameter elongated rod with rod length of 10-50 mm; extruding at 90-150 degrees C; cooling extruded material through countercurrent air cooler; screening particles; recycling particle with greater sizes; packaging particles that meet certain size requirement; and storing.
NOVELTY - The cell has sewage entrance (1) whose upper portion is provided with a pre-distribution room (2). A liquid distribution plate (3) is provided in fluidization bed portion (5) whose lower portion is provided with fluidization particle (15). A positive electrode (14) is vertically positioned inside the fluidized bed portion. The top portion of fluid bed portion is provided with a sealing cap (8). The distance between the anode electrode (13) and the cathode is 10-20 mm. A stainless steel wire net is connected to outside of anaerobic fluidization bed portion through flange.    USE - Sewage treatment microbial fuel cell used in industrial application.    ADVANTAGE - The cost of the fuel cell is reduced, the high performance of the fuel cell is achieved and operation reliability of the cell is improved, the sewage treatment efficiency is improved, the sewage treatment speed is improved, and the production of electric power is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment microbial fuel cell.    Sewage entrance (1)    Pre-distribution room (2)    Liquid distribution plate (3)    Fluidization bed portion (4)    Sealing cap (8)    Anode electrode (13)    Positive electrode (14)    Fluidization particle (15)
NOVELTY - Production of calcium superphosphate comprises mixing concentrated phosphoric acid sludge and phosphogypsum slag acidic wastewater, adding calcium powder and reacting for 15-90 minutes, drying, sieving, and packaging. The weight ratio of concentrated phosphoric acid sludge and phosphogypsum slag acidic wastewater is 4-8:1. The weight ratio of concentrated phosphoric acid sludge and calcium powder is 3-4:1.    USE - Method for producing calcium superphosphate (claimed).    ADVANTAGE - The method converts waste into valuable product and improves utilization rate of phosphorus, produces high-quality calcium superphosphate product, has low cost, and is environment-friendly.    DETAILED DESCRIPTION - Production of calcium superphosphate comprises mixing concentrated phosphoric acid sludge and phosphogypsum slag acidic wastewater, adding calcium powder and reacting for 15-90 minutes, drying, sieving, and packaging. The concentrated phosphoric acid sludge has total phosphorus pentoxide (P2O5) content of 20-30%, soluble P2O5 of 15-20%, and moisture content of 40-60%. The phosphogypsum slag acidic wastewater has P2O5 content of 2-5%, fluorine content of 0.3-1%, and sulfate content of less than or equal to 0.4%. The calcium powder is limestone having calcium oxide content of greater than or equal to 90%. The weight ratio of concentrated phosphoric acid sludge and phosphogypsum slag acidic wastewater is 4-8:1. The weight ratio of concentrated phosphoric acid sludge and calcium powder is 3-4:1.
NOVELTY - Soil additive comprises degraded soybean straw and composite microbial preparation comprising Phanerochaete, Trichoderma koningii, Paracoccus denitrificans, Rhodococcus and filamentous bacteriae in ratio of 1-3:2-8:3-8:1-3:2-8.    USE - Soil additive used as biofertilizer (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil additive, which involves:    (A) cutting soybean straw into pieces of 10-30cm;    (B) mixing straw with composite microbial preparation;    (C) adding water (30-40% of the amount of straw) to obtained mixture; and    (D) fermenting obtained mixture for 2-3 days to obtain soil additive.
NOVELTY - Carbon enriched additive is prepared by performing fermentation of rape stalk and vegetable straw by adding composite microorganism. Composite microorganism comprises Bacillus licheniformis, Aspergillus niger, Escherichia coli, Trichoderma reesei and filamentous bacterium in ratio of 1-4:3-6:1-5:3-6:2-8.    USE - Carbon enriched additive used for preparing biological fertilizer (claimed).    ADVANTAGE - The carbon enriched additive promotes crop growth and development, enhances cold resistance, drought resistance, diseases resistance and stress resistance, and improves yield and quality of plant products, and soil physical and chemical properties.
NOVELTY - Green water soluble fertilizer is prepared by utilizing 1000-1500 pts. wt. pine needle, 700-900 pts. wt. sugar, 500-700 pts. wt. lees, 600-1000 pts. wt. wheat, 600-800 pts. wt. diamine and 3500-4200 pts. wt. water.    USE - Green water soluble fertilizer.    ADVANTAGE - The green water soluble fertilizer is safe and eco-friendly, ensures disease-resistant property, improves soil microecological environment and soil fertility, promotes growth of crop root, stem, leaf and fruit, increases yield and quality of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing green water soluble fertilizer, which involve:    (A) spreading sheet (3-5 cm) of pine needle and wheat under bamboo and drying naturally;    (B) cutting the sheet by using a cutter into small sections and then grinding through 100 meshes by using a pulverizer into powder;    (C) mixing powder with sugar, lees and bean straw in warm water and fermenting at 30-45 degrees C for 5-7 days; and    (D) mixing remaining components with fermented product, and then sterilizing in ultraviolet and ozone and filling.
NOVELTY - Fertilizer synergist comprises borax (100 g/Kg), zinc sulfate (190 g/Kg), ferrous sulfate (180 g/Kg), maggnesium sulfate (100 g/Kg), copper sulfate (50 g/Kg ), calcium sulfate (150 g/Kg), urease inhibitor (30 g/Kg), Bacillus subtilis (20 g/Kg), Bacillus cereus (30 g/Kg), carboxyl salt (20 g/Kg) poly-aspartic acid (28 g/Kg), aluminum-magnesium mineral salts (30 g/Kg), potassium nitrophenolate (16 g/Kg), DA-616 g/Kgrams, ABT rooting powder 10 g/Kg.    USE - Fertilizer synergist.    ADVANTAGE - The fertilizer synergist ensures reduced doasge of fertilizer and rate of volatilization of fertilize, and improved crop yield.
NOVELTY - A biological enzyme preparation comprises 50-70 pts. wt. biological enzyme, 80-120 pts. wt. nutrient salt and balance mixed microbial agent. The mixed microbial agent has viable count of not less than 3.7 billion colony forming unit (cfu) of microbial strains per gram of enzyme preparation.    USE - Biological enzyme preparation used in aerobic stage process of municipal and industrial wastewater treatment (claimed).    ADVANTAGE - The biological enzyme preparation can fast improve municipal and industrial wastewater treatment process and increase aerobic bacteria density to degrade pollutants in sewage and to reduce sludge production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biological enzyme preparation, comprising adding biological enzyme and mixed microbial agent to obtain mixture, then adding mixture with nutrient salt, drying at 10-15 degrees C to water content of 1-1.5% to obtain the biological enzyme preparation.
NOVELTY - Refined multifunctional organic fertilizer comprises 15-25 pts. wt. waste sludge of alcohol, 15-25 pts. wt. waste leftovers of monosodium glutamate, 4.5-5.5 pts. wt. chicken excrement, 4.5-5.5 pts. wt. pig excrement, 4.5-5.5 pts. wt. phosphorus ore powder, 35-51 pts. wt. crop straw powder, 4.5-5.5 pts. wt. potassium feldspar powder, and 0.5-1 pts. wt. ferment bacteria.    USE - Used as refined multifunctional organic fertilizer.    ADVANTAGE - The organic fertilizer overcomes of the problems of traditional composting process, where considerable part of the organic carbon is oxidized into carbon dioxide to comes out, which causes environmental pollution, resulting in the loss of organic carbon, converts nitrogen to ammonia to outflow and causes heavy loss of nutrition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the refined multifunctional organic fertilizer, comprising (i) selecting raw materials, and processing, (ii) controlling carbon and nitrogen content in the fermented materials, and controlling water content, (iii) adding the ferment bacteria to control pH of compost fermentation, and (iv) fermenting for specific time.
NOVELTY - Plant material organic fertilizer comprises 30-40 pts. wt. fermented plant straw and leaves, 25-30 pts. wt. corn cob, 20-30 pts. wt. chicken manure fermented product, 15-20 pts. wt. calcium-magnesia phosphate fertilizer and 10-15 pts. wt. lysine.    USE - Used as plant material organic fertilizer.    ADVANTAGE - The fertilizer has quick effect, does not no pollute, has high nutrient value, can make energy recycling, can increase growing speed of crop, can maintain high quality of crops, can develop crop root, branches and leaves, is good for health of human body, and can increase the utilization rate of the energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing plant material organic fertilizer comprising uniformly stirring the raw materials, reacting for 4-5 days at below 25-30 degrees C, then stirring uniformly, drying, then compressing into granule shape, or directly using.
NOVELTY - Vegetable organic fertilizer comprises 30-40% leaves, 25-50% vegetable waste, 5-10% ammonium chloride, and 5-10% potassium additive.    USE - Used as vegetable organic fertilizer.    ADVANTAGE - The organic fertilizer is natural and non-polluting, high nutrient value, increases the vegetable growing speed, maintains the color and luster of vegetable, and increases the utilization rate of the energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the vegetable organic fertilizer, comprising stirring the mentioned components, covering tightly with a plastic film, placing in a closed environment at 20-30 degrees C for 5-8 days, when the temperature reaches 40 degrees C, stirring once every 3-5 days, and in the decaying stage, crushing the waste.
NOVELTY - Organic fertilizer comprises 30-40 pts. animal manure fermented product, 20-30 pts. vegetable waste, 15-20 pts. algae fermentation product, 10-20 pts. urea, 10-15 pts. potassium sulfate, 8-10 pts. diammonium phosphate and 3-5 pts. anti-cropping agent.    USE - The organic fertilizer is useful for garlic plant (claimed).    ADVANTAGE - The organic fertilizer is natural and economical, produces high quality garlic by increasing yield up to 20-30%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer, comprising crushing the raw materials, covering tightly with a plastic film, reacting at 20-35 degrees C for 2-3 days, air-drying, pelletizing and administering on garlic plant during planting period of garlic clove growing period.
NOVELTY - Multifunctional vegetables foliar fertilizer comprises 20-30 parts bean cake, 3-5 parts humic acid, 2-3 parts nitrogen, potassium and phosphorus solution mixture, 5-10 parts aqueous solution of rare earth element fertilizer, 0.3 parts Bacillus thuringiensis and 0.5 parts black fungus.    USE - Multifunctional vegetables foliar fertilizer used for killing Plutella xylostella.    ADVANTAGE - The multifunctional vegetables foliar fertilizer has insecticidal property, and applicable to prepare plant medicine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing multifunctional vegetables foliar fertilizer, which involves:    (A) mixing components, and then fermenting at 30-4o degrees C for 3-5 days; and    (B) stirring fermented product uniformly to obtain final product.
NOVELTY - Organic fertilizer, comprises 25-50 % cotton straw, 20-30% human and animal excreta, 15-20% leaves, 10 ml emamectin benzoate, 20-30 ml imidacloprid, 25 ml carbosulfan and 2-3 % livestock and poultry excrement rotten agent.    USE - The organic fertilizer is useful for preventing cotton bollworm (claimed).    ADVANTAGE - The organic fertilizer provides rich nutrition for the crops, improves soil manure, physical properties of soil, soil structure, soil fertility, and provides fertile land for next cultivation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising cutting cotton straw and leaves into 1-2 cm long, mixing uniformly cotton straw, human and animal excreta, leaves and livestock and poultry excrement rotten agent, fermenting under closed environment for 20-30 days, adding emamectin benzoate, imidacloprid and carbosulfan, and mixing uniformly.
NOVELTY - Ethanol fuel production involves pre-processing collected waste and old cotton clothes with 2-8%sodium hydroxide solution at 20-40 degrees C for 2-3 hours, and then washing with water. The washed clothes are dried after removing zipper, button and other attachment. The treated cotton clothes are acidified with diluted acid solution at 85-95 degrees C, and then treated with an oxidizing agent for 7-12 days. The formed mixture is filtered by using filter screen.    USE - Method for producing ethanol fuel (claimed).    ADVANTAGE - The method produces the ethanol fuel in a simple, cost-effective and eco-friendly manner by using waste and old cotton clothes.    DETAILED DESCRIPTION - Ethanol fuel production involves pre-processing collected waste and old cotton clothes with 2-8%sodium hydroxide solution at 20-40 degrees C for 2-3 hours, and then washing with water. The washed clothes are dried after removing zipper, button and other attachment. The treated cotton clothes are acidified with diluted acid solution at 85-95 degrees C, and then treated with an oxidizing agent for 7-12 days. The formed mixture is filtered by using filter screen, where the solution is hydrolyzed to obtain glucose solution. The obtained glucose solution is neutralized by using sodium hydroxide solution, and then fermented by using carbon source in a fermentation tank to obtain fuel alcohol.
NOVELTY - Drying ginseng extract involves vacuum belt drying of ginseng extract at speed of 160- 200mm/minute, where heating plate temperature is kept 90-100 degrees C and feed rate is maintained at 15-25 l/hours.    USE - Method for drying ginseng extract (claimed).    ADVANTAGE - The method enables to mild dry ginseng extract in a cost-effective and eco-friendly manner.
NOVELTY - The device comprises a cylinder housing whose top surface is designed as a semispherical, a platform, cone, sphere, ellipsoid, and mutual combination of geometrical shape. The bottom surface of the cylinder housing is provided with a material discharging pipe for discharging the material through a three-way pipe opening valve. The bottom surface is provided with a seal door with pedestrian ladder. A hollow double spiral hot liquid tube is formed of an air inlet hole provided with an external heat source for heating biogas liquid.    USE - Plastic structured anaerobic device mounted in spiral radiating heater.    ADVANTAGE - The biogas production efficiency of biogas liquid is greatly increased and the time and cost saving are achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the plastic structured anaerobic device mounted in spiral radiating heater.    Discharge port switch valve (2)    Insulation layer (3)    Wall (4)    Corridor (5)    Biogas outlet (7)
NOVELTY - Anaerobic reactor with rubber line structure comprises a device body as a cylinder. A gas storage tank is set at the top of the reactor.    USE - Used as an anaerobic reactor with rubber line structure.    ADVANTAGE - The anaerobic reactor: utilizes an internal warming device, an internal stirring device and an auto-alarm; reduces the construction cost; and increases the methane production efficiency of biogas slurry.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the anaerobic reactor with rubber line structure.
NOVELTY - The steel concrete structure anaerobic device has device main portion that is provided with a cylinder. Top portion of device main portion is provided with semi-spherical sum storage cabinet (6) and bottom portion is provided with material discharging pipe which is provided with three-way pipe opening valve in turn. A pedestrian ladder is arranged at the bottom of can sealing door (15). A heat separate layer is arranged at the device main portion.    USE - Anaerobic device for steel concrete structure.    ADVANTAGE - The external phase is connected in order to supply heat source. The biogas production efficiency of biogas liquid can be greatly increased. The time and cost can be saved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of anaerobic device for steel concrete structure.    Port switch valve (1)    Insulating layer (3)    Semi-spherical sum storage cabinet (5)    Marsh gas outlet (7)    Can sealing door (15)
NOVELTY - Preparation of organic fertilizer involves mixing dried chicken manure and active humic acid, adding to mill, crushing, spraying decomposing agent to resultant product, screening, retaining undersize product, sterilizing and deodorizing.    USE - Preparation of organic fertilizer (claimed).    ADVANTAGE - The method enables preparation of organic fertilizer by simple, economical, environmentally-friendly and environmentally-friendly process, with reduced energy consumption, within short period of time.
NOVELTY - Extraction of hesperidin and synephrine from Citrus aurantium involves crushing C.aurantium, extracting C.aurantium, obtaining C.aurantium extract, concentrating the resultant product, obtaining concentrated cream, separating hesperidin and synephrine from the resultant product, purifying hesperidin, filtering ionized synephrine, collecting filtrate containing synephrine ions, extracting filtrate, removing impurities, obtaining acid solution, back extracting free molecules of synephrine, crystallizing, and refining synephrine.    USE - Extraction of hesperidin and synephrine from C.aurantium (claimed).    ADVANTAGE - The method enables environmentally-friendly extraction of hesperidin and synephrine from C.aurantium with reduced wastewater discharge, by conserving resource.
NOVELTY - A fracturing fluid comprises 0.2-0.4 wt.% cationic surfactant, 0.1-0.15 wt.% salicylate, 1- 1.5 wt.% potassium chloride, 0.06 wt.% pH regulator and 0.06-0.08 wt.% anti-residue agent, and remainder of water. The total amount of all components is 100 wt.%. The cationic surfactant is chosen from cetyltrimethylammonium chloride, octadecyltrimethylammonium chloride and tetramethyl sulfamide.    USE - Fracturing fluid is used for cleaning low-temperature coal bed methane reservoir (claimed).    ADVANTAGE - The fracturing fluid enables cleaning of coal bed methane reservoir at low-temperature of 15-30 degrees C.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of cleaning fracturing fluid; and    (2) usage of fracturing fluid for cleaning coal bed methane reservoir at low temperature of 15-30 degrees C.
NOVELTY - Microorganism products are produced from agricultural solid waste that are fermented by yellow Brevibacterium which is preserved under preservation number CCTCC NO. M2013087 in Wuhan China Type Culture Collection center on March 15, 2013.    USE - Microorganism products for reducing soil alkalinity of saline shoal and synthesizing glumatic acid.    ADVANTAGE - The microorganism products reduce pH value of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microorganism products, which involves:    (A) inoculating Brevibacterium CCTCC NO: M2013087 into a liquid seed culture medium, where culture medium temperature is 37 degrees C, shaking speed is 150 revolutions per minute, incubation time is 24 hours, seed bacteria is greater than 1x 109 colony-forming units per gram;    (B) inoculating seed to fermentation tank to obtain liquid fermentation culture medium, where cultivation temperature is 28-33 degrees C, dissolved oxygen ventilating amount is 30-100 wt.%, speed is 150-220 revolutions per minute, Brevibacterium broth unit is 1x 109 colony-forming units per gram;    (C) mixing 90-100 parts vinegar, 18-20 parts corn core powder,5-5.5 parts ammonium sulfate, 0.5-1 parts dipotassium phosphate and 0.25 parts magnesium sulfate and sterilizing at 100-110 degrees C for 30 minutes;    (D) cooling to room temperature to obtain 5 vol.% Brevibacterium broth;    (E) incubating at 30-35 degrees C incubation, turning solid fermentation medium every 3-5 days to obtain solid;    (F) fermenting for 15-20;    (G) adding 0.5 wt.% pure solid citric acid;    (H) uniformly mixing and keeping stable for 2-3 days;    (I) adding 30-35 vol.% obtained product to the fermented compost and vinegar; and    (J) drying at low temperature to obtain 30% moisture and 5.5 pH value of microorganism products.
NOVELTY - The method involves introducing the fermentation raw material from the feedstock pipe (10) into U-type fermentation pipeline (30), so as to produce marsh gas. The marsh gas is discharged through the discharge pipe (20). The marsh gas is made to pass through the water pressure chamber (40) before discharging. The circulation of marsh gas slurry is performed in the fermentation cell, so that the marsh gas is continuously produced by promoting the circulation of slurry.    USE - Marsh gas generating method.    ADVANTAGE - The fermentation path can be increased so that the marsh gas fermentation process can be performed easily without manual intervention. The operation difficulty of the fermentation device can be reduced. The fermentation efficiency of the fermentation system can be increased and uniform distribution of strain can be achieved. The assembling of the system can be simplified. The manufacturing cost of the system can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of the marsh gas generating system.    Feedstock pipe (10)    Discharge pipe (20)    U-type fermentation pipeline (30)    Water pressure chamber (40)    Cloth bacteria device (50)
NOVELTY - Invention relates to field of biotechnology and deals with method of separating mixture of DNA and proteins from epimastigote forms of strain TPAP/MX/2002/Albarrada of Trypanosoma cruzi culture. Characterised method includes obtaining biomass of said strain culture, with further washing of obtained biomass, its concentration to content of not less than 6 x 108 cells in 1 ml, introduction of synthetic preparation of human defensin alpha -1.    USE - Medicine.    ADVANTAGE - Invention makes it possible to obtain product with reduced content of protein components and can be used in further obtaining of preparations.2 cl, 2 ex    DETAILED DESCRIPTION - Invention relates to field of biotechnology and deals with method of separating mixture of DNA and proteins from epimastigote forms of strain TPAP/MX/2002/Albarrada of Trypanosoma cruzi culture. Characterised method includes obtaining biomass of said strain culture, with further washing of obtained biomass, its concentration to content of not less than 6 x 108 cells in 1 ml, introduction of synthetic preparation of human defensin alpha -1 with molecular weight 3.4 kDa into obtained concentrated biomass in amount 20 mcg/ml to its final concentration 3.97 mcM and exposure until pores are formed in lipid membranes. After that obtained suspension is shaken by shaker with further exposure at room temperature for not less than 24 hours, with the following centrifuging obtained medium with separation of mixture of DNA and proteins in liquid phase.
NOVELTY - Preparation of biomass carbonized molding material involves pulverizing natural biomass material to size of 100 mesh, adding 55-90 wt.% clay to 10-45 wt.% obtained powder, mixing uniformly to obtain a mixture, mixing 5-30 wt.% water, stirring, mold-pressing, drying to moisture content of 8% or less, demolding and sealing at 800-1300 degrees C for 0.5-10 hours under anaerobic conditions by smoldering process.    USE - Preparation of biomass carbonized molding material for purifying air and water.    ADVANTAGE - The method enables preparation of biomass carbonized molding material with excellent mechanical strength, without affecting the environment.
NOVELTY - A manganese carbonate-glycerol-zinc solid base catalyst is obtained by mixing manganese chloride and zinc chloride, adding potassium carbonate solution at 50-70 degrees C, washing resulting mixture, filtering, drying manganese carbonate/zinc oxide precipitate, immersing manganese carbonate/zinc oxide precipitate in glycerol, heating resulting mixture to 150-180 degrees C, stirring for 2-6 hours, washing with methanol, and drying. The molar ratio of manganese ion and zinc ion in manganese chloride and zinc chloride is 1:1.    USE - Manganese carbonate-glycerol-zinc solid base catalyst is used for producing biodiesel.    ADVANTAGE - The manganese carbonate-glycerol-zinc solid base catalyst provides biodiesel which can effectively suppresses the loss of manganese carbonate-glycerol-zinc, when used repeatedly.
NOVELTY - Microbial composting method involves crushing food waste, adding microbial materials, charging fumes, stirring for predetermined time to obtain a bio-organic fertilizer and maintaining at constant temperature.    USE - Microbial composting method (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composting apparatus.
NOVELTY - A subsurface flow wetland system comprises water distribution area (2), purification area (3), catchment area (4), water inlet pipe (1), and water outlet pipe (5) in which purification area comprises sulfur/limestone mixed matrix (31), gravel matrix (32), and zeolite matrix (33).    USE - A subsurface flow wetland system for increasing sewage treatment plant tail water nitrogen and phosphorus removal.    ADVANTAGE - Subsurface flow wetland system increases sewage treatment plant tail water nitrogen and phosphorus removal and does not cause biological blocking.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of subsurface flow wetland system.    Water inlet pipe (1)    Water distribution area (2)    Purification area (3)    Catchment area (4)    Water outlet pipe (5)    Sulfur/limestone mixed matrix (31)    Gravel matrix (32)    Zeolite matrix (33)
NOVELTY - Producing biogas involves mixing raw material wood, bran or bamboo with lime and water, where the obtained mixture is soaked in dealkalization performing tank for 16-20 days. The dealkalized bamboo mixture is pulverized to prepare bamboo slurry. The prepared bamboo slurry is formulated with hydro-alcoholic solution, and then heated at 280-290 degrees C. The bamboo slurry is then subjected into fermentation tank to carry anaerobic fermentation for 11-13 or 15-17 days till all of the floating raw material sink into the fermentation tank.    USE - Method for producing biogas from bamboo (claimed).    ADVANTAGE - The method enables to produce biogas from bamboo, in an efficient manner. The remaining liquid as a by-product during bio-gas production is utilized as plant fertilizer.    DETAILED DESCRIPTION - Producing biogas involves mixing raw material wood, bran or bamboo with lime and water, where the obtained mixture is soaked in dealkalization performing tank for 16-20 days. The dealkalized bamboo mixture is pulverized to prepare bamboo slurry. The prepared bamboo slurry is formulated with hydro-alcoholic solution, and then heated at 280-290 degrees C. The bamboo slurry is then subjected into fermentation tank to carry anaerobic fermentation for 11-13 or 15-17 days till all of the floating raw material sink into the fermentation tank. The fermentation broth is mashed and then introduced into the distillation device comprising distilled ethanol, and then heated at definite temperature to collect distillate. The obtained distillate is filtered by filtration to collect raffinate from which the resultant residue is removed. The collected raffinate is mixed with mold and a condensing agent to produce biogas along with remaining liquid. The produced biogas with remaining liquid is passed through biogas slurry dewatering machine.
NOVELTY - Preparing volatile organic compound involves collecting sewage. Bacterial inoculum is added into culture medium and then fermented to obtain fermentation culture, where culture medium comprises erythritol, ammonium nitrate, potassium dihydrogen phosphate, disodium hydrogen phosphate, yeast extract, magnesium sulfate, oil and balanced quantity of water.    USE - Method for preparing volatile organic compound (claimed) for treating waste water.    ADVANTAGE - The method enables to preparing volatile organic compound that has wide applications.
NOVELTY - Ochrobactrum anthropi SH14 strain is preserved at China center for type culture collection under preservation number (CCTCC NO: M2013681), and is new.    USE - Ochrobactrum anthropi SH14 strain used for degrading pesticide residues i.e. ethoxyethyl ester found in water body and soil and for degrading prepared azoxystrobin formulations (all claimed).    ADVANTAGE - The Ochrobactrum anthropi SH14 strain protects ecological environment and human health by degrading ethoxyethyl ester in a short time, and thus performs the environment-friendly role in a cost-effective manner. Ochrobactrum anthropi SH14 strain, thus solves the agricultural production problem caused by high levels of pesticide residues, in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for growing Ochrobactrum anthropi SH14 strain, which involves inoculating 5-10% Ochrobactrum anthropi SH14 strain seed culture medium into fermenter containing fermentation culture medium, and then performing fermentation at 30 degrees C and 200-250 revolutions per minute for 48 hours to obtain Ochrobactrum anthropi SH14 strain cells.
NOVELTY - Artificial cultivating of Pleurotus ostreatus using coffee ground mixed culture material, comprises adding specific ratio of coffee grounds into the Pleurtus ostreatus culture material, mixing the material, bagging, sterilizing, spawn running, and fruiting management to obtain fruiting bodies.    USE - The method is useful for artificial cultivating of Pleurotus ostreatus using coffee ground mixed culture material (claimed).    ADVANTAGE - The method realizes recycling of coffee ground waste, reduces energy consumption, realizes environmentally friendly, ecological and circulating mode, produces high quality product, reduces cost and is more suitable for Pleurotus ostreatus mushroom stalk production phase (claimed).
NOVELTY - Method of cultivating organic Dendrobium involves (a) selecting and crushing water absorbent rock, mixing with lime and sterilizing for 15 hours, and rinsing and drying rock, (b) fermenting sheep manure, heating, and anaerobically fermenting using EM liquid, (c) mixing crushed rock and fermented sheep manure to obtain a culture matrix, (d) soaking sawdust in biogas water aerobically and spraying on irrigated matrix, (e) spraying purified mountain spring water, and (f) installing UV light for destroying insects.    USE - Method of cultivating organic Dendrobium (claimed).    DETAILED DESCRIPTION - Method of cultivating organic Dendrobium involves (a) selecting good water absorbent rock, crushing to particles of less than 1 cm, mixing with lime in a ratio of 1:2 and sterilizing for 15 hours, rinsing with water, and drying, (b) fermenting sheep manure as a fertilizer, heating at 125-128 degrees C for 30-35 minutes to kill harmful bacteria, carrying out anaerobic fermentation using EM liquid at 35-40 degrees C and humidity of 45-50% for 3-4 days, (c) mixing the crushed rocks and fermented sheep manure in a ratio of 1:1 to obtain a culture matrix, (d) soaking sawdust in biogas water in a ratio of 5:2 aerobically for 8-10 days, and spraying once every 10 days on irrigated matrix, (e) spraying purified mountain spring water every 3 days on irrigated matrix, and (f) installing UV light at the top of frame to destroy insects and insecticidal plant.
NOVELTY - A terpenylphenolic compound is new.    USE - New terpenylphenolic compound used as antileishmanial agent (claimed).    ADVANTAGE - The terpenylphenolic compound has high order of antileishmanial activity. Synthesis of the terpenylphenolic compound is simple, economically feasible, environmentally friendly, and easily processable.    DETAILED DESCRIPTION - A terpenylphenolic compound of formula (A) is new.    R=C9H13, when R2 and R3 represent H and R1 and R4 represent OH, C9H13 when R2 and R4 represent H and R1 and R3 represent OH, C4H7, when R2 and R3 represent H and R1 and R4 represent OH, C14H23, when R2 and R3 represent H and R1 and R4 represent OSO3Na, C9H15, when R2 and R3 represent H and R1 and R4 represent OSO3Na, C9H15, when R2 and R4 represent H and R1 and R3 represent OSO3Na, or C9H15, when R3 and R4 represent H and R1 and R2 represent OSO3Na.    An INDEPENDENT CLAIM is included for preparation of terpenylphenolic compound of formula (A).
NOVELTY - Synthesis of liquid methane and coproducing methanol purge gas comprises purging methanol in heat exchanger (1), controlling reactor temperature at 430-480 degrees C and pressure at 3-5 MPa using electric heater (2), reacting with nickel catalyst and hydrogen in methane reactor (3), reducing gas temperature to 400-420 degrees C, continue cooling heat exchanger, feeding gas in waste heat boiler (4), cooling to 320-3540 degrees C, cooling to 140-160 degrees C; and cooling using water cooler (5) to 20-50 degrees C, isolating methane, and purifying cryogenic liquid methane.    USE - Method for synthesizing liquid methane and coproducing methanol purge gas (claimed).    ADVANTAGE - The safe and environment-friendly method ensures comprehensive recovery, save energy, and reduces consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of liquid methane synthesis and methanol purge gas coproduction device (Drawing includes non-English language text).    Heat exchanger (1)    Electric heater (2)    Methane reactor (3)    Waste heat boiler (4)    Water cooler (5)
NOVELTY - Separation of butane and butene involves adding gas comprising 4C olefin feedstock to lower portion of absorption tower, adding acetonitrile solvent comprising dissolved silver or dispersed silver into absorption tower, separating butane gas as absorption tower top distills and olefin-rich phase as bottom fraction, analyzing bottom fraction, processing separated solvent, separating mixture comprising butane gas and carbon olefin as top distills, recovering acetonitrile from bottom fraction and recycling acetonitrile to absorption tower.    USE - Separation of butane and butene (claimed).    ADVANTAGE - The method enables separation of butane and butene having high purity and stability, with reduced energy consumption.    DETAILED DESCRIPTION - Separation of butane and butene involves adding gas comprising 4C olefin feedstock to lower portion of absorption tower, adding acetonitrile solvent comprising 0.01 wt.% dissolved silver or dispersed silver into absorption tower, separating butane gas as absorption tower top distills and olefin-rich phase as bottom fraction, adding bottom fraction to analytical column, analyzing, adding separated solvent to upper portion of absorption tower, adding overhead fraction to acetonitrile tower, separating mixture comprising butane gas and carbon olefin as top distills and mixed solution comprising N,N-dimethylformamide and acetonitrile as bottom fraction, recovering acetonitrile and recycling acetonitrile to absorption tower.
NOVELTY - Detecting bluetongue virus 16 (BTV16) comprises amplifying a target gene through reverse transcriptase (RT)-PCR using specific primer pair and a fluorescently labeled probe.    USE - The method is used for detecting BTV16.    ADVANTAGE - The method for detecting BTV16 has high specificity, sensitivity, and efficiency, and is simple, rapid and environment-friendly.    DETAILED DESCRIPTION - Detecting BTV16 comprises amplifying a target gene through RT-PCR using specific primer pair and a fluorescently labeled probe, where the primer pair comprises an upstream primer BTV16-L2-1585F: gctccaatgtttaatgcaaaagtg and a downstream primer BTV16-L2-1705R: ttaacagatcgatacaatccgcac, and the probe comprises BTV16-L2-1622PB: tcgagttagcgcaacgaaagaatgaagac.
NOVELTY - Detecting apple stem grooving virus (ASGV) comprises performing real-time quantitative PCR on the test sample using ASGV-Probe-F and ASGV-Probe-R as primers and ASGV-Probe.    USE - The method is used for detecting ASGV.    ADVANTAGE - The method for detecting ASGV has high specificity and is environment-friendly.    DETAILED DESCRIPTION - Detecting ASGV through real-time PCR comprises (a) exposing the cDNA template to ASGV-cp-F and ASGV-cp-R primers and performing PCR amplification, performing agarose gel electrophoresis on PCR products, connecting the obtained sequence with a vector, transforming the competent cells with the vector, selecting positive clones and obtaining positive recombinant plasmid standards; (b) performing real-time quantitative PCR using ASGV-Probe-F and ASGV-Probe-R as primers and ASGV-Probe; and (c) obtaining Ct values and comparing the results with standard values, where ASGV-cp-F, ASGV-cp-R, ASGV-Probe-F, ASGV-Probe-R and ASGV-Probe respectively comprises gggcttcacaggcaatcag, agagtggacaaactctagac, agatttggaggatcgacttgtca, ctcgttcaaagagttctgcctaga, and ttgtccctgaattgaaaacctttgctgc (SEQ ID NO: 1-5), given in the specification.
NOVELTY - An oxidation catalyst comprises solid tin-zirconium metal oxide composite (I) obtained using mixture comprising 50-70 wt.% tin dioxide, 15-40 wt.% zirconium dioxide and remainder of stabilizer oxide precursor. The molar ratio of tin and zirconium in the catalyst is 1.1.    USE - Oxidation catalyst is used for catalytic exhaust aftertreatment of natural gas powered vehicle.    ADVANTAGE - The method enables preparation of oxidation catalyst by simple and economical process.    DETAILED DESCRIPTION - An oxidation catalyst comprises solid tin-zirconium metal oxide composite of formula: Sn1-xZrxM0.1O2 (I), where M is rare-earth metal and x is coefficient, obtained using mixture comprising 50-70 wt.% tin dioxide, 15-40 wt.% zirconium dioxide and remainder of stabilizer oxide precursor. The molar ratio of tin and zirconium in the catalyst is 1.1. An INDEPENDENT CLAIM is included for preparation of oxidation catalyst.
NOVELTY - Device comprises sheep shed, water supply equipment, and feeding equipment. The device comprises a sheep manure accumulation pond, the sheep shed is adjacent to the sheep manure accumulation pond, terrain of the sheep manure accumulation pond is lower than that of the sheep shed, so that the sheep manure can be conveniently collected through the flow by gravity so as to carry out sheep manure accumulation, the sheep shed and the sheep manure accumulation pond are connected through an open trench or an underground concealed conduit.    USE - The device is used for breeding sheep and producing sheep manure (claimed).    DETAILED DESCRIPTION - Device comprises sheep shed, water supply equipment, and feeding equipment. The device comprises a sheep manure accumulation pond, the sheep shed is adjacent to the sheep manure accumulation pond, terrain of the sheep manure accumulation pond is lower than that of the sheep shed, so that the sheep manure can be conveniently collected through the flow by gravity so as to carry out sheep manure accumulation, the sheep shed and the sheep manure accumulation pond are connected through an open trench or an underground concealed conduit, and the bottom of the sheep shed is made of nodular cast iron. An INDEPENDENT CLAIM is included for method for breeding sheep and producing sheep manure, which involves arranging adjacent combined facilities for sheep breeding and sheep manure production, performing existing sheep breeding in the shed, and collecting the sheep manure in the accumulation pond.
NOVELTY - Method for producing biofuel, involves (a) crushing marine algae to obtain marine algal powder, (b) adding acid catalyst and acidic solvent to the marine algal powder, and performing thermal hydrolysis at 100-150 degrees C for 30 minutes-1 hour, (c) regulating pH of obtained hydrolyzate using acid catalyst, (d) adding enzyme to the hydrolyzate for producing monosaccharides, (e) culturing microorganism, and (f) fermenting monosaccharides using the microorganism to obtain product.    USE - The method is useful for producing biofuel. The biofuel is chosen from methanol, ethanol, propanol, butanol and acetone (all claimed).
NOVELTY - The device has a soaking tank (1) that is located above a spray pipe group (4) comprising vertical spray pipe and transverse spray pipe. The vertical spray pipe is connected to middle portion of the soaking tank. Multiple spray holes are uniformly distributed in the spray pipe group. A water inlet pipe (8) is connected with main water pipe (11) through spray pipe group. A water pipe (2) is provided to open and close a water discharge valve (3). A control valve (7) is provided to control the water injection amount from a water pump (8).    USE - Device for soaking corncob for use in food factory.    ADVANTAGE - The time taken for soaking the corncob is reduced. The energy consumption needed for the soaking device is reduced. The uniformity of soaking the corncob is enhanced within short time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for soaking corncob.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for soaking corncob.    Soaking tank (1)    Water discharging pipe (2)    Water discharge valve (3)    Spray pipe group (4)    Water inlet pipe (8)    Main water pipe (11)
NOVELTY - Biogas pool comprises pre-processing pool (1), dregs filter (2), inlet (3), fermentation tank (4), hydraulic room (5), pumping feed pump (6), warming reflux pool (7), feed fluid return line (8), solar water heaters (9), day window seat (10) and movable lid, inspection hole (11), windpipe (12), overflow spout (13), discharging outlet (14). The pre-processing pool is present in forefront of the digester and the inlet is provided between the dregs filter. Bottom of the inlet is connected to discharge end of the fermentation tank, which is connected to the feed end.    USE - Biogas pool.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas pool.    Pre-processing pool (1)    Dregs filter (2)    Inlet (3)    Fermentation tank (4)    Hydraulic room (5)    Pumping feed pump (6)    Warming reflux pool (7)    Feed fluid return line (8)    Solar water heaters (9)    Day window seat (10)    Inspection hole (11)    Windpipe (12)    Overflow spout (13)    Discharging outlet (14)
NOVELTY - Production of fuel ethanol involves hydrolyzing waste residue from brewing, and performing fermentation process.    USE - Production of fuel ethanol (claimed).    ADVANTAGE - The method provides fuel ethanol by environmentally-friendly process.
NOVELTY - Preparation of polyurethane foam immobilized microbe involves ultrasonically dispersing and mixing polyester polyol, triethanolamine, water, methyl silicone oil, dibutyltin dilaurate and ground graphite felt powder, adding diphenylmethane diisocyanate, foaming, obtaining polyurethane foam, washing with distilled water, preparing lysogeny broth culture medium, providing the polyurethane foam into the culture medium, sterilizing, cooling, then inoculating an immobilized microbe which is Stenotrophomonas maltophilia strain T-8 in resultant product, and washing with distilled water.    USE - Preparation of polyurethane foam immobilized microbe used in treatment of azo dye sewage.    ADVANTAGE - The method enables effective preparation of polyurethane foam immobilized microbe having macroporous reticular structure, and high specific surface area. The polyurethane foam immobilized microbe enables effective decolorization of azo dye.    DETAILED DESCRIPTION - Preparation of polyurethane foam immobilized microbe involves ultrasonically dispersing and mixing polyester polyol, triethanolamine, water, methyl silicone oil, dibutyltin dilaurate and ground graphite felt powder for 5-10 seconds, adding diphenylmethane diisocyanate, stirring until whitening for 3-5 seconds, naturally foaming for 24 hours, obtaining polyurethane foam, washing with distilled water, drying, preparing lysogeny broth culture medium, providing the polyurethane foam into the culture medium, sterilizing, cooling, then inoculating an immobilized microbe which is Stenotrophomonas maltophilia strain T-8 in resultant product, shaking at 120-140 rpm and 25-35 degrees C for 3-5 days, and washing with distilled water.
NOVELTY - Method for controlling acidity and alkalinity in dry anaerobic fermentation of straws, involves (a) crushing straws, (b) adding sodium hydroxide solution to the crushed straw, uniformly stirring the mixture and pretreating the mixture to obtain mixture having crystallinity smaller than 0.39, (c) adding crude protein powder to the pretreated straw, uniformly adding water and adjusting total solid content in the mixture, and (d) subjecting the obtained mixture to dry anaerobic fermentation at 35-40 degrees C.    USE - The method is useful for controlling acidity and alkalinity in dry anaerobic fermentation of straws (claimed).    ADVANTAGE - The method is simple, produces fermented straws which is rich in nutrients, and prevents organic acid accumulation.
NOVELTY - Preparing mash involves preprocessing crop straws with steam and then Saccharomyces cerevisiae and cellulase to obtain mixture. The mixture is hydrolyzed and then fermented to obtain mash. Saccharomyces cerevisiae is cultured in corn mash and hydrolyzed sugars to obtain activated Saccharomyces cerevisiae culture. Saccharomyces cerevisiae culture is fermented in corn mash and hydrolyzed sugars to obtain expanded culture and high quantity of sugar solution. Cellulase is added into sugar solution and then hydrolyzed to obtain sugar liquid.    USE - Method for preparing mash (claimed).    ADVANTAGE - The method enables to prepare mesh, that is prepared in simple manner, reduces sugar loss, and improves production efficiency.
NOVELTY - Preparing vanillin involves adding substrate, lipase, and dibasic acid or dibasic acid derivatives are added into reaction kettle and then heating at 20-40 degrees C to obtain mixture. The mixture is filtered to obtain filtrate. The filtrate is diluted using aqueous solution and then extracted with organic solvent to obtain extract. The extract is dried using ethyl alcohol to obtain the product.    USE - Method for preparing vanillin (claimed).    ADVANTAGE - The method enables to prepare vanillin that is prepared in simple manner with 85% yield, and is eco-friendly.
NOVELTY - Preparation of N-2-quinolyl aryl sulfonamide (III) involves reacting arylsulfonamide (I) and quinoline derivative (II) in presence of trivalent compound as oxidizing agent and triarylphosphine compound as additive in organic solvent. The aryl sulfonamide (I) is preferably chosen from methyl benzenesulfonamide, 4-chlorophenyl sulfonamide, 4-nitrobenzenesulfonamide and 4-trifluoromethyl-benzenesulfonamide. The oxidizing agent is preferably chosen from iodobenzene di(trifluoroacetate) and 2-trifiuoroethoxy iodobenzene.    USE - Preparation of N-2-quinolyl aryl sulfonamide used for preparing medicine.    ADVANTAGE - The method enables preparation of N-2-quinolyl aryl sulfonamide by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of N-2-quinolyl aryl sulfonamide (III) involves reacting arylsulfonamide of formula (I) and quinoline derivative of formula (II) in presence of trivalent compound as oxidizing agent and triarylphosphine compound as additive in organic solvent. The aryl sulfonamide (I) is preferably chosen from methyl benzenesulfonamide, 4-chlorophenyl sulfonamide, 4-nitrobenzenesulfonamide and 4-trifluoromethyl-benzenesulfonamide. The oxidizing agent is preferably chosen from iodobenzene di(trifluoroacetate) and 2-trifiuoroethoxy iodobenzene. The triarylphosphine compound is chosen from triphenylphosphine and 4-N-morpholine-diphenyl phosphine. The organic solvent is chosen from ether, benzene, toluene, 1,4-dioxane, dimethyl sulfoxide, N,N-dimethylformamide, methanol, ethanol, 1,2-dichloroethane, butanol, dichloromethane, chloroform, cyclohexane, N-butyl ether, carbon tetrachloride, ethyl acetate, petroleum ether, methyl tert-butyl ether, tetrahydrofuran, acetone and acetonitrile.    R1,R2=not defined.    N.B: R1 and R2 are not defined.
NOVELTY - N-cyclopentyl-1,4,5,6-tetrahydro-2-methoxy-4-methyl-5-acetyl-6-oxo-3-pyridine-carbonitrile and N-(5-(1-piperazinyl)-2-piperidinyl) guanidine are condensed to obtain 6-acetyl-8-cyclopentyl-5-methyl-2-((5-(1-piperazinyl)-2-pyridinyl)amino)-5,6-dihydro-pyrido(2,3-d)pyrimidine-7(8H)-one. 6-Acetyl-8-cyclopentyl-5-methyl-2-((5-(1-piperazinyl)-2-pyridinyl)amino)-5,6-dihydro-pyrido(2,3-d)pyrimidine-7(8H)-one is subjected to dehydrogenation reaction in presence of sodium selenate to obtain palbociclib (I).    USE - Preparation of palbociclib (claimed).    ADVANTAGE - The method provides palbociclib with high efficiency by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - 2-Acetyl-2-butenoate and malononitrile are subjected to cyclization reaction under alkaline conditions to obtain 1,4,5,6-tetrahydro-2-methoxy-4-methyl-5-acetyl-6-oxo-3-pyridine-carbonitrile. 1,4,5,6-Tetrahydro-2-methoxy-4-methyl-5-acetyl-6-oxo-3-pyridine-carbonitrile and halo-substituted cyclopentane are reacted in presence of acid binding agent to obtain N-cyclopentyl-1,4,5,6-tetrahydro-2-methoxy-4-methyl-5-acetyl-6-oxo-3-pyridine-carbonitrile. N-cyclopentyl-1,4,5,6-tetrahydro-2-methoxy-4-methyl-5-acetyl-6-oxo-3-pyridine-carbonitrile and N-(5-(1-piperazinyl)-2-piperidinyl) guanidine are condensed to obtain 6-acetyl-8-cyclopentyl-5-methyl-2-((5-(1-piperazinyl)-2-pyridinyl)amino)-5,6-dihydro-pyrido(2,3-d)pyrimidine-7(8H)-one. 6-Acetyl-8-cyclopentyl-5-methyl-2-((5-(1-piperazinyl)-2-pyridinyl)amino)-5,6-dihydro-pyrido(2,3-d)pyrimidine-7(8H)-one is subjected to dehydrogenation reaction in presence of sodium selenate to obtain palbociclib of formula (I).
NOVELTY - Medicinal composition comprises 10-200 pts. wt. iron, 10-100 pts. wt. cobalt chloride, 5-12 pts. wt. manganese, 1-15 pts. wt. copper, 1-10 pts. wt. zinc oxide, 10-12 pts. wt. nickel chloride, 5-30 pts. wt. ammonium, 10-100 pts. wt. EDTA, and 1-10 pts. wt. hydrochloric acid.    USE - Medicinal composition is useful for increasing anaerobic biological activity of anaerobic bacteria containing methanogenic bacteria under anaerobic conditions, increasing efficiency of gas production, and treating sewage.    ADVANTAGE - The medicinal composition has high efficiency.
NOVELTY - Synthesizing phenylhydrazine comprises adding diluted sulfuric acid in aniline at 0-5 degrees C, dropping ammonium nitrite, and carrying out heat preservation reaction for 4-6 minutes; reducing temperature to - 5 to - 10 degrees C; adding reducing agent with stirring; when the reaction system is increased to 40 degrees C, adding diluted sulfuric acid and adjusting pH to 2-4, heating to 70-100 degrees C, reacting for 4-6 hours; and separating the reaction product to obtain the phenylhydrazine. The mol ratio of aniline to sulfuric acid is 1:1.5-3, and the mol ratio of aniline to ammonium nitrite is 1:0.95-1.1.    USE - Method for synthesizing phenylhydrazine (claimed).    ADVANTAGE - The method is simple and environment-friendly.
NOVELTY - The new type utility claims have one kind can mobile solid oxide fuel cell power generation system, comprising: pile unit, electric unit, combustion system, it comprises burning room, fuel gas supply system, and corresponding fuel gas processing system of the fuel gas supply system, a steam generating system, air supply system, and air treatment system, tail sum circulation use system, exhaust system, machine frame component and panel module, multiple safety assurance and automatic safety alarm system, connected with the electric stack unit is used for connecting the interface load, and set in the I/O interface on the panel component. This utility new type and can provide mobile SOFC power generation system, use modularized design, each system integrated height, reduce have cost, increase have power generation efficiency can be suitable for fuel gas and multi-type plant, increase have.
NOVELTY - The new type utility claims have portable multi-index marsh gas detecting instrument. Multi-index portable methane detection instrument of the instrument box (1), a display screen (2), a charging indication lamp (3), indicating lamp (4), a testing indicator light (5), alarm indicator lamp (6), the first potentiometer (7), the second potentiometer (8), third potentiometer (9), switch (10), power supply switch (11), outside power supply connecting socket (12), sum room cover (13), an air inlet (14), a PH test button (15), a leakage testing function switch (SA2) according to claim 16, testing leakage detection function switch (SA1) according to claim 17, correcting switch (18), sensor lead interface (19) composed of. Inner box is installed can charging power source, circuit plate. The utility model is new type finish have marsh gas in process of using marsh gas methane concentration measure function, marsh gas leakage detect alarm function, marsh gas liquid draining PH value testing, vulcanization hydrogen concentration measure function, anti-explosion power source may ensure the safety of test.
NOVELTY - Preparing N-oxydiethylene-2-benzothiazole sulfonamide (rubber accelerator NOBS), involves mixing sodium chloride and alkaline solution in a reactor, cooling to room temperature, feeding chlorine gas, adding 1% phenolphthalein indicator to the solution to change color of solution from red to yellow, terminating chlorine gas feeding to prepare sodium hypochlorite solution, adding 10% ammonium sulfate, potassium iodide and starch, heating, stirring, cooling, filtering, recovering unreacted raw materials, centrifugally-dehydrating, drying, and packaging.    USE - Preparing N-oxydiethylene-2-benzothiazole sulfonamide (rubber accelerator NOBS) (claimed).    ADVANTAGE - The method enables preparation of N-oxydiethylene-2-benzothiazole sulfonamide (rubber accelerator NOBS) in an economical and environmentally-friendly manner.
NOVELTY - The device has an absorption column (10) comprising a tank (12) and a separation zone (11). A contact unit contacts a gas mixture and a liquid solution by counter current circulation to selectively absorb a gas constituent. The tank receives a volume (16) of absorbing solution. A pipe (19) recovers the separated gas constituent from a second gas constituent. The tank is dimensioned such that cross sectional surface is made to allow downward speed of the solution in the volume to be lower than upward speed of the gas mixture in the volume when the tank contains the volume.    USE - Device for separating a gas constituent e.g. methane, and another gas constituent i.e. carbon dioxide, in a gaseous mixture i.e. biogas (all claimed), to recover the constituents for use in chemical, agricultural or algae production industry.    ADVANTAGE - The device suppresses a leak source of gas mixture in the liquid seal so as to improve output of separation of the gas constituents. The device is manufactured in an inexpensive manner and used and maintained in a simple manner. The device can be installed on same sites in which methanation systems are implanted, and can continuously treat a gas mixture stream issued from the systems.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an absorption column of a separation device.    Absorption column (10)    Separation zone (11)    Tank (12)    Volume of absorbing solution (16)    Pipe (19)
NOVELTY - The new type utility claims have one plant biomass fuel transport system in parallel, comprising of spiral feeder, a large inclination conveyer and the material transport belt is composed of two strip in parallel the transport system, feedstock end large inclination conveyer is set with spiral feeder, the discharging end set for biomass fuel distribution give one strip or two strip feedstock transport belt and electric three-way distributor. Because of formed have transport system is two strip in parallel, when comprising one strip when large inclination conveyer or/and the material transport belt show failure, by electric three-way distributor for biomass fuel switching to another transport device in parallel and for future use, the at least one strip has large inclination conveyer, one strip transport system A trestle strip conveyor and one strip the material transport belt composed of the still can normal operation to ensure the biomass fuel supply lasting give gasification furnace.
NOVELTY - The new type utility claims have one plant biomass fuel gas integrated processor, the internal integrated of box body set with cavity body, water tank, dual level , collecting tank, washing groove and fuel gas room. Biomass fuel gas realize multifunctional processing ability, biomass fuel gas treatment time, increase treatment efficiency, after processing the unqualified biomass fuel gas directly supplied with sum device does not need follow-up treatment; whole platform processing device small volume, saves occupied square meter, water groove with washing method replaced tower spray method, reducing tar water production, reduce the cost of water treatment.
NOVELTY - The pyrogasification plant has a reaction chamber (2) with base frame (3) which supports lateral wall (4) such that material to be pyrogasified is introduced and transformed into syngas, tar and char. A lateral wall is consists of external supporting structure which supports internal metal cartridge (5) with tubular shape and has upper and lower extremities (5a,5b) both of which are open. The material (6) to be pyrogasified crosses the internal metal cartridge from upper to lower extremities and remaining material is contained by internal lateral surface of internal metal cartridge.    USE - Pyrogasification plant used for production of syngas.    ADVANTAGE - The structural resistance of the internal metal cartridge against the mechanical and thermal stresses at work during the pyrogasification process is increased, since the internal metal cartridge used in the plant is replaceable. The internal metal cartridge is allowed to freely dilate along the central axis without subject to troublesome deformation or crushing and without damaging the grid element. The high process efficiency is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows an axonometric and partially sectioned view of the reaction chamber of the plant.    Reaction chamber (2)    Base frame (3)    Lateral wall (4)    Internal metal cartridge (5)    Upper extremity (5a)    Lower extremity (5b)    Material (6)
NOVELTY - Bifuel mixture preparation involves mixing a portion of ethanol with a portion of diesel based on moment inductor. The moment inductor determines occurrence of molecular association between molecules of diesel and ethanol. The molecular association between diesel and ethanol is obtained as a result of passage of the fuels properly dosed through a filter element catalyst mounted on a catalyst fuel filter and another catalyst fuel filter.    USE - Method for preparing bifuel mixture for diesel engines.    ADVANTAGE - The method prepares bifuel mixture in a simple, cost-effective and eco-friendly manner with high yield. The prepared bifuel mixture provides high compression rates in the diesel engines, and reduces polluting byproducts emissions including sulfur dioxide, nitrogen dioxide and carbon dioxide.    DETAILED DESCRIPTION - Bi-fuel mixture preparation involves mixing a portion of ethanol with a portion of diesel based on moment inductor. The moment inductor determines occurrence of molecular association between molecules of diesel and ethanol. The molecular association between diesel and ethanol is obtained as a result of passage of the fuels properly dosed through a filter element catalyst mounted on a catalyst fuel filter and another catalyst fuel filter. The catalyst fuel filters are physically formed by a permeable body produced based on carbon fibers and organometallic compounds, ion exchange resin and silicon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bipolar molecule.
NOVELTY - The hydrogen-hydrogen-oxygen (HHO) project system comprises platinum plates (01) which are cut and pierced in a parallel manner with each other, and a positive and negative circuit which is properly sealed by an acrylic plate (03). A high strength hose (04) is connected to a bubbler exit to engine induction system, which is controlled by valves (05). An electronic element is connected to the cell and motor by wires for monitoring the system by using stainless steel screws (06) for mounting and fixing.    USE - Hydrogen-hydrogen-oxygen (HHO) project system for producing hydrogen as amendment of fuel fossil.    ADVANTAGE - The hydrogen-hydrogen-oxygen (HHO) project system efficiently generates power with low production cost and lower degree of pollution, and increases interest by using most abundant element hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen fuel cell. (Drawing includes non-English language text).    Platinum plates (01)    Acrylic plate (03)    High strength hose (04)    Valves (05)    Stainless steel screws (06)
NOVELTY - Valuable materials are collected from waste material by processing waste material which contains plastic and metal with steam in the presence of nickel microparticles at 450-700 degrees C, gasifying plastic, and collecting metal.    USE - Method of collecting valuable materials from waste material.    ADVANTAGE - Useful metal can be easily recovered, without manual dismantlement, reduction of process expenses can be achieved, waste material which does not contain nickel and waste material with low nickel content can be effectively processed, formation of slag can be prevented, corrosion of non-ferrous metal smelter can be prevented, and gas containing hydrogen gas obtained by gasification of plastic can be easily utilized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for collecting valuable materials which comprises reactor where waste material is supplied and steam gasification of plastic is carried out, steam introduction apparatus which introduces steam into reactor, heating apparatus which heats waste material supplied in reactor at 450-700 degrees C, magnetic classification apparatus for classifying magnetic metal containing nickel and non-magnetic metal, and magnetic metal mixing apparatus which mixes greater than or equal to 1 part of classified magnetic metal and to-be-processed waste material.
NOVELTY - Recovery of lipid or hydrocarbon from fermentation mixture involves providing a fermentation mixture comprising aqueous phase and liquid product phase comprising lipid or hydrocarbon produced by microbial fermentation in a fermentation vessel (a), feeding at least portion of the aqueous phase and portion of the liquid product phase to a vessel (b), forming mixture (A) and performing phase-separation process of the aqueous and product phase by injecting gas into the mixture and collecting the product phase comprising the lipid or hydrocarbon.    USE - Recovery of lipid or hydrocarbon from fermentation mixture used for producing biofuel, chemical intermediate and flavor or fragrance compound.    ADVANTAGE - The recovery of lipid or hydrocarbon from fermentation mixture is efficiently preformed by preventing or reducing the formation of a cream layer in the vessel (b) and economical process.    DETAILED DESCRIPTION - Recovery of lipid or hydrocarbon from fermentation mixture involves providing a fermentation mixture comprising aqueous phase and liquid product phase comprising lipid or hydrocarbon produced by microbial fermentation in a fermentation vessel (a) or in compartment (c1) of fermentation reactor, feeding at least portion of the aqueous phase and portion of the liquid product phase to a vessel (b) or to a compartment (c2) of the fermentation reactor, forming mixture (A) and performing phase-separation process of the aqueous and product phase by injecting gas into the mixture, thereby separating the product phase from the aqueous phase and collecting the product phase comprising the lipid or hydrocarbon.
NOVELTY - Continuous or semi-continuous process for preparing a formulation comprising a mixture of nicotine and a liquefied propellant gas, comprises introducing the nicotine and liquefied propellant gas into a mixing vessel (2) in a controlled manner.    USE - The process is useful for preparing a formulation, which is useful in a container that is useful in a device (all claimed) including smoking article.    ADVANTAGE - The process: utilizes the propellants with low environmental risk; provides the containers or canisters, which can be used directly, hence allows self-administration by the end user; and does not cause the problems associated with evaporation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a formulation prepared by the process;    (2) a container containing the formulation; and    (3) a device comprising the container, an activation mechanism, and a mouthpiece.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the process for preparing a formulation.    Mixing vessel (2)    Batch or flow meter (3)    Means for monitoring concentration component of formulation in vessel (5)
NOVELTY - Sewage treatment device comprises three modules. The first module is bio module for removing organic matter, chemical oxygen demand (COD), biochemical oxygen demand (BOD) and volatile solid (SV). The second module is N module for removing biological nitrogen removal by denitrification and nitrification and the third module is P module for removing phosphorus.    USE - Sewage treatment device used for removing effluent from pig farming and utilizing biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of sewage treatment system.    Digester (1)    Damping box flow (2)    Sieve (3)    Sandbox (4)    Biogas unit (5)
NOVELTY - Preparing sulfonated coal involves carrying out hydrothermal carbonization and sulfonation of residual saccharide pre-hydrolyzed lignocellulosic biomass in single step, where aqueous solution of residual saccharides of 1-80% weight by weight concentration is mixed with sulfonating agent of 5-70% weight by weight. The mixture is heated at 100-250 degrees C for 2-15 hours.    USE - Method for preparing sulfonated coal used as catalyst in catalytic reactions such as dehydration, hydrolysis, esterification or transesterification in gaseous phase or liquid phase (claimed).    ADVANTAGE - The method enables to prepare sulfonated coal that is safe, selective, eco-friendly, regenerative, reusable and minimizes the necessary quantities of reagents.
NOVELTY - Purifying biodiesel involves carrying out transesterification of triglycerides and reacting with an alcohol. The crude biodiesel is washed with water saturated with carbon dioxide.    USE - Method for purifying biodiesel used in diesel engines (claimed).    ADVANTAGE - The method enables to purify biodiesel that is biodegradable, nontoxic, does not contribute to global warming, has renewable raw materials and meets all specifications of the international standards.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a biodiesel purifying device. (Drawing includes non-English language text).
NOVELTY - A gas-separation membrane has a gas-separation layer (1) containing polyimide compound which has a carbamoyl group. The amount of the carbamoyl group contained in the polyimide compound is 0.1-3 mmol/g.    USE - Gas-separation membrane is used for gas-separation module used in gas-separation apparatus for separating carbon dioxide from gas containing carbon dioxide and methane (all claimed) generated from thermal power station, cement plant and iron mill blast furnace.    ADVANTAGE - The gas-separation membrane has excellent gas-separation performance even when separating gas containing impurity components e.g. toluene in high voltage conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gas-separation method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic sectional view of gas-separation membrane. (Drawing includes non-English language text)    Gas-separation layer (1)    Porous layer (2)    Gas-separation composite film (10)
NOVELTY - Method for treating human waste, involves separating stool and urine from excrement, and adding deodorant to the separated urine.    USE - The method is useful for treating human waste which is useful as fertilizer (claimed).    ADVANTAGE - The method prevents generation of offensive odor by neutralizing ammonia.
NOVELTY - Biorefining process comprises providing a lignocellulosic biomass feedstock; and extracting, hydrolyzing, and/or digesting the feedstock, or its component, with a liquid or vapor solution comprising reactant sulfur dioxide (SO2) or its derivative, to generate cellulose-rich solids and an intermediate liquid stream.    USE - The method is used for biorefining. The method is used for converting biomass into fermentable sugars, cellulose, and lignin.    ADVANTAGE - Provided are improved and economical biorefining methods, as well as economic recovery and recycle of SO2 or its derivatives. The method reduces or eliminates the need for purchasing and storing pure SO2 and improves the environmental air emissions of SO2 from power boilers, when using any fuels containing sulfur.    DETAILED DESCRIPTION - Biorefining process comprises (a) providing a lignocellulosic biomass feedstock; (b) extracting, hydrolyzing, and/or digesting the feedstock, or its component, with a liquid or vapor solution comprising reactant SO2 or its derivative, to generate cellulose-rich solids and an intermediate liquid stream; (c) combusting or gasifying a sulfur-containing fuel to generate heat and an exhaust gas stream comprising produced SO2; (d) optionally removing a portion of hemicellulosic sugars and/or lignin, if present, from the intermediate liquid stream; (e) contacting a portion of the exhaust gas stream with the intermediate liquid stream to dissolve the produced SO2 into the intermediate liquid stream; and (f) recycling some of the intermediate liquid stream back to step (b) to reuse the produced SO2 as the reactant SO2.
NOVELTY - Organization of loading of biogas installations operating on the combined raw materials, that pass from the agri-business, cattle-breeding complexes, poultry processing facilities, municipal services system and enterprises in the public power supply, and also on the enterprises of wholesale and retail environment, where the preliminarily is inputting raw materials from the parameters of temperature, humidity, acidity ratio the C:N:P, ability loading consortium for active symbiosis, size of particles.    USE - The method is useful for the organization of loading of biogas installations operating on the combined raw materials (claimed).    DETAILED DESCRIPTION - Organization of loading of biogas installations operating on the combined raw materials, that pass from the agri-business, cattle-breeding complexes, poultry processing facilities, municipal services system and enterprises in the public power supply, and also on the enterprises of wholesale and retail environment, where the preliminarily is inputting raw materials from the parameters of temperature, humidity, acidity ratio the C:N:P, ability loading consortium for active symbiosis, size of particles, with the nonconformity to humidity and temperatures of the raw materials which preheat and dilute by warm water, optimum ratio C:N:P and acidity are regulated by the ratio of the amount of different types of raw materials in the receiving tank, with the nonconformity to required size of particles of the incoming raw materials, conducting additional crushing of particles.
NOVELTY - Eco-friendly mangoes preservation involves harvesting 7-8 mangoes, and then pre-cooling. Cooled mangoes are washed, and then preservative is sprayed on surface of mangoes. The mangoes are packed, and stored at room temperature. Preservative comprises potassium cinnamate (10-20 g/L), phytic acid, salicylic acid, and emulsifying agent AEO-5.    USE - Eco-friendly method for preserving mangoes (claimed).    ADVANTAGE - The eco-friendly method reduces occurrence of diseases in mangoes by 31.8-45.5%.
NOVELTY - A gas occlusion material comprises metal-organic frameworks comprising metal cluster containing metallic element (m1), and multidentate ligand(s) containing aromatic ring(s) crosslinked with the metal cluster, metallic element (m1) different from metallic element (m1), and additional metallic element (m3) supported by the metal-organic frameworks. The metal-organic frameworks by which the addition metallic element supported changes structurally between small pore structure and large pore structure based on the amount of gas adsorptions.    USE - Gas occlusion material is used for occluding hydrocarbons e.g. methane, and hydrogen gas.    ADVANTAGE - The gas occlusion material enables removal of high amount of gas.    DETAILED DESCRIPTION - A gas occlusion material comprises metal-organic frameworks comprising metal cluster containing metallic element (m1), and multidentate ligand(s) containing aromatic ring(s) crosslinked with the metal cluster, metallic element (m1) different from metallic element (m1), and additional metallic element (m3) supported by the metal-organic frameworks. The metal-organic frameworks by which the addition metallic element supported changes structurally between small pore structure and large pore structure based on the amount of gas adsorptions, and has difference of the energy of the small pore structure and energy of the large pore structure in absolute zero-point of more than -50 kJ/mol to 0 kJ/mol (excluding 0 kJ/mol).
NOVELTY - The device has an air pre-heater connected to an upper fuel gas outlet of a gasifier and an air blower. An outlet channel of the air pre-heater is arranged with a gasification air pipe and a combustion-supporting air pipe in parallel. The combustion-supporting air pipe is connected to a hearth of a steam generator, and the gasification air pipe is connected with the hearth that is arranged with an inner steam coil. An end of a steam disk pipe is connected with a water pump through a water inlet pipe and another end is connected with the gasifier through a reducing area of a steam pipeline.    USE - Biomass steam and air unite gasification device.    ADVANTAGE - The device fully uses the hot biomass fuel gas and coal slag and increases utilization rate of the system heat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass steam and air unite gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass steam and air unite gasification device.
NOVELTY - The process involves allowing high temperature gas to enter though an air inlet pipe from a water washing tank to a lower part of a water chamber. The gas after purification is inserted into a multi-tube condenser. A purifier is arranged with a cooling water tank, a water tank and a sewage tank. The cooling water tank is mounted on an upper part of the purifier. The water tank is mounted at a left lower part of the cooling water tank. The sewage tank is mounted on a lower part of the cooling water tank. A side of the water washing tank is arranged with a water pump.    USE - Biomass pyrolysis sum purification process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass pyrolysis sum purifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a biomass pyrolysis sum purifier.
NOVELTY - The method involves collecting methane in the nanoporous material, in which methane is stored. The methane is selectively stored in the hydrophobicity pore of the nanoporous material. The methane nitrogen is contacted to the nanoporous material saturated with hydrophilic solvent. The hydrophilic pore and the nanoporous material are saturated with hydrophilic solvent. The nanoporous material is metal organic source structure. The metal organic source structure is copper(II)-benzene-1,3,5-tricarboxylate.    USE - Method for separating methane nitrogen using nanoporous materials.    ADVANTAGE - The method involves collecting methane in the nanoporous material, in which methane is stored, and thus ensures efficiently separating methane nitrogen using nanoporous materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of storage quantity to the material.
NOVELTY - The new type utility claims have one plant biomass forming fuel and preparation system and preparation system comprises raw material pre-processing system, low temperature pyrolysis system, high temperature gasification system, compact molding system and boiler system. The utility model is new type of preparation system integration have biomass gasification and biomass forming technology, the whole system is tightly connected to operation maintenance cost low, the obtained molding fuel property is good.
NOVELTY - The hydrogen-oxygen gas mixture generator (14) has magnetic field forming device (4) that applies magnetic field to the electrolyzer (3) provided with electrodes (3b,3c) through which asymmetric impulse voltage is applied. An air pump (7) is directly connected to gas-liquid separator (2) that separates liquid from water electrolysis hydrogen-oxygen gas mixture. A flashback arrester such as dry mini flashback arrester is provided in the combustion burner, and has outlet compactly connected to the end of combustion burner at distance of 50 to 200 millimeters, preferably 60 to 150 millimeters.    USE - Hydrogen-oxygen gas mixture generator for gas mixture of hydrogen and oxygen e.g. Brown gas by water electrolysis.    ADVANTAGE - Dry mini flashback arrester is provided in the combustion burner to increase efficiency and ensure safe utilization of the combustion burner. Increases energy efficiency for water electrolysis by applying Magnetohydrodynamics (MHD) effects and catalytic effects to water electrolysis in the magnetic field.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the hydrogen-oxygen gas mixture generator.    Gas-liquid separator (2)    Electrolyzer (3)    Electrodes (3b,3c)    Magnetic field forming device (4)    Air pump (7)    Hydrogen-oxygen gas mixture generator (14)
NOVELTY - The fuel cell has a first partition section (53) which is set at a first clearance gap section (52) formed in a section enclosed by annular first sealing section (50) to prohibit contact between first separator (30) and membrane electrode assembly (MEA). A second partition section (56) is set at second clearance gap section (55) formed in section enclosed by annular second sealing section (51) to prohibit contact between second separator (40) and MEA. The partition sections do not overlap with each other when seen from the thickness direction of a solid polymer electrolyte membrane (11).    USE - Polymer electrolyte form fuel cell for generating electrical energy.    ADVANTAGE - Improves electric power generation performance, reliability, and durability while reducing the cost by effectively blocking reactive gas flow to predetermined flow paths.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the polymer electrolyte form fuel cell. (Drawing includes non-English language texts).    Solid polymer electrolyte membrane (11)    First separator (30)    Second separator (40)    Annular first sealing section (50)    Annular second sealing section (51)    First clearance gap section (52)    First partition section (53)    Second clearance gap section (55)    Second partition section (56)
NOVELTY - Wholly bio-based methyl tertiary butyl ether (MTBE) and wholly bio-based ethyl tertiary butyl ether, are claimed.    USE - Wholly bio-based ethyl and methyl tertiary butyl ethers used as additives in fuel composition (claimed), and to form anti-knock fuel compositions.    ADVANTAGE - The ethers are manufactured using catalyst having improved stability due to reduced amount of sulfur.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel composition comprising wholly bio-based methyl or ethyl tertiary butyl ethers and gasoline; and    (2) process for making gasoline fuel additive, which involves converting acetic acid to isobutene in the presence of a catalyst, and reacting the isobutene with methanol or ethanol.
NOVELTY - The method involves introducing a carbonaceous material into a reaction chamber (15) located in a closed chamber (3). The water vapor is introduced into the reaction chamber through electrodes to cool the electrodes, and partially converted into plasma by passing through an electric arc (2) generated by electrodes. The temperature of reaction chamber is maintained to below 1000 degrees C. The pressure in reaction chamber is maintained at atmospheric pressure. The plasma gas is circulated in a loop in closed chamber so as to circulate at electrodes and in reaction chamber.    USE - Method for gasifying carbonaceous material type biomass or organic waste for generation of synthesis gas.    ADVANTAGE - The operation cost of the plasma-chemical reactor is reduced. The requirement of reactor cooling system is avoided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plasma-chemical reactor for gasifying carbonaceous material type biomass or organic waste for generation of synthesis gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the plasma-chemical reactor.    Plasma-chemical reactor (1)    Electric arc (2)    Closed chamber (3)    Passage pipe (14)    Reaction chamber (15)
NOVELTY - The new type utility claims have one kind stacked type biomass continuous baking reactor, the baking reactor comprises reactor main body is cylindrical structure, the mounting shaft on reactor main body rotate on axis, mounted on reactor main body up and connected and rotate shaft and driving component, at least one block mounted on the tower plate with the fan-shaped gap inside the reactor body, mounted on the rotating shaft and upper and tower plate surface is jointed on the scraping plate, output end arranged on tower plate under the baking medium input pipe, medium input pipe and input end respectively through out of extends to reactor main body outside, upper surface of each block respectively provided with bubbling hole tower plate, each tower plate and between block corresponding to the baking medium input pipe respectively set with one block with the fan-shaped gap and tray, tray over the gap and corresponding to the upper tower plate and the gap size and arrangement position of each match, upper tray mounted with at least two and output end of one corresponding to baking the medium input pipe is connected, the air outlet of wind cap towards the corresponding tower plate. Suitable for biomass pre-processing.
NOVELTY - The new type utility claims double channel raw material biomass fixed bed gasification pyrolysis furnace device, comprising a furnace body, the inner furnace body provided with the separating channel and pyrolysis gasification channel, outlet of the gasification channel connected pyrolysis entrance of channel, and the channel and pyrolysis gasification channel respectively added with biomass, end of the pyrolysis channel set with connected furnace body outside the gas outlet. The utility model is new type formed have mutually separating the gasification and pyrolysis channel in channel in the furnace body, and the biomass in respectively on two channel, biomass production, high temperature fuel gas of biomass gasification in channel, biomass fuel gas using high temperature pyrolysis of biomass raw material channel part, at the same time through material layer of biomass pyrolysis and channel, integrated to remove dust and tar in the biomass fuel gas, realize stable production of low dust content of biomass fuel gas, for processing and using the follow-up biomass fuel gas supply have the advantageous condition in in one set device. The utility model is new type can apply for the biomass fuel gas purification.
NOVELTY - The new type utility claims have one kind of the traditional Chinese medicine dregs made biomass fuel and comprehensive processing system, comprising in turn connected medicine slag crushing head device, dehydrating device, drying device, forming pelletizing device, between the slag crushing device and dehydration device by one transport belt transmission connection, in interval on the transport belt equipped with at least two of kick-out device, the the traditional Chinese medicine dregs made of biomass fuel and comprehensive treatment system by first set with medicine slag crushing device, taking the medicine slag, carrying out crushing, using slag component distribution uniformity, reducing slag accumulation volume, reduce volume of follow-up processing device, change based on residue characteristic for follow-up processing foundation, comprising dehydrating device for slag water can reduce to lower level, reducing drying process cost, drying device through thermal dehydration, can make the medicine slag and grass in water is effective to make the traditional Chinese medicine dregs water content, compression molding is accord with requirement, dry dregs at last by pelletizing device forming process to be biomass fuel.
NOVELTY - The device has outer sum room portion (21) that is arranged in outside of ring sum room portion. The outer sum room portion and inner sum room portion (22) are respectively connected with material fluidizing wind entrances (5). A wind cap is positioned to center shaft of guide tube in annular arrangement to form wind distribution area. The air flow quantity at top end of wind cap is maintained to adjust pyrolysis reaction. One leg is regulated by control material in ring sum room portion.    USE - Device for separating coke from heat type biomass oil, for use in system for separating coke from heat type biomass oil (claimed).    ADVANTAGE - The automatic separation of the coke is realized, and the high performance of the coke is obtained. The structure of the device for separating the coke is compact, and the device is easily installed in the mobile platform.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of separating coke from heat type biomass oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for separating the coke from the heat type biomass oil. (Drawing includes non-English language text)    Material fluidizing wind entrance (5)    Spiral feeder (6)    Regenerator (7)    Outer sum room portion (21)    Inner sum room portion (22)
NOVELTY - The method involves performing biomass gasification furnace fume self-purification process by a device. Absorption biomass fuel drying process is performed on a sedimentation area. A biomass feedstock pipe is formed with a gas discharging outlet. A first cyclone separator and a second cyclone separator are connected by a first level purification unit. A combustion gas pipeline is provided with an insulating layer through a nozzle. The nozzle is connected with a furnace head. High temperature fuel gas is sprayed on a boiler hearth combustion unit through the gas discharging outlet.    USE - Biomass gasification furnace fume self-purifying method.    ADVANTAGE - The method enables reducing nitrogen oxides and high heat air pyrolysis catalyst discharging amount in biomass fuel gas purification process by a combustion system. The method enables realizing biomass gasification furnace fume self-purifying process and avoiding content dust and tar burning phenomenon.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a biomass gasification furnace fume self-purifying method.
NOVELTY - The method involves executing an automatic control program. A control cabinet body is connected with a human machine interface. A feeding time value and a feeding speed value are calculated. Biomass pyrolysis process is performed through a biomass gasification furnace (14). A combustion-supporting pipe (11) is connected with a fuel gas nozzle (10). A spiral transport machine (5) is connected with the biomass gasification furnace. Control cabinet recovering process is performed according to pre-set program instruction cycles. Biomass gasification furnace operating process is performed.    USE - Automatic biomass gasification furnace feeding method.    ADVANTAGE - The method enables increasing automation degree and performing frequency conversion regulating process so as to avoid feeding accident rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification furnace.    Spiral transport machine (5)    Baffle plate (6)    Fuel gas nozzle (10)    Combustion-supporting pipe (11)    Biomass gasification furnace (14)
NOVELTY - The device has a burner connected with a heat storage type high temperature heat exchanger. A terminal gasification waste heat recovery and purification device is connected with an outlet of a gasification furnace. An end of the terminal gasification waste heat recovery and purification device is connected with a gas storage room. The gas storage room is provided with two outlets. An outlet of the burner is connected with a fume inlet of the high temperature heat exchanger. An inlet of the gasification furnace is connected with a working medium outlet of the high temperature heat exchanger.    USE - Organic solid fuel gas gasification device.    ADVANTAGE - The device has high gas heating value, and utilizes gasification fuel gas as energy source to supply heat for gasification reaction so as to achieve self-sustaining operation of gasification reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an organic solid fuel gas gasification device. '(Drawing includes non-English language text)'
NOVELTY - The furnace has a furnace main body (2) whose end is provided with a plasma generator (4). A rotary nozzle (3) is fixed with an iron generator and an end of the furnace main body. A thermocouple unit and an oxygen quantity detector (19) are equipped with an outer side of the furnace main body. A control cabinet is connected with the thermocouple unit and the oxygen quantity detector. The plasma generator is equipped with a blanking system and the rotary nozzle. The control cabinet is fixed with the rotary nozzle through an internal program unit.    USE - High-temperature plasma rubbish gasification splitting furnace.    ADVANTAGE - The furnace improves heating effect so as to generate steam and power. The furnace improves solid waste rubbish gasification efficiency, and avoids secondary pollution and heavy metal toxic substance discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a high-temperature plasma rubbish gasification splitting furnace.    Furnace main body (2)    Rotary nozzle (3)    Plasma generator (4)    Storage hopper (6)    Pressure table (13)    Oxygen quantity detector (19)
NOVELTY - The method involves passing water vapor as gasification agent into a hearth of an iron-making blast furnace. Coal, rubbish and biomass residue carbon reaction is generated. Coal, rubbish and biomass gasification process is performed. Ash formulation is produced by using a gasification furnace to produce a cement clinker, where the cement clinker contains calcium carbonate. The calcium carbonate is replaced by calcium oxide. Carbon content, sulfur and chlorine content of gasification furnace gas are reduced to realize near zero discharging process.    USE - Method for modifying an iron-making blast furnace into a coal, rubbish and biomass gasification furnace.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for modifying an iron-making blast furnace into a coal, rubbish and biomass gasification furnace.
NOVELTY - Pipeline planting system comprises a sewage biogas energy utilization system and a sewage water resource utilization system. The system further comprises a collection tank whose one end is connected to a water outlet pipe, while the other end is connected to a water intake pipe; and a biogas slurry connection pipe for absorbing nutrients and moisture from plant roots.    USE - The system is useful in sewage treatment (claimed), and in construction of buildings.    ADVANTAGE - The system saves water; and is economical, and environmental friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the pipe line planting system.
NOVELTY - The furnace has a conveying shell (11) located in output material chamber (10). The discharge opening is fixed to feedstock with a flashboard valve. An inserting plate valve (9) is opened, when discharge opening of inlet combustion chamber (4) is opened. The shell is located far away from material chamber. A spiral conveyor (12) is mounted in the material chamber for discharging coal material by gravity through discharge opening (13). The discharge opening is fixed close to the shell, such that water is sprayed to output material chamber using a spray device (14).    USE - Efficient continuous biomass carbonizing furnace.    ADVANTAGE - The continuous carbonization is performed in furnace, to increase the surface quality and to continuously remove the biomass coal using biomass carbonizing process. The production efficiency is high, and furnace is easy to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the efficient continuous biomass carbonizing furnace.    Inlet combustion chamber (4)    Inserting plate valve (9)    Output material chamber (10)    Conveying shell (11)    Spiral conveyor (12)    Discharge opening (13)    Spray device (14)
NOVELTY - Pretreating lignocellulosic biomass having a lignin component, a hemicellulose component, and a cellulose component, for conversion to sugar, comprises contacting the biomass with an oxidizing agent at a first temperature for a first period of time sufficient to partially remove or decompose the lignin component, thus producing lipoxygenase (LOX) biomass; and contacting the LOX biomass with an ionic liquid (IL) at a second temperature for a second period of time, thus producing a first mixture comprising IL and LOX biomass.    USE - The method is used for pretreating lignocellulosic biomass having a lignin component, a hemicellulose component, and a cellulose component, for conversion to sugar (claimed).    ADVANTAGE - Efficient methods of enhancing saccharification of cellulose and hemicellulose from biomass for fuel and chemical production that do not require high temperatures are provided.    DETAILED DESCRIPTION - Pretreating lignocellulosic biomass having a lignin component, a hemicellulose component, and a cellulose component, for conversion to sugar, comprises contacting the biomass with an oxidizing agent at a first temperature for a first period of time sufficient to partially remove or decompose the lignin component, thus producing LOX biomass; contacting the LOX biomass with an IL at a second temperature for a second period of time, thus producing a first mixture comprising IL and LOX biomass; contacting the first mixture with a solvent, thus producing a second mixture comprising LOXIL-treated biomass and solvent, where the IL is substantially soluble in the solvent and one of the cellulose component or the hemicellulose component is substantially insoluble in the solvent; and separating the LOXIL-treated biomass from the solvent to produce pretreated lignocellulosic biomass. An INDEPENDENT CLAIM is a pretreated lignocellulosic biomass produced from the method above.
NOVELTY - The utility model relates to a water bath roller type dry fermentation device, belonging to agricultural biomass using technology field. The device comprises the fermentation warehouse level and may rotate by roller body composed of the roller outside sleeved with insulating shell body, between shell and form water bath roller; outer circle surface of shell set with circle track, track respectively support in corresponding to the gap distribution supporting device at the rotating center roller and feedstock end and discharging end respectively connected with water inlet pipe and water outlet pipe of water bath interlayer, outside end and out water tube pass through the boiler and external pipeline and hot water pump connected to outside end of the water inlet pipe, the discharge end circle centre of roller body also is installed in the roller body on the upper end air outlet pipe. The utility model is new type structure compact structure, small square meter small and mass transfer heat transfer uniformity, full fermentation, increase have yield, and low energy consumption, stable operation, convenient to realize automatic control, saves use and reduce labour intensity.
NOVELTY - The new type utility claims have one kind of intelligent container mould group type temperature electrolytic made fluorin device, the whole module group type device comprises temperature electrolytic cell made of fluorin and matching system, fluorine purification system, hydrogen tail sum clean processing system, safe storage sum system, process analysis system, digital intelligent monitoring management system. Device system for temperature of electrolytic cell made of fluorin process of anhydrous hydrofluoric acid, temperature of electrolytic made fluorin, reaction temperature control, fluorine purification, hydrogen tail sum clean discharge and subsidiary technology system equal process, to integrate modular structure, full intelligent control combined integrated method. Whole device using modular container type design, the vehicle can move and local fast modular installation, production operation. Device is not only with compact structure, simple operation, stable production, safe reliability, product high purity, no pollute discharge, and the equal function are can according to user using scale, fanancial cost equal control requirement and flexible combination arrangement, satisfying different client requirement.
NOVELTY - Foliar fertilizer formulation comprises 20-40% seaweed fermentation product, 25-50% clam shell powder, 25-50% wheat bran powder, 45-65% potassium sulfate, and 3-4% phosphorus.    USE - As foliar fertilizer formulation for vegetable (claimed).    ADVANTAGE - The foliar fertilizer formulation provides inorganic element such as sodium, potassium, iron and calcium, increases yield of vegetable, and enables people to eat natural vegetable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the foliar fertilizer formulation, which involves mixing the above-mentioned materials, fermenting mixture in closed environment for 10-20 days, stirring materials, and collecting product.
NOVELTY - Manufacture of mesoxalic acid diester (hydrate) involves mixing malonic diester, carboxylic compound, and chlorous acid compound, supplying the obtained mixture to a circulation reactor, and reacting mixture in the circulation reactor.    USE - Manufacture of mesoxalic acid diester (hydrate) used as raw material for manufacturing pyrazine-2-one-3-carboxylate derivative used in manufacture of pharmaceuticals and agrochemicals.    ADVANTAGE - The method enables stable and efficient manufacture of mesoxalic acid diester (hydrate) with high productivity and quality, and reduced non-uniformity and occurrence of explosion, and continuous oxidation reaction of active methylene portion, without modifying active methylene portion of malonic diester, by simple, fast, economical, and environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous production apparatus, which consists of a mixing unit for mixing malonic diester, carboxylic compound, and chlorous acid compound, a temperature rising unit for heating the mixture, and a reaction unit for heating the mixture. The temperature rising unit and reaction unit are provided in the circulation reactor.
NOVELTY - Bioorganic fertilizer formulation comprises 50-60 parts root debris, 40-50 parts chicken and duck excrement, 30-50 parts dried seaweed, 2-5 parts composting agent, 15-20 parts gelatin, and vinegar (required amount).    USE - The bioorganic fertilizer formulation is useful for enhancing fertility of soil.    ADVANTAGE - The bioorganic fertilizer formulation increase air permeability of soil, enhances yield of grains, cash crops, vegetables and fruits, and improves quality of agricultural products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bioorganic fertilizer formulation, which involves mixing the above-mentioned materials, forming mixture into heap, sealing and performing anaerobic fermentation for 30-40 days in summer and 90-120 days in winter, collecting product, drying the product, preparing dried product into granules, and packing the granules in a bag.
NOVELTY - The new type utility claims have one plant tobacco special for composite structure particle slow release fertilizer, of three layer structure composite composed of, from inside to outside in turn divided organic fertilizer layer (1), inorganic fertilizer layer (2), macromolecule organic compound envelope layer (3). Can make organic fertilizer and inorganic fertilizer reasonable collocation, time saving, environment-friendly, efficient, but also can improvement soil structure, also can be fertilizer and labour, prevent ferterlization excessive to cause the tobacco ' burning seedlings phenomenon, which solves balance requirement and supply the nutrient balance problem equal.
NOVELTY - The utility model is new type relates to one kind of kitchen garbage processing device, garbage treatment technology field, belonging to the kitchen garbage processing device comprises feeding port sealing cover, an exhaust fan, a motor, stirring column, a speed reducer, a main shaft, a shell, insulating layer, suction filtering plate, a discharging mouth, a net-like clapboard, one time fermentation room, second time fermentation room, discharge room, a feeding port, a one time fermentation room and between second time fermentation room by a net-like clapboard; shell bottom is set with insulating layer, insulating layer and set with internal heating tube, speed reducer and main shaft connection, upper main shaft provided with stirring column, upper feeding port set with port sealing cover, one time fermentation room and right upper part provided with discharge room, discharge room and tail sum processing device of air inlet wherein each connected, outside the second time fermentation room set with discharging mouth. The utility model is new type of high temperature microorganism kitchen garbage processing device can be fast continuous process of kitchen garbage.
NOVELTY - Method for processing sewage containing low concentration of external carbon source, involves mixing and crushing rice hull, wheat straw, crop straw and corn stalk rich in cellulose, subjecting obtained mixture to acidic fermentation to obtain fermented product containing 16-42% or 40-70% acetic acid, and 5-16% or 15-26% propionic acid, and filtering the fermented product to obtain supernatant which directly acts as carbon source.    USE - The method is useful for processing sewage containing low concentration of external carbon source (claimed).
NOVELTY - Process of rapid composting of organic fertilizer from pineapple waste comprising nitrogen, phosphorus and potassium to stimulate and promote plant growth is disclosed.    USE - The process is useful for rapid composting of organic fertilizer from pineapple waste to stimulate and promote plant growth. No biological data given.
NOVELTY - Improvement of biomass combustion exhaust gas temperature involves feeding biomass fuel to biomass gasifier, gasifying with hot gas to clean the combustor, introducing portion of normal combustion air to heat exchanger using hot gas stove at 500-900 degrees C, co-firing, introducing biomass gas and hot air, controlling combustion exhaust gas temperature at 1300-1700 degrees C, high-temperature thermally heating to 600-900 degrees C, introducing hot air mixture into the oven at room temperature, controlling exhaust gas temperature at 150-200 degrees C, and directly discharging into the atmosphere.    USE - Improvement of biomass combustion exhaust gas temperature (claimed).    DETAILED DESCRIPTION - Improvement of biomass combustion exhaust gas temperature involves feeding biomass fuel to biomass gasifier, gasifying with hot gas to clean the combustor, introducing portion of normal combustion air to heat exchanger using hot gas stove at 500-900 degrees C, co-firing, introducing biomass gas and hot air, controlling combustion exhaust gas temperature at 1300-1700 degrees C, high-temperature thermally heating to 600-900 degrees C, introducing hot air mixture into the oven at room temperature, controlling the temperature of the oven at 500-900 degrees C, further controlling exhaust gas temperature at 150-200 degrees C, and directly discharging into the atmosphere.
NOVELTY - High viscosity material slurry granulation nozzle comprises material slurry feeding pipe (1) and material slurry dispersion rotating disc (2).    USE - High viscosity material slurry granulation nozzle used for producing compound fertilizer (claimed).    ADVANTAGE - The granulation nozzle is environment-friendly, has good atomization effect, qualified particle strength and no dust emission, and saves fan power.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of high viscosity material slurry granulation nozzle.    Material slurry feeding pipe (1)    Material slurry dispersion rotating disc (2)
NOVELTY - Preparing biologicalcoal/attapulgite nano composite material using attapulgite and swill oil, comprises carrying out direct adsorption of attapulgite with swill oil, filter pressing the attapulgite adsorption oil, adding attapulgite oil in pressure tank, carrying out anaerobic carbonization, washing, drying, and sieving to obtain material.    USE - The method is useful for preparing biologicalcoal/attapulgite nano composite material using attapulgite and swill oil (claimed).    ADVANTAGE - The nano composite material improves soil and can purify water.
NOVELTY - A kitchen waste compost comprises hopper, crushing machine, spiral transport machine, fermentation tank, and oil water separating tank. A lower part of the hopper has the crushing machine. The crushing machine has crushing cutter. The spiral transport machine is downstream the crushing machine and has the oil water separation tank.    USE - Processor for processing kitchen waste (claimed).    ADVANTAGE - The processor avoids environment pollution.
NOVELTY - A microorganism compound fertilizer comprises 20-50 pts. wt. Aspergillus niger and 20-35 pts. wt. Bacillus subtilis microbial inoculum.    USE - Microorganism compound fertilizer.    ADVANTAGE - The fertilizer can increase grain yield by 8-30% and increase vegetable yield by 10-40%. It can improve quality and flavor of food.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of microorganism compound fertilizer comprising taking A. niger culture and B. subtilis culture, and fermenting.
NOVELTY - A fungus slag fertilizer is produced by taking off bag mushroom, crushing into particle diameter of 5-20 mm, and drying for 24 hours; soaking in water, stacking at 2-6 m at 20-35 degrees C; carrying out fermentation for 24-72 hours at 40 degrees C; and crushing, uniformly stirring, spraying water, stacking again, covering with transparent plastic film, and carrying out second time fermentation.    USE - Method for producing fungus slag fertilizer (claimed).    ADVANTAGE - The method has low cost and simple preparation steps. It uses waste which reduces pollution in environment.    DETAILED DESCRIPTION - Producing fungus slag fertilizer comprises (A) taking off bag mushroom, crushing into particle diameter of 5-20 mm, and drying for 24 hours; (B) soaking in water, stacking at 2-6 m at 20-35 degrees C, the width being 1.5-2 m and the height being 0.5-1.2 m; (C) carrying out fermentation for 24-72 hours at 40 degrees C; (D) crushing, uniformly stirring, spraying water, stacking again, covering with transparent plastic film, and carrying out second time fermentation; (E) fermenting at 55-65 degrees C for 24-36 hours, removing the stack body on the transparent plastic film, crushing, uniformly stirring, spraying water, stacking again, covering with transparent plastic film, and carrying out continuous fermentation; and (F),taking the same method every 2-3 days until the stack temperature does not rise again, maintaining weight and water content at 50-55%, fermenting for 40-55 days, and obtaining mushroom fertilizer.
NOVELTY - A growing bamboo seedling special fertilizer comprises 50-80 pts. wt. bamboo sawdust powder, 10-15 pts. wt. chicken manure, 10-15 pts. wt. perlite20-30 pts. wt. plant ash and 5-10 pts. wt. ammonium phosphate.    USE - Growing bamboo seedling special fertilizer.    ADVANTAGE - The fertilizer has mineral elements and nutritional components, and reasonable proportion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of growing bamboo seedling special fertilizer comprising mixing bamboo sawdust powder and chicken manure, adding leavening agent and water for 20-30 days, adding perlite, plant ash and ammonium phosphate, mixing, crushing, drying, granulating, and subpacking.
NOVELTY - A fertilizer compound comprises 23-26 wt.% potassium sulfate, 6-8 wt.% potassium chloride, 32-35 wt.% monoammonium phosphate, 25 -29 wt.% urea, 0.5-1.5 wt.% bio-fermentation bacteria, and balance organic fungicides.    USE - Fertilizer compound used for adjusting porosity soil, and promoting plant growth and cultivation of plant roots.
NOVELTY - Preparation of sweet potato fertilizer involves mixing 32-38 pts. wt. animal manure, 22-25 pts. wt. corn stalk and 12-18 pts. wt. bagasse, fermenting, crushing into 100 mesh powder, weighing 40-50 pts. wt. urea, 30-40 pts. wt. superphosphate, 10-30 pts. wt. potassium sulfate, 10-20 pts. wt. borax and 2-3 pts. wt. crushed mineral, crushing into 100 mesh powder, mixing fermented animal manure and urea mixed powder, adding carbendazim, thiram and microbial inoculum, granulating into 0.2-0.4 mm granules, drying, packaging and storing.    USE - Method for preparing sweet potato fertilizer.
NOVELTY - Pomelo special fertilizer package comprises inorganic-organic winter fertilizer with nitrogen, phosphorus pentoxide and potassium oxide at mass ratio of 8-10:12-15:10-15, sulfur nitrate-based spring fertilizer with nitrogen, phosphorus pentoxide and potassium oxide at mass ratio of 16-20:8-12:18-20, and sulfur nitrate-based summer fertilizer with nitrogen, phosphorus pentoxide and potassium oxide at mass ratio of 12-15:8-10:22-25.    USE - Pomelo special fertilizer package used for improving quality and yield (claimed).    ADVANTAGE - The fertilizer package has balanced nutrition and high efficiency.
NOVELTY - Selenium-enriched ecological foliar fertilizer comprises 1-1.5 pts. wt. sodium selenite, 65-75 pts. wt. potassium dihydrogen phosphate, 8-10 pts. wt. boric acid, 5-10 pts. wt. peat, 5-10 pts. wt. humic acid, 0.2-0.4 pt. wt. sodium nitrophenolate, 3-3.5 pts. wt. mepiquat chloride, 10-15 pts. wt. active fungus and 2.8-3 pts. wt. kaolin.    USE - Selenium-enriched ecological foliar fertilizer used for improving soil and improving growth and quality of crops (claimed).    ADVANTAGE - The fertilizer reduces dosage and reduces use of pesticide.
NOVELTY - Bioorganic fertilizer comprises animal manure, pile material and complex fermentation medium comprising Bacillus licheniformis (CGMCC 10037), Bacillus subtilis (CGMCC 10038), Ureibacillus thermosphaericus (CGMCC 10039), Bacillus thuringiensis (CGMCC 10036), Bacillus amyloliquefaciens, Geobacillus pallidus, Pseudomonas and Bacillus cereus.    USE - Bioorganic fertilizer.    ADVANTAGE - The fertilizer improves production efficiency, and has good synergistic effect and pesticidal effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bioorganic fertilizer comprising taking pig, chicken or cow manure as animal manure and hay, branch or straw as pile material at weight ratio of 3-4.5:1-1.5, mixing, drying until moisture content is 55-60%, adding 108-109 colony forming unit/mL complex fermentation medium with 15-20 wt.% Bacillus licheniformis (CGMCC 10037), 10-15 wt.% Bacillus subtilis (CGMCC 10038), 10-15 wt.% Ureibacillus thermosphaericus (CGMCC 10039), 15-20 wt.% Bacillus thuringiensis (CGMCC 10036), 10-15 wt.% Bacillus amyloliquefaciens, 5-10 wt.% Geobacillus pallidus, 6-12 wt.% Pseudomonas and 3-8 wt.% Bacillus cereus, performing aerobic fermentation at 60-75 degrees C, adding water, turning 2-3 times until germination index is greater than 80% and moisture content is 30%, adding 3-5 mL/kg 108-109 colony forming unit/mL Bacillus thuringiensis (CGMCC 10036), mixing and maintaining moisture content at 30%.
NOVELTY - Fixing phosphoric acid enhanced biological carbon involves crushing biomass waste and then adding the crushed material with aqueous solution of phosphoric acid. The obtained material is mixed and then the mixed material is kept under nitrogen protection atmosphere at 400-600 degrees C to perform pyrolysis reaction and to obtain modified biochar.    USE - Method for fixing phosphoric acid enhanced biological carbon (claimed).    ADVANTAGE - The method enables to fix phosphoric acid enhanced biological carbon in cost-effective manner, with high density, and has imprived biological coal product stability and reduced carbon loss.
NOVELTY - Dry adhesive char biomass briquette production method comprises crushing the raw material to a semi-coke powder; adding 1.5-2.5 mass% semi-coke powder and starch powder to a dry feed mixing equipment, and mixing uniformly; adding semi-coke raw material to the dried mixed material, further adding 18-23% aqueous solution of sodium hydroxide and borax, mixing and kneading; extrusion molding the mixed material; and using drying device at 160-220 degrees C wet bulb temperature of drying coal, drying the moisture to 2%, and cooling package to obtain the semi-coke coal.    USE - Dry adhesive char biomass briquette production method (claimed).    ADVANTAGE - The method has high accuracy for dry adhesive char biomass briquette production.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the dry adhesive char biomass briquette production method (Drawing includes non-English language text).
NOVELTY - Production of bio-polymer pellet fuel comprises taking ground wood or sawdust; pressing into cylindrical wood pellets; adding wood pellets to starch glue or plastic glass; mixing to obtain mixed material; extruding mixed material; and drying to obtain bio-polymer pellet fuel.    USE - Production of bio-polymer pellet fuel.    ADVANTAGE - The method uses plant to produce bio-polymer pellet fuel, thus reducing waste disposal and treatment while increasing added value of production. It has simple operation, is easy to implement, and has low production cost.
NOVELTY - Bio-carbon fuel comprises honeycomb comprising 72 kg bamboo waste, waste wood, dregs, cassava residue, sludge and other major biofuel, 4 kg carbonaceous shale, 4 kg cinder, 0.50 kg combustion improver (used in industrial sodium chloride, solid alcohol, or naphthenic salt), 8 kg adhesive (yellow mud powder or kaolin), and 11 kg water; or block (plate) shaped, cylindrical, hollow cylinder, strip, sheet and other products with same formula with that of honeycomb.    USE - Bio-carbon fuel.    ADVANTAGE - The bio-carbon fuel is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of bio-carbon fuel by crushing raw materials; grinding carbonaceous shale to less than 3 mm particle size and binder to less than 2 mm particle size; and adding raw materials in water to dissolve to obtain bio-carbon fuel.
NOVELTY - Immobilized carrier comprises porous material for accelerating discharge of biogas, and gel-forming polymer for producing biogas in which anaerobic microorganisms are fixed.    USE - The immobilized carrier is useful for producing biogas (claimed).    ADVANTAGE - The immobilized carrier improves overall biogas production rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing carrier, involves (a) mixing gel-forming polymer and porous material, and (b) adding cross-linking solution to the mixture, and gelling the mixture; and    (2) method for producing biogas, involves adding sample containing organic material to the carrier, and reacting mixture.
NOVELTY - Pre-treating straw for preparing ethanol fuel, comprises: (i) mixing straw and 3-5% sulfuric acid in the mass ratio of 1:8-10, treating with stirring at 120 degrees C for 1 hour, filtering, and vacuum drying; (ii) mixing the dried product with 3-5% sodium hydroxide in the mass ratio of 1:8-10, treating with stirring at room temperature for 1 hour, then filtering and vacuum drying; and (iii) ultrasonicating the dried product at room temperature for 3-5 minutes, where the ultrasonic power is 120 W, suction filtering and vacuum drying.    USE - The method is useful for pre-treating straw for preparing ethanol fuel (claimed).    ADVANTAGE - The method removes hemicellulose and lignin, and improves fuel yield.
NOVELTY - Soil modifying agent comprises 10-30 wt.% Penicillium oxalicum liquid, 5-20 wt.% succinic acid filamentous Bacillus liquid, 10-30 wt.% Trichoderma liquid, 5-20 wt.% Bacillus licheniformis broth and 15-35 wt.% Rhodococcus liquid.    USE - Soil modifying agent.    ADVANTAGE - The soil modifying agent increases soil fertility without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil modifying agent, which involves mixing straw, wheat flour and mixed microbial inoculum to obtain mixture that is fermented at room temperature.
NOVELTY - Fermented peanut composite comprises Bacillus mucilaginosus, Paracoccus denitrificans, Trichoderma reesei and succinic acid filamentous bacterium in a ratio of (1-5):(1-4):(3-6):(3-6).    USE - Fermented peanut composite used as biological fertilizer (claimed).    ADVANTAGE - The fermented peanut composite ensures improved disease and stress resistance of soil, and improved quality of product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fermented peanut composite used as biological fertilizer involves:    (A) cutting peanut straw into 10-30 cm segments;    (B) adding bacteria (5-3.5%), and water to obtained product;    (C) fermenting the obtained product for 2-3 days; and    (D) adding additive to fermented product to obtain final product.
NOVELTY - Processing cattle excrement involves soaking 10-30 wt.% cattle excrement and starch with water and then stirred to obtain suspension. Suspension is heated and boiled and auxiliary material is added uniformly, and then anaerobic fermentation is carried out at 30-60 degrees C for 16- 48 hours in a fermentation tank. The fermentation tank is rotated at speed of 10-30 revolutions per minute, and then sterilized to obtain fermentation product.    USE - Method for processing cattle excrement (claimed) used for cultivating pond fish feed and used as fertilizer in farmland.    ADVANTAGE - The method enables to complete metabolism of organic matter in cattle excrement, and is easy to operate.
NOVELTY - Preparing fertilizer involves granulating potassium-rich feldspar, and silicon oxide. Magnesium slag pellets are mixed with feldspar in a ratio of (50-60):(40-50). Obtained mixture is melted by heating at high temperature for 50-70 minutes. Melted material is cooled, dried and ground to obtain final product.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method is simple, eco-friendly, and cost effective.
NOVELTY - Organic fertilizer comprises straw (60-80 pts. wt.), livestock and poultry excrement (5-10 pts. wt.), humic acid (1-2 pts. wt.), boric acid (1-5 pts. wt.), potassium nitrate (1-5 pts. wt.), potassium dihydrogen phosphate (1-5 pts. wt.), carbamide (1-2 pts. wt.), ammonium molybdate (1-2 pts. wt.), phosphoric acid (1-2 pts. wt.), compound sodium nitrophenolate (1-2 pts. wt.), Aeromonas powder (0.01-0.02 pts. wt.), and Candida albicans powder (0.01-0.02 pts. wt.).    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer ensures effective absorption of nutrients by plants and decomposition of organic pollutants, and improves quality of crops.
NOVELTY - Organic fertilizer comprises 80-150 pts. wt. dairy manure, 50-100 pts. wt. chicken manure, 10-30 pts. wt. mushroom, 0.1-2 pts. wt. microbial agent, 10-30 pts. wt. calcium magnesium phosphate and 10-20 pts. wt. fly ash.    USE - Organic fertilizer used for growing vegetables.    ADVANTAGE - The organic fertilizer requires easy to obtain raw materials, and ensures low production cost.
NOVELTY - A trifluoromethyl substituted azide compound is prepared by, in an organic solvent and in the presence of catalyst, performing addition reaction on trifluoromethylation agent and trimethylsilyl azide to obtain olefin carbon-carbon double bond with carbon on trifluoromethyl. The catalyst is copper salt or copper complex. The copper salt includes cuprous iodide, cuprous chloride, and cuprous bromide. The copper complex is acetonitrile hexafluorocopper phosphate, copper tetrafluoroborate and acetonitrile trifluoromethanesulfonic copper.    USE - Method for preparation of trifluoromethyl substituted azide compound (claimed).    ADVANTAGE - The method has mild reaction condition, high selectivity, and simple processing steps. It is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparation of trifluoromethyl substituted azide compound comprises, in an organic solvent and in the presence of catalyst, performing addition reaction on trifluoromethylation agent and trimethylsilyl azide to obtain olefin carbon-carbon double bond with carbon on trifluoromethyl. The catalyst is copper salt or copper complex. The copper salt is cuprous iodide, cuprous chloride, cuprous bromide, copper chloride, cupric bromide, copper, copper acetate and copper triflate. The copper complex is acetonitrile hexafluorocopper phosphate, copper tetrafluoroborate and acetonitrile trifluoromethanesulfonic copper. The trifluoromethylation agent is a compound of formula (I) or (II).
NOVELTY - Preparing benzophenone comprises adding liquid benzene into condensation reaction kettle, adding benzoyl chloride dropwise into storage tank, heating the liquid benzene at 65-70 degrees C, stirring, adding ferric chloride into kettle, simultaneously adding benzoyl chloride dropwise into the kettle, using vacuum device for removing hydrochloric acid gas produced during the reaction, heating at 80 degrees C, recovering excess benzene by distillation, opening water jackets in the reaction kettle to drop the materials temperature to room temperature and carrying out centrifugal filtration process.    USE - The method is useful for preparing benzophenone (claimed).    ADVANTAGE - The method: utilizes ferric chloride as catalyst, which greatly improves the yield of benzophenone; reduces the wastage of raw materials; and is economical.
NOVELTY - Synthesis of benzoxepine compound (I) comprises taking o-fluorophenyl acetylene compound (II) and ketone compound (III) as raw materials, alkali as promoter and organic solvent as solvent, under inert atmosphere protection and stirring condition, heating at 80-150 degrees C, reacting for 6-24 hours, when reaction is completed, cooling to room temperature, concentrating by decompression distilling to obtain crude product, and purifying by column chromatography to obtain (I). The compound (III) is cyclopentanone, cyclohexanone or cyclooctanone.    USE - Synthesis of benzoxepine compound (I) (claimed) used for medicine and organic synthesis.    ADVANTAGE - The method uses safe raw materials, which are easy to obtain, has simple operation, low cost and good adaptability of functional group and substrate, and is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Synthesis of benzoxepine compound of formula (I) comprises taking o-fluorophenyl acetylene compound of formula (II) and ketone compound of formula (III) as raw materials, alkali as promoter and organic solvent as solvent, under inert atmosphere protection and stirring condition, heating at 80-150 degrees C, reacting for 6-24 hours, when reaction is completed, cooling to room temperature, concentrating by decompression distilling to obtain crude product, and purifying by column chromatography to obtain (I). The compound (III) is cyclopentanone, cyclohexanone or cyclooctanone.    R1=H, methyl, ethyl, F, Cl, Br or cyano;    R2=H, methyl, ethyl, phenyl, p-fluorophenyl, p-chlorophenyl, p-bromophenyl, p-methylphenyl, p-methoxyphenyl, pyridyl, furyl or 3,4-dimethoxylphenyl; and    R3=methyl, ethyl, phenyl, p-fluorophenyl, p-chlorophenyl, p-bromophenyl, p-methylphenyl, or p-methoxyphenyl.
NOVELTY - Mulberry plant organic fertilizer comprises 30-40 pts. wt. silkworm excrement, 20-30 pts. wt. sheep manure, 15-20 pts. wt. soybean straw, 3-5 pts. wt. fish scale and fish bone and baking soda (specific amount).    USE - Used as mulberry plant organic fertilizer.    ADVANTAGE - The fertilizer has low production cost and is rich in organic content, promotes the growth of mulberry, and is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the mulberry organic fertilizer, comprising collecting good fish scale and fish bone, grinding, crushing soybean straw, mixing uniformly, adding baking soda, piling, and carrying out fermentation for 1-2 months under sealed condition.
NOVELTY - Biological organic fertilizer comprises 20-30 pts. wt. edible fungus residue, 10-20 pts. wt. weed powder, 30-50 pts. wt. human and animal excreta, 1-3 pts. wt. probiotic bacteria raw liquid, 15-20 pts. wt. gelatin and tartaric acid.    USE - Used as biological organic fertilizer.    ADVANTAGE - The fertilizer: improves soil conditioning and soil microbial activity, maintains soil structure, increases soil air permeability, increases soil fertility, reduces water loss and evaporation; reduces stress and damage in drought and saline condition; increases production rate and quality of grain crops, vegetables and fruits; and increases sugar and vitamin contents in melon and thus improves taste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the biological organic fertilizer, comprising adding probiotic bacteria raw liquid into raw materials, stirring uniformly, stacking in cellar, sealing and carrying out anaerobic fermentation for 8-10 days in summer, and 15-30 days in winter, completing alcohol fermenting, drying, crushing and directly bagging or directly using.
NOVELTY - High-yield organic fertilizer composition, comprises 50 pts. chicken manure (20-40%), 50 pts. pig manure, shrimp shell, 6 pts. crab shell, and 5 pts. clam shells.    USE - Used as high-yield organic fertilizer composition.    ADVANTAGE - The fertilizer balances the role of amino acid, stimulates the action of the active substance, and carries out fermentation of decomposed microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the high-yield organic fertilizer composition, comprising crushing shrimp shell, crab shell and clam shells, uniformly stirring with manures, drying at 60-70 degrees C for 1-2 hours, pelletizing into granules.
NOVELTY - Fungal organic fertilizer comprises 40% wheat straw foam, 20% rice straw foam, 20% pig manure, 10% carrot foam, and composite microbial inoculum (required amount).    USE - Used as fungal organic fertilizer.    ADVANTAGE - The fertilizer is rich in nutrient, is easy to use, can increase fungus yield by 10-15%, can increase production speed of fungus series, and can save energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer comprising uniformly stirring raw materials, under natural ventilating condition, adding composite microbial inoculum, plane strip stack type floor stacking fermenting, where the stack height is not greater than 1 m, width is not greater than 3 m, the fermentation time is 6-8 days, when temperature reaches to more than 60 degrees C, after fermentation, stacking to height of 2 m, carrying out second time fermentation for 5-7 days, under ventilating condition, finally obtaining organic fertilizer.
NOVELTY - Organic fertilizer composition comprises 20-40% corn cob, 25-50% corn straw, 45-65% animal manure and proper amount of water for fermentation.    USE - The organic fertilizer composition is useful for corn (claimed).    ADVANTAGE - The organic fertilizer composition is simple and economical to prepare, and improves the yield of corn.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing organic fertilizer composition, comprising crushing the corn cob and corn straw, then uniformly mixing with other raw materials, fermenting at 20-30 degrees C for 10-20 days, killing virus at high temperature, then preparing into granules at 60-100 degrees C.
NOVELTY - Organic fertilizer composition, comprises 20-40% chicken manure fermented material, 25-50% pig manure fermented material, 10-15% nitrogen, potash fertilizer, 10-15% phosphate fertilizer, and auxiliary agent.    USE - The fertilizer is useful for high yield fruit (claimed).    ADVANTAGE - The fertilizer has high nutrient content, saves energy, reduces environment pollution, increases plant chlorophyll content and promotes photosynthetic function, delays aging process, and increases crop yield by 10-15%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising uniformly stirring the mentioned materials, drying at 60-80 degrees C to 80%, and pressing into granules.
NOVELTY - Organic fertilizer composition comprises 50 pts. ash, 20 pts. sand, 25 pts. human and animal manure fermentation material and rice water.    USE - The organic fertilizer is useful for pumpkin (claimed).    ADVANTAGE - The organic fertilizer composition is simple and promotes growth of the pumpkin, increases fragrant and sweetness, and increases the yield to 15-20 %.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer composition, comprising stirring the above mentioned materials in fermentation cellar for 3-5 days, adding rice water, customizing, drying, and sprinkling directly around the roots of pumpkin.
NOVELTY - Organic fertilizer comprises 50-60 wt.% household waste, 15 wt.% chicken manure, 0.5-1 wt.% sterilizing liquid, 0.25-1 wt.% tartaric acid, and organic phosphorus and hydrogen peroxide (specific amount).    USE - Used as organic fertilizer.    ADVANTAGE - The fertilizer is energy-saving and environmentally friendly, provides nutrients to crops, and makes land more fertile.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising adding sterilizing liquid into household waste, stirring uniformly, removing water, added remaining raw material, stirring uniformly, adding hydrogen peroxide solution, fermenting at 20-40 degrees C for 15-20 days, carrying out drying, sterilizing at 60-80 degrees C for 30-50 minutes and processing into granular organic fertilizer.
NOVELTY - Organic fertilizer composition, comprises 20-40% sesame oil residue, 40-50% corn stalks, 35-40% chicken manure, 5-15% multivitamin and plant coenzyme.    USE - The organic fertilizer is useful for fruit tree (claimed).    ADVANTAGE - The organic fertilizer can penetrate into the plant root cell wall membrane, so as to promote the plant leaf to absorb nutrients and water quickly, promote photosynthesis, improve the plant chlorophyll content, reduce the aging process of plant leaf fibers, extend plant cell life, and increase fruit production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer composition, comprising chopping corn stalks, placing sesame oil residue, corn stalk and chicken manure in cellar and reacting, maintaining the temperature at 20-30 degrees C for 8-10 days, according to the land pH, stirring 3 times, adding multivitamin and plant coenzyme and adding lime powder to obtain the product.
NOVELTY - Green plant organic fertilizer composition comprises 20-30 pts. wt. straw leavening product, 10-20 pts. wt. banana leavening product, 3-5 pts. wt. spinach leaves, 5 pts. wt. rice water, and sand (specific amount).    USE - Used as green plant organic fertilizer composition.    ADVANTAGE - The organic fertilizer composition: contains adequate chlorophyll and nutrient supplement for promoting plant photosynthesis; contains spinach leaves mixed with rice water to flourish and produce more vivid colors; makes the soil more fertile; utilizes potassium-rich banana peel for promoting well-developed root system; and promotes the growth rate of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the green plant organic fertilizer composition, comprising taking the spinach leaves, crushing, adding remaining materials, stirring uniformly, placing in sealed environment, reacting for 3-5 days, then adding two times of rice water, stirring for two times, when sour taste is produced, finally drying at environment of 60-80 degrees C, then placing the dry material in a plastic bag to obtain the green plant organic fertilizer, and using method of the fertilizer comprising uniformly mixing and stirring the green plant and soil according to ratio of 2:8.
NOVELTY - Alcohol-based clean fuel comprises 65-75 pts. wt. methanol, 1-3 pts. wt. petroleum ether or naphtha, 15-30 pts. wt. gasoline, 0.1-0.2 pts. wt. ethyl tert.-butyl ether, 0.5-1.5 pts. wt. Tween (RTM: Non-inonic surfactant)-80 or benzotriazole, 0.5-2 pts. wt. quinoline, 1-3 pts. wt. oleic acid or triethanolamine, 0.3-1.5 pts. wt. tert.-butyl alcohol or isobutyl alcohol, 0.1-1 pts. wt. diethylene glycol butyl ether, 0.1-2 pts. wt. cyclohexanone and 0.1-1 pts. wt. cerium oxide.    USE - Alcohol-based clean fuel for vehicle.
NOVELTY - Preparing biomass pellet fuel involves taking biomass pellet as raw material, crushing biomass pellet, and then drying crushed biomass pellet to remove water content. The dried biomass pellet is mixed spiral mixing machine. The mixture is granulated, and then silicon carbide is added to granulated material. The obtained product is dried in a drying machine to obtain the desired product.    USE - Method for preparing biomass pellet fuel (claimed).    ADVANTAGE - The method enables to prepare biomass pellet fuel in a cost-effective and eco-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of biomass pellet fuel preparation method. (Drawing includes non-English language text).
NOVELTY - Performing biodiesel transesterification involves mixing methyl alcohol and alkali catalyst in a mixer (1) and then pumping the obtained mixture through waste oil metering pump into continuous ester exchange reactor (2). The obtained material is entered into a glycerine soap separator (3) and then the glycerin soap and methanol-containing crude methyl ester are separated. The glycerin soap is entered into a glycerol separator to separate glycerine and waste oil. The methanol-containing crude methyl ester is entered into a continuous methanol recycler (5) and rectifying tower (6).    USE - Method for performing biodiesel transesterification (claimed).    ADVANTAGE - The method enables to perform biodiesel transesterification with exchange reaction rate more than 95% and ester conversion rate more than 98%.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a method for performing biodiesel transesterification.    Mixer (1)    Continuous ester exchange reactor (2)    Glycerine soap separator (3)    Continuous methanol recycler (5)    Rectifying tower (6)
NOVELTY - Multifunctional carbosulfan is prepared by heating di-n-butylamine to 60-70 degrees C, stirring, cooling to 0 degrees C, slowly dripping disulfur dichloride, maintaining temperature at 60-80 degrees C, adding sulfuryl chloride, and preserving heat for 2 hours to obtain intermediate product, where mole ratio of di-n-butylamine and sulfuryl chloride is 1:55; reacting intermediate product with carbofuran under alkaline condition at 10-20 degrees C for 2 hours; and after reaction, adding water, stirring for 10 minutes, filtering unreacted carbofuran and recycling, and decompressing filtered liquid to obtain carbosulfan.    USE - Method for preparing multifunctional carbosulfan used in preventing pests including aphids in citrus and other fruits, vegetables, corn, cotton, rice, sugarcane and other crops.    ADVANTAGE - The method has carbosulfan yield rate of 90% and di-n-butylamino sulfur chloride yield of 88%. The multifunctional carbosulfan is fast-acting, low in residue, safe to use, and not harmful to crops.
NOVELTY - Glass steel mixing structure anaerobic device, which is cylindrical comprises a semi-spherical gas storage cabinet at the top part.    USE - Used as glass steel mixing structure anaerobic device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the glass steel mixing structure anaerobic device.
NOVELTY - The new type utility claims have one kind chicken manure and drying device, comprising pedestal, pedestal upper part set with a drying box, drying box upper part side edge set with feed inlet, feed inlet set with bottom transport belt, the transport belt two end with driving roller set, drying set with multiple layer internal transport belt, the transport belt one end set with baffle plate, a drying most bottom one side set with discharging mouth, the discharging mouth and end of transport belt of the lowest end relative, a drying most bottom set with heat source, a drying box top part set with waste sum collection device, a waste collecting device end sum and sum absorbing device connected with the waste. Automatic continuous drying the utility new type supply have one kind chicken manure and drying equipment, can realize chicken manure and, device and square meter floor space small, energy saving and environment-friendly, effective to avoid volatilization of harmful gas, improves have operating environment and drying process.
NOVELTY - Planting Pleurotus cornucopiae involves mixing 32 pts. wt. Sorghum shell, 60 pts. wt. straw powder, 8 pts. wt. corn powder, 1.5 pts. wt. lime powder and 1.3-1.4 pts. wt. water uniformly to obtain culture material that is packaged and sterilized. The obtained culture material is utilized for planting Pleurotus cornucopiae.    USE - Method for planting Pleurotus cornucopiae (claimed).    ADVANTAGE - The method enables to plant Pleurotus cornucopiae in low cost, safe and eco-friendly manner, and ensures increased soil organic matter, fertility and farmer income.
NOVELTY - Organic fertilizer comprises potato skin (7-15 pts. wt.), banana (6-10 pts. wt.), cassava residue (6-9 pts. wt.), straw (20-30 pts. wt.), pig manure (10-15 pts. wt.), and bentonite (6-10 pts. wt.).    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is economical and simple to prepare, and increases disease resistance and drought resistance in crop. The organic fertilizer does not damage soil and provides plant nutrients that are necessary for plant growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) mixing potato skin, banana, cassava residue, straw, pig manure and bentonite; and    (B) fermenting obtained mixture in closed condition for 10-12 days.
NOVELTY - An infected animal tissue harmless treatment method comprises weighing infected animal tissue, putting in reaction container, adding 25-50 wt.% water and 5-20 wt.% alkali, reacting under 0.2-0.5 MPa, heating at 110-150 degrees C, carrying out hydrolysis for 0.5-3 hours, stirring, carrying out hydrolysis for 3-9 hours, crushing, dehydrating and condensing for 3-12 hours, and cooling to 70 degrees C.    USE - Infected animal tissue harmless treatment method (claimed).    ADVANTAGE - The method is environment-friendly. The product is suitable for preparing biological fertilizer or compost.
NOVELTY - Synthesizing triazine derivatives (I and II) involves reacting sodium methyl mercaptan and compound A.    USE - Method for synthesizing triazine derivatives used for preparing herbicide (claimed).    ADVANTAGE - The method is efficient, eco-friendly, and economical, and does not produce odor, and has high yield and wide industrial applicability.    DETAILED DESCRIPTION - Synthesizing triazine derivatives (I and II) involves reacting sodium methyl mercaptan and compound A.    R1=alkyl group; and    R2=alkyl group or group of formula (III).    .
NOVELTY - Preparing humic acid involves heating wheat straw at high temperature for carbonization. Carbonized product is treated with activated nitric acid. Obtained product is extracted with alkali to obtain humic acid precipitate.    USE - : Method for preparing humic acid (claimed).    ADVANTAGE - The method is simple and convenient, and enables to prepare humic acid in mild conditions.
NOVELTY - Thioketal polymer comprises alkoxy compound (I) and mercapto compound polymerized together. Mercapto compound has -S-S- group or mercapto group (II).    USE - Thioketal polymer used for preparing drug carrier for biomedical and esthetic healthcare products (claimed).    ADVANTAGE - The thioketal polymer is safe, eco-friendly, and has biological compatibility and wide applicability in biological medicines, medical appliances and esthetic health care field.    DETAILED DESCRIPTION - Thioketal polymer comprises alkoxy compound (I) and mercapto compound polymerized together. Mercapto compound has -S-S- group or mercapto group of formula (II). Molecular weight of thioketal polymer is 10000-200000.    R=1-5C alkyl group.    .
NOVELTY - A Platycrater arguta culturing and propagating method involves collecting immature fruits of Platycrater arguta. The surfaces of the fruits are sterilized and washed, followed by picking off immature seeds and some ovary tissue and inoculating to culture medium at 18-22 degrees C under dark for 24 hours and in weak condition under illumination intensity of 20 mu mol.m-2s-1 and illumination time of 12 hour/days till the seed germination. The germinated seed is transferred into strong seedling rooting culture medium.    USE - Method for culturing and propagating Platycrater arguta.    ADVANTAGE - The method enables culturing and propagating the Platycrater arguta with reduced defect of undeveloped propagating of the seeds, reduced pollution rate and high operability, in a simple and practical manner.    DETAILED DESCRIPTION - A Platycrater arguta culturing and propagating method involves collecting immature fruits of Platycrater arguta. The surfaces of the fruits are sterilized and washed, followed by picking off immature seeds and some ovary tissue and inoculating to culture medium at 18-22 degrees C under dark for 24 hours and in weak condition under illumination intensity of 20 mu mol.m-2s-1 and illumination time of 12 hour/days till the seed germination. The germinated seed is transferred into strong seedling rooting culture medium at 18-22 degrees C, illumination intensity of 20 mu mol.m-2.s-1 and illumination time of 12 hour/days.
NOVELTY - A waste oil as raw material is centrifuged and dedoped. Phosphoric acid is added to waste oil, naturally-sedimented by gravity, dephosphorized, unglued and dehydrated. Concentrated sulfuric acid with concentration of 98% is added to waste oil, and methanol as gas phase is passed from the bottom. Fatty acids in raw material is completely converted to fatty acid methyl ester and settled. The supernatant comprising ester phase is collected. A solution of sodium hydroxide and methanol is added and fatty acid glyceride and methanol are transesterification-reacted, to obtain biodiesel.    USE - Usage of waste oil for production of biodiesel (claimed).    ADVANTAGE - The method provides biodiesel, without water-removal section and esterification section.
NOVELTY - A biogas purification system has cleaning module for purifying impurities in biogas supplied from anaerobic digestion, membrane for separating portion of carbon dioxide from biogas passing the refining module, and pressure swing adsorption module to produce high-purity biomethane while separating carbon dioxide from partially separated additional biogas.    USE - Biogas purification system is used for producing high-purity biomethane.    ADVANTAGE - The biogas purification system efficiently produces high-purity biomethane with high productivity, in short period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for control method of purification system of biogas.
NOVELTY - A landscape water body purification device comprises sedimentation area and processing area in which sedimentation area comprises gentle slope (6), steep slope (5), and sludge discharge pipe (8), and processing area comprises sand layer, gravel layer, and supporting layer.    USE - A landscape water body purification device for lake.    ADVANTAGE - Landscape water body purification device improves lake water quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of landscape water body purification device.    Bamboo baffle wall (4)    Steep slope (5)    Gentle slope (6)    Reverse flushing pipe (7)    Sludge discharge pipe (8)
NOVELTY - A microaerobic biological treatment device comprises microaerobic reactor (1), sedimentation tank (2), slurry dissolved oxygen tank (3), air blower (4), dissolved oxygen sensor (5), airflow rate control device (6), sludge return pump (7), microaerobic reactor water inlet pipe (8), microaerobic reactor water outlet pipe (9), sedimentation tank water outlet pipe (10), sludge return pipe (11), sludge discharge pipe (12), aeration pipe (13), and valve (14).    USE - A microaerobic biological treatment device for low carbon/nitrogen dry manure removal pig farm wastewater (claimed).    ADVANTAGE - Microaerobic biological treatment device is low-cost, has simple and compact structure, small occupied space, and low power consumption, and does not require external carbon source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of microaerobic biological treatment device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of microaerobic biological treatment device.    Microaerobic reactor (1)    Sedimentation tank (2)    Slurry dissolved oxygen tank (3)    Air blower (4)    Dissolved oxygen sensor (5)    Airflow rate control device (6)    Sludge return pump (7)    Microaerobic reactor water inlet pipe (8)    Microaerobic reactor water outlet pipe (9)    Sedimentation tank water outlet pipe (10)    Sludge return pipe (11)    Sludge discharge pipe (12)    Aeration pipe (13)    Valve (14)
NOVELTY - N4-(3-chloro-4-fluorophenyl)-7-(((3S)-tetrahydro-3-furanyl)oxy)-4,6-quinazoline diamine is prepared by performing reduction reaction on 4-((3-chloro-4-fluorophenyl)amino)-6-nitro-7-((S)-tetrahydrofuran-3-yloxy)quinazoline, potassium hydroxide, and saccharide substance mixture in polar solvent and water mixed solvent.    USE - Preparation of N4-(3-chloro-4-fluorophenyl)-7-(((3S)-tetrahydro-3-furanyl)oxy)-4,6-quinazoline diamine.    ADVANTAGE - Preparation of N4-(3-chloro-4-fluorophenyl)-7-(((3S)-tetrahydro-3-furanyl)oxy)-4,6-quinazoline diamine is non-toxic, easy, and low-cost and has high product yield and purity.
NOVELTY - Reinforced concrete-anaerobic tank system comprises an anaerobic tank (34), a purification tower, power machine body (52), water tank (53), water outlet (54), and a cool water entrance (55). Generators (51) of the reinforced concrete-anaerobic tank system comprises reinforced concrete building materials. The anaerobic tank is cylindrical and comprises top design gas storage cabinet, which is placed in contact with the ground. The bottom portion of anaerobic tank is provided with a raw-material introduction pipe, a raw-material distributor, and marsh gas outlet (46).    USE - Reinforced concrete-anaerobic tank system used for supplying power to gas station, town, farm, and sewage farm.    ADVANTAGE - The environment-friendly reinforced concrete-anaerobic tank system effectively increases the biogas production efficiency, in an economical manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of reinforced concrete-anaerobic tank system.    Anaerobic tank (34)    Marsh gas outlet (46)    Generators (51)    Power machine body (52)    Water tank (53)    Water outlet (54)    A cool water entrance (55)
NOVELTY - Anaerobic tank system comprises an anaerobic tank (34), a purification tower, anaerobic tank warming systems, power machine body (52), water tank (53), water outlet (54), and a cool water entrance (55). Generators (51) of anaerobic tank system comprises timber cushion layer, a concrete layer and building materials made of plastic film or rubber. The cylindrical anaerobic tank comprises top design gas storage cabinet, which is placed in contact with ground. The bottom portion of anaerobic tank is provided with raw-material introduction pipe, a raw-material distributor and biogas outlet (46).    USE - Anaerobic tank system used for supplying biogas to power supply station, gas station, town, farm, and sewage farm.    ADVANTAGE - The environment-friendly anaerobic tank system effectively increases biogas production efficiency, in an economical manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view anaerobic tank system.    Anaerobic tank (34)    Biogas outlet (46)    Generators (51)    Power machine body (52)    Water tank (53)    Water outlet (54)    Cool water entrance (55)
NOVELTY - Biogas electricity generating device comprises a feed tube (10) and a fermentation pipeline (30) that runs slurry under certain pressure difference. The center position of the fermentation pipeline annular conduit is provided with a spacer ring (36). The feed tube and discharge tube sidewalls (42) are arranged in vertical insertion tube separator, and extends to the annular fermentation slurry pipe below the liquid level position. The spacer ring has a fermentation gas pipeline plate that forms a fermentation zone between adjacent air resistance plate (34) and a fermentation area (303).    USE - Biogas electricity generating device.    ADVANTAGE - The biogas electricity generating device effectively promotes flow of slurry to perform fermentation by pressure difference.    DESCRIPTION OF DRAWING(S) - The drawing shows a three-dimensional schematic view of a biogas electricity generating device.    Feed tube (10)    Fermentation pipeline (30)    Air resistance plate (34)    Spacer ring (36)    Discharge tube sidewalls (42)    Fermentation area (303)
NOVELTY - Producing biogas involves performing fermentation of raw materials into U-shaped fermentation pipeline (30) to produce biogas, which is then collected in the provided inlet/outlet pipe placed between feedstock sidewall (10) and a feedstock pipe (12). The feedstock pipe in placed adjacent to fermentation gas block area. The fermentation gas block area is connected to biogas storing chamber and biogas fermentation zone. The squeeze biogas fermentation zone is linked to U-shaped fermentation pipeline to flow slurry within it. Discharge tube (20) leads to a feeding tube and bacterial chamber (50).    USE - Method for producing biogas using ultra high-efficient biogas production system (claimed).    ADVANTAGE - The method enables to produce biogas using ultra high-efficient biogas production system, in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas production system.    Feedstock sidewall (10)    Feedstock pipe (12)    Discharge tube (20)    U-shaped fermentation pipeline (30)    Bacterial chamber (50)
NOVELTY - Producing biogas involves performing raw material fermentation by passing it into feeding tube (10), which then leads to U-type fermentation pipeline (30) to produce biogas. The feeding tube is provided with one-way check valve to complete circular flow of raw material fermentation. The generated biogas is then collected by sidewall of feeding tube, where the space between the sidewall of feeding tube is provided with a discharge tube (20) that leads to a hydraulic part (40) and a bacterial pipeline (50).    USE - Method for producing biogas through U-shaped biogas generating system (claimed).    ADVANTAGE - The method enables to produce biogas through U-shaped biogas generating system that is provided with multiple sections to control fermentation raw material slurry flow, in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of through U-shaped biogas generating system.    Feeding tube (10)    Discharge tube (20)    U-type fermentation pipeline (30)    Hydraulic part (40)    Bacterial pipeline (50)
NOVELTY - Scenedesmus quadricauda SDEC-13 strain is preserved in China center for type culture collection under accession number (CCTCC NO: M2014498), and is new.    USE - Scenedesmus quadricauda SDEC-13 strain used for extracting oils for production of bio-diesel and for treating sewage and/or waste gas use (all claimed).    ADVANTAGE - The lipid-rich Scenedesmus quadricauda SDEC-13 strain shows great potential to yield high amount of oil, and easily converts carbon dioxide found in the exhaust gas to biomass. The environmental-friendly and cost-friendly Scenedesmus quadricauda SDEC-13 strain comprises 27.2% dry weight lipid and 82.87% saturated fatty acid content. The carbon source nutrients effectively enhances saturated fatty acid content in Scenedesmus quadricauda SDEC-13 strain from 82.87% to 98%. - Scenedesmus quadricauda SDEC-13 strain effectively treats industrial waste water or municipal domestic sewage water, and industrial waste gas. Scenedesmus quadricauda SDEC-13 strain powder having 82.87% saturated fatty acid content yields biodiesel containing cetane number 57. 82.87% Saturated fatty acid content results to low iodine value i.e. 83. 36 g iodine/100g in biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for culturing Scenedesmus quadricauda SDEC-13 strain, which involves:    (A) growing Scenedesmus quadricauda SDEC-13 strain into bluegreen medium at 25 plus minus 1 degrees C and illumination intensity 2000-3000Lux for 7 days; and    (B) transferring grown algal cells into selenium-enriched culture media under carbon dioxide condition at 25 plus minus 1 degrees C and illumination intensity 2000-3000Lux for 7 days to obtain the product.
NOVELTY - Endophytic fungi NT12J04 strain, is preserved in China center for type culture collection under accession number (CCTCC NO: M2014332) and is new. The The 18 s rDNA test shows that the genome of endophytic fungi NT12J04 strain has 1678 nucleobases sequence (SEQ ID NO: 1), given in the specification.    USE - Endophytic fungi NT12J04 strain used for producing elicitors, which acts as bio-fertilizer for promoting growth of Dendrobium candidum (claimed).    ADVANTAGE - The Endophytic fungi NT12J04 strain efficiently promotes growth of Dendrobium candidum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing elicitors, which involves:    (A) inoculating endophytic fungi NT12J04 strain into fungal culture medium to obtain endophytic fungi NT12J04 strain mycelia, which are then subjected to fermentation to obtain fermentation broth, which is then preserved with sterilized liquid nitrogen; and    (B) subjecting fermentation broth to filtration to collect filtrate containing elicitors, which are then introduced into Murashige and Skoog medium to culture Dendrobium candidum plants.
NOVELTY - Endophytic fungi NT04Y01 strain is preserved in China center for type culture collection under accession number (CCTCC NO: M2014331), and is new. The 18 s rDNA test shows that the genome of endophytic fungi NT04Y01 strain has 1682 nucleobases sequence (SEQ ID NO: 1), given in the specification.    USE - Endophytic fungi NT04Y01 strain used for producing elicitors, which acts as bio-fertilizer for promoting growth in Dendrobium officinale (claimed).    ADVANTAGE - The endophytic fungi NT04Y01 strain efficiently promotes growth in Dendrobium officinale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing elicitors, which involves:    (A) inoculating endophytic fungi NT04Y01 strain into fungal culture medium to obtain endophytic fungi NT04Y01 strain mycelia, which are then subjected to fermentation to obtain fermentation broth, which is then preserved with sterilized liquid nitrogen; and    (B) subjecting fermentation broth to filtration to collect filtrate containing elicitors, which are then introduced into Murashige and Skoog medium to culture Dendrobium officinale plants.
NOVELTY - Culture medium comprises 1-20 millimolar glucose, 50-400 picogram/ml iron oxide nanoparticles, 1-30 nanomolar insulin, 80-120 Units/l penicillin, 80-120 Units/l streptomycin, and Dulbecco modified eagle medium.    USE - Culture medium used for inducing differentiation of human umbilical cord mesenchymal stem cells into fat-like cells (claimed).    ADVANTAGE - The culture medium comprises a simple-inducible factor, which is non-toxic and non-hazardous substances. The culture medium greatly reduces the maturation time, and thus greatly reducing the time to induce differentiation in human umbilical cord mesenchymal stem cells. The culture medium thus has broad clinical application prospects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for inducing differentiation of human umbilical cord mesenchymal stem cells into fat-like cells, which involves soaking human umbilical cord mesenchymal stem cells into the prepared culture medium for nine days to obtain fat-like cells.
NOVELTY - Processing kitchen waste involves collecting kitchen waste for the removal of inorganic and refractory organic material. The inorganic and refractory organic material removed-kitchen waste is then formulated with water in a molar ratio of 1:4, where the obtained solid slurry is pulverized and then sieved to obtain remaining kitchen waste slurry, which is then subjected into conditioning agent containing tank.    USE - Method for processing kitchen waste for obtaining biohydrogen (claimed).    ADVANTAGE - The method enables to process kitchen waste using anaerobic fermentation at room temperature, in an efficient manner.    DETAILED DESCRIPTION - Processing kitchen waste involves collecting kitchen waste for the removal of inorganic and refractory organic material. The inorganic and refractory organic material removed-kitchen waste is then formulated with water in a molar ratio of 1:4, where the obtained solid slurry is pulverized and then sieved to obtain remaining kitchen waste slurry, which is then subjected into conditioning agent containing tank. The obtained precipitated remaining kitchen waste slurry is then subjected to filtration to remove larger precipitated substances. The remaining precipitate-free kitchen waste slurry is subjected to heat treatment at 80-180 degrees C and 1-1.5 atmospheric pressure for 0.25-1.0 hours. The processed kitchen waste slurry is then treated with hydrogen production bacteria in a sealed fermenter to generate fermented hydrogen, which is then passed through a heat exchanger to obtain biohydrogen.
NOVELTY - Method for enhancing fermentation efficiency of lignocellulosic biomass, involves (a) providing a lignocellulosic biomass, (b) preprocessing the lignocellulosic biomass by mixing the lignocellulosic biomass with acid solution, (c) neutralizing acid-treated lignocellulosic biomass using alkali solution, (d) saccharifying the lignocellulosic biomass obtained in step (c) to obtain saccharified solution, and (e) subjecting the saccharified solution to capacitive deionization (CDI) for removing organic acid.    USE - The method is useful for enhancing fermentation efficiency of lignocellulosic biomass (claimed) which is used for producing ethanol.
NOVELTY - Preparation of solid catalyst involves adding aluminum isopropoxide into a sealed container at ambient temperature, adding ultrapure water, mixing, heating at 85 plus minus 3 degrees C for 1-45 minutes, adding nitric acid solution, stirring, adding calcium nitrate tetrahydrate solution, mixing, maintaining the resultant solution for 30-60 minutes, heating at 70-75 degrees C, drying the resultant material in an oven at 100-120 degrees C for 6-24 hours, milling the dried catalyst, and calcining at 300-800 degrees C for 1-24 hours.    USE - Preparation of solid catalyst used for transesterification of microalgae and vegetable oil for production of methyl and ethyl ester biodiesel.    ADVANTAGE - The method provides solid catalyst having excellent catalytic activity. The production of methyl and ethyl ester biodiesel is economically performed using the solid catalyst, with reduced water consumption and without requiring refining process.
NOVELTY - Continuous bulk polymerization of medicinal polyacrylic resin comprises (i) mixing 30-60 pts. wt. dimethylaminoethyl methacrylate and 40-70 pts. wt. other acrylic monomers to form a monomer mixed liquid; (ii) adding an initiator to the monomer mixed liquid, and carrying out pre-polymerization to obtain a viscous liquid; (iii) conveying the viscous liquid to a continuous operation reactor, gradually heating and reacting, keeping the material in a molten viscous flow state to obtain the molten material; and (iv) devolatilizing the molten material to remove the residual monomers.    USE - The method is useful for continuous bulk polymerization of medicinal polyacrylic resin (claimed).    ADVANTAGE - The method is safe and environmentally friendly.    DETAILED DESCRIPTION - Continuous bulk polymerization of medicinal polyacrylic resin comprises (i) mixing 30-60 pts. wt. dimethylaminoethyl methacrylate and 40-70 pts. wt. other acrylic monomers to form a monomer mixed liquid, where the other acrylic monomer is methyl methacrylate, butyl methacrylate, ethyl acrylate and/or butyl acrylate; (ii) adding an initiator accounting for 0.3-5% of the monomer mixed liquid to the monomer mixed liquid, and carrying out pre-polymerization at 50-80 degrees C for 60-120 minutes to obtain a viscous liquid with the transformation rate of 5-30%, where the viscosity is 1000-100000 mPax second; (iii) conveying the viscous liquid to a continuous operation reactor at the flow rate of 0.1-0.3 l/minute, gradually heating and reacting at 0.6-10 MPa, keeping the material in a molten viscous flow state to obtain the molten material, where the temperature is 70-300 degrees C; and (iv) devolatilizing the molten material to remove the residual monomers and controlling dimethylaminoethyl methacrylate of the molten material to less than or equal to 0.1%, butyl methacrylate to less than or equal to 0.08% and methyl methacrylate to less than or equal to 0.08%.
NOVELTY - Staphylococcus pasteuri KY-06 with preservation number CGMCC No. 8839 is new.    USE - Staphylococcus pasteuri KY-06 with preservation number CGMCC No. 8839 for anaerobic digestion biogas reaction (claimed) used for sewage treatment.    ADVANTAGE - S. pasteuri KY-06 maintains anaerobic digestion system stability and has strong degradation ability, and anaerobic digestion biogas reaction is low-cost and has no secondary pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic digestion biogas reaction which involves inoculating S. pasteuri in enrichment culture medium, shaking and culturing at 30 degrees C to logarithmic growth phase to obtain 106-1010 cells/ml bacteria liquid, centrifuging to obtain supernatant, measuring cellulose and organic matter catabolism ability, and inoculating in anaerobic digestion reaction system with inoculum amount of 0.1-0.5.    DESCRIPTION OF DRAWING(S) - The drawing shows an image of the phylogenetic tree of S. pasteuri KY-06. (Drawing includes non-English language text).
NOVELTY - A catalyst contains 0.5-5 %mass cerium oxide-cobalt oxide component as carrier and 0.1-0.5 %mass palladium.    USE - The catalyst is useful for catalytic combustion of methane.    ADVANTAGE - The catalyst improves methane combustion activity and reduces methane combustion temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst, which involves mixing 75 wt.% cobalt oxide with mesoporous silica (KIT)-6 template to obtain cobalt oxide-KIT-6 template, then adding 25 wt.% cobalt oxide-KIT-6 template and mixture of cerium oxide and palladium to obtain palladium-cerium oxide-cobalt oxide-KIT-6 template, and finally removing KIT-6 template with sodium hydroxide solution.
NOVELTY - Cultivation method of mushroom using crop straw involves (a) cooking crop straw, adding cellulase to crop straw to obtain enzymolysis residues, (b) preparing mushroom cultivation medium, and (c) inoculating mushroom into medium and cultivating mushroom.    USE - The method is useful for cultivating mushroom chosen from Pleurotus ostreatus, Pleurotus pulmonarius, Pleurotus eryngii, Flammulina, Agrocybe aegerita, Ganoderma lucidum, Hericium erinaceus and Phellinus igniarius, preferably P.ostreatus and P.igniarius (all claimed).    ADVANTAGE - The method improves mushroom yield, and is cost-effective and reduces environmental pollution by completely utilizing by-product of straw fermentation industry (i.e. digested residue).
NOVELTY - A Bacillus thuringiensis strain JB-007 (KACC91894P) having absorption efficacy of anionic dye and heavy metal, is new.    USE - The B.thuringiensis strain JB-007 is useful in biomass and biosorption agent for providing absorption efficacy of anionic dye and metal (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition comprising the strain or its culture medium as an active ingredient;    (2) biological biomass for anion absorber using the strain;    (3) biosorption agent comprising the biological biomass of the strain; and    (4) method for preparing the biological biomass, involves culturing the strain, performing acid treatment of the culture, and drying culture.
NOVELTY - A Bacillus catenulatus strain JB-022 (KACC91896P) having absorption efficacy of cationic dye and metal, is new.    USE - The B.catenulatus strain JB-022 is useful in biomass and biosorption agent for providing absorption efficacy of cationic dye and metal. The cationic metal is heavy metal, precious metals and rare metals including copper, zinc, calcium, barium, magnesium, strontium, cobalt, nickel, iron, cadmium, lead, chromium, manganese, silver, tin, antimony, molybdenum, indium, gallium, vanadium, neodymium, lanthanum, cerium and yttrium (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) composition comprising the strain or its culture medium as an active ingredient;    (2) biological biomass for cation absorber using the strain;    (3) biosorption agent comprising the biological biomass of the strain; and    (4) method for preparing the biological biomass, involves culturing the strain, performing acid treatment of the culture, and drying culture.
NOVELTY - Gas-phase pressure swing adsorption separation of ethylbenzene involves conveying 8C aromatic hydrocarbon mixture as raw material into a pressure swing adsorption apparatus, carrying out pressure swing adsorption separation to obtain ethylbenzene-rich pressure swing adsorption aspirate, and separating the non-aromatic hydrocarbon in the aspirate to obtain ethylbenzene, separating the non-aromatic hydrocarbon in the adsorption residue to obtain m-xylene and o-xylene, and countercurrent depressurizing. The 8C aromatic hydrocarbon mixture does not contain p-xylene.    USE - Gas-phase pressure swing adsorption separation of ethylbenzene (claimed).    ADVANTAGE - The method enables gas-phase pressure swing adsorption separation of ethylbenzene having high purity.
NOVELTY - Tomato cultivation medium and its preparation method are claimed. The cultivation medium comprises rice husk, beans vine, cucumber vines, Rhodospirillales, river sand, fermentation microorganism I and fermentation microorganism II, where the fermentation microorganism I contains high temperature resistant actinomycetes, Monascus purpureus, Aspergillus niger, Bacillus subtilis, Candida utilis and Kluyveromyces marxianus, and the fermentation microorganism II comprises Lactobacillus plantarum and L.bifidus.    USE - The tomato cultivation medium is useful for preventing tomato root diseases.    ADVANTAGE - The tomato cultivation medium is rich in nitrogenase enzyme, active amino acids, plant growth regulators and nutrients, and safe, as it is nontoxic, environmentally-friendly and odorless, and does not directly damage seedlings.    DETAILED DESCRIPTION - Tomato cultivation medium and its preparation method are claimed. The cultivation medium comprises 30 wt.% rice husk, 10 wt.% beans vine, 20 wt.% cucumber vines, 10 wt.% Rhodospirillales, 30 wt.% river sand, 0.1 wt.% fermentation microorganism I and 0.1 wt.% fermentation microorganism II, where the fermentation microorganism I comprises 20% high temperature resistant actinomycetes, 10% Monascus purpureus, 10% Aspergillus niger, 10% Bacillus subtilis, 10% B.megaterium, 10% B.altitudinis, 10% B.atrophaeus, 10% Candida utilis and 10% Kluyveromyces marxianus, and the fermentation microorganism II comprises 50% Lactobacillus plantarum and 50% L.bifidus.
NOVELTY - An disodium tedizolid phosphate compound (I) is new, where it has X-ray powder diffraction pattern with peaks given in the specification.    USE - Compound (I) is used for medical technology field (claimed).    ADVANTAGE - The green and environment-friendly method has simple and easy operation, mild reaction condition, and small dosage of organic solvent.    DETAILED DESCRIPTION - An disodium tedizolid phosphate compound of formula (I) is new, where it has X-ray powder diffraction pattern with peaks given in the specification.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Biogas digester comprises a wall (1), the bottom (2), top hood (3) and two external circulation pipes. The bottom and top hood are connected by walls. The groups of external circulation pipe are located on opposite sides of the wall. Each set of external circulation pipe comprises a horizontal pipe (4) and bend tube (5).The horizontal pipe is connected with the side wall and located in the upper end of the side wall. The elbow is located on the side wall of the lower end. The circulation pump is connected with the horizontal pipe. The elbow and cover of circulation pump are located outside.    USE - Biogas digesters used for stirring and swirling outer loop (claimed).    ADVANTAGE - The biogas digester is side-mounted, easy to install, easy to transport, and suitable for rural areas.    DETAILED DESCRIPTION - Biogas digester comprises a wall (1), the bottom (2), top hood (3) and two external circulation pipes. The bottom and top hood are connected by walls. The groups of external circulation pipe are located on opposite sides of the wall. Each set of external circulation pipe comprises a horizontal pipe (4) and bend tube (5).The horizontal pipe is connected with the side wall and located in the upper end of the side wall. The elbow(5) is located on the side wall of the lower end. The circulation pump is connected with the horizontal pipe. The elbow and cover of circulation pump are located outside the circulation pump.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biogas digester.    Wall (1)    Bottom (2)    Top hood (3)    Horizontal pipe (4)    Bend tube (5)
NOVELTY - An Sphingomonas hengshuiensis (CCTCC NO: M2014575) for degrading cypermethrin, is new.    USE - The S.hengshuiensis is useful for degrading cypermethrin and pesticide residues (all claimed).    ADVANTAGE - The S.hengshuiensis has 91.3% cypermethrin degradation rate, and is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing lyophilized S.hengshuiensis powder which involves (a) taking 50 ml and 1.5 ml centrifuge tubes, washing tubes with tap water for several times, then rinsing washed tubes with distilled water for 2-3 times and autoclaving tubes at 121 degrees C for 20 minutes, (b) taking S.hengshuiensis strain containing culture medium in 50 ml centrifuge tubes, centrifuging at 28 degrees C and 150 rotations per minute for 2 days, separating cells and washing separated cells with sterile distilled water, (c) pre-freezing cells obtained in step (b) at -80 degrees C for 1-2 hours, (d) centrifuging samples obtained in step (c), freeze-drying at -1 to -50 degrees C for 30 minutes and then maintaining in freeze-dryer for 8-20 hours, and (e) transferring freeze-dried S.hengshuiensis aseptically into sterile 1.5 ml centrifuge tubes, sealing with paraffin film, labeling tubes with species name and other information, and storing at -20 degrees C.
NOVELTY - Method of fermenting sludge, involves subjecting the sludge to fermentation process, mixing wood material with fermented sludge, then adding humic acid and urea, stirring uniformly, stacking the mixture at 20-25 degrees C for 3-5 days, where the weight ratio of sludge and wood material is 40-45:55-60, and the humic acid and urea is 70-75:25-30.    USE - The method is useful for fermenting sludge (claimed) which is used as fertilizer.    ADVANTAGE - The method increases the yield of fertilizer, prevents loss of nutrient component in sludge and wood chips, increases efficiency and quality of fertilizer and enhances utilization rate of fertilizer.
NOVELTY - Preparing Eucommia ulmoides pinoresinol diglucoside, using Eucommia ulmoides powder as raw material to prepare Eucommia ulmoides pinoresinol diglucoside, comprises adding cellulase and then adding water in Eucommia ulmoides powder to extract, using two level film separation technology combined resin adsorption elution process to extract pinoresinol diglucoside, separating and purifying, collecting ethanol eluate, concentrating under reduced pressure, and vacuum drying to obtain the product pinoresinol diglucoside powder.    USE - The method is useful for preparing Eucommia ulmoides pinoresinol diglucoside (claimed).    ADVANTAGE - The method can achieve dissolution rate more than 90%, has short extraction time, has simple separating process, can maintain stably the membrane flux for long time, which is easy to clean and has long use life, uses nanofiltration membrane to reduce the load of the subsequent process, and prolong the use life of resin, achieves chemical oxygen demand value of not greater than 100 of nano-filter liquor, which can be recycled in production process, has no waste water discharge, uses macroporous resin to purify pinoresinol diglucoside, and prepares pinoresinol diglucoside powder with purity more than 40%, and extraction rate more than 1%.
NOVELTY - An ether chloroaluminate ionic liquid comprises ether and chloroaluminate in a ratio of 0.6-0.75.    USE - Ether chloroaluminate ionic liquid is used as catalyst in production of gasoline (claimed).    ADVANTAGE - The gasoline with high octane value can be produced with high selectivity using ether chloroaluminate ionic liquid under mild reaction condition with reduced energy consumption by environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of gasoline, which involves reacting isobutane and butene at 10-100 degrees C for 10-90 minutes under pressure of 0.4-2 MPa in presence of ether chloroaluminate ionic liquid as catalyst.
NOVELTY - Recycling landfill garbage involves analyzing and removing composted garbage of landfill, where composted garbage is screened using screening machine and then disposed off separately.    USE - Method for recycling landfill garbage (claimed).    ADVANTAGE - The method enables to recycles landfill garbage that ensures effective use of landfill for long time.
NOVELTY - Organic humus comprises organic matter, soil, mushroom and beneficial microorganisms. Organic humus is subjected to aging process by utilizing mixture of Agaricus bisporus, fermented cassava residue, plant ash and bamboo-humus in ratio of 4-6:2-3:5-10:1-2. Organic humus soil comprises 1.5-3% total nutrient content, 25% brown organic matter granules, 30-45% water content, where total porosity of the organic humus soil 0.5-0.8g/cm3, pH is 5.8-7.0 and particle diameter is 0.1-4mm.    USE - Organic humus used for planting (claimed) in forest, municipal and garden greening.    ADVANTAGE - The organic humus replaces grass peat, and is nutritious.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic humus, which involves:    (A) drying components in sunlight and then crushing through a machine to obtain powder; and    (B) sieving the powder, adding bacillus composition, and then fermenting for 30-60 days to obtain final product.
NOVELTY - Organic granular substrate comprises fermented corn cob granules, vermiculite and ash or carbon bran in volume ratio of 70-90:5-15:5-15. The diameter of particle size is less than 6mm. The organic granular substrate has 50-60% particle of diameter 3-4mm. The organic granular substrate has 3-5% of total nutrient content, 50% organic matter content, 35-45% moisture content, 75-90% total porosity, 0.4-0.6g/cm3 bulk density and 1:2-3 gas-water ratio. The pH of organic granular substrate is 5.8-6.8.    USE - Organic granular substrate used for cultivating flower (claimed).    ADVANTAGE - The organic granular substrate has brown or deep brown color without peculiar smell, and ensures good air permeability.
NOVELTY - A high temperature resistant alpha -amylase mutant has amino acid sequence of fully defined 483 amino acids (SEQ ID NO: 7), given in the specification is new.    USE - A high temperature resistant alpha -amylase mutant for food, detergents, cosmetics, and feed.    ADVANTAGE - Product has high stability and enzyme activity and increased efficiency and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high temperature resistant alpha -amylase mutant.
NOVELTY - Bio-organic fertilizer comprises 97-98 pts. wt. fermented compost, 1-2 pts. wt. nano-carbon powder, 0.5-1 pt. wt. microbial agent and 0.4-0.5 pt. wt. trace element chelate powder. The fermented compost comprises rapeseed meal, soybean meal, fulvic acid and microbial agent for fermentation. The microbial inoculum comprises Paenibacillus azotofixans, Bacillus megaterium and B.mucilaginosus. The viable count of microbial inoculum is greater than or equal to 5000 million/g. The fertilizer contains linoleic acid, free amino acids and fulvic acid.    USE - The bio-organic fertilizer is useful for planting tobacco (claimed).    ADVANTAGE - The bio-organic fertilizer improves yield and quality of crops, preferably tobacco, and promotes soil improvement and quantity of fragrance substances in tobacco leaves.    DETAILED DESCRIPTION - Bio-organic fertilizer comprises 97-98 pts. wt. fermented compost, 1-2 pts. wt. nano-carbon powder, 0.5-1 pt. wt. microbial agent and 0.4-0.5 pt. wt. trace element chelate powder. The fermented compost comprises rapeseed meal, soybean meal, fulvic acid and microbial agent for fermentation in a mass ratio of 60-70:20-30:5-10:0.5-1. The microbial inoculum comprises Paenibacillus azotofixans, Bacillus megaterium and B.mucilaginosus in a mass ratio of 4-5:3-4:2-3. The viable count of microbial inoculum is greater than or equal to 5000 million/g. The fertilizer contains greater than or equal to 4% linoleic acid, greater than or equal to 3% free amino acids and greater than or equal to 5% fulvic acid. An INDEPENDENT CLAIM is included for method for preparing the bio-organic fertilizer, which involves mixing the rapeseed meal, soybean meal, fulvic acid and microbial agent for fermentation, fermenting obtained mixture to obtain fermented compost, mixing the fermented compost with remaining components, and fermenting obtained product.
NOVELTY - Fertilizer comprises 40-50 pts. wt. inorganic fertilizer, 20-30 pts. wt. organic fertilizer, 5-10 pts. wt. amino acid composition, 0.1-0.5 pt. wt. microelement, 0.05-0.1 pt. wt. fertilizer activating agent, 0.1-0.5 pt. wt. water-retaining agent, 0.1-0.5 pt. wt. soil conditioner and 0.05-0.1 pt. wt. pest repellent.    USE - As fertilizer for Ilex (claimed).    ADVANTAGE - The fertilizer improves soil environment, quality of Ilex and yield of Ilex to 10%.    DETAILED DESCRIPTION - Fertilizer comprises 40-50 pts. wt. inorganic fertilizer, 20-30 pts. wt. organic fertilizer, 5-10 pts. wt. amino acid composition, 0.1-0.5 pt. wt. microelement, 0.05-0.1 pt. wt. fertilizer activating agent, 0.1-0.5 pt. wt. water-retaining agent, 0.1-0.5 pt. wt. soil conditioner and 0.05-0.1 pt. wt. pest repellent. The inorganic fertilizer comprises nitrogen, phosphorus and potassium in a mass ratio of 15-20:5-10:5-10. The organic fertilizer is obtained by mixing Saccharomyces cerevisiae, fermentation agent, and calcium superphosphate to obtain a liquor, adding water to the liquor, stirring the mixture, adding rapeseed meal, peanut bran, soybean meal, and straw powder to liquor, and fermenting mixture by agitation for 20-30 days. An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves mixing pest repellent, microelement, fertilizer activating agent, water-retaining agent, soil conditioner, amino acid composition, organic fertilizer and inorganic fertilizer, crushing the mixture, granulating the mixture, sieving the granules, and packaging granules after detection .
NOVELTY - Cover material comprises 5-30 pts. wt. straw, 5-30 pts. wt. paper, 5-20 pts. wt. pulp sludge, 20-50 pts. wt. kaolin, 0.01-0.1 pt. wt. Eucalyptus bark and 0.01-0.5 pt. wt. microbial solution. The microbial solution is solution comprising fungal spores.    USE - The cover material is useful for covering fibrous garbage of landfill (claimed).    ADVANTAGE - The cover material enables rapid degradation of garbage, and has good physical strength and flame retardance property.
NOVELTY - The tank has a cylindrical-shaped closed cover (1) attached with a gear motor (15) and an agitator part (5), which is mounted on a shaft scraper element (10) that is hinged with a breaking element (9) and mixing elements (7, 8). A heating system includes a heat exchanger, which comprises a coil and fermentation material delivery tubes (25, 27). A jacket (20) of a tank connection part (21) is attached with the heating system, and the agitator is equipped with a rigid structure (16) fixed at the motor. The material delivery tubes include an outlet (26) with a bottom portion (13) along an axis.    USE - Fermentation tank i.e. micro biogas fermentation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fermentation tank.    Cylindrical-shaped closed cover (1)    Agitator (5)    Mixing elements (7, 8)    Breaking element (9)    Shaft scraper element (10)    Bottom portion (13)    Gear motor (15)    Rigid structure (16)    Jacket (20)    Tank connection part (21)    Fermentation material delivery tubes (25, 27)    Outlet (26)
NOVELTY - The method involves selecting oxidizing agent inflow and specific orbiter for a control unit through a pre-stored database (DB). The chosen inflow oxidizing agent is output by an output unit to an oxidizing agent pipe. The chosen specific orbiter is output in a cooling body. An orbiter is fixed at the cooling body to generate a gasification product and cool a pulverized coal pipe. The oxidizing agent pipe and the cooling body are fixed together while surrounding the pulverized coal pipe. An oxidizing agent and pulverized coal are discharged to form a spiral flow in the orbiter.    USE - Method for operating a fuel injection system for a coal gasifier.    ADVANTAGE - The method enables utilizing the DB database before operating the fuel injection system for the coal gasifier, inputting the pulverized coal inflow, demand yield of the gasification product and pulverized coal, selecting the orbiter from multiple orbiters, easily producing the gasification product for the coal gasifier in an optimum condition, forming screw threads on the inner periphery of the cooling body, detaching the orbiter from the cooling body so as to improve efficiency of the fuel injection system for the coal gasifier, controlling an opening and closing area of the oxidizing agent pipe, preventing yield of actual gasification product from being reached in demand yield, and controlling oxidizing agent inflow.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel injection system for a coal gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel injection system. '(Drawing includes non-English language text)'
NOVELTY - Manufacture of hydrogen-reduced compound involves performing reductive hydrogenation of organic compound comprising nitro group, unsaturated carbon double bond, unsaturated carbon triple bond or aromatic ring in a batch-type by contacting with hydrogen using reaction installation provided with reactors (3,4), and reducing nitro group, unsaturated carbon double bond, unsaturated carbon triple bond or aromatic ring of the organic compound.    USE - Manufacture of hydrogen-reduced compound (claimed).    ADVANTAGE - The method enables economical, smooth and efficient manufacture of hydrogen-reduced compound without fluctuation of hydrogen consumption and without providing hydrogen gas accumulator of high installation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of structure of reaction installation.    Hydrogen supply line (2)    Reactors (3,4)    Controlling valve (5)    Controlling valve (6)    Stirrers (9,10)
NOVELTY - Process for thermal cracking of fuel involves cracking fuel on a solid carrier to produce hydrogen and carbon species and combusting carbon on the solid carrier. The reactions are carried out in fluidized bed(s) (2,3).    USE - Process for thermal cracking of fuel used to produce hydrogen and/or syngas.    ADVANTAGE - The fuel is thermally cracked economically with excellent solid-handling and heat transfer performances and minimized water consumption and high methane utilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fluidized bed system (1), which consists of fluidized beds containing solid carrier(s) arranged alternately to crack fuel and regenerated in a combustion process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of fluidized bed system.    Fluidized bed system (1)    Fluidized beds (2,3)    Fuel supply (6)    Regeneration gas supply (8)    Product line (10)
NOVELTY - The method involves heating a shredded or crushed fibrous biomass into tubular and hollow printed product. The printed product is carbonized. An interval of the blades of a screw (29f) from a screw type extrusion molding machine to produce printed products is 10 times or more than the length (L) of the maximum sieve opening which the shredded or crushed fibrous biomass goes through. The friction resistance of the fibrous biomass is applied to move to the side of a hot printing section.    USE - Method for producing carbonized product.    ADVANTAGE - The coke usage amount is reduced, and the reduction in the amount of carbon di-oxide that is released is derived from fossil fuels is achieved. The increase in the cost of production of carbonized products due to expanded facilities is reduced, and the power consumption is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for screw type extrusion molding machine for use in manufacture of fibrous biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the printing machine.    Printing machine (29)    Sheath (29a)    Mold (29b)    Screw (29c)    Screw blade (29f)
NOVELTY - Producing jet fuel components comprises e.g. (a) generating or providing syngas, (b) converting the syngas using an alcohol-synthesis catalyst to a first stream comprising methanol, ethanol, and, optionally, higher alcohols, (c) separating the methanol from the ethanol and, optionally, higher alcohols, (d) converting at least some of the methanol to dimethyl ether, (e) converting the dimethyl ether to at least one jet fuel range hydrocarbons and aromatics using a zeolite catalyst, and (f) dehydrating the ethanol and, optionally, higher alcohols to form ethylene and, optionally, higher olefins.    USE - The process is useful for producing jet fuel components (claimed), such as diesel fuel and gasoline.    ADVANTAGE - The process provides renewable jet fuel composition.    DETAILED DESCRIPTION - Producing jet fuel components, comprises: (a) generating or providing syngas; (b) converting the syngas using an alcohol-synthesis catalyst to a first stream comprising methanol, ethanol, and, optionally, higher alcohols; (c) separating the methanol from the ethanol and, optionally, higher alcohols; (d) converting at least some of the methanol to dimethyl ether; (e) converting the dimethyl ether to at least one jet fuel range hydrocarbons and aromatics using a zeolite catalyst; (f) dehydrating the ethanol and, optionally, higher alcohols to form ethylene and, optionally, higher olefins; (g) oligomerizing the ethylene and, optionally, higher olefins to produce olefins in the jet fuel range; (h) optionally hydrogenating and/or isomerizing the olefins in the jet fuel range to form paraffins in the jet fuel range; and (i) combining at least one product of step (c) with at least one of the products of step (h). INDEPENDENT CLAIMS are also included for a composition comprising jet components produced by the above process, or the jet components and jet propellant (JP) 8, JPA, JP4, or JP1.
NOVELTY - The porous electrical power collector (9a) has first electrode layer (3) that is provided in one side of solid electrolyte layer (2). A gas containing oxygen is made to act on first electrode layer. A second electrode layer (4) is provided in other side of solid electrolyte layer. A gas containing hydrogen is made to act on second electrode layer. An air hole surface is equipped with hydrogen storage layer, while providing continuous pores for flowing gas containing hydrogen.    USE - Porous electrical power collector of electrochemical apparatus such as gas decomposition apparatus and fuel cell (all claimed).    ADVANTAGE - The hydrogen gas concentration which acts on second electrode layer is adjusted effectively, when the consumption of fuel gas is changed with the change of the required output, by providing air hole surface that is equipped with hydrogen storage layer, while providing continuous pores for flowing gas containing hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrochemical apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.    Solid electrolyte layer (2)    Electrode layer (3,4)    Porous electrical power collector (9a)    Gas flow paths (10,11)    Gaskets (15,16)
NOVELTY - The utility model relates to biomass fuel gas to hydrogen field, specifically relates to a hydrogen increasing device of trash biomass fuel gas , comprising mixer, used for fuel gas and saturated steam for trash and biomass prepared and mixed, increasing hydrogen furnace, used for using CO and H2O happen reaction, oxygen water pre-heater, for increasing hydrogen and fuel gas cooling, steam drum, used for providing saturated steam. The utility model is new type provided by the device not only miniaturization, and unit investment is small, the device is simple and easy, and reduce large have production cost.
NOVELTY - A plant flying deethanization tower, durene comprises, valve group, propylene tower feeding port, a deethanizer tower feeding port, depropanization tower, tower B through valve group and propylene tower feedstock wherein connected, propane tower by valve group and deethanizer tower mouth connected with feedstock, and wherein said upper propane tower line provided with one strip line directly connected with propylene tower feeding port, and the middle provided with valve, advantages is: add one strip line across the deethanization tower, directly give propylene tower for material, thus it not only can prevent the C2 content low cause deethanizer pressure low, it can not give propylene tower feed by pressing, but also can through stopping deethanization tower, reducing energy consumption.
NOVELTY - Product comprises glycerin 90% free of inorganic salts.    USE - Product e.g. biodiesel and industrial grade methyl ester (all claimed) used in chemical industry and cosmetics industry.    ADVANTAGE - The product is obtained with high yield and flexibility, and has high purity enabling the production of acrylic acid, 1,2-propanediol, polyglycerin, epoxy resins and surfactants based on polyglycerin more economically viable.
NOVELTY - Method for producing hydrogen gas involves filling water (32) containing electrolyte into container (30), and generating a rotating magnetic field with flux lines (15) rotating through a portion (43) of the container such that water is dissociated within the portion of the container into hydrogen gas (50) and oxygen gas (51) due to the rotating magnetic field.    USE - Method for producing hydrogen gas used for hydrogen-fueled vehicle e.g. cars, trucks and airplanes.    ADVANTAGE - The method enables efficient production of hydrogen gas with excellent electroconductivity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of an apparatus for generating hydrogen gas from water.    Housing (10)    Magnets (13A,13B)    Magnetic flux lines (15)    Container (30)    Water (32)    Portion (43)    Hydrogen gas (50)    Oxygen gas (51)
NOVELTY - Storage method of trifluoro ethylene involves storing trifluoro ethylene in one or more compound chosen from alkali metal, alkaline-earth metal, aluminum, copper, zinc, or chlorides, and in state which is not made to contact.    USE - Storage method of trifluoro ethylene. Uses include but are not limited to refrigerant for refrigerators, refrigerant for air-conditioning equipment, working fluid for electric power generation system, working medium for latent-heat transport apparatus and secondary-cooling medium.    ADVANTAGE - The method enables efficient storage of trifluoro ethylene with excellent stability and without polymerization inhibitor.
NOVELTY - The utility model supplies one kind of vertical type biomass particle machine main shaft, comprising cross shaft, cross in centre on shaft end to set with rectangular supporting pole, and cross shaft and rectangular support pole for casting molding, cross shaft lower end centre to set with circular groove, the circular groove in round one side provided with rectangular convex strip, circular groove set with matched use with the rotate shaft groove, rectangular support pole upper end to centre is provided with one of a rectangular groove, rectangular groove set with matched using vertical rectangular cuboid support pole transverse setting transverse rectangular of cross shaft and between the transverse rectangular vertical rectangular plate provided with distance can shaft is adjustable. The utility model is through change the traditional machine main shaft and set with incline pressing plate, the following can be on the premise of no enlargement of equipment, further increase work efficiency of the shaft can further increase output value of biomass particle machine, the utility model is new type small volume, high efficiency, the utility model is new type structure is simple, using suitable and is worthy of popularizing use.
NOVELTY - Device comprises water inlet pipe (1), concrete pool body (2), concrete baffle plate (3), cover plate (5), water outlet, injection pipe (7), quantitative water pump and biological enzyme storage tank. Injection pipe is made up of polyethylene material, and arranged on cover plate. Biological enzyme storage tank (9) is provided with telescopic function for regulating sewage height in concrete pool.    USE - Device used for treating ecological sediments (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows schematic diagram of device.    Water inlet pipe (1)    Concrete pool body (2)    Concrete baffle plate (3)    Cover plate (5)    Injection pipe (7)    Biological enzyme storage tank (9)
NOVELTY - The utility model relates to an organic matter self-turning machine, it comprises right angle bracket, a steel wire rope and cutting pump, the right angle bracket of upper transverse rod, a vertical rod and an inclined support pole composed of; the cross rod at one end and upper end is fixedly connected with the vertical supporting rod, and the upper transverse rod end part formed with the first upper pulley to fix, the transverse rod at another end and an inclined support pole fixedly connected with, and on the upper transverse rod end part set with the second pulley to fix, the inclined support another end pole is fixed on middle part of vertical pole support region, the vertical support pole and middle part are also set with winding device, one end steel wire rope is fixed on the winding roller in the winding device, another end the steel wire rope of the in turn to fix the first pulley, the second pulley to fix and after cutting pump fixedly connected to cutting pump is in suspension state. The organic matter from fermentation turning machine has reasonable design, simple structure, it not only can turning the material in fermentation pool, and for the material and fermentation pool has the cutting function.
NOVELTY - The utility model is a municipal sludge unite plant kitchen garbage Anaerobic digestion device, wherein comprises orderly connected and used for the kitchen garbage sorting device (1), machine for crushing the kitchen garbage crushing device (2), Anaerobic digestion tank used for municipal sludge and kitchen garbage mixing and material mixing device (3) and used for municipal sludge and kitchen garbage digestion and unite (4). The utility model is a type of beneficial effect wherein: for municipal sludge and kitchen garbage unite by Anaerobic digestion, it not only can well of a kitchen garbage to acidification caused by the bad influence, stable reaction pH value and balance nutrition raw material component, but also can increase digestive efficiency of Anaerobic reaction, add marsh gas yield and the reaction water force residence time. A mounting system device of a relux Anaerobic digestion tank, to increase effective digestion efficiency and removing scum caused by the negative influence equal.
NOVELTY - N-tert.-Butyl-2-benzothiazole sulfonamide preparation involves adding 2-mercaptobenzothiazole, catalyst, water and an emulsifier in aqueous phase in a three-necked flask equipped with a thermometer, reflux condenser and constant pressure ball dropping funnel with stirring magnetically. The tert.-butylamine and hydrogen peroxide are added in the reaction mixture through pressure-equalizing dropping funnel at 65 degrees C with stirring. The resulting mixture is cooled, filtered, washed and dried to obtain N-tert.-butyl-2-benzothiazole sulfenamide.    USE - Method for preparing N-tert.-butyl-2-benzothiazole sulfonamide as rubber accelerator (claimed).    ADVANTAGE - The method prepares the N-tert.-butyl-2-benzothiazole sulfonamide in a simple, cost-effective and eco-friendly manner with increased product yield on industrial scale.
NOVELTY - A semi-automatic excrement treatment device comprises box body, stacking fermentation platform and rotary mechanism. The body has discharging mouth. The stacking platform has blades. The rotating mechanism comprises pole, connecting rod, rotating shaft, and swinging rod.    USE - Semi automatic excrement treatment device.
NOVELTY - Dragon fruit plant fertilizer comprises 20-30 pts. wt. chicken manure, 12-16 pts. wt. corn stalk, 10-15 pts. wt. pumpkin vine, 6-9 pts. wt. bagasse, 6-9 pts. wt. urea, 3-5 pts. wt. superphosphate, 3-5 pts. wt. potassium humate, 0.1-0.3 pt. wt. chitosan, 0.5-1 pt. wt. trace elements, 1-2 pts. wt. amino acid, 5-8 pts. wt. herbal extract and 0.5-1 pt. wt. microbial inoculum.    USE - Dragon fruit plant fertilizer.
NOVELTY - Sweet potato fertilizer comprises 32-38 pts. wt. animal manure, 22-25 pts. wt. corn stalk, 12-18 pts. wt. bagasse, 40-50 pts. wt. urea, 30-40 pts. wt. superphosphate, 10-30 pts. wt. potassium sulfate, 10-20 pts. wt. borax, 2-3 pts. wt. crushed mineral, 0.5-1 pt. wt. carbendazim, 0.5-1 pt. wt. thiram and 1-2 pts. wt. microbial inoculum.    USE - Sweet potato fertilizer.
NOVELTY - The utility model claims a spiral algae cultivation stirring device, comprising a pedestal, a shell and a power unit; in the pedestal is equipped with a rotating disc horizontally; on the disc is set with shell in rotating disc on the upper end opening to the shell cover with glass upper cover, glass upper cover on upper surface is fixedly mounted with wind power unit, a wind unit of worm wheel worm mechanism of blade and transmission kinetic energy composed of the stirring shaft extends into the inner shell to the upper stirring shaft mounted with agitator blade component, agitator blade component comprises the first agitator blade bottom of distribution, the second and third agitator blade agitator blade, the first agitator blade, the second agitator blade and paddle size third stirring gradually enlargement. The utility model is new type wind power unit by using stirring shaft rotate slowly, stirring to the spiral algae liquid stirs inner shell for stirring, and the product, device and sum of the structure is simple, energy saving and environment-friendly, spiral algae breeding environment, reduce working personnel working intensity.
NOVELTY - The furnace has a pumping chamber which is provided with a bin and a safe pressure relief valve connected to upper smoke room set with smoke chimney. The bin is extended to groove type funnel, and connected to middle portion connecting block (9). A groove type funnel is provided with a prismatic funnel hole for receiving hopper corresponding to upper portion of gasification furnace core (5). The furnace core is provided with an insulating layer for blowing hot air to an ignition device (13). A double layer sleeve is sleeved outside the furnace core.    USE - Biomass gasification furnace.    ADVANTAGE - Environment-friendly and energy-saving furnace has compact structure, high temperature gasification reaction, short heating time, suitable ignition and high durability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification furnace.    Biomass gasification furnace (1)    Furnace main portion (2)    Gasification furnace core (5)    Middle portion connecting block (9)    Ignition device (13)
NOVELTY - Bromo-microbicidal composition comprises 2,2-dibromo-3-nitrilopropionamide and acid or alkali.    USE - The bromo-microbicidal composition is useful for processing wastewater (claimed).    ADVANTAGE - The composition reduces the treatment cost up to 80%, rapidly decomposes into non-toxic carbon dioxide, ammonia and bromide ions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of the composition, comprising adjusting the pH of wastewater to 6-9 using acid or alkali, then adding 2,2-dibromo-3-nitrilopropionamide and processing for 5-48 hours.
NOVELTY - A sludge drying powder with water content of 15-25 wt.%, calorie reinforcing agent or abridged transcript calorie reinforcing agent and wood composite are mixed, to obtain homogeneous fuel mixture. The homogeneous fuel mixture is molded, dried and pulverized. Pulverized mixture, diluting agent and effluent sludge cake comprises sawdust and/or husk powder are mixed. An additive is added to mixture and mixed, to obtain biomass solid fuel. The binder comprises glucoside solution, algae abstraction concentrate, chitosan solution and/or corn starch.    USE - Manufacture of biomass solid fuel (claimed).    ADVANTAGE - The method enables environmentally-friendly and economical manufacture of biomass solid fuel having high quality.    DETAILED DESCRIPTION - A sludge drying powder with water content of 15-25 wt.%, calorie reinforcing agent or abridged transcript calorie reinforcing agent and wood composite are mixed, to obtain homogeneous fuel mixture. The homogeneous fuel mixture is molded, dried and pulverized. Pulverized mixture, diluting agent and effluent sludge cake comprises sawdust and/or husk powder are mixed. An additive chosen from deodorizing agent, activated chemical comprising barium oxalate, sodium bicarbonate, sodium oxide, calcium oxide, sodium nitrate, calcium nitrate, alumina, charcoal dust, dry distillation carbide and binder is added to mixture and mixed, to obtain biomass solid fuel. The binder comprises glucoside solution, algae abstraction concentrate, chitosan solution and/or corn starch.
NOVELTY - Extracting and separating capsaicin, paprika oleoresin and chili extract crude product, comprises e.g. smashing red pepper into certain granularity, taking hydrous alcohol as extraction solvent, using three segment extraction method of capsaicin, paprika oleoresin and chili extract liquid, adding red peppers raw materials in same extraction container, regulating and controlling concentration adding amount, extraction temperature, and extraction time, obtaining capsaicin, chili and pepper oleoresin three refined extract liquid, concentrating and distilling under reduced pressure.    USE - The method is useful for extracting and separating capsaicin, paprika oleoresin and chili extract crude product (claimed).    ADVANTAGE - The method achieves good yield, has simple technique and easy to operate and control, achieves less equipment investment, can assure easy solvent recovery, is economical, has short period of separation and extraction, and is suitable for industrial scale production.    DETAILED DESCRIPTION - Extracting and separating capsaicin, paprika oleoresin and chili extract crude product, comprises smashing red pepper into certain granularity raw material, taking hydrous alcohol as extraction solvent, using three segment extraction method of capsaicin, paprika oleoresin and chili extract liquid, adding red peppers raw materials in same extraction container, regulating and controlling concentration adding amount, extraction temperature, and extraction time, obtaining capsaicin, chili and pepper oleoresin three refined extract liquid, so that they are separated from the extraction stage, again using three extracting liquid respectively, concentrating and distilling under reduced pressure, solvent recovering and removing residual solvent, and preparing capsaicin, paprika oleoresin and chili extract three crude product.
NOVELTY - Producing fuel from biomass waste comprises (i) smashing biomass waste and taking the smashed biomass waste in a reaction device, (ii) carrying out heat exchange reaction of the smashed biomass waste by a heat carrier and thermal cracking to generate thermal cracking vapor and biological carbon, (iii) separating thermal cracking vapor and biological carbon, and then separating biological carbon and heat carrier, (iv) further separating charcoal from the thermal cracking vapor and heat carrier, and (v) condensing the thermal cracking vapor to generate bio-oil and non-condensable gases.    USE - The method is useful for producing fuel from biomass waste (claimed).    ADVANTAGE - The method is suitable for large-scale production.    DETAILED DESCRIPTION - Producing fuel from biomass waste comprises (i) smashing biomass waste and taking the smashed biomass waste in a reaction device, (ii) carrying out heat exchange reaction of the smashed biomass waste by a heat carrier in the reaction device and subjecting to thermal cracking in the reaction device to generate thermal cracking vapor and biological carbon, (iii) separating thermal cracking vapor and biological carbon, and then separating biological carbon and heat carrier, (iv) further separating charcoal from the thermal cracking vapor and heat carrier, and (v) condensing the thermal cracking vapor to generate bio-oil and non-condensable gases.
NOVELTY - Clopidogrel free base is prepared by dissolving (S)-o-chlorophenyl glycine methyl ester in solvent, performing N,N-disubstitution reaction in presence of catalyst e.g. piperidine, morpholine, pyridine, or tributylamine and methacrylate to obtain (S)-N,N-bis(methoxycarboxyethyl)-o-chlorophenyl glycine methyl ester, performing intramolecular condensation reaction at - 20-30 degrees C in presence of solid sodium methoxide to obtain (S)-2-(3-methoxycarboxy-4-oxo)piperidin-2-o-chlorophenylacetate, and performing substitution reaction with 1,2-dihalogenated ethyl acetate at 0-50 degrees C.    USE - Preparation of clopidogrel free base.    ADVANTAGE - Preparation of clopidogrel free base is low-cost, simple, safe, environment-friendly, and controllable and has high product purity and selectivity and mild condition.    DETAILED DESCRIPTION - Clopidogrel free base of formula (I) is prepared by dissolving (S)-o-chlorophenyl glycine methyl ester in solvent, performing N,N-disubstitution reaction in presence of catalyst e.g. piperidine, morpholine, pyridine, or tributylamine and methacrylate to obtain (S)-N,N-bis(methoxycarboxyethyl)-o-chlorophenyl glycine methyl ester of formula (II), performing intramolecular condensation reaction at - 20-30 degrees C in presence of solid sodium methoxide with molar ratio sodium methoxide:compound of formula (II) to obtain (S)-2-(3-methoxycarboxy-4-oxo)piperidin-2-o-chlorophenylacetate of formula (III), performing substitution reaction with 1,2-dihalogenated ethyl acetate at 0-50 degrees C to obtain compound of formula (IV), reacting with bisulfate salt at 0-50 degrees C to obtain compound of formula (V), heating to 30-70 degrees C, and performing decarboxylation cyclization reaction at pH of 1-5 in which 1,2-dihalogenated ethyl acetate is 1,2-dichloro ethyl acetate or 1,2-dibromo ethyl acetate, and bisulfate salt is sodium bisulfate, potassium bisulfate, or their water-containing crystalline material.    X=Cl or Br.
NOVELTY - Extraction of curculigoside involves drying Curculigo, pulverizing to product having particle size of 100-120 mesh, mixing pulverized material with ethyl acetate, refluxing, obtaining crude extract, distilling resultant crude, dissolving in water, heating, filtering, extracting resultant product using ethyl acetate, vacuum-distilling, recovering ethyl acetate, dissolving resultant material in ethyl acetate, processing using silica gel column, eluting using methanol, vacuum-distilling resultant product, recrystallizing using ethanol, and drying at 70 degrees C.    USE - Extraction of curculigoside used for producing polysaccharide, starch and wine.    ADVANTAGE - The method enables extraction of curculigoside by economical and environmentally-friendly process, with reduced energy consumption.
NOVELTY - Strain of microalgae Chlorella vulgaris 711-54 has high properties of wastewater treatment degree of agricultural and alcohol production, significant productivity and high content of valuable compounds in biomass. The strain is deposited in the Russian Collections of Microalgae in the institution of the Russian Academy of Sciences of Institute of Plant Physiology n.a. KA Timiryazev (IPPAS) with the assigned identifier Chlorella vulgaris IPPAS C-2015 and can be used for treatment of wastewater of agricultural and alcohol production.    USE - Biotechnology.    ADVANTAGE - Invention enables to improve the quality of treatment of the said wastewater.1 tbl, 4 dwg
NOVELTY - The apparatus (100) has casing (120) whose internal space is made vacant, and is divided into head-space and down space. A separator element is provided with delivering opening (140) that is arranged for opening and closing of down space in casing. A heating wire element is positioned between lower-hole portion and center portion of casing. A mixer (150) is positioned in lower-hole portion, and is connected with rotary motor (160). An injector is attached to wall of casing for spraying sodium hydroxide and methanol.    USE - Apparatus for manufacturing bio-diesel using disposable edible oil.    ADVANTAGE - The bio-diesel is manufactured conveniently and is used effectively by providing delivering opening arranged for opening and closing of down space in casing, and injector attached to wall of casing for spraying sodium hydroxide and methanol.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the manufacturing apparatus for bio-diesel.    Apparatus for manufacturing bio-diesel (100)    Casing (120)    Delivering opening (140)    Mixer (150)    Rotary motor (160)
NOVELTY - Environment-friendly separation of bisphenol A and recycling of industrial salt includes subjecting bisphenol A and epichlorohydrin to etherification reaction and oxidative dechlorination reaction, vacuum-distilling, standing, and separating epichlorohydrin lower layer and aqueous solution upper layer; centrifuging remaining fraction to obtain crude bisphenol A and salt solution, washing crude bisphenol A with water, separating liquid, distilling, and filtering to obtain pure bisphenol A; and filtering salt solution, washing, and drying.    USE - Method for environment-friendly separation of bisphenol A and recycling of industrial salt (claimed).    ADVANTAGE - The method is environment-friendly, and it has wide source of raw materials and reduced production cost.    DETAILED DESCRIPTION - Environment-friendly separation of bisphenol A and recycling of industrial salt comprises:    (A) subjecting bisphenol A and epichlorohydrin to ring-opening etherification reaction and ring-closing oxidative dechlorination reaction, vacuum-distilling to separate solvent and excess epichlorohydrin, standing for more than 2 hours, filtering liquid through separating funnel, and separating epichlorohydrin lower layer and aqueous solution upper layer; and    (B) centrifuging vacuum distillation remaining fraction to obtain crude bisphenol A and salt solution, washing crude bisphenol A with water, separating liquid, distilling, and filtering through multi-layer filter paper to obtain pure bisphenol A; and centrifugally filtering salt solution, washing residual resin with industrial alcohol, and drying salt.
NOVELTY - Preparing aryl-heteroaryl and aryl-aryl type derivatives comprises: dissolving a diazonium salt and an aromatic compound in a solvent; adding a catalyst; reacting for 1-12 hours; and isolating reaction products, where a material that contributes ascorbic acid or its derivative is used as the catalyst.    USE - The method is useful for preparing aryl-heteroaryl and aryl-aryl type derivatives (claimed), which are useful for synthesizing pharmaceutical drugs, food additives, agrochemicals, colorants and fragrances.    ADVANTAGE - The process provides aryl-heteroaryl and aryl-aryl type derivatives in a simple and quick manner without utilizing heavy metals and CH activation i.e. without pre-activation and hazardous organic substances, hence economical and environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for aryl-heteroaryl or aryl-aryl compounds obtained by the above process according to claims 1 to 15.
NOVELTY - Calcium carbide tail gas is compressed, pre-purified, portion of calcium carbide furnace tail gas is subjected to pressure-swing adsorption to obtain carbon monoxide-enriched gas. The other portion of calcium carbide furnace tail gas is subjected to shift reaction using iron-chromium-based high temperature conversion catalyst and copper-zinc-based low temperature conversion catalyst to obtain high-concentrated hydrogen. Carbon monoxide-enriched gas and high-concentrated hydrogen are mixed and purified to obtain chemical product comprising methanol, natural gas and synthetic oil.    USE - Production of chemical product comprising methanol, natural gas and synthetic oil using calcium carbide furnace tail gas (claimed).    DETAILED DESCRIPTION - Calcium carbide tail gas is compressed, and pre-purified to remove naphthalene, benzene, tar and partially unsaturated hydrocarbon. Sulfur, phosphorus, arsenic, fluorine, chlorine, hydrogen cyanide and metal carbonyl are removed and deoxidized. A portion of calcium carbide furnace tail gas is subjected to pressure-swing adsorption to obtain carbon monoxide-enriched gas. The other portion of calcium carbide furnace tail gas is subjected to shift reaction using iron-chromium-based high temperature conversion catalyst and copper-zinc-based low temperature conversion catalyst to obtain high-concentrated hydrogen. Carbon monoxide-enriched gas and high-concentrated hydrogen are mixed, mixed gas is purified, and metal carbonyl is removed to obtain chemical product comprising methanol, natural gas and synthetic oil.
NOVELTY - The utility model is new type relates to one kind used for processing kitchen garbage microorganism and reaction device, comprising a machine body, set with feedstock wherein and microorganism feeding tank and activated coal and the internal, machine body set with crusher, and reaction tank and the phase connected with the crusher, on upper crusher corresponding to feedstock wherein the feedstock provided with channel, reaction tank corresponding to microorganism feeding box set with microorganism channel, provided with discharging mouth and leachate collecting box bottom at internal of machine body, provided with ventilating mouth on left side of machine body, upper reaction tank corresponding to ventilating mouth set with ventilating pipeline, crusher by kitchen waste transport pipe connected to feedstock wherein the reaction tank, reaction tank provided with internal stirrer, provided with multiple agitator blade on the whole in stirrer, stirrer driven by motor drive, provided with operation control platform on the machine body right side up in the machine body. The utility model is new type structure is compact, for providing good microorganism is growing and breeding environment.
NOVELTY - The utility model is new type relates to one kind organic fertilizer and production device, specifically is one kind organic waste for agriculture fertilizer device. Comprising shell and mounted on the main shaft in the shell, the main shaft and driving motor transmission connected with, on main shaft set with fin, wherein upper end of the shell set with centrifugal fan, the main shaft has parallel set the two, and each under one rotate shaft each equipped with one arc slot, the inner side of two arc groove fixedly connected with the two arc groove outside is respectively fixedly connected on the inner wall in the shell body, and on the rotating shaft fixedly connected with multiple connecting rods, said multiple connecting rods arranged in spiral distribution on a rotating shaft, wherein the fin fixedly connected on end part of the connecting pole, and triangular cavity between two arc groove is mounted with electric heat tube. The agriculture organic waste for preparing fertilizer device using type structure, structure is simple, reasonable, distributing heating preserving and moisturizing effect, uniformly turning, manufacturing, operation cost low.
NOVELTY - The new type utility claims have one plant can continue production and thermal cracking of biomass fuel gas and complete device, comprising biomass splitting device, a cyclone separation dust collector, cooling system, indirect, electrical tar precipitator, a draught fan and purification system, the system of air pipe connection, low in fan drive, splitting fuel gas from biomass splitting device through pipe enter into cyclone separating dust remover, then entering into cooling system, indirect cooler, tar, finally enter into purification system, after purification and can combustion gas by discharging air, the purification absorption of liquid discharging mouth, the whole set device disposable implement have splitting for removing carbon, removing dust, cooling and purification of gas in turn, discharging the fuel gas is clean dust-free gas, is high, discharging the liquid main constitute of wood acetic acid liquid and wood tar and can be widely used for industrial application.
NOVELTY - A saccharification catalyst comprises active point provided on surface of carrier which has specific surface area of 100-1200 m2/g and particle diameter of 0.2-5 mm.    USE - A saccharification catalyst for bioethanol manufacturing apparatus (claimed).    ADVANTAGE - Saccharified liquid can be easily separated and recovered, and saccharification reaction can be fully promoted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bioethanol manufacturing apparatus which contains saccharification catalyst.
NOVELTY - Treating sewage involves feeding organic sewage into sewage processing system and the performing catalytic oxidation reaction of sewage. The sewage is fed into nanofilter system to obtain pure water. Heat is produced during catalytic oxidation reaction and then heat is collected for power generation. The heat is supplied to power equipment.    USE - Method for treating sewage used for generating power (claimed).    ADVANTAGE - The method enables to treat sewage increases sewage processing economic benefits, and has high efficiency.
NOVELTY - Pellets from pressed biomass, used as fuel pellets, are pressed from mixture of base biomass from timber-based material and charcoal particles, which correct calorific value of the pellet. The particles are connected together by binder on the basis of starch. The fuel pellets particles from the timber-based material and the particle from the charcoal comprise 65-75 wt.% wood particles. The fuel pellets comprise timber-based material particles which are sawdust with particle size of 0.2-2.0 mm, and the surface of charcoal has particle size of 0.3-1.5 mm. The binder is used with starch.    USE - The pellets from pressed biomass are useful as fuel pellets.    DETAILED DESCRIPTION - Pellets from pressed biomass, used as fuel pellets, are pressed from mixture of base biomass from timber-based material and charcoal particles, which correct calorific value of the pellet. The particles are connected together by binder on the basis of starch. The fuel pellets particles from the timber-based material and the particle from the charcoal comprise 65-75 wt.% wood particles. The fuel pellets comprise timber-based material particles which are sawdust with particle size of 0.2-2.0 mm, and the surface of charcoal has particle size of 0.3-1.5 mm. The binder is used with starch. The binder in the fuel comprises 1-3 wt.% based on the total weight of wood sawdust and charcoal particles.
NOVELTY - The new type utility claims have one plant kitchen garbage processing device, comprising pre-sorting device, compressing device and solid mixing device mixing, fermentation device and oil liquid separating device, the pre-processing device comprises one of high temperature disinfecting tank, the high temperature disinfecting tank upper part set with kitchen garbage entrance, the bottom set with kitchen garbage outlet, the sorting device set in kitchen garbage outlet to the high temperature disinfecting tank bottom and the well, the sorting device also set with solid outlet and liquid waste outlet, and the separating device liquid outlet and waste oil liquid separating device, solid waste outlet and waste slag compressing device and the sorting device, the compressing device and solid waste slag mixing device, mixing the solid mixing device mixing and fermentation device. The utility model is new type can be for processing kitchen garbage harmless treatment, with low cost, small investment and is very fit dining hall, restaurant kitchen waste product is equal and more.
NOVELTY - The patent application claims a fermentation groove, a washing tower, a wooden meal room, methane fermentation groove top part set with motor, a motor provided with agitator blade, the agitator blade is hollow, on wayside stirring set with a channel number, fermentation groove connected ozone pipe, ozone sum fan connected enter into a water washing tower, a washing water pump for a washing tower washing water from a bottom suction later, one of the water washing tower, another of agitator blade and connected, a pipe also is connected and a blower, tower top connected purification sum pipe enter into indoor wood chips, wood chips room connected with marsh gas pipe, a marsh gas pipe connected marsh gas tank. A water absorbing ammonia, formation of ammonia water for regulating the PH value in the fermentation groove, at the same time a improved device to ensure the fermentation groove in PH everywhere equal, a aerobic fungus provide suitable fermentation environment.
NOVELTY - The utility model is new type relates to one kind of biomass gasification furnace, specifically is one kind at using biological waste as straw, bamboo, wood as raw material and biomass multi-equal layer sum by fire furnace, comprising connection closeness of upper furnace body, lower furnace body, the upper end of the top furnace cover set with feedstock device, on the furnace body side wall set with one of the first air inlet and several of the second air inlet and multiple third air inlet, inner lower furnace body set with tank body, lower furnace body circle on side set with fuel gas outlet, lower furnace body bottom set with ash tray, ash disc transmission device bottom ash formed with spiral transport machine. The utility model is new type product equipped with two multi-air inlet on the furnace body above the gasification furnace, can finish the whole multi-fire layer in furnace body, wherein production can increase the fuel gas efficiency.
NOVELTY - The utility model is new type relates to one kind of biomass gasification furnace is used for scraping device, specifically is one kind hydraulic lifting electric scraping device, comprising shell, the shell top of the same circle are set with cloth of three hydraulic pressure oil jar side up, the top also set with hydraulic station, hydraulic pressure station and hydraulic pressure oil jar and carrying on oil pipeline and oil return pipeline through oil channel between each connected, top end of piston rod of the hydraulic pressure oil jar fixed with top plate, the top plate bottom seat by the middle installation bracket fixed with speed reducing motor, input end of speed reducing motor and centre shaft connected with phase, center shaft from the lower part of shell, and fixed mixing material disk, material disk bottom are uniformly set with cloth material mixing teeth on lower centre shaft terminal. The utility model is new type product structure is simple, it can realize rotating and lifting movement at the same time, to realize tube on gasification furnace different position in working time of raw material for smooth processing the goal, suitable process.
NOVELTY - The new type utility claims have one kind of biomass gas reaction, comprising the first reaction furnace, comprising the first container, the first container provided with inner stop combustion device, upper end part provided with cooling water entrance, lower end part and circulation water pipe is connected with upper end part of the first container provided with feedstock wherein, lower end part set with coal outlet, upper end part and lower end part set with fuel gas outlet and fuel gas input pipeline connected, lower part provided with combustion head, the second reaction furnace, comprising the second container, the second container in the second stop provided with combustion device, upper end part provided with the second cooling water entrance, coal entrance, lower part set with slag outlet, upper end part provided with third gas outlet and fuel gas input pipeline connected, lower part set with the second combustion head, coal outlet by conveyor and coal entrance connected. The utility model is new type equipped with the first, the second reaction furnace, biomass fuel will resolve out the coal further generating water coal and water react, increase effective have heat value of the biomass fuel, reducing have exhaust gas and discharge the waste residue, with high can, efficient, clean and environment-friendly.
NOVELTY - Biomass is processed which involves heating slurry comprising a reduced recalcitrance lignocellulosic material to a temperature of not greater than 120 degrees C for a time sufficient to further reduce the recalcitrance of the material.    USE - The processes are useful for processing biomass and biomass material (all claimed) including plant biomass, animal biomass, and municipal waste biomass; and for enhancing sugar yields from biomass. The processed biomass or biomass material is useful for producing useful products, such as fuels.    ADVANTAGE - The heating recalcitrance reduction methods, such as the heating method or irradiation in combination with heating, can be advantageous because they provide an efficient method for recalcitrance reduction and enhancing sugar yields from biomass. In particular, the methods are efficient in heating large quantities of biomass material to high temperatures in a short period of time, enabling implementation of the method at a plant scale. In addition, the methods can be synergistically combined with other recalcitrance reduction methods so that a high yield of products can be derived from a feedstock biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for processing a biomass material which involves heating a reduced recalcitrance lignocellulosic material to a temperature of not greater than 20 degrees C using steam and forming a slurry by combining the steam and the reduced recalcitrance lignocellulosic material where the steam condenses and wets the reduced recalcitrance lignocellulosic material by condensation onto the reduced recalcitrance lignocellulosic material (e.g. an interior or exterior surface of the reduced recalcitrance lignocellulosic material).
NOVELTY - The new type utility claims have one plant for biomass as fuel is energy-saving and emission-reducing device of boiler can emission. Biomass bin, biomass fuel feedstock controller, biomass gasification furnace, biomass gasification furnace fuel gas outlet pipe, second time wind distribution controller, biomass fuel gas combustion shower nozzle, hearth, waste heat recovery device, a dust remover, a smoke mouth along the connection time, the biomass gasification furnace top provided with biomass gasification furnace pressure sensor, bottom biomass gasification furnace provided with gasification furnace temperature sensor, a biomass gasification furnace lower part provided with one time wind controller, a fire grate and regulator, hearth upper part set with steam steam drum, steam at steam drum set with steam drum steam pressure sensor and hearth middle part provided with hearth temperature sensor, hearth lower part over hearth set with pressure sensor, waste heat recovery device provided with comprehensive monitor. The utility model is new type can reduce production cost and effectively finish wood waste residue, comprehensive use of biomass waste. Finish computer intelligence, simple and convenient operation, safe operation reliability.
NOVELTY - Copolymer (A) comprises: (M1) 83.5-96.5 mol.% ethylene; (M2) 3-11.5 mol.% vinyl ester; and (M3) 0.5-5 mol.% (meth)acrylate. The weight average molecular weight (Mw) of the copolymer (A) is 35000-150000 g/mol.    USE - The copolymer is useful as a pour point depressant for crude oil by adding at least one copolymer (A) to the crude oil; for prevention of wax deposits on surfaces in contact with crude oil, by adding at least one formulation of the copolymer (A) in an organic solvent to the crude oil; and useful as rheology modifier for crude oil by adding formulation of the copolymer (A) in an organic solvent to the crude oil (all claimed). It can also be used as flow enhancer for crude oils.    ADVANTAGE - The copolymer comprising ethylene, vinyl ester, and (meth)acrylate can be easily provided as formulations in non-polar solvents having a sufficient stability during transport, storage and use even in cold environments and can have a good performance as pour point depressant, wax inhibitors and rheology modifiers for crude oil.    DETAILED DESCRIPTION - Copolymer (A) comprises: (M1) 83.5-96.5 mol.% ethylene; (M2) 3-11.5 mol.% vinyl ester of general formula H2C=CH-O-(O)C-R1; and (M3) 0.5-5 mol.% (meth)acrylate of general formula H2C=C(R2)-COOR3. The weight average molecular weight (Mw) of the copolymer (A) is 35000-150000 g/mol.    R1=H or 1-4C alkyl moiety;    R2=H or methyl; and    R3=selected from (R3a) branched alkyl moieties having 4-18 carbon atoms, (R3b) cyclic alkyl moieties having 5-12 carbon atoms, and (R3c) optionally alkyl substituted aryl moieties having 6-12 carbon atoms.    An INDEPENDENT CLAIM is included for a polymer composition (X) at least comprising the copolymer (A), and organic solvent (B), where the concentration of the copolymer (A) is 5-25 wt.% with respect to the sum of all components of the polymer composition (X).
NOVELTY - The apparatus (1) has stirring blade that is fixed to surrounding of rotating shaft. Exhausting unit discharges internal air stored into container (2) to container exterior. External air is introduced in container by air supply unit. Apparatus ferments and dries organic waste that is composted and is taken out from container lower portion. Organic waste thrown in container from container upper portion is stirred. Internal air is exhausted by exhausting unit. External heat insulation panel (9a-9d) is installed so that apparatus covers cylindrical outer periphery of container through space.    USE - Waste treatment apparatus used as enclosed fermentation-drying apparatus for composting organic waste such as foodstuff residue discharged from livestock excretion such as hen droppings, pig feces, cattle feces and horse dung, emitted from livestock farming management structure and food industry office.    ADVANTAGE - The waste treatment apparatus has heat exchange unit to heat the external air introduce in the container from air supply unit by the heat of the exhaust gas from the exhausting unit. The fermentation heat of processed material is utilized effectively. The running cost is made low. The stirring blade shape and air flow volume used for the waste material processing method are limited. The processing time of drying and composting of organic waste is shortened, and the quantity which processes per day increases. The generation amount of nasty smell substance is reduced, and the manure of the fertilizer effect is manufactured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a waste material processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view and top view of the waste treatment apparatus.    Waste treatment apparatus (1)    Container (2)    Ventilation piping (6a)    External heat insulation panel (9a-9d)    Ventilating fan (12)
NOVELTY - Microbial agent comprises Debaryomyces hansenii YC 7058 (KFCC 11575P).    USE - The microbial agent is useful for removing odor of livestock wastewater present in livestock manure by nitrifying ammonia (claimed).    ADVANTAGE - The microbial agent nitrifies ammonia with high efficiency, and avoids soil contamination.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing microbial agent, comprising inoculating and culturing Debaryomyces hansenii YC 7058 on culture media containing proteose peptone no.3, beef Extract, yeast extract, dextrose, polysorbate 80, ammonium citrate, sodium acetate, magnesium sulfate, manganese sulfate and dipotassium phosphate.
NOVELTY - Chemical-looping process involves delivering fuel gas to a fixed-bed reactor along flow direction (f1) with respect to the fixed-bed reactor, and delivering fuel gas to a fixed-bed reactor along reverse flow direction (f2) of the fuel gas, which is opposite to the flow direction (f1), while oxidizing the fuel gas.    USE - Chemical-looping process of fuel gas e.g. methane, natural gas, syngas and bio-syngas (all claimed).    ADVANTAGE - The method enables efficient chemical-looping process of fuel gas with excellent selectivity and workability. The reversal of the flow direction of fuel gas effectively improves oxygen carrier utilization, carbon dioxide capture efficiency, carbon-deposition resistance, mitigation of cold zones, and elimination of gas-solids separation.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating chemical-looping process of fuel gas.
NOVELTY - Algicide comprises Bacillus, rice straw, xanthan gum, limestone, polyvinyl alcohol and water.    USE - Algicide used for removing harmful cyanobacteria from fresh water bodies such as lakes, reservoirs, landscape ponds and in agriculture farming.    ADVANTAGE - The algicide is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing algicide, which involves:    (A) crushing rice straw and limestone to 40 mesh size;    (B) adding water to obtain mixture;    (C) adding Bacillus, xanthan gum and polyvinyl alcohol to the obtained mixture; and    (D) mixing evenly to obtain the product.
NOVELTY - A hydrogen pump (100) comprises anode (102) including catalyst which oxidizes hydrogen, cathode (103) including catalyst which reduces proton and proton conductor (101) arranged between the anode and the cathode. The proton conductor has perovskite-type crystal structure and comprises cerium-group 2 element-containing complex (I). The electric charge of the complex (I) has deviated from electrical neutrality in range of -0.13-0.14.    USE - Hydrogen pump is used for extraction of hydrogen gas.    ADVANTAGE - The hydrogen pump has excellent durability and stability.    DETAILED DESCRIPTION - A hydrogen pump comprises anode including catalyst which oxidizes hydrogen, cathode including catalyst which reduces proton and proton conductor arranged between the anode and the cathode. The proton conductor has perovskite-type crystal structure and comprises cerium-group 2 element-containing complex of formula: AaB"1-xB'x O3-d (I). The electric charge of the complex (I) has deviated from electrical neutrality in range of -0.13-0.14.    A=group 2 element;    B"=Ce or group 4 element;    B'=group 3 element, group 13 element or lanthanoid;    x=0-0.5;    a=more than 0.5 to 1;and    d=0 to less than 3.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen pump.    Hydrogen pump (100)    Proton conductor (101)    Anode (102)    Cathode (103)    Anode side reaction container (111)    Cathode side reaction container (112)
NOVELTY - A water vapor electrolyzer (100) has an anode (102) containing catalyst (A) for oxidizing hydrogen in gas containing water, cathode (103) containing catalyst (B) for reducing proton, and proton conductor (101) comprising perovskite-type crystal structure (I) provided between the anode and the cathode.    USE - Water vapor electrolyzer is used for producing hydrogen gas by electrolyzing water vapor.    ADVANTAGE - The water vapor electrolyzer provides hydrogen gas with high purity.    DETAILED DESCRIPTION - A water vapor electrolyzer has an anode containing catalyst (A) for oxidizing hydrogen in gas containing water, cathode containing catalyst (B) for reducing proton, and proton conductor comprising perovskite-type crystal structure of formula: AaB'1-xB''xO3-s (I) provided between the anode and the cathode, where A is alkaline-earth metal, preferably barium or strontium, B' is group-IV tetravalent transition metal or cerium, B'' is group-3 or group-13 trivalent element, preferably yttrium or indium, a is more than 0.4 and less than 0.9, x is more than 0.2 to less than 0.6, and s is not defined.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of water vapor electrolyzer.    Water vapor electrolyzer (100)    Proton conductor (101)    Anode (102)    Cathode (103)    External power supply (104)
NOVELTY - A water vapor electrolyzer (100) comprises an anode (102) containing catalyst for oxidizing hydrogen in gas containing water, a cathode (103) containing catalyst for reducing proton, and a proton conductor (101) arranged between the anode and cathode. The proton conductor has perovskite-type crystal structure including cerium-lanthanide composite oxide including group 2 element(s), element chosen from cerium and group 4 element, and group 3 element, group 13 element, or lanthanide.    USE - Water vapor electrolyzer is used for producing hydrogen gas.    ADVANTAGE - The water vapor electrolyzer enables production of high-purity hydrogen gas.    DETAILED DESCRIPTION - A water vapor electrolyzer comprises an anode containing catalyst for oxidizing hydrogen in gas containing water, a cathode containing catalyst for reducing proton, and a proton conductor arranged between the anode and cathode. The proton conductor has perovskite-type crystal structure including cerium-lanthanide composite oxide (AaB"1-xB'xO3-d, where A is group 2 element(s), preferably barium, strontium or calcium, B" is element chosen from cerium and group 4 element, preferably zirconium, cerium or titanium, B' is group 3 element, group 13 element, or lanthanide, preferably ytterbium, yttrium or neodymium, a is more than 0.5 and 1 or less, x is 0-0.5, and d is 0 or more and less than 3). The electric charge of cerium-lanthanide composite oxide is deviated from electrical neutrality in -0.13 or more and less than 0.14. The Water vapor electrolyzer produces hydrogen gas by water vapor electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of water vapor electrolyzer.    Water vapor electrolyzer (100)    Proton conductor (101)    Anode (102)    Cathode (103)    External power supply (104)
NOVELTY - A dehydrogenation apparatus comprises anode including dehydrogenation catalyst, cathode including catalyst which reduces proton, and proton conductor positioned between the anode and cathode. The proton conductor comprises perovskite-type crystal structure containing metal oxide complex (I). The electric charge of the perovskite-type crystal structure is deviated from electrical neutrality in -0.13 or more and less than +0.14. The dehydrogenation apparatus is made to generate hydrogen gas by dehydrogenation.    USE - Dehydrogenation apparatus is used in manufacture of hydrogen gas.    DETAILED DESCRIPTION - A dehydrogenation apparatus comprises anode including dehydrogenation catalyst, cathode including catalyst which reduces proton, and proton conductor positioned between the anode and cathode. The proton conductor comprises perovskite-type crystal structure containing metal oxide complex of formula: AaB'1-xB"xO3-( delta ) (I), where A is group 2 element, B' is Ce or group 4 element, B" is group 3 element, group 13 element or lanthanoid, a is more than 0.5 and 1 or less, x is 0-0.5, and delta is 0 or more and less than 3. The electric charge of the perovskite-type crystal structure is deviated from electrical neutrality in -0.13 or more and less than +0.14. The dehydrogenation apparatus is made to generate hydrogen gas by dehydrogenation.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the dehydrogenation apparatus.    Dehydrogenation apparatus (100)    Proton conductor (101)    Anode (102)    Cathode (103)    External power supply (104)
NOVELTY - Nickel oxide, iron oxide, binder, and nickel and/or metal with smaller ionization tendency than nickel, are kneaded. The kneaded mixture is molded and baked to obtain sintered ceramic electrode.    USE - Manufacture of sintered ceramic electrode. Uses include but are not limited to chlorine evolution reaction, oxygen evolution reaction, hydrogen-producing reaction, reductive reaction of oxygen and in electrolyte solution containing sludge containing organic substance.    ADVANTAGE - The method enables manufacture of sintered ceramic electrode with high electroconductivity and dissolution resistance.
NOVELTY - Enhancing the digestibility of substrates for biogas production in anaerobic digesters, comprises treating a substrate, with at least one proteolytic enzyme alone or in combination with at least one carbohydrase. The proteolytic enzyme is an acid stable serine protease derived from Nocardiopsis dassonvillei dassonvillei (DSM 43235), Nocardiopsis prasina (DSM 15649), Nocardiopsis prasina (DSM 14010), Nocardiopsis sp. (DSM 16424), Nocardiopsis alkaliphila (DSM 44657) and Nocardiopsis lucentensis (DSM 44048), as well as homologous proteases.    USE - The method is useful for enhancing the digestibility of substrates for biogas production in anaerobic digesters (claimed), where the biogas is used for the production of thermal and electrical energy.    ADVANTAGE - The method: utilizes combination of amylase and/or a non-starch-polysaccharide-degrading enzyme mixture, thus improving degradation or conversion rate of plant material; increases the gas yield and the speed of gas formation; reduces viscosity in the fermenter; is economical; and provides biogas that is capable of producing 11% of the renewable energy (in Germany (2009)).
NOVELTY - The utility model claims a sanitary towel with healthcare and conditioning hematophagous function, comprising non-woven cloth, plant essence chip, the first dust free paper, macromolecule absorbing layer, second dust-free paper, breathable film, environment-friendly glue, release paper and coating the non-woven cloth, the plant essence core, said first dust free paper, the high molecular absorber layer, the second dust free paper, the ventilating film, the environment-friendly gum, the release paper and the coated barrier in turn, the edge for mutual connection. The utility model by natural plant essence extracting chip manufacture, and combine high molecular absorber layer, ventilating film and environment-friendly glue for female irregular menstruation, dysmenorrhea symptom equal with good conditioning effect.
NOVELTY - The new type utility claims have one plant limbs anesthesia assistant device, comprising anesthetic agent box, cushion block, the whole multi-fixing sucker, the whole multi-medicine preparation bucket, multi-skid-proof cushion block, multi-group medicament classify module, one to four and one for adhesive bandage; four cushion block laying in anesthetic agent box on the fixing sucker uniformly distribute on bottom anesthetic agent box, one to four and one end is connected with bottom of anesthetic agent box on two side, to one adhesive patch formed at another end to one limb bandage and the multi-medicine preparation of bucket by adhesive set on anesthetic agent box inside, multiple skid-proof cushion block on inner wall of multiple laying of medicament bucket upper, multi-group medicament classify module by skid-proof cushion set in the whole multi-bucket in medicine preparation, medicine preparation classify component comprises plastic medicament bag, a supporting ring, a rubber film and sealing cover. The utility model is new type energy saving and environment-friendly, clean and sanitary, can according to the different treatment project use, medical waste can collective recovery, increase working efficiency and effective anesthetic doctor, reduce work intensity.
NOVELTY - The utility model relates to biochemical technology field, especially relates to an intelligent environment-friendly biological deodorizing filter chamber filter. The utility model solves technology problem that it can regulate odour throughput, intelligent and environmental protection and biological deodorizing filter chamber. In order to solve said technology problem, the utility model is new type supply have this kind one intelligent environmental protection and biological deodorization filtering device, comprising filter chamber with large, thin filler layer, air inlet pipe, connected pipe, an air outlet pipe, odor sensor, electric control valve I, returning pipe, electric control valve II, the ozone pipe, electric control valve at III, sum pump and control unit, large filler layer provided with air inlet pipe, large, thin filler layer connected by connecting pipe, filler layer and air outlet pipe and return pipe connected with air outlet pipe, return pipe and ozone pipe respectively set with electric control valve I, electric control valve and electric control valve II III, control unit and electric control valve and the sum pump connection. The utility model reaches to adjust by weight of odour effect.
NOVELTY - Earthworm biological fertilizer comprises 5-7 pts. wt. earthworm manure, 1-3 pts. wt. peat, 1-2 pts. wt. humic acid, 3-5 pts. wt. mushroom, 2-4 pts. wt. lees, 1-2 pts. wt. calcium superphosphate, 1.5-2.5 pts. wt. potassium sulfate, 0.5-1.5 pts. wt. fish meal, and 2-4 pts. wt. peanut cake.    USE - Earthworm biological fertilizer is useful for ginseng, lawn, flowers, vegetables, fruit trees and other plants or soil.    ADVANTAGE - The earthworm biological fertilizer is non-toxic, harmless, and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of earthworm biological fertilizer involving taking earthworm and then cultivating for 3-6 months, washing the earthworm and then drying until a moisture content is 20-25%, screening the earthworm, adding peat, humic acid, mushroom, calcium superphosphate, potassium sulfate, fish meal and peanut cake to the screened earthworm, uniformly mixing, crushing the mixture and then stacking for 7-10 days, and fermenting.
NOVELTY - Coal ash biological fertilizer comprises 20-30 pts. wt. fly ash, 1-3 pts. wt. ferment fungus, 1-3 pts. wt. active fungus, 10-20 pts. wt. municipal sludge, 3-5 pts. wt. monoammonium phosphate, 2-4 pts. wt. potassium sulfate, 7-9 pts. wt. urea, 1-3 pts. wt. fish meal, and 2-4 pts. wt. peanut cake.    USE - Coal ash biological fertilizer is useful for production of agricultural crops.    ADVANTAGE - The pollution-free coal ash biological fertilizer has excellent soil fertility, and can decompose and eliminate chemical fertilizers, pesticides and other toxic heavy metals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Coal ash biological fertilizer involving taking fly ash with a humidity of 30-45% and then fermenting at 45-70 degrees C for 5-7 days, adding ferment fungus and active fungus to the fly ash, uniformly mixing, adding fish meal and peanut cake to the mixture and then uniformly stirring, adding municipal sludge to the mixture and then stirring, stacking the mixture and then fermenting, adding potassium sulfate and monoammonium phosphate to the mixture and then fermenting, adding urea to the mixture and then fermenting, and stirring.
NOVELTY - Yeast-containing microbial fertilizer comprises 3-5 pts. wt. yeast, 20-30 pts. wt. humus, 10-14 pts. wt. starch, 3-5 pts. wt. weathered coal, 1-3 pts. wt. bentonite, 3-5 pts. wt. peat, 7-9 pts. wt. sweet potato powder, 15-25 pts. wt. carbon, 4-6 pts. wt. fish meal, and 20-40 pts. wt. diatomite.    USE - Yeast-containing microbial fertilizer (claimed).    ADVANTAGE - The yeast-containing microbial fertilizer has rich in nitrogen and potassium contents and nutrient content, is non-toxic, harmless and environmentally-friendly, and can be prepared with high yield and quality and prolonged service life.
NOVELTY - The structure has a gasification furnace core whose inner and outer walls are fixed with an insulating layer. The insulating layer is provided with a receiving hopper. A throat is conical in structure. The throat is used for incline downward blowing toward a reaction room and an air nozzle. The insulating layer is fixed with the gasification furnace core for blowing hot air to an ignition device. The ignition device is provided with a built-in heating wire of a blower.    USE - Biomass gasification furnace core structure.    ADVANTAGE - The structure is compact, and has high gasification reaction temperature, short temperature start-up time and high ignition gas production efficiency. The structure enables carbon as high temperature tar cracking catalyst, and can significantly reduce tar content of the gas that can be simplified for removing filter dust from furnace. The structure is suitable for small biomass gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification furnace core structure.
NOVELTY - A biochemical crude oil comprises 0.1-50 wt.% bio-oil and 50-99.9 wt.% petroleum and/or alcohol as main fuel.    USE - Biochemical crude oil (claimed).    ADVANTAGE - The biochemical crude oil is manufactured with high yield, by economical and environmentally-friendly process.
NOVELTY - A catalyst comprises 30-90 parts mass gamma -aluminum oxide spherical carrier having particle diameter of 2 mm, 20-60 parts mass silver nitrate, 40-120 parts mass sodium carbonate, 40-90 parts mass sodium hydroxide, 40-110 parts mass lanthanum nitrate and 40-80 parts mass cerium nitrate.    USE - Catalyst is used for purifying methanol fuel.    ADVANTAGE - The methanol fuel purified using the catalyst is environmentally-friendly.
NOVELTY - A composite diesel oil contains 170-640 pts. wt. methanol, 270-700 pts. wt. heavy oil, 5-250 pts. wt. xylene, 5-50 pts. wt. acetone, 15-200 pts. wt. butanol, 1-5 pts. wt. toluene, 1-5 pts. wt. benzotriazole, 1-5 pts. wt. tetrachloroethylene, 5-50 pts. wt. ethylhexyl nitrate, 1-40 pts. wt. Tween 80 (RTM: Polysorbate 80), 5-100 pts. wt. solvent oil and 5-50 pts. wt. butyl acetate.    USE - The composite diesel oil is useful for vehicle fuel.    ADVANTAGE - The composite diesel oil is environmentally-friendly, and has high cetane number, dynamic performance and fuel-saving effect.
NOVELTY - A pour point depressant contains 3-30 wt.% alpha -hydroxy-polyester compound (I) and 70-97 wt.% poly(meth)acrylate (II).    USE - The pour point depressant is useful for biodiesel and petrochemical diesel.    ADVANTAGE - The pour point depressant has excellent depression effect.    DETAILED DESCRIPTION - A pour point depressant contains 3-30 wt.% alpha - hydroxyl-polyester compound of formula (I) and 70-97 wt.% poly(meth)acrylate of formula (II).    R1,R6=1-22C alkyl;    R2,R4,R5,R7=H or CH3;    R3=H or 1-6C alkyl;and    n,m=1-100.    An INDEPENDENT CLAIM is included for preparation of pour point depressant, which involves adding mixture of alkyl methacrylate and/or alkyl acrylate, alpha -hydroxy-ester compound , 0-200 wt.% diluent, 0.01-3 wt.% initiator and 0.01-3 wt.% chain transfer agent to reactor under the protection of nitrogen, reacting the mixture at a temperature of 30-180 degrees C for l-24 hours and pressure of 0.1-l MPa.
NOVELTY - An environmentally-friendly hydrogen-rich fuel gas contains 93-96 wt.% methanol, 0.2-0.5 wt.% magnesium naphthenate, 0.5-2 wt.% aluminum powder, 0.5-2 wt.% sodium hydroxide and 0.5-2 wt.% water.    USE - Environmentally-friendly hydrogen-rich fuel gas (claimed).    ADVANTAGE - The environmentally-friendly hydrogen-rich fuel gas has high temperature combustion and low smoke emission.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environmentally-friendly hydrogen-rich fuel gas, which involves adding sodium hydroxide to reaction vessel, drying mixture, adding aluminum powder, magnesium naphthenate and methanol to reaction vessel, evenly stirring mixture at 4 rpm, adding water, sealing and storing.
NOVELTY - A solid alcohol fuel comprises 1.2-1.4 pts. wt. paraffin, 4.7-4.8 pts. wt. stearic acid, 0.61-0.63 pt. wt. sodium hydroxide, 90-91 pts. wt. industrial alcohol and 2-3 pts. wt. distilled water.    USE - Solid alcohol fuel is used as heat source in domestic appliances, travel applications, sports applications and soldier field.    ADVANTAGE - The solid alcohol fuel has excellent hardness and stability.
NOVELTY - Method for processing sugarcane and/or sweet Sorghum feedstock, involves (a) extracting raw juice from the feedstock by pressing and/or crushing, and to recover a residual bagasse, (b) pretreating the bagasse, (c) mixing the pretreated bagasse with desired quantity of raw juice, and (d) hydrolyzing the pretreated bagasse obtained from step (c) by enzymatic hydrolysis using a cellulase enzyme preparation under conditions where the aqueous liquid phase of the hydrolysis mixture comprises sucrose derived from the added raw juice.    USE - The method is useful for processing sugarcane and/or sweet Sorghum feedstock, which is useful for producing fermentation product, and fuel or fuel additive. The fuel or fuel additive is useful for generation of power, heat and/or steam (all claimed).    ADVANTAGE - The method enables to increase ethanol production by consuming low steam.    DETAILED DESCRIPTION - Method for processing sugarcane and/or sweet Sorghum feedstock, involves (a) extracting raw juice from the feedstock by pressing and/or crushing, and to recover a residual bagasse, (b) pretreating the bagasse obtained from step (a), (c) mixing the pretreated bagasse obtained from step (b) with desired quantity of raw juice, and (d) hydrolyzing the pretreated bagasse obtained from step (c) by enzymatic hydrolysis using a cellulase enzyme preparation under conditions where the aqueous liquid phase of the hydrolysis mixture comprises at least 5, 10, 15, 20, 25, 30, 40, 50, or 60 g/l sucrose derived from the added raw juice. INDEPENDENT CLAIMS are included for the following:    (1) fermentation product produced by performing the above-mentioned method;    (2) product comprising or consisting essentially of the hydrolyzate, dissolved solids, mixture of dissolved solids and raw juice, and concentrated solution; and    (3) fuel or fuel additive for generation of power, heat and/or steam.
NOVELTY - A surface-treating agent comprises a copolymer containing monomer composition containing 10-80 mol% nitrogen-containing monomer (a) (I) and 20-90 mol% cationic (meth)acrylamide. The copolymer has weight average molecular weight of 5000-150000.    USE - Surface-treating agent is used in manufacture of surface-treated polyamide reverse-osmosis membrane (claimed) for membrane filter. Uses include but are not limited to manufacture of drinking water, water and sewer services processing, waste liquid processing, and desalination of seawater.    ADVANTAGE - The surface-treating agent enables manufacture of surface-treated polyamide reverse-osmosis membrane having excellent water permeability with effective modification of surface and suppressed generation of fouling for long period, by environmentally-friendly process.    DETAILED DESCRIPTION - A surface-treating agent comprises a copolymer containing monomer composition containing 10-80 mol% nitrogen-containing monomer (a) of formula (I) and 20-90 mol% cationic (meth)acrylamide. The copolymer has weight average molecular weight of 5000-150000.    R1=H or methyl;    R2,R3=1-4C alkylene;and    R4-R6=1-4C alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) surface-treated polyamide reverse-osmosis membrane, which consists of a surface, processed using the surface-treating agent; and    (2) manufacture of surface-treated polyamide reverse-osmosis membrane, which involves surface-treating the polyamide reverse-osmosis membrane using the surface-treating agent, and washing the polyamide reverse-osmosis membrane using pure water.
NOVELTY - Method for manufacturing alcohol involves using cellulose containing raw material as substrate to culture cellulosome-producing bacteria, and alcohol-fermenting bacteria in same container.    USE - The method is useful for manufacturing alcohol chosen from ethanol, butanol, isopropanol, and their combinations (claimed).    ADVANTAGE - The method enables to manufacture product with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for manufacturing alcohol using biomass raw material which contains sugar which can assimilate alcohol fermentation bacteria in addition to cellulose, which comprises first culture tank for culturing alcohol fermentation bacteria using sugar substrate recovered from biomass, second culture tank for culturing cellulosome-producing bacteria and alcohol fermentation bacteria, and alcohol storage tank for accommodating alcohol recovered from first culture tank and second culture tank.
NOVELTY - Removal of carbon dioxide from carbon dioxide-containing gas involves contacting liquid medium with carbon dioxide-containing gas in absorption zone in presence of biocatalyst which promotes the absorption of carbon dioxide from the gas phase into the liquid medium, producing a rich liquid medium (4), introducing the rich liquid medium into a stripping zone, and obtaining lean liquid medium (7). The temperature of the rich liquid medium exiting the absorption zone is 20 degrees C or less of the temperature of the lean liquid medium exiting the stripping zone.    USE - Removal of carbon dioxide from carbon dioxide-containing gas e.g. flue gas obtained after combustion of carbon-based fuels.    ADVANTAGE - The method enables simple, economical and energy efficient removal of carbon dioxide from carbon dioxide-containing gas by minimizing vapor compression power requirements and diffusional limitations and eliminating carbon dioxide capture processes using capital-intensive heat recuperation equipment.    DETAILED DESCRIPTION - Removal of carbon dioxide from carbon dioxide-containing gas involves contacting liquid medium with carbon dioxide-containing gas in absorption zone in presence of biocatalyst which promotes the absorption of carbon dioxide from the gas phase into the liquid medium, producing a rich liquid medium, introducing the rich liquid medium into a stripping zone operating under reduced pressure and comprising biocatalyst which promotes the desorption of carbon dioxide from the liquid medium into the gas phase, and obtaining lean liquid medium. The temperature of the rich liquid medium exiting the absorption zone is 20 degrees C or less of the temperature of the lean liquid medium exiting the stripping zone.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of carbon dioxide capture system.    Flue gas (1)    Clean gas (3)    Rich liquid medium (4)    Lean liquid medium (7)    Compressor (101)
NOVELTY - Separation of fermentation inhibitor from biomass-derived hydrolyzate involves introducing a biomass-derived liquid hydrolyzate stream comprising fermentation inhibitor into a stripping column, introducing a steam-rich vapor stream to stripping column, recovering stripped liquid stream and stripper vapor output stream, compressing stripper vapor output stream, introducing compressed vapor stream and water-rich liquid stream into an evaporator, and recycling at least a portion of evaporator output vapor stream to stripping column as steam-rich vapor stream.    USE - Separation of fermentation inhibitor from biomass-derived hydrolyzate (claimed).    ADVANTAGE - The method enables economical separation of fermentation inhibitor from biomass-derived hydrolyzate.    DETAILED DESCRIPTION - Separation of fermentation inhibitor from biomass-derived hydrolyzate involves providing and introducing a biomass-derived liquid hydrolyzate stream comprising fermentation inhibitor into a stripping column, introducing a steam-rich vapor stream to stripping column to strip at least a portion of fermentation inhibitor from liquid hydrolyzate stream, recovering a stripped liquid stream and a stripper vapor output stream from stripping column, where the stripped liquid stream has lower fermentation inhibitor concentration than the liquid hydrolyzate stream, compressing stripper vapor output stream to generate a compressed vapor stream, introducing compressed vapor stream, and a water-rich liquid stream into an evaporator, recovering an evaporated liquid stream and evaporator output vapor stream from evaporator, and recycling at least a portion of evaporator output vapor stream to stripping column as steam-rich vapor stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a simplified block-flow diagram of separation of fermentation inhibitor from biomass-derived hydrolyzate using evaporator and stripping column.
NOVELTY - Dissolving-grade pulp composition comprises at least 90 wt.% glucan and 0.6-5 wt.% xylan, where the composition has a weight-average molecular weight of at least 500000 g/mol.    USE - The composition is useful for making cellulose acetate, as an intermediate in ethanol, xylitol, furfural, methyl furfural, or valerolactone production, as feedstock to produce ethanol and/or as a fuel to a recovery boiler and as a starting material to produce functional chemicals, such as adhesives and sweeteners.    ADVANTAGE - The composition: has distinct molecular weight and elemental metal ion content which are different from commercially available composition; and is prepared by method which is cost-effective.
NOVELTY - Producing organic waste e.g. biomass and waste water, for further processing, preferably for a gasification, comprises (a) introducing organic wastes into an aerobic and/or anaerobic fermenter, and adding an inoculum, and (b) supplying carbon dioxide obtained in the fermenter to a gas reformer to convert the carbon dioxide into methane gas.    USE - The method is useful for producing organic waste e.g. biomass and waste water, for further processing, preferably for a gasification (claimed).    ADVANTAGE - The method produces biogas containing 90% methane.
NOVELTY - Preparing organic waste, including biomass or effluents, for further processing, preferably for gasification, comprises allowing the organic waste to enter into an aerobic fermenter (1), mixing with an inoculum, feeding the resulting carbon dioxide into a gas reformer (7), which is converted into methane gas.    USE - The method is useful for preparing organic waste, including biomass or effluents for further processing preferably for gasification (claimed).    ADVANTAGE - The method: improves biogas generation containing 90% methane; .    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a device for preparing organic waste, including biomass or effluents for further processing preferably for gasification.    Aerobic fermenter (1)    Gas dome (4)    Floor (6)    Gas reformer (7)    Pipe (8)
NOVELTY - A hydrogen generating apparatus (10) comprises catalyst base layer (11a) which is formed of ion-binding conductor, 1st electrode (11) which has photocatalyst layer (11b) that is formed of apatite which contains titanium ion as metal ion, and is laminated on catalyst base layer, and 2nd electrode (12) which is electrically connected with 1st electrode and has hydrogen generation catalytic function.    USE - An apparatus for generating hydrogen (claimed).    ADVANTAGE - Hydrogen is generable.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) electrode comprising catalyst base layer (11a) which is formed of ion-binding conductor, and photocatalyst layer (11b) which is formed of apatite that contains titanium ion as metal ion and is laminated on catalyst base layer; and    (2) generation of hydrogen which involves electrically connecting catalyst base layer with 1st electrode (11) and reducing water using 2nd electrode (12) which has hydrogen generation catalytic function.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen generating apparatus.    Hydrogen generating apparatus (10)    1st electrode (11)    Catalyst base layer (11a)    Photocatalyst layer (11b)    2nd electrode (12)    Board (13)
NOVELTY - The utility model is new type relates to medical appliance technology field, especially one kind detection, comprising cup body and cup cover, the cup body upper side wall provided with handle, on the cup cover set with ureter, ureter upper end connected with the urine bucket and taking and taking urine bucket connected, taking the urine bucket inner side wall provided with multiple layer buffer cotton. A detection A urine gathering the utility new type provide the, structure is simple, time suitable, taking urea and patient is easy to observe how the urine, can according to need when the doctor , but also can effectively prevent the small getting for urine splash, body and ground, which avoids have infection and the pollute to environment, personnel after getting in urine, for it is easy to carry out detection, give patient and care personnel caused by suitable.
NOVELTY - Preparation of metal organic framework (MOF) porous adsorbent material comprises carrying out hydrothermal synthesis of MOF porous absorbing material with metal ion nitrate and organic ligand and N, N-dimethylformamide and N, N-diethyl formamide, stirring, reacting at 80-250 degrees C for 12-120 hours, filtering, oven drying, and preparing metal organic framework porous material.    USE - Method for preparing MOF porous adsorbent material used for separating 4-8C isoparaffin (claimed).    ADVANTAGE - The method can provide material having large surface area, pore structure of highly ordered, controlled pore size and controlled surface. The material can adsorb isoparaffin mixture from the positive feed n-paraffins, and has high selectivity.    DETAILED DESCRIPTION - Preparation of MOF porous adsorbent material comprises carrying out hydrothermal synthesis of MOF porous absorbing material with metal ion nitrate and organic ligand at a ratio of 1:1-15, and N, N-dimethylformamide and N, N-diethyl formamide at a volume ratio of 1:1-5, stirring, reacting at 80-250 degrees C for 12-120 hours, filtering, oven drying the product, and preparing metal organic framework porous material. The metal ion is nitrate ion zinc, copper, nickel, aluminum, chromium or lithium, and the organic ligand is terephthalic acid, benzene tricarboxylic acid, triethyl imidazole, 2-methylimidazole, benzimidazole 5-chlorobenzene, or 1,4-benzenedicarboxylic acid ester.
NOVELTY - The integrated structure has a sewage processing pool (2) whose entrance end is connected with water outlet of drain pipe (1). A middle portion of sewage processing pool is provided with a partition (31) for dividing into solid impurities removing process pool (21) and biological treatment pool (22). The biological treatment pool is provided with an oxygen supply pipe (7) and a biological rotating disc (8). The oxygen supply pipe is opened in atmosphere. The biological rotating disc is rotated based on pressure difference of atmospheric pressure and biological treatment pool pressure.    USE - Air-driven rotating biological wastewater pretreatment device integrated structure.    ADVANTAGE - The accommodation space of biological wastewater pretreatment device is reduced. The separation and biological enzyme catalysis treatment of sewage are performed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the air-driven rotating biological wastewater pretreatment device integrated structure.    Drain pipe (1)    Sewage processing pool (2)    Oxygen supply pipe (7)    Rotating disc (8)    Solid impurities removing process pool (21)    Biological treatment pool (22)    Partition (31)
NOVELTY - Organic matrix comprises 30-38 pts. wt. cow dung, 25-30 pts. wt. mushroom residue, 40-50 pts. wt. corn core, 12-18 pts. wt. rice hull, 10-12 pts. wt. grass peat, 6-8 pts. wt. perlite, and 3-5 pts. wt. orchid seed.    USE - Organic matrix used for pepper plant (claimed).    ADVANTAGE - The matrix provides nutrient elements to meet plant growth needs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of matrix comprising taking cow dung, mushroom residue, corn core, rice hull, peat, perlite, and orchid seed, mixing, placing in fermentation pool, sealing with plastic film, adding water, adjusting water content to 50-60%, where carbon/nitrogen ratio is 30-40, static state composting, fermenting at 40-45 degrees C, turning when fermentation matrix central temperature exceeds 60 degrees C, co-fermenting for 45 days; drying to a water content of 8-10%, crushing to less 8 mm; sieving to less than 6 mm, packaging and sealing.
NOVELTY - A microbial water soluble compound fertilizer comprises 5-8 wt.% composite microorganism fermentation liquid, 6-12 wt.% peanut meal, 5-10 wt.% rotten chicken manure, 3-5 wt.% nitrate base humic acid, 10-20 wt.% egg, 6-8 wt.% biological fungus fertilizer and balance water.    USE - Microbial water soluble compound fertilizer.    ADVANTAGE - The fertilizer is rich in nutrition, increases soil granule structure, promotes crop growth, and increases crop yield and quality. It is suitable for drip irrigation, flushing and spraying.
NOVELTY - A methanol is produced by mounting pressure swing adsorption device into waste methanol production device exhaust vent, feeding natural gas, coke furnace coal and other feed gas into methanol production device, generating, collecting methanol through external device, sending into pressure swing adsorption device, processing, separating carbon monoxide, carbon dioxide, methane, hydrogen and nitrogen, transporting carbon monoxide, carbon dioxide and methane into pipeline methanol production device, and recovering hydrogen and nitrogen.    USE - Method for producing methanol (claimed).    ADVANTAGE - The method increases yield, saves raw material and power consumption to 8-10%, avoids waste air discharge, and reduces air pollution and purifying material consumption to 10-15%.
NOVELTY - A gossypol rapid separation and purification method via macroporous resin comprises taking cottonseed, crushing, adding 80 wt.% ethanol, heating at 50-70 degrees C, filtering, diluting with water, adding 40 wt.% ethanol, purifying via macroporous resin, adding water, eluting with 40 wt.% ethanol and 80 wt.% ethanol, collecting eluate, concentrating, adding acetone-glacial acetic acid mixed solution, and recrystallizing.    USE - Gossypol rapid separation and purification method via macroporous resin (claimed).    ADVANTAGE - The method is simple, low-cost, environment-friendly and suitable for industrialization. It has high product purity.
NOVELTY - Method for enhancing biochar carbon storage method using phosphorus mineral involves preparing suspension using phosphorus-containing mineral and calcium dihydrogen phosphate, mixing biomass waste, heating to 500-600 degrees C at rate of 10-20 degrees C/minute for 2-4 hours, and producing modified biochar.    USE - Method for enhancing biochar carbon storage method using phosphorus mineral (claimed).    ADVANTAGE - The method enables simple preparation of biochar at low cost, without affecting the environment. The carbon loss is reduced, and biochar product stability is increased.
NOVELTY - Preparation of system involves providing a water-soluble cadmium selenide nanoparticle surface-capped with mercaptosuccinate (CdSe-MSA), providing nitrogenase accessory factor Y(NafY)-iron-molybdenum cofactor complex comprising NafY protein and iron-molybdenum cofactor (FeMo-co) and mixing CdSe-MSA and FeMo-co under anaerobic conditions to form CdSe-MSA-FeMo-co complex system. When illuminated with visible light source, the CdSe-MSA-FeMo-co complex system is capable of photocatalytically producing hydrogen gas.    USE - Preparation of system used for production of hydrogen gas (claimed) for fuel cell.    ADVANTAGE - The method provides system having excellent stability. The water-soluble cadmium selenide nanoparticle-trioctylphosphine nanoparticles exhibit photoactivity in organic solvent due to intrinsic quantum confinement characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of hydrogen gas, which involves illuminating CdSe-MSA.NafY.FeMo-co system with visible light source. The system produces hydrogen gas for an extended period of at least 5 hours.
NOVELTY - The utility model is new type relates to one kind novel transfusion warming quilt, comprising medical adhesive tape film, send heat bag layer, medical air-permeable adhesive tape layer with holes, package layer outside, the medical adhesive tape film adhesive for medical air-permeable adhesive tape layer two end holes, send heat bag layer is adhesive tape layer center, to the length at left end are medical adhesive tape film is in the right end are medical adhesive tape film and length is half of the outside package layer for medical adhesive tape film, send heat bag layer, medical air-permeable adhesive tape layer with holes. The utility model is new type is one kind using suitable, low price, comfortable and environment-friendly, temperature, lasting effect and transfusion warming quilt patch.
NOVELTY - The utility model relates to a device for anaerobic fermentation, by micro-fermentation tank, water channel, the weight cylinder, one end uniform with the transfusion needle head and hose 1 and hose 2 make up, wherein weight cylinder is inverted water channel inside, and internal is filled with saturated salt water, the hose needle is 1 plug through the micro-fermentation tank in the micro-fermentation tank, another end in the inverted amount of cylinder, to the hose weight 1 is located in the external cylinder and the weight setting one cylinder can move the switch element, the hose (2) and needle plug through the micro-fermentation tank in the micro-fermentation tank, the end provided with 2 of closed element. The utility model is new type the device, structure is simple, can collect the gas sample by Anaerobic fermentation of marsh gas and marsh gas, and gas sample environment and maintain good fermentation system Anaerobic suitable and fast process of detection analysis.
NOVELTY - The utility model relates to a raw material processing device used for marsh gas production, specifically is used for marsh gas production and raw material pre-processing device, comprising slag input pipe 1, organic liquid input tube 2, wherein water 3, stirring 4, shower nozzle 5, water tank 6, stirring column 7, a discharging port 8, electrical machine 9, wherein the stirring chamber 4, its bottom set with motor 9, one side equipped with a discharging port 8, the upper part set with water tank 6, and the water tank 6, the one side equipped with slag input pipe 1, another side set with organic liquid input pipe 2, the water tank 6 is set with shower nozzle bottom 5. water mouth 3 is set with water box 6 on, the stir chamber 4 equipped with stirring in column 7, the stirring post (7) main shaft is the main shaft through out of the stirring chamber 4 and bottom motor 9 matching install, the utility model is new type structure is simple, use is convenient, suitable operation, using suitable to solve have traditional marsh gas production raw material pre-processing efficiency is low, problem of time and labour cost and reliability utility.
NOVELTY - A methane tank temperature control system, including, control circuit, electric circuit. Control circuit connected to micro-controller as core, micro-controller for temperature sensor transmit the data by receiving, using micro-controller to receive the up data and uplink to upper computer, and for receiving data and carrying out processing to generate control signal to control heating device, electric circuit connected to storage battery is based on solar energy plate give out electric energy storage in the storage battery and the electric energy in the storage battery on one hand by chopping wave circuit is micro-controller and temperature sensor power supply, another one aspect through boost circuit and inverter circuit for heating device of marsh gas pool for internal power.
NOVELTY - The utility model is new type belongs to biological use field, especially relates to one kind using biodegradable and ecological environment-friendly toilet. The lower part comprises toilet room, toilet, and biodegradable chamber, provided with toilet door, floor and ventilating mouth, wherein the ventilating toilet side wall or top part of pedestal pan fixed up on the floor in the toilet room, biodegradation chamber the toilet indoor; in biodegradable chamber preset with hermitia illucens larva and auxiliary material. The utility model is new type using black soldier fly can resolve characteristics of organic garbage, used for decomposing toilet excrement, needs no other auxiliary device, decomposing residue can directly used for fertilizer manufacture, larva can directly as feed, or carrying out deep processing, at last realize zero discharge of resource circulation use.
NOVELTY - Preparing an oil comprising at least one long chain polyunsaturated fatty acid, comprises contacting oil-medium with lipid biomass and a culture of microorganisms, bioconversion and separation of the obtained oil, where the biomass is the aqueous bacterial and fungal suspension containing lignocellulosic feedstock from another fermentation. Preparing feed comprises preparation of the oil, where the oil separated from the precipitate is fermented, and fiber-containing lipids is used as a product for animal feed.    USE - The process is useful for preparing oil that is used as ingredient in food industry, cosmetic industry or pharmaceuticals.
NOVELTY - Processing pig excrement comprises introducing pig manure and fermentation agent into pressing machine, providing air and water, high-temperature fast fermenting, crushing, and stacking in field for 8-10 days to obtain organic fertilizer.    USE - Method for processing pig excrement to obtain organic fertilizer (claimed).    ADVANTAGE - The method is simple to operate and convenient to maintain, and has no seasonal restriction, small one-time investment and low operational cost.
NOVELTY - A 4-methyl-5-alkoxy oxazole derivative (I) is new.    USE - 4-Methyl-5-alkoxy oxazole derivative.    ADVANTAGE - The raw materials are cheap and easy to obtain. The method is simple, low-cost, safe, and environment-friendly.    DETAILED DESCRIPTION - A 4-methyl-5-alkoxy oxazole derivative of formula (I) is new. An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Alcohol ether diesel oil comprises 0-70 wt.% base diesel oil and 30-100 wt.% alcohol ether additive, where the alcohol ether additive comprises 100-600 pts. wt. alcohol, 200-500 pts. wt. oleic acid, 50-150 pts. wt. ethanolamine and 20-70 pts. wt. cyclohexane or mixture of cyclohexane, cyclohexylamine and water.    USE - Alcohol ether diesel oil used as fuel in various vehicles and industrial boilers.    ADVANTAGE - The alcohol ether diesel oil is cost-effective and prepared in simple manner, has good safety, and ensures good atomization and full combustion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing alcohol ether diesel oil, which involves:    (A) adding alcohol, oleic acid, ethanolamine and cyclohexylamine in a reaction container;    (B) stirring the obtained material at 15-40 degrees C for 5-40 minutes to obtain alcohol ether additive;    (C) mixing the alcohol ether additive and base diesel oil in another container to obtain semi-finished product; and    (D) precipitating the mixed material for 10-40 hours to obtain the desired product.
NOVELTY - Preparing solid biomass fuel involves taking biomass as raw material, and then drying biomass in presence of sun light for 5-10 days. The sun-dried biomass is transported into a dryer to undergo the pre-heating process. The heat of the dryer originates from the high temperature exhaust gas produced from the combustion of biomass fuel. The biomass raw material pre-heating temperature is controlled in the range of 100-180 degrees C. The pre-heating time is controlled for 10-30 minutes. The pre-heated bio-mass raw material is directly transported to a pulverizer to undergo the pulverizing process.    USE - Method for preparing solid biomass fuel (claimed).    ADVANTAGE - The method enables to prepare solid biomass fuel in a simple and cost-effective manner.    DETAILED DESCRIPTION - Preparing solid biomass fuel involves taking biomass as raw material, and then drying biomass in presence of sun light for 5-10 days. The sun-dried biomass is transported into a dryer to undergo the pre-heating process. The heat of the dryer originates from the high temperature exhaust gas produced from the combustion of biomass fuel. The biomass raw material pre-heating temperature is controlled in the range of 100-180 degrees C. The pre-heating time is controlled for 10-30 minutes. The pre-heated bio-mass raw material is directly transported to a pulverizer to undergo the pulverizing process. The biomass baked raw material is transported to the mixing machine. The raw material mixture is transported to the pellet mill.
NOVELTY - Cleansing device comprises medical waste filter device (1), a feedstock device (2), a processing device (3), a solid liquid separation device (4) and a granulating device (5) that is connected to the solid liquid separation device. The medical waste filter device is connected to the feedstock device. The feedstock device is connected to the processing device.    USE - Device for cleansing system of waste solids biofuels (claimed).    ADVANTAGE - The device enables cleansing system of waste solids biofuels in a simple and efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for cleansing system of waste solids biofuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a cleansing device. (Drawing includes non-English language text).    Medical waste filter device (1)    Feedstock device (2)    Processing device (3)    Solid liquid separation device (4)    Granulating device (5)
NOVELTY - Preparing biodiesel involves adding methanol into a reaction flask, heating reaction flask at certain temperature, performing distillation of hot material, and then filtering distilled product to obtain filtrate. Glycerin and vegetable oil methyl ester are added to filtrate. The mixture is analyzed through gas chromatography.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables to prepare biodiesel in a simple manner.
NOVELTY - Biodiesel preparation involves charging reaction vessel with 300-400 grams fat and oil in a molar ratio of 10:1-12 in methanol. 1-5% catalyst is also added in the reaction mixture at 100-120 degrees C with a stirring speed of 400-700 revolutions per minute for 2-4 hours o form a crude product. The formed crude product is removed by centrifugation, and washed with methanol to obtain the finished product.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method prepares biodiesel in a simple and cost-effective manner by reducing energy consumption.
NOVELTY - Solid base catalyst preparation involves mixing 300-400 lipid and methyl alcohol in a mol ratio of 10:1-12:1 in a reaction kettle, and then adding 1-3% catalyst to form a mixture. The formed reaction mixture is heated at 60-70 degrees C for 2-4 hours to form a crude product. The formed crude product is centrifuged for removing the catalyst, which is dried in vacuum for obtaining the finished product.    USE - Method for preparing solid base catalyst for biodiesel (claimed).    ADVANTAGE - The method prepares solid base catalyst in a simple and eco-friendly manner without generating waste water.
NOVELTY - Super carbosulfan is prepared by heating di-n-butylamine to 100-300 degrees C, stirring, cooling to 0 degrees C, slowly dripping disulfur dichloride, maintaining temperature at 160-170 degrees C, adding sulfuryl chloride, and preserving heat for 2 hours to obtain intermediate product, where mole ratio of di-n-butylamine and sulfuryl chloride is 10:5; reacting intermediate product with carbofuran under alkaline condition at 10-20 degrees C for 2 hours; and after reaction, adding water, stirring for 10 minutes, filtering unreacted carbofuran and recycling, and decompressing filtered liquid to obtain super carbosulfan.    USE - Method for preparing super carbosulfan (claimed) used in preventing and treating aphids in orange and other fruits, vegetables, corn, cotton, rice, and sugarcane.    ADVANTAGE - The method has carbosulfan yield rate of 90% and di-n-butylamino sulfur chloride yield of 88%. The super carbosulfan has fast effect and low residue, and is safe to use and is not harmful to crops.
NOVELTY - Processing food wastes, comprises (a) collecting food waste discarded from a restaurant or home, (b) planting of halophytes on upper of the collected food wastes, and (c) absorbing the salt by halophytes to minimize concentration of salt.    USE - The method is useful for processing food wastes (claimed).    ADVANTAGE - The method minimizes concentration of salt in food waste, and is environmentally friendly, and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of halophytes to obtain desire source of animal by drying at room temperature, heating, heat drying by microwave or freeze drying the halophytes.
NOVELTY - A biofuel additive comprises 40-50 pts. wt. xylene, 20-30 pts. wt. methanol, 5-10 pts. wt. long chain fatty acids, 10-15 fat ethyl hexyl and 5-10 hydrogen peroxide.    USE - Biofuel additive (claimed).    ADVANTAGE - The biofuel additive has excellent product stability, improved thermal efficiency, combustion efficiency and reduced fuel consumption.
NOVELTY - Fuel additive comprises 40-50 pts. wt. ethanol, 20-30 pts. wt. olefin, 5-10 pts. wt. cycloalkane, 10-15 pts. wt. n-butyl alcohol and 1-5 pts. wt. polycyclic aromatic hydrocarbon.    USE - Fuel additive.    ADVANTAGE - The fuel additive is cost-effective and eco-friendly, and ensures complete combustion and reduces oil consumption.
NOVELTY - The utility model is new type category stirring device manufacturing technology field, relating to one kind used for compost material mixture of gear transmission. It comprises shell, stirring system, driving device, for hopper, a discharging mouth, shell is strip type cylindrical structure, stirring system is provided with uniform peripheral distribution shape type slurry is double-shaft blade type stirring device, driving device is motor drive device, for hopper is over big square-shaped hopper, a discharging mouth is circular mouth, transverse housing formed by left and right two supporting frame is fixed at floor, stirring system is equipped with location inner side and shell through gear shaft and driving device connected with the driving device is set with right end housing outside position, for hopper set at the right position on the shell, a discharging mouth is set with left seat shell as follows. The utility model is new type comprises following characteristics: structure is compact, the occupation space is small; operation suitable, working efficiency high, mixing uniformity is not less than 85%, especially fit viscous material and corrosion resistance with strong stirring using the material.
NOVELTY - Modified biochar-wetland phosphorus sewage processing involves planting aquatic plants in filler layer of artificial wetland, collecting aquatic organisms in harvest season, preparing modified biochar, applying modified biochar to artificial wetland, and continuing growth of aquatic plants.    USE - Modified biochar-artificial wetland phosphorus sewage processing method (Claimed).    ADVANTAGE - The method eliminates the vulnerability to climate temperature, aquatic disposal, and re-release matrix phosphorus adsorption saturation.
NOVELTY - Preparing passivated slow-release fertilizer involves grinding magnesium phosphate slag, urea and industrial potassium sulfate to obtain powder. The phosphoric acid solution is stirred magnesium phosphate slag powder to obtain inorganic binder that is mixed with urea powder and industrial potassium sulfate powder. The obtained mixture is granulated to obtain product.    USE - Method for preparing passivated slow-release fertilizer (claimed).    ADVANTAGE - The method enables to prepare passivated slow-release fertilizer that ensures simple and low cost preparation, large-scale industrial production, no pollution, energy consumption saving and magnesium slag utilization.
NOVELTY - Organic slow release fertilizer is prepared by crushing 70-100 pts. wt. mushroom residue to obtain powder that is mixed with 30-40 pts. wt. corn core powder, 10-20 pts. wt. chicken manure, 5-10 pts. wt. plant ash, 10-20 pts. wt. wheat bran, 15-20 pts. wt. composite microbial inoculum and water uniformly. The obtained mixture is fermented and then fermented material is mixed with 5-10 pts. wt. urea, 5-10 pts. wt. ammonium dihydrogen phosphate, 3-6 pts. wt. potassium chloride, 20-30 pts. wt. active coal and 5-10 pts. wt. cellulose uniform to obtain fertilizer core material.    USE - Organic slow release fertilizer.    ADVANTAGE - The organic slow release fertilizer is effective.    DETAILED DESCRIPTION - Organic slow release fertilizer is prepared by crushing 70-100 pts. wt. mushroom residue to obtain powder that is mixed with 30-40 pts. wt. corn core powder, 10-20 pts. wt. chicken manure, 5-10 pts. wt. plant ash, 10-20 pts. wt. wheat bran, 15-20 pts. wt. composite microbial inoculum and water uniformly. The obtained mixture is fermented and then fermented material is mixed with 5-10 pts. wt. urea, 5-10 pts. wt. ammonium dihydrogen phosphate, 3-6 pts. wt. potassium chloride, 20-30 pts. wt. active coal and 5-10 pts. wt. cellulose uniform to obtain fertilizer core material. The fertilizer core material is mixed with 15-20 pts. wt. bentonite and 5-10 pts. wt. acrylic resin to obtain mixture that is dried and then mixed with mixture of 5-10 pts. wt. paraffin and 5-10 pts. wt. stearic acid as sealing agent. The obtained mixture is dried to obtain slow release fertilizer.
NOVELTY - Preparing organic liquid fertilizer involves mixing mannitol or sorbitol (10 pts. wt.), water (70 pts. wt.) and soluble calcium salt (80 pts. wt.) under stirring condition at 55-65 degrees C. Soluble calcium salt is added to obtained heated mixture, and temperature is increased to 70-90 degrees C. Obtained mixture is stirred for 60 minutes to obtain the final product.    USE - Method for preparing organic liquid fertilizer (claimed).    ADVANTAGE - The method is simple, and enables to prepare organic liquid fertilizer which provides enhanced mobility of elemental calcium in plants.
NOVELTY - Use of protein in either: (a) regulating abscisic acid tolerance in plants; or (b) breeding the plant varieties with increased abscisic acid tolerance, is claimed. The protein comprises fully defined 609 amino acids (SEQ ID NO: 3), as given in the specification.    USE - The protein or gene is useful for regulating abscisic acid tolerance in plants and breeding the plant varieties with increased abscisic acid tolerance for weeding (claimed).    ADVANTAGE - The weeding method is pollution-free and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) gene encoding the protein, useful in (a) or (b);    (2) cultivating increased abscisic acid tolerance transgenic plants, comprising transferring the gene encoding the protein into a recipient plant to obtain a transgenic plant having increased abscisic acid tolerance than the recipient plant; and    (3) transgenic plant weeding method, comprising adopting abscisic acid solution (in molar concentration) as an herbicide, where the weeds cannot tolerate the molar concentration of abscisic acid, but the transgenic plant is tolerant.
NOVELTY - Propagating aerobic fermentation strain comprises (i) uniformly mixing raw materials; (ii) spraying the prepared aerobic fermentation agents to the first part of raw materials, stirring, and forming a first stack; (iii) spraying the prepared aerobic fermentation agents to the second part of raw materials, stirring, and forming a second stack; (iv) repeating the step (iii) until the nth stack is formed, and turning each stack; (v) sequentially taking quantitative semi-finished product from the first stack to the nth stack, mixing, and taking the mixture as the next fermentation agent.    USE - The method is useful for propagating aerobic fermentation strain (claimed).    ADVANTAGE - The method: produces the semi-finished product by the fermentation process, which can served as an inoculation source; serves the fermented materials as finished products; requires low sites; is simple; saves the amount of the agents; shortens the composting fermentation period; and reduces the production cost.    DETAILED DESCRIPTION - Propagating aerobic fermentation strain comprises (i) uniformly mixing raw materials, and dividing the materials into 2-15 pts. wt.; (ii) spraying the prepared aerobic fermentation agents to the first part of raw materials, uniformly stirring, and forming a first stack; (iii) spraying the prepared aerobic fermentation agents to the second part of raw materials after the set time at intervals, stirring, and forming a second stack by using the same method; (iv) repeating the step (iii) until the nth stack is formed, and turning each stack once per day; and (v) after the nth stack is formed within 5-7 days, sequentially taking quantitative semi-finished product from the first stack to the nth stack, mixing, and taking the mixture as the next fermentation agent.
NOVELTY - Cadmium passivating agent comprises the sugar cane filter mud, bacteria and calcium fertilizer as raw materials. The sugar cane filter sludge is prepared by carrying out sulfitation method of lime and sulfur dioxide, which are clarifying agents. The weight ratio of sugar cane sulfitation filtered mud and bacteria is 100:1-2. The mud filtrate is air-dried to obtain compost. The dried mud and calcium fertilizer are mixed in the weight ratio of 10:0.8-1.    USE - Cadmium passivating agent for soil.    ADVANTAGE - The cadmium passivating agent reduces 65-86% cadmium content in rice particle.
NOVELTY - Comprehensive utilization of whole plant straw comprises taking plant straw, manual separating cellulose, lignin and hemicellulose; adding cellulase into cellulose to obtain plant fiber and cellulose alcohol; taking lignin, performing liquefaction process to obtain phenol raw material substitute; and taking hemicellulose, and carrying out liquefaction to obtain xylose or furfural.    USE - Method for comprehensively utilizing whole plant straw (claimed).    ADVANTAGE - The method is simple.
NOVELTY - Method for preparing organic fertilizer, involves (a) collecting fallen leaves, and removing impurities from the leaves, (b) crushing the leaves using crusher, (c) passing crushed leaves through a roller, (d) mixing the crushed leaves with ash, sawdust, ocher, microorganism, effective microorganism (EM), salt water, water-soluble phosphoric acid and water-soluble potassium using mixer, (e) performing primary fermentation at 60-80 degrees C, (f) performing secondary fermentation at room temperature for 30 days, and (g) maintaining water content of obtained product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method prepares fertilizer which improves nutritional content of soil.    DETAILED DESCRIPTION - Method for preparing organic fertilizer, involves (a) collecting fallen leaves, and removing impurities from the leaves, (b) crushing the leaves using crusher, (c) passing crushed leaves through a roller, (d) mixing 60 wt.% ash, 15 wt.% sawdust, 15 wt.% crushed leaves, 4 wt.% ocher, 2 wt.% microorganism, 1 wt.% effective microorganism (EM), 1 wt.% salt water, 1 wt.% water-soluble phosphoric acid and 1 wt.% water-soluble potassium using mixer, (e) subjecting obtained mixture to primary fermentation at 60-80 degrees C, where the mixture is stirred twice/day during primary fermentation, (f) subjecting fermented product to secondary fermentation at room temperature for 30 days, and (g) maintaining water content of obtained product.
NOVELTY - 3 Pts. wt. white mud is added to a vertical mixer, 1 pt. wt. waste sulfuric acid is slowly added, and stir-reacted at 70-90 degrees C for 3-5 minutes. Bellflower is pulverized to 15-20 mesh and mixed with the reaction mixture in a ratio of 1:2. Bacillus subtilis is added and thermally reacted, turning once every 12 hours. The contents are discharged after 20 days, dried, and crushed to 15-20 mesh to obtain an organic fertilizer.    USE - Use of industrial waste to produce organic fertilizer (claimed).    ADVANTAGE - The method enables effective usage of industrial waste, provides high-quality organic fertilizer which can be easily absorbed and utilized, and is simple, easy and economical.
NOVELTY - Method for preparing liquid fertilizer, involves adding 100 pts. wt. water, 20-30 pts. wt. bean water, 0.5-2 pts. wt. saccharides, 2.5-4 pts. wt. fermentation aid and 1-2 pts. wt. microbial enzyme to first fermenter, performing primary fermentation at room temperature, filtering fermented product, adding obtained product to second fermenter, and performing secondary fermentation and aging process.    USE - The method is useful for preparing liquid fertilizer (claimed).    ADVANTAGE - The method prepares liquid fertilizer which enables soil improvement.
NOVELTY - Invention relates to agriculture. The method of composting the organic part of food wastes comprises a liquid phase and a solid phase fermentation using microorganism culture, at that the microorganism culture is used as activated sludge which was previously grown on the liquid phase of the said food waste, at that the food wastes are preliminary crushed to the fraction of 1/3 mm, a part of the crushed food wastes is centrifuged, and the resulting liquid phase is fed for fermentation for growing the activated sludge, the liquid-phase fermentation is carried out for 7/10 days, the temperature in the first 5 days is provided from 28 degrees C to 32 degrees C, and the temperature in the subsequent days - from 42 degrees C to 44 degrees C, then the solid phase obtained by centrifuging the crushed food wastes is mixed with the remaining crushed food wastes to form the composted mixture, after which the activated sludge obtained during the liquid phase fermentation is added to the composted mixture in an amount of not less than 3% by weight of the composted mixture.    USE - Agriculture.    ADVANTAGE - Invention enables to simplify the process of composting the organic part of food wastes, and also to increase the efficiency of the process.2 ex
NOVELTY - The preparation method of 4-hydroxy-thiobenzamide derivative (I) involves adding water and sodium hydroxide to 4-hydroxy-benzonitrile compound (II), uniformly mixing, stirring the mixture, adding sodium hydrosulfide and ammonium hydrosulfide to the mixture, and reacting.    USE - The method is useful for preparation of 4-hydroxy-thiobenzamide derivative (I) (claimed).    ADVANTAGE - The method enables economical preparation of 4-hydroxy-thiobenzamide derivative (I) in an environmentally-friendly manner.    DETAILED DESCRIPTION - The preparation method of 4-hydroxy-thiobenzamide derivative of formula (I) involves adding water and sodium hydroxide to 4-hydroxy-benzonitrile compound of formula (II), uniformly mixing, stirring the mixture, adding sodium hydrosulfide and ammonium hydrosulfide to the mixture, and reacting.
NOVELTY - Extraction of palmatine chloride comprises crushing Chinese herbal medicinal materials, adding acidic aqueous solvent, refluxing, filtering, recovering solvent, adjusting pH, standing, filtering, concentrating, adjusting pH, adding sodium chloride, standing, filtering, and drying; adding alkaline aqueous solvent, reflux extracting, filtering, adjusting pH, standing, filtering, concentrating, acidifying, adding sodium chloride, standing, filtering, and drying; and repeating second step, precipitating, extracting with ethanol, filtering, and adjusting pH with hydrochloric acid.    USE - Method for extracting palmatine chloride used for preparing drug for treating and preventing colon cancer (claimed).    ADVANTAGE - The method recovers has more than 85% palmatine hydrochloride, short production process, and low cost and is environment-friendly.    DETAILED DESCRIPTION - Extraction of palmatine chloride comprises crushing Chinese herbal medicinal materials, adding 0.1-5 wt.% acidic aqueous solvent, refluxing, filtering, recovering solvent, adding base to adjust pH to 8-14, standing, filtering, concentrating, adjusting pH to 0.5-7, adding 5-20% sodium chloride, standing, filtering, and drying precipitate; adding alkaline aqueous solvent, reflux extracting, filtering, adjusting pH to 8-10 using base, standing, filtering, concentrating, acidifying with hydrochloric acid until pH is 0.5-7, adding 5-20% sodium chloride, standing, filtering, and drying precipitate; and repeating second step, precipitating, extracting with 95% ethanol, filtering, and adjusting pH to 0.5-7 with hydrochloric acid, where Chinese herbal medicine comprises leatherleaf Mahonia, golden cypress, herba fibraureae recisae, Coptis chinensis, and radix berberidis.
NOVELTY - 2-(2-Fluorophenyl)-6,8-dioxa-12-azapentacyclo(11.8.0.0,05,04)henicosa-1,3,5(9),10,12,14(19),15,17-octaene-20,21-dione (I) is new.    USE - 2-(2-Fluorophenyl)-6,8-dioxa-12-azapentacyclo(11.8.0.0,05,04)henicosa-1,3,5(9),10,12,14(19),15,17-octaene-20,21-dione.    ADVANTAGE - The 2-(2-fluorophenyl)-6,8-dioxa-12-azapentacyclo(11.8.0.0,05,04)henicosa-1,3,5(9),10,12,14(19),15,17-octaene-20,21-dione ensures stronger activity, good absorption and green, simple and high yield preparation.    DETAILED DESCRIPTION - 2-(2-Fluorophenyl)-6,8-dioxa-12-azapentacyclo(11.8.0.0,05,04)henicosa-1,3,5(9),10,12,14(19),15,17-octaene-20,21-dione of formula (I) is new..
NOVELTY - Extraction of neomycin sulfate from neomycin sulfate-containing fermentation broth comprises acidifying neomycin sulfate-containing fermentation broth to pH of 2.0-4.0, filtering, adjusting pH to 6.0-8.0, dynamically adsorbing filtrate by weak acid cation exchange resin to obtain saturated resin, pre-washing impurities of saturated resin with 0.05-0.1 mol/L sodium hydroxide solution, analyzing with 0.2-2.0 mol/L sodium hydroxide solution, bleaching analytical liquid with ultrafiltration membrane, nano-filtering, desalting and spray-drying.    USE - Method for extracting neomycin sulfate from neomycin sulfate-containing fermentation broth (claimed).    ADVANTAGE - The method has high yield and production efficiency, low cost, good finished product quality and no environmental pollution.
NOVELTY - Preparing organic fertilizer involves crushing 70-90 pts. wt. inoculated fungus residue to obtain powder having diameter of 0.5-1 mm. The powder is mixed with water (3-6 times), 1-3 pts. wt. protease and 1-3 pts. wt. cellulase, and then heated to carry out enzymolysis and cooled to obtain enzymolysis liquid. The enzymolysis liquid is dried, and then 40-50 pts. wt. dairy manure, 30-50 pts. wt. corn straw, 20-30 pts. wt. cottonseed, 5-10 pts. wt. humic acid, 10-20 pts. wt. wheat bran, 10-20 pts. wt. rice bran, 10-20 pts. wt. soybean and 1-3 pts. wt. yeast are mixed uniformly.    USE - Method for preparing organic fertilizer used for planting radix scutellariae (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that increases yield and baicalin content of radix scutellariae.    DETAILED DESCRIPTION - Preparing organic fertilizer involves crushing 70-90 pts. wt. inoculated fungus residue to obtain powder having diameter of 0.5-1 mm. The powder is mixed with water (3-6 times), 1-3 pts. wt. protease and 1-3 pts. wt. cellulase, and then heated to carry out enzymolysis and cooled to obtain enzymolysis liquid. The enzymolysis liquid is dried, and then 40-50 pts. wt. dairy manure, 30-50 pts. wt. corn straw, 20-30 pts. wt. cottonseed, 5-10 pts. wt. humic acid, 10-20 pts. wt. wheat bran, 10-20 pts. wt. rice bran, 10-20 pts. wt. soybean and 1-3 pts. wt. yeast are mixed uniformly. The mixture is covered through a film and dried to obtain fertilizer with 20-30 wt.% water content. The fertilizer is mixed with 5-10 pts. wt. silicon, 5-10 pts. wt. vermiculite, 10-16 pts. wt. bentonite, 10-20 pts. wt. urea, 6-8 pts. wt. monoammonium phosphate, 6-8 pts. wt. potassium sulfate, 10-15 pts. wt. wood carbon powder and 5-12 pts. wt. calcium superphosphate are mixed uniformly. The mixture is compressed, and then pelletized through a pelletizer.
NOVELTY - Anti-clotting medicine ticagrelor is synthesized by adding dihydroxysuccinate derivative and 5-aminopyridine derivative in 1st solvent, adding 1st alkali, performing high-temperature reaction, placing in dichloromethane, adding acid, reacting with alkali metal nitrite, placing in 2nd solvent, adding 2nd alkali, reacting with (1R,2S)-2-(3,4-difluorophenyl)cyclopropanamine, and deprotecting.    USE - Synthesis of anti-clotting medicine ticagrelor.    ADVANTAGE - Synthesis of anti-clotting medicine ticagrelor is simple, easy, and environment-friendly and has reduced cost and improved product purity.    DETAILED DESCRIPTION - Anti-clotting medicine ticagrelor of formula (I) is synthesized by adding dihydroxysuccinate derivative of formula (V) and 5-aminopyridine derivative of formula (Va) in 1st solvent, adding 1st alkali, performing high-temperature reaction to form compound of formula (IV), placing in dichloromethane, adding acid, reacting with alkali metal nitrite to obtain compound of formula (III), placing in 2nd solvent, adding 2nd alkali, reacting with (1R,2S)-2-(3,4-difluorophenyl)cyclopropanamine of formula (IIIa) to obtain compound of formula (II), and deprotecting..
NOVELTY - 85-95 Wt.% grain by-products and 5-15 wt.% microorganisms are mixed with water and fermented to obtain liquid enzyme, such that the content of water is 5-15 times by volume ratio. 25-35 Wt.% obtained liquid enzyme, 35-45 wt.% vegetable oil, 15-25 wt.% fuel oil and 5-15 wt.% hexane are mixed to obtain energy-producing raw materials. 5-15 Wt.% borax is added with respect to total weight of the energy source to obtain enzyme energy composition.    USE - Manufacture of enzyme energy composition (claimed) used as fuel.    ADVANTAGE - The method efficiently and economically provides environmentally-friendly enzyme energy composition with suppressed generation of toxic gas and greenhouse gas.
NOVELTY - Organic nutraceutical composition comprises fermented product chosen from Japanese apricot, purslane, Artemisia annua, Oenanthe javanica, loofah, dandelion, fruit and vegetable culture.    USE - The organic nutraceutical composition is useful for cultivation of grapes and red pepper (claimed).    ADVANTAGE - The composition is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic farming method, which involves applying nutrient and insect repellent to fruit and vegetables, where the insect repellent is Phytolacca acinosa, folium ginkgonis, garlic, lacquer resin or pyroligneous liquor.
NOVELTY - The ammonia synthesis catalyst system comprises an ammonia synthesis unit (2) connected to a pre-treatment unit (1), a front processing unit, and a carbon monoxide conversion device (4). The conversion device is connected with a transformation tower (5) and a screen (6), where the screen is connected with a liquid nitrogen washing device (7). The ammonia synthesis unit includes an ammonia compressor (8), a heating furnace (9), and ammonia synthesis device (10). The ammonia synthesis device is provided with ammonia synthesis catalyst bed layer (11).    USE - Ammonia synthesis catalyst system.    ADVANTAGE - The ammonia synthesis catalyst system greatly increases production efficiency of synthesis ammonia, avoids waste generation, reduces production cost, and enhances utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ammonia synthesis catalyst system. (Drawing includes non-English language text).    Pre-treatment unit (1)    Ammonia synthesis unit (2)    Carbon monoxide conversion device (4)    Transformation tower (5)    Screen (6)    Liquid nitrogen washing device (7)    Ammonia compressor (8)    Heating furnace (9)    Ammonia synthesis device (10)    Ammonia synthesis catalyst bed layer (11)
NOVELTY - Separating butane and butylene comprises absorbing butane and butylene using organic polar solvent dissolved and/or dispersed with 0.1 wt.% silver salt. The silver salt is soluble silver salt.    USE - Method for separating butane and butylene (claimed).    ADVANTAGE - The method has low energy consumption, simple process, easy operation, little investment, stable production quality and wide raw material sources. It improves quality of butylene and butane.
NOVELTY - The methane fermentation device has a feedstock pipe (10) and a discharging pipe (20) which are detachably connected with a straight pipe (30). A discharging pipe blocking plate (34) is connected with the discharging pipe. A feedstock pipe blocking plate is connected with the feedstock pipe. One-way valves are respectively provided in the feedstock pipe and discharging pipe, for controlling fermentation methane gas flowed in the feedstock pipe and discharging pipe.    USE - Straight hydraulic super-efficient methane fermentation device for use in agricultural field.    ADVANTAGE - The methane gas slurry circulation flow stirring performance is improved, and the uniform distribution of strain is promoted using the stirring methane gas slurry circulation flow. The gas production is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the straight hydraulic super-efficient methane fermentation device.    Feedstock pipe (10)    Discharging pipe (20)    Straight pipe (30)    Discharging pipe blocking plate (34)    Drain pipe (51)
NOVELTY - Nocardia coeliaca is preserved in China general microbiological culture collection with preservation number CGMCC NO:10256.    USE - Nocardia coeliaca used for treating domestic sewage (claimed).    ADVANTAGE - The Nocardia coeliaca increases treatment efficiency and treatment amount of sewage.
NOVELTY - Method for producing microbial support, involves (a) inoculating microorganism chosen from Leuconostoc sp., Lactobacillus sp., Lactococcus sp., Streptococcus sp., Aspergillus sp., Bacillus sp., Saccharomyces sp., Pseudomonas sp., and Candida sp. in rice bran, and fermenting at 40-60 degrees C for 1-5 days, (b) preparing support by mixing 25-30% fermented rice bran and 70-75% porous material and (c) inoculating 0.1-10 vol.% photosynthetic bacteria on the support and aging for 12-36 hours.    USE - The method is used for producing microbial support which is used in organic waste treatment (all claimed).    ADVANTAGE - The method is cost-effective and consumes less energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of organic waste treatment.
NOVELTY - Extraction of kidney bean alpha-amylase inhibitor involves soaking kidney beans, crushing, filtering, standing at room temperature, centrifuging, taking supernatant liquid, performing enzyme inactivation, adding absolute ethanol to supernatant liquid with gentle stirring to precipitate protein, centrifuging, removing lower residual precipitate, adjusting pH, adding alkaline protease enzyme hybrid protein, adding 1 mol/L hydrochloric acid, adjusting pH, centrifuging, taking supernatant liquid, adding absolute ethanol to supernatant liquid, centrifuging and taking precipitate.    USE - Method for extracting kidney bean alpha-amylase inhibitor.    ADVANTAGE - The method is simple, low cost and environmental-friendly. The kidney bean alpha-amylase inhibitor is suitable for large-scale industrial production. It has high purity, high activity and has good economic benefit.
NOVELTY - Continuous production of herbicide 2,4-dichlorophenoxyacetic acid, comprises taking phenol and chlorine, passing into microchannel reactor, conducting continuous chlorination of 2,4-dichlorophenol, and recovering hydrogen chloride gas; taking 2,4-dichlorophenol and sodium hydroxide preparation into sodium chloroacetate aqueous solution preparation, carrying out condensation reaction, and filtering; and mixing the obtained 2,4-dichlorophenoxy sodium acetate and water, carrying out acid acidification reaction, regulating pH value, vacuum filtering the finish material, washing, and drying.    USE - Method for continuous production of herbicide 2,4-dichlorophenoxyacetic acid.    ADVANTAGE - The method is efficient, environment-friendly, sustainable and suitable for industrial production, saves energy, reduces emission of pollutants, and achieves safe continuous industrial production.    DETAILED DESCRIPTION - Continuous production of herbicide 2,4-dichlorophenoxyacetic acid, comprises:    (A) taking phenol and chlorine as raw materials at molar ratio of 50:100, passing into microchannel reactor, conducting continuous chlorination of 2,4-dichlorophenol, and recovering hydrogen chloride gas;    (B) taking 2,4-dichlorophenol and sodium hydroxide preparation into sodium chloroacetate aqueous solution preparation, reacting under 30-60 degrees C, carrying out condensation reaction, controlling the series of reaction temperature in condensation reaction kettle, and passing the finish material in vacuum pressure filter to obtain 2,4-dichlorophenoxy sodium acetate; and    (C) mixing 2,4-dichlorophenoxy sodium acetate and water to formulate 2,4-dichlorophenoxyacetic acid aqueous solution of sodium acetate, adding into acidification reaction kettle in series and carrying out acid acidification reaction, regulating pH value, vacuum filtering the finish material, washing, and drying.
NOVELTY - Preparation of 2-hydroxy-chloroacetanilide (II) comprises slowly dropping o-aminophenol (I) in acetone solution with acetyl chloride and ammonia, dropping water at 20 degrees C to precipitate 2-hydroxy-chloroacetanilide, filtering, and calcining to obtain crude 2-hydroxy-chloroacetanilide; and adding acetic acid solution to adjust pH to 4, adding activated carbon and diatomaceous earth, heating to carry out boiling for 10 minutes, filtering, cooling, crystallizing, filtering, and drying to obtain pure 2-hydroxy-chloroacetanilide.    USE - Method for preparation of 2-hydroxy-chloroacetanilide (claimed).    ADVANTAGE - The method is simple, environment-friendly and suitable for large-scale industrial production, saves resources, can recover acetone solvent, and it has short reaction time, reduced production cost, increased production efficiency of up to 80%.    DETAILED DESCRIPTION - Preparation of 2-hydroxy-chloroacetanilide of formula (II) comprises slowly dropping o-aminophenol of formula (I) in acetone solution with acetyl chloride and ammonia, dropping water at 20 degrees C to precipitate 2-hydroxy-chloroacetanilide, filtering, and calcining to obtain crude 2-hydroxy-chloroacetanilide; and adding acetic acid solution to adjust pH to 4, adding activated carbon and diatomaceous earth, heating to carry out boiling for 10 minutes, filtering, cooling, crystallizing, filtering, and drying to obtain pure 2-hydroxy-chloroacetanilide.
NOVELTY - A metal salt and organic acid rosin resin-containing acrylic resin (I) is new.    USE - Metal salt and organic acid rosin resin-containing acrylic resin used for environment-friendly self-polishing ocean antifouling paint (claimed).    ADVANTAGE - The compound (I) is environment-friendly and it has good compatibility with other components of paint. The self-polishing paint has good coating toughness and long antifouling period.    DETAILED DESCRIPTION - A metal salt and organic acid rosin resin-containing acrylic resin of formula R-X-R1 (I) is new.    R=benzoic acid, naphthenic acid, salicylic acid, furoate, chlorobenzoic acid, 2,4-dichlorobenzoic acid, proline, leucine, phenylalanine or arginine acid radicals;    X=Zn2+, Cu2+, Mg2+ or Ca2+; and    R1=rosin acid, different rosin acid or rosin acid dimer.    INDEPENDENT CLAIMS are included for:    (1) preparation of compound (I); and    (2) an environment-friendly self-polishing ocean antifouling paint comprising 20-60 pts. wt. compound (I), 1-20 pts. wt. cuprous oxide, 1-20 pts. wt. a plasticizer, 1-30 pts. wt. filler, and 20- 60 pts. wt. solvent.
NOVELTY - Pefloxacin mesylate freeze-dried powder comprises antioxidants in raw materials which are filled into 7 ml vials.    USE - Small volume vials freeze-dried powder (claimed).    ADVANTAGE - The method increases product quality, increases yield, and reduces energy consumption for freeze-drying and evaporation, packing volume and transportation cost, and is cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation method of pefloxacin mesylate freeze-dried powder involves mixing water for injection, pefloxacin mesylate, mannitol and antioxidant and stirring to dissolve, and concentrating mixture, adding activated carbon for decarburizing and filtering mixture, refined filtering mixture, diluting filtrate with remaining water for injection, heat preserving solution at 20-25 degrees C, filling heat preserved solution in 7 ml vials, and freeze-drying and capping product; and    (2) production device comprising dispensing heat preservation tank, first grid pump, pump rod filter, first sterilizing filter, sterile liquid storage tank, second grid pump, second sterilizing filter, filling machine and freeze dryer.
NOVELTY - Preparation of 2-amino-6-chloro-9-(4-hydroxy-3-hydroxymethylbutyl)purine involves preparing 2-amino-6-chloro-9-(4-hydroxy-3-hydroxymethylbutyl)purine aqueous alkaline solution, adjusting pH to 8-10 using hydrochloric acid, stirring for 30-60 minutes, filtering, discarding filter cake, neutralizing filtrate with hydrochloric acid, evaporating methanol under reduced pressure, removing water, adding acetone into concentrated residue, stirring, crystallizing, filtering and drying.    USE - Preparation of 2-amino-6-chloro-9-(4-hydroxy-3-hydroxymethylbutyl)purine used as intermediate in production of famciclovir and penciclovir.    ADVANTAGE - The method enables simple preparation 2-amino-6-chloro-9-(4-hydroxy-3-hydroxymethylbutyl)purine having high quality, with low energy consumption.    DETAILED DESCRIPTION - Preparation of 2-amino-6-chloro-9-(4-hydroxy-3-hydroxymethylbutyl)purine involves adding 2-amino-6-chloro-9-(3-ethoxycarbonyl butyrate-4-yl)purine, 2-amino-6-chloro-9-(3-methoxycarbonyl butyrate-4-yl)purine or 2-amino-6-chloro-9- (3-methoxycarbonyl butyrate-4-yl)purine to reaction flask, adding dichloromethane and sodium borohydride, slowly adding methanol at room temperature, stirring for 4-6 hours, adding water, stirring for 15-20 minutes, separating aqueous layer, obtaining 2-amino-6-chloro-9-(4-hydroxy-3-hydroxymethylbutyl)purine aqueous alkaline solution, adjusting pH of the aqueous layer to 8-10 using hydrochloric acid, stirring for 30-60 minutes, filtering, discarding filter cake, neutralizing filtrate with hydrochloric acid, evaporating methanol under reduced pressure, removing water, adding acetone into concentrated residue, stirring, crystallizing at 0-10 degrees C for 3-5 hours, filtering, drying, and obtaining product with high-performance liquid chromatography purity of more than 99.5% and ignition residue of less than 3%.
NOVELTY - Use of Paenibacillus peoriae as soil ecological improving and repairing agent is claimed.    USE - Paenibacillus peoriae is used as soil ecological improving and repairing agent (claimed), which is used for enhancing stress resistance, disease resistance, drought resistance, and cold resistance ability of crops.    ADVANTAGE - The agent comprising strain improves the soil ecological system, increases yield, improves quality and ecological environment protection, has pure natural organic nutrient which can improve soil granule structure, make soil loosen, breaks soil plate structure, improves air permeability, increases fertilizer use rate, provides crop growth required magnesium, boron, and microelement.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) soil ecological improving and repairing agent comprising Paenibacillus peoriae, organic substance and microelement; (2) use method of soil ecological improving and repairing agent comprising during crop growth earlier stage, uniformly sowing 30-50 kg/acre or applying in planting field the agent, then ploughing soil; and (3) preparing soil ecological improving and repairing agent comprising selecting Paenibacillus peoriae to carry out fermentation culture, then mixing strain and organic substance and microelement to obtain the soil ecological improving and repairing agent.
NOVELTY - The structure has a combination type fire outlet (22-2) formed with a combination type air outlet hole (21-2) and a fire outlet bush. A wall lining part is connected with a large tapered tube wall. The combination type fire outlet is fixed with a fire sleeve, which is provided with an air channel. An air outlet furnace is connected with a conical pipe wall along axis direction. The air outlet hole is formed with an air blowing device through an indirect belt. A fire outlet bushing wall is formed with the air outlet hole. An air outlet sleeve is connected with an air inlet channel.    USE - Fuel down feeding biomass gasification furnace structure.    ADVANTAGE - The structure increases rate of energy-saving furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a fuel down feeding biomass gasification furnace structure.    Fire damper (1)    Combination type air outlet hole (21-2)    Combination type fire outlet (22-2)    Air hole bushing (35-1)    Air outlet hole bushing (36)
NOVELTY - The method involves heating a gasification reaction agent of a biomass fuel in a fuel fluidized bed reactor, where an air speed of the fuel fluidized bed reactor is 600 to 800m3/h. An air pressure of the fuel fluidized bed reactor is 2-4kpa participate. A high temperature heat carrier is filled with the gasification reaction agent.    USE - Biomass fuel fluidized bed reactor gasification method.    ADVANTAGE - The method enables achieving smooth internal rolling state of the fuel fluidized bed reactor to realize slow gasification reaction, improving gas production rate to reduce heat loss in a carbon yield, achieving small gasification reaction process quantity and simplifying circulation heating heat carrier supplementing stage to increase a system operation safety.
NOVELTY - Preparation of Salvia granule involves crushing 1000 g Salvia, placing in percolation tank, adding 4000-5000 mL 40-70% ethanol, soaking at 10-30 degrees C for 20-40 hours, collecting leachate, filtering at 45-55 degrees C, recovering ethanol, drying leachate to obtain paste, adding sucrose powder and citric acid, mixing, granulating, drying at 85-95 degrees C.    USE - Method for preparing Salvia granule.    ADVANTAGE - The method has high stability and high accuracy. It ensures high quality Saliva.
NOVELTY - Preparation of varenicline intermediate (III) comprises adding trifluoromethanesulfonic acid into reaction flask, stirring, adding concentrated nitric acid solution, and reacting with 2,3,4,5-tetrahydro-1,5-methano-1H-3-benzazepine derivative (II) at room temperature for 5-8 hours.    USE - Method for preparing varenicline intermediate (claimed).    ADVANTAGE - The method is environment-friendly, avoids column chromatography operation, and improves yield and purity of product.    DETAILED DESCRIPTION - Preparation of varenicline intermediate of formula (III) comprises adding trifluoromethanesulfonic acid into reaction flask, stirring, adding concentrated nitric acid solution, and reacting with 2,3,4,5-tetrahydro-1,5-methano-1H-3-benzazepine derivative of formula (II) at room temperature for 5-8 hours.
NOVELTY - Preparing insecticidal acetofenate comprises (i) mixing organic solvent and insecticidal acetofenate wet product, distilling and dehydrating, (ii) spray heating or through film evaporator heating distillation dehydration, carrying out dehydration process and wet smashing, modulating, carrying out packaging process continuous operation, and (iii) complexing mancozeb and zinc, dehydrating and carrying out crystal transformation process in organic solvent.    USE - The method is useful for preparing insecticidal acetofenate (claimed).    ADVANTAGE - The method reduces harmful impurities and dust pollution, and avoids the occurrence of product drying process fire accident.
NOVELTY - Method for regenerating activated carbon involves (a) degrading organic matter of activated carbon by adsorption using microorganisms, (b) drying the activated carbon using microwave, and (c) cooling the dried activated carbon and storing the cooled activated carbon.    USE - The method is useful for regenerating activated carbon using the apparatus (all claimed).    ADVANTAGE - The method conserves energy, does not cause pollution, and improves activated carbon production efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for activated carbon regeneration apparatus which has microwave oven including furnace, stove legs, microwave generating unit and vacuum pump. The furnace is rectangular hollow structure having cavity height of 500 mm, depth of 1000 mm, and is made up of stainless steel (304). The furnace legs are mounted under the furnace for supporting the furnace. The microwave generating unit is mounted on the top of the furnace, where the power of each microwave generator is 1000 Wt.% The vacuum pump is mounted on the side wall of the furnace.
NOVELTY - Method for recycling household landfill leachate, involves (a) pumping leachate decomposed by anaerobic bioreactor or landfill leachate into methane-producing phase into first-stage ultrafiltration membrane and subjecting the obtained product to membrane separation to obtain primary concentrated liquor, (b) pumping primary concentrated liquor into second-stage ultrafiltration membrane, and (c) passing the second-stage concentrated liquor into submerged combustion evaporation system and performing concentration and purification of the obtained liquor.    USE - The method is useful for recycling household landfill leachate which is useful for preparing organic liquid fertilizer.    DETAILED DESCRIPTION - Method for recycling household landfill leachate, involves (a) pumping leachate decomposed by anaerobic bioreactor or landfill leachate entering into methane-producing phase into first-stage ultrafiltration membrane, where the decomposition is performed at operation pressure difference of 0.3-0.5 MPa and subjecting the obtained product to membrane separation to obtain primary concentrated liquor, (b) pumping the primary concentrated liquor into second-stage ultrafiltration membrane to obtain second-stage concentrated liquor, where the ultrafiltration is performed at 1-1.5 MPa, and (c) passing the second-stage concentrated liquor into submerged combustion evaporation system and performing concentration and purification at greater than or equal to 75- degrees C in combustion evaporation system, where the combustion evaporation system has depth of 0.3-0.6 m.
NOVELTY - Benzylamino cyclohexyl acetic acid (I) and octahydropentalene compound (II) are subjected to coupling reaction in presence of peptide coupling agent under preset temperature to obtain cyclohexylpentalene intermediate (III). The cyclohexylpentalene intermediate (III) is hydrolyzed in presence of solvent to obtain telaprevir intermediate (1R,3aS,6aS)-2-((S)-2-((S)-2-cyclohexyl-2-((pyrazine-2-carbonyl)-amino)-acetylamino)-3,3-dimethyl-butyryl)-octahydro-pentalene-1-carboxylic acid (IV).    USE - Preparation of telaprevir intermediate (claimed).    ADVANTAGE - The method provides telaprevir intermediate by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Benzylamino cyclohexyl acetic acid of formula (I) and octahydropentalene compound of formula (II) are subjected to coupling reaction in presence of peptide coupling agent under preset temperature to obtain cyclohexylpentalene intermediate of formula (III). The cyclohexylpentalene intermediate (III) is hydrolyzed in presence of solvent to obtain telaprevir intermediate of formula (IV).    R=1-8C alkyl, preferably methyl, ethyl, propyl, isopropyl or butyl.
NOVELTY - Method for controlling snails and slugs in flowers in greenhouse cultivation, involves enhancing greenhouse management, enhancing light, controlling water, changing ground layout into planting table layout, cleaning indoor environment for disinfection, performing soil or matrix treatment before field planting, and performing manual capture, and chemical control.    USE - The method is useful for controlling snails and slugs in flowers in greenhouse cultivation (claimed).    ADVANTAGE - The method is simple, cost-effective, and environmentally-friendly.
NOVELTY - The invention provides a method for automatically removing tar oil from a fixed-bed biomass gasification furnace. The lower section of the gasification furnace produces biomass gas, the upper section of the gasification furnace is provided with a gas channel, the space in the gas channel is cooled, and the temperature of the gas produced by the lower section of the gasification furnace is reduced when the gas passes through the gas channel from bottom to top, so that tar oil in the gas is separated out. According to the method, the production efficiency of the gas is not influenced, and no pollution is caused to an external environment and circulating water; one part of the heat produced by gas cooling is used for drying fuel on a drying layer in the furnace, so that little heat is taken away through cooling of the circulating water; during cooling of the gas, a great amount of tar oil is recycled and participates in gasification again, so that the energy utilization rate is greatly improved, and the saved heat is more than the lost heat caused by cooling; and furthermore, as the temperature of the gas is low, the requirement on an auxiliary machine, an instrument, pipelines and the like is greatly reduced, and thus the investment cost is saved.
NOVELTY - A Brevibacillus reuszeri (CGMCC No: 10254) which is a biodeammonianitrogen engineered bacteria, is new.    USE - The B.reuszeri is useful for removing high concentrations of ammonia and nitrogen from sewage chosen from domestic sewage, industrial waste water and landfill leachate (all claimed).    ADVANTAGE - The B.reuszeri has chemical oxygen demand (COD) removal efficiency of 97.22-99.72%, and ammonia and nitrogen removal efficiency of 97.88-99.84%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) construction method of B.reuszeri, which involves producing denitrifying bacteria genome for removing ammonia and nitrogen by (a) cloning ammonia monooxygenase gene using PCR and introducing into pSM6 recombinant vector to produce denitrifying specific sites in vector, (b) screening out ammonia monooxygenase gene expressed denitrifying bacteria using genetic engineering techniques, where expressed genetically engineered bacteria can handle high concentration of ammonia and nitrogen, and (c) amplifying genetically engineered bacteria using fermentation techniques; and (2) use of B.reuszeri for removing ammonia and nitrogen from sewage by using membrane reactor system, where membrane is a resin and concentration of ammonia and nitrogen in sewage is 2000-5000 mg/l.
NOVELTY - Domestic garbage nano hydroxide activator gasification machine and regeneration solid fuel production equipment belongs to garbage processing equipment technology field, especially relates to one plant domestic garbage nano hydroxide activator gasification machine and regeneration solid fuel production equipment. The utility model is new type provide one plant heat efficiency high, domestic garbage nano hydroxide activator gasification machine and regeneration solid fuel production device of energy saving and environment-friendly. The utility model is new type comprises box body, inside the main box body upper part structure set with bucket body, bucket body set with upper end feeding port, a bucket body with lower end set with outlet, bucket body below the inner box body set with sum in tank, gasification tank on set with heater, gasification tank upper end set with inlet, gasification tank upper part set with gas outlet, sum for box lower end set with slag outlet, sum in side the box body inner box set with pressure pump gasification, gasification of pump input end head place at middle part in gasification tank, under the bucket body end outlet and gasification tank upper end inlet through connection pipe connected.
NOVELTY - Preparation of chlorinated phthalic anhydride includes subjecting nitrophthalate to reduction reaction in the presence of catalyst, and high-pressure hydrogenating to obtain amino phthalate; diazotizing with sodium nitrite aqueous solution to obtain diazonium salt; chlorinating with chlorinating reagent to obtain crude chlorophthalic acid; and dehydrating, distilling, heating, and vacuum-dehydrating.    USE - Method for preparation of chlorinated phthalic anhydride (claimed) used for polyimide, pharmaceutical and dye industries.    ADVANTAGE - The method is simple, environment-friendly and suitable for industrial production, achieves high-purity product, and it has low cost and equipment requirement.    DETAILED DESCRIPTION - Preparation of chlorinated phthalic anhydride comprises:    (A) subjecting nitrophthalate to reduction reaction in the presence of 0.08-0.8 mol.% catalyst, and high-pressure hydrogenating to 60-100 degrees C for 3-15 hours to obtain amino phthalate;    (B) diazotizing with sodium nitrite aqueous solution at below 5 degrees C for 0.5-3 hours to obtain diazonium salt;    (C) chlorinating with chlorinating reagent at below 5 degrees C for 0.5-6 hours to obtain crude chlorophthalic acid; and    (D) dehydrating, distilling to carry out purification, heating to 120-260 degrees C, and vacuum-dehydrating.    The molar ratio of water, nitrophthalate and catalyst is 100:10-100:40.
NOVELTY - Rhodococcus erythropolis (CGMCC NO. 10253) i.e. Nirs gene expressing recombinant nitrobacteria, is new.    USE - The Rhodococcus erythropolis is useful for removing ammonia nitrogen in sewage including domestic sewage, industrial wastewater and landfill leachate (all claimed).    ADVANTAGE - The strain: has ammonia nitrogen removal rate of 99.8-99.99%; chemical oxygen demand removal rate of 95-98%; and total nitrogen removal rate of 99.7-99.9% (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (i) constructing Rhodococcus erythropolis; and (ii) use of Rhodococcus erythropolis in removing ammonia nitrogen in sewage, comprising adopting a membrane bioreactor system, where the membrane bioreactor system is a flow aerobic membrane bioreactor system, whose film is made of resin.
NOVELTY - The production method of pentane involves performing hydrogenation reaction of eicosapentaenoic acid and hydrogen in a fixed bed reactor containing hydrogenation catalyst bed at liquid hourly space velocity of 1-5 hour-1, pressure of 1-4 MPa and temperature of 20-100 degrees C, reusing partially hydrogenated product as solvent for reaction and passing hydrogenated product through fixed bed of strongly acidic cation exchange resin to remove residual unsaturated hydrocarbon.    USE - The method is useful for producing pentane (claimed).    ADVANTAGE - The method enables simple and economical preparation of pentane with low energy consumption.    DETAILED DESCRIPTION - The production method of pentane involves performing hydrogenation reaction of eicosapentaenoic acid and hydrogen in a fixed bed reactor containing hydrogenation catalyst bed at liquid hourly space velocity of 1-5 hour-1, pressure of 1-4 MPa and temperature of 20-100 degrees C, reusing partially hydrogenated product as solvent for reaction, and passing hydrogenated product through a fixed bed of strongly acidic cation exchange resin to remove residual unsaturated hydrocarbon at temperature of 10-40 degrees C, liquid hourly space velocity of 1-5 hour-1 and pressure of 0.1-8 MPa. The molar ratio of hydrogen and eicosapentaenoic acid is 2-5:1. The catalyst contains 10-50 wt.% nickel and diatomaceous earth. The weight ratio of eicosapentaenoic acid and solvent is 1:6-10.
NOVELTY - Solid-liquid phase transfer catalytic synthesis of benzyl salicylate comprises adding salicylate, benzyl chloride, catalyst A and catalyst B into the reaction vessel, reacting at 80-200 degrees C for 2-20 hours, adding water into the reaction liquid, stratifying, separating the organic layer, washing the organic layer, dehydrating and distilling under reduced pressure, collecting the fraction at 164-165 degrees C,725-735 Pa, to obtain the products.    USE - The method is useful for solid-liquid phase transfer catalytic synthesis of benzyl salicylate (claimed).    ADVANTAGE - The method is simple, consumes low energy, causes little pollute, and produces high yield and good quality product.    DETAILED DESCRIPTION - Solid-liquid phase transfer catalytic synthesis of benzyl salicylate comprises adding salicylate, benzyl chloride, catalyst A and catalyst B into the reaction vessel, reacting at 80-200 degrees C for 2-20 hours, adding water into the reaction liquid, stratifying, separating the organic layer, washing the organic layer, dehydrating and distilling under reduced pressure, collecting the fraction at 164-165 degrees C,725-735 Pa, to obtain the products; where the catalyst A is crown ethers, crown ether derivatives and/or PEG200-6000; the catalyst B is an alkali metal halide salt; the molar ratio of salicylate salt and benzyl chloride is 0.9-2: 1; the molar ratio of catalyst A and benzyl chloride is 10:100; and the molar ratio of catalyst B with benzyl chloride is 10:1000.
NOVELTY - Production of ethanolamine comprises pumping ethylene oxide feed (1) and liquid ammonia feed (2) to tubular adiabatic fixed bed reactor and transferring to adiabatic fixed bed reactor with both reactors filled with binder-free ZSM-5 zeolite.    USE - Method for producing ethanolamine.    ADVANTAGE - The method has high safety, and has low equipment investment and energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of ethanolamine production.    Ethylene oxide feed (1)    Ammonia feed (2)    Preheated liquid ammonia (6)    Tubular adiabatic fixed bed reactor discharge (8)    Adiabatic fixed bed reactor discharge (9)
NOVELTY - Synthesis of levalbuterol comprises taking acetophenone derivative (i) and 1,1-dimethylethylamine or N-benzyl-tert-butylamine as organic amine, performing Hoffman alkylation to obtain 2-methylamino-1-phenyl-ethanone derivative (ii), performing reduction to obtain 2-methylamino-1-phenylethanol derivative (iii), adding (+)-dibenzoyl-D-tartaric acid, L-(+)-tartaric acid or (+)-di-o-4-toluoyl-D-tartaric acid as optically pure organic acid, reacting to obtain 2,2-dimethyl-1,3-dioxane derivative (iv) and reacting with hydrochloric acid.    USE - Method for synthesizing levalbuterol.    ADVANTAGE - The method is simple, environment-friendly and has short synthetic route.    DETAILED DESCRIPTION - Synthesis of levalbuterol comprises taking acetophenone derivative of formula (i) and 1,1-dimethylethylamine or N-benzyl-tert-butylamine as organic amine, performing Hoffman alkylation to obtain 2-methylamino-1-phenyl-ethanone derivative of formula (ii), performing reduction to obtain 2-methylamino-1-phenylethanol derivative of formula (iii), adding (+)-dibenzoyl-D-tartaric acid, L-(+)-tartaric acid or (+)-di-o-4-toluoyl-D-tartaric acid as optically pure organic acid, reacting to obtain 2,2-dimethyl-1,3-dioxane derivative of formula (iv) and reacting with hydrochloric acid.    X=Br or Cl.
NOVELTY - Synthesizing tolfenamic acid comprises adding the chlorobenzoic acid and an alkali metal hydroxide into the methyl isobutyl ketone, and heating for reaction; adding the reaction mixture to 3-chloro-2-methylaniline, adding inorganic base acid-binding agent loaded by alumina into reaction mixed liquid, and heating up for the reaction; cooling, adding water for extraction, separating liquid, acidifying the aqueous phase with hydrochloric acid, crystallizing, filtering, where the filter cake is the crude product of tolfenamic acid, and recrystallizing to obtain refined tolfenamic product.    USE - Method for synthesizing tolfenamic acid (claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - Aranidipine is prepared by adding propiolic alcohol and ethanediol and reacting to obtain 2,2-ethylenedioxypropanol; adding 2,2-ethylenedioxypropanol and diketene and carrying out ring opening reaction in acetic acid to obtain 2,2-ethylenedioxy propyl ester; subjecting 2,2-ethylenedioxy propyl ester to ammoniation reaction to obtain 3-amino-2-butenoic acid-2,2-ethylenedioxy propyl acetate; and subjecting 3-amino-2-butenoic acid-2,2-ethylenedioxy propyl acetate and 2-(2-nitrobenzylidene)-3-oxo-butyric acid methyl ester to condensation reaction, and hydrolyzing to obtain aranidipine.    USE - Method of preparing aranidipine (claimed).    ADVANTAGE - The method has high yield and no purification process of intermediate product and is green and environment-friendly. It utilizes NiCl2 and ethylenediamine to speed up the entire reaction.
NOVELTY - A 4-(4-(((4-chloro-3-(trifluoromethyl)phenyl)carbamoyl)amino)-3-fluorophenoxy)-N-methylpyridine-2-carboxamide compound (I) or its hydrate is prepared by reacting 4-(4-amino-3-fluorophenoxy)pyridine-2-carboxamide compound (II) with 4-chloro-3-trifluoromethyl-phenyl isocyanate compound (IV).    USE - Method of preparing 4-(4-(((4-chloro-3-(trifluoromethyl)phenyl)carbamoyl)amino)-3-fluorophenoxy)-N-methylpyridine-2-carboxamide compound (claimed).    ADVANTAGE - The method has simple operation and low residue, and is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparation of 4-(4-(((4-chloro-3-(trifluoromethyl)phenyl)carbamoyl)amino)-3-fluorophenoxy)-N-methylpyridine-2-carboxamide compound of formula (I) or its hydrate comprises reacting 4-(4-amino-3-fluorophenoxy)pyridine-2-carboxamide compound of formula (II) with 4-chloro-3-trifluoromethyl-phenyl isocyanate compound of formula (IV) to obtain compound (I), carrying out acid treatment to prepare salt of compound (I), washing salt with purified water, and adding mixture of organic solvent and purified water, and crystallizing to prepare hydrate of compound (I).
NOVELTY - A levamisole hydrochloride is prepared by taking L-tetramisole, dissolving in acetone, adding sodium selenate and activated charcoal, mixing, filter, stirring under hydrogen chloride gas, drying until pH is 3-5, and purifying.    USE - Method for preparing levamisole hydrochloride (claimed).    ADVANTAGE - The method has high product yield, is environment-friendly and suitable for industrialization.
NOVELTY - The utility model is new type supply have A A low carbon alcohol synthesis system. The low carbon alcohol synthesis system comprises orderly connected the feed gas processing module, an air outlet group and low carbon alcohol synthesis module and production process module, process module comprises feed gas feed gas compressor group and feed gas heating unit, feed gas compressor connected to feed gas heating unit and air inlet; the air outlet and air inlet feed gas heating unit is low carbon alcohol synthesis module comprises low carbon alcohol synthesizer, low carbon alcohol synthesizer is connected, product process module comprises low carbon alcohol separation part, low carbon alcohol separation part comprises low carbon alcohol separator, low carbon alcohol separator comprising low carbon alcohol separator inlet, low carbon alcohol separator inlet connected to low carbon alcohol synthesizer of air outlet, low carbon alcohol separation part comprises outlet of drainage used for low carbon alcohol product. The utility model is new type of technology scheme implementation have coal-based gas mixture efficient conversion is low carbon alcohol product of goal, and finish have clean using coal resource of goal.
NOVELTY - Producing solid fuel using food waste, comprises screening plastic, plastic goods and bones from the collected food waste, milling or crushing the food waste by a roller in porridge shape, adding effective microorganisms solution and vinegar into the food waste, crushing waste timber, mixing the waste timber particles with sawdust, pouring the mixture with the food waste into a mold, molding the mixture to obtain solid fuels, and paper strips banding an outer surface of the solid fuel.    USE - The method is useful for producing solid fuel using food waste (claimed).    ADVANTAGE - The method shortens processing time.    DETAILED DESCRIPTION - Producing solid fuel using food waste, comprises screening plastic, plastic goods and bones from the collected food waste, milling or crushing the food waste by a roller in porridge shape, adding effective microorganisms solution and vinegar into the food waste, crushing waste timber into small particles size of less than or equal to 2 mm, mixing the waste timber particles with sawdust in weight ratio of 4:6, pouring the mixture having moisture content of 80% with the food waste into a mold, molding the mixture at pressure of 200-500 T until moisture contents of more than 15% to obtain solid fuels having diameter of 15 cm, height of 14 cm and pore diameter of 25-32 mm, and paper strips banding an outer surface of the solid fuel.
NOVELTY - The utility model provides a combined natural gas purification plant low concentration acid gas processing device, comprising solid phase direct oxidation reaction and liquid phase oxidation reaction, the solid-phase direct oxidation reaction and liquid phase oxidation reaction in series connection, the solid-phase direct oxidation reaction and second level condensing separator and the liquid sulfur and tail condenser sum in each oxidation reaction phase connection. Solves have natural gas purification process low concentration acid gas treatment plant sulfur recovery rate and low operation cost and high problem, total sulfur recovery rate reach 99.9%, full using novel oxidation catalyst selectivity, increase sulfur recovery rate, high quality sulphur recovery, low sulfur containing acid sum by liquid phase oxidation process the discharge sum standard reducing running cost.
NOVELTY - A solid with solid reactant comprises 1st portion extending along 1st segment of dimension of solid and having 1st solid reactant concentration and 2nd portion extending along 2nd segment of dimension of solid and having 2nd solid reactant concentration in which 1st and 2nd solid reactant concentrations provide concentration gradient along axis of solid.    USE - Solid with solid reactant for hydrogen generator used for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen generator employing solid and liquid reactants.    Removable hydrogen generator (14)    Liquid outlet connection (18)    Reaction area (52)    Liquid delivery component (64)    Effluent entryway (86)
NOVELTY - Preparing organic fertilizer involves squeezing citrus fruits, where squeezed material is stirred with microbial bed material, thermophilic bacteria, additive material, sawdust, rice bran and broad leaved tree. The obtained mixture is heated in microwave. The obtained material is fermented aerobically to obtain product.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that is suitable for acidic soil.
NOVELTY - The method (10) involves mixing a hydrocarbon feedstock with a catalyst (30), where the hydrocarbon feedstock reacting in presence of the catalyst forms hydrocarbon products. Oxygenated hydrocarbon products and hydrocarbon products are recovered, where solid particles of biomass feedstock are injected into riser reactor zone at a point upstream when the hydrocarbon feedstock is introduced and at downstream of the point when the catalyst is introduced or at a point downstream when the hydrocarbon feedstock and the catalyst are introduced. The catalyst is a zeolitic catalyst.    USE - Fluid catalytic cracking method for co-processing a hydrocarbon feedstock and a renewable biomass feedstock.    ADVANTAGE - The method enables improving moisture content when the products have low solubility in water, thus separating the moisture content from the water in an easy manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a riser reactor zone.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a fluid catalytic cracking process.    Fluid catalytic cracking method (10)    Catalyst (30)    Biomass inlet (35)    Stripper (68)    Catalyst regenerator (70)
NOVELTY - Antiperspirant aerosol composition comprises: (a) 1-25 wt.% antiperspirant active particulates; (b) a propellant; (c) 15-40 wt.% or 5 wt.% silicone component, where the silicone component comprises non-volatile silicones; and (d) an active release agent comprising an aliphatic polyhydric alcohol having 2-12 carbon atoms. The antiperspirant active particulates are the only solid particulates in the antiperspirant aerosol composition.    USE - The antiperspirant aerosol composition is useful for controlling underarm wetness.    ADVANTAGE - The particulate actives enhance dry feel and efficacy on skin.
NOVELTY - A hydrogen producing apparatus comprises hydrogen producing container (20) which accommodates hydrogenated metal (5) which produces hydrogen gas (9) by reacting with water and is equipped with water tank (10) which supplies water and introduces gas (3a) of hydrogen or oxygen (3) into water (1) accommodated in water tank, unit (12, 14) to deaerate dissolved inert gas in water, and feed water line (21) which supplies water (7) subjected to deaeration process to hydrogen producing container. The apparatus supplies hydrogen gas to fuel cell.    USE - A hydrogen producing apparatus for fuel cell (claimed).    ADVANTAGE - Concentration of inert gas of emitted hydrogen gas can be reduced, therefore preventing voltage drop of fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen producing apparatus for fuel cells. (Drawing includes non-English language text).    Water (1)    Oxygen or hydrogen (3)    Gas (3a)    Hydrogenated metal (5)    Water subjected to deaeration process (7)    Hydrogen gas (9)    Water tank (10)    Unit (12, 14)    Hydrogen producing container (20)    Feed water line (21)
NOVELTY - The cell has a cathode-side diffusion layer (2b) arranged with a movable frame in a stacking direction. A resilient sealing element (4) is arranged between an anode-side separator plate (1a) and an edge area of a proton-leading layer (3), which is pressed by the sealing element against the edge area such that the proton-leading layer encloses a space for an anode-side diffusion layer (2a). The proton-leading layer is attached with the frame such that thickness of the frame and the sealing element are defined by the frame in the diffusion layers along stacking direction.    USE - Fuel cell for generating electrical energy in a fuel cell stack (claimed).    ADVANTAGE - The proton-leading layer is attached with the frame such that thickness of the frame and the sealing element are defined by the frame in the diffusion layers along stacking direction, thus manufacturing the cell in a simple and efficient manner with high precision and ensuring reliable operability of the fuel cell stack.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a fuel cell stack.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a fuel cell.    Anode-side separator plate (1a)    Anode-side diffusion layer (2a)    Cathode-side diffusion layer (2b)    Proton-leading layer (3)    Resilient sealing element (4)
NOVELTY - Production of organomineral waste-based vermicompost comprises uniformly mixing 25 wt.% buckwheat husks, 50 wt.% beet pulp and 25 wt.% aluminum salt slag, and moistening to prepare substrate; placing substrate in container with height of 1.2-1.5 m and keeping for 15-20 days; and adding worms at 1000 pieces/1 m2, moistening substrate to 70%, and composting for 4-4.5 months.    USE - Method for producing organomineral waste-based vermicompost (claimed).
NOVELTY - The apparatus (100) has a combustor (4) which heats a modifier (1). A temperature detector (7) detects the temperature of the modifier. A composition determination device (20) determines the composition of the raw material. A controller switches the operation mode and performs the operation control based on the signal from the composition determination device. The composition determination device determines the composition of the raw material after passing for predetermined period from the predetermined operation point.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - Since the composition determination device determines the composition of the raw material after passing for predetermined period from the predetermined operation point, the hydrogen generating apparatus responds appropriately with respect to the composition change of the raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Combustor (4)    Temperature detector (7)    Composition determination device (20)    Hydrogen generating apparatus (100)
NOVELTY - A hydrogen generating apparatus (100) comprises 1st modification-catalyst layer (1) and 2nd modification-catalyst layer (2) which modify raw material, temperature rising layer (3) which heats up gas which flows out of 1st modification-catalyst layer, and heater (4) which heats temperature rising layer in which 2nd modification-catalyst layer is arranged in downstream of temperature rising layer.    USE - A hydrogen generating apparatus used for fuel cell system (claimed).    ADVANTAGE - Size and cost are reduced. Amount of modification catalyst of the apparatus is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system comprising hydrogen generating apparatus (100) and fuel cell electric-power-generated using hydrogen-containing-gas supplied from hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the structure of hydrogen generating apparatus. (Drawing includes non-English language text).    1st modification-catalyst layer (1)    2nd modification-catalyst layer (2)    Temperature rising layer (3)    Heater (4)    Hydrogen generating apparatus (100)
NOVELTY - Manufacture of activated fulvic acid involves adding humin to fulvic acid-containing aqueous solution, and adjusting the oxidation-reduction potential of the mixture to 0 mV or less.    USE - Manufacture of activated fulvic acid used as fertilizer for agriculture, fisheries or water purification, purification of contaminated soil, and deodorizing.    ADVANTAGE - The method enables economical and efficient manufacture of activated fulvic acid with high purity, and reduced ingesting specific metal, high growth promotion effect of agricultural products, disease generation inhibitory effect, health enhancement effect, direct or indirect bioactivity effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for activated fulvic acid-containing aqueous solution.
NOVELTY - A fuel cell (100) comprises anode (102) including catalyst which oxidizes hydrogen in fuel, cathode (103) including catalyst which reduces oxygen in the gas, and proton conductor (101) which is arranged between anode and cathode and has perovskite type crystal structure.    USE - A fuel cell for generating electric power in household and industry.    ADVANTAGE - Fuel cell is more practical.    DETAILED DESCRIPTION - A fuel cell (100) comprises anode (102) including catalyst which oxidizes hydrogen in fuel, cathode (103) including catalyst which reduces oxygen in the gas, and proton conductor (101) which is arranged between anode and cathode and has perovskite type crystal structure of formula AaB1-xB'xO3-(delta).    A=alkaline-earth metal;    B=tetravalent transition metal or cerium;    B'=trivalent group 3 or group 13 element;    a=0.4-0.9; and    x=0.2-0.6.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.    Fuel cell (100)    Proton conductor (101)    Anode (102)    Cathode (103)    External load (104)
NOVELTY - A fuel cell (100) comprises anode (102) including catalyst which oxidizes hydrogen in fuel, cathode (103) including catalyst which reduces oxygen in gas, and proton conductor (101) which is arranged between anode and cathode and has perovskite type crystal structure. Electric charge of formula has shifted from - 0.13-0.14.    USE - A fuel cell for generating electric power in household or industry.    ADVANTAGE - Fuel cell is more practical.    DETAILED DESCRIPTION - A fuel cell (100) comprises anode (102) including catalyst which oxidizes hydrogen in fuel, cathode (103) including catalyst which reduces oxygen in gas, and proton conductor (101) which is arranged between anode and cathode and has perovskite type crystal structure of formula AaB1-xB'xO3-(delta). Electric charge of formula has shifted from - 0.13-0.14.    A=group 2 element;    B=Ce and group 4 element;    B'=group 3 element, group 12 element or lanthanoids;    a=0.5-1;    x=0-0.5; and    delta=0-3.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell.    Fuel cell (100)    Proton conductor (101)    Anode (102)    Cathode (103)    External load (104)
NOVELTY - Glycerol metabolism promotion method involves culturing Paenibacillus macerans strain NS-1 (2) (FERM P-22124) and applying reduction potential to electrode (9) which is in contact with culture solution (4) containing quinone (5) and glycerol (3).    USE - Glycerol metabolism promotion method for ethanol production (claimed).    ADVANTAGE - Glycerol metabolism can be promoted, simplification of culture system can be achieved, cost of culture system can be reduced, and productivity of ethanol can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for ethanol production which involves performing glycerol metabolism promotion method and recovering ethanol (7) from culture solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the glycerol metabolism promotion method. (Drawing includes non-English language text).    NS-1 strain (2)    Glycerol (3)    Culture solution (4)    Quinone (5)    Ethanol (7)    Electrode (9)
NOVELTY - The refrigerant circulation system has a condensation system which recovers cold from LNG (20) supplied from an LNG tank and uses the cold to cool refrigerant to below the evaporation temperature of an evaporator (25) and liquefy the refrigerant. The refrigerant may be indirectly cooled using brine which recovers the cold from LNG.    USE - Refrigerant circulation system for ship air conditioner, such as used in LNG or cargo transport ship or LNG-fueled ship.    ADVANTAGE - Refrigerant heating using steam is unnecessary, contributing to energy savings of the steam generator. Impact on global warming potential is low since carbon dioxide is used as natural refrigerant. Sensible heat increment of refrigerant liquid can increase refrigerant cooling effect and also avoid pump cavitation. Refrigerant or brine temperature control prevents coagulation of refrigerant or brine accompanying excessive cooling. The pressure control valve can be disposed upstream or downstream of the evaporator to increase degree of freedom in design. Evaporation pressure is controllable independently by the pressure control valve, simplifying adjustment of evaporation temperature, and ensuring predetermined cooling air temperature. Flow volume, pressure and temperature of refrigerant in the evaporator according to cooling load become settled, enabling exact adjustment of cooling air temperature and humidity. Ensures stable main engine drive by maintaining amount of LNG flow and gas temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of an air conditioning system with refrigerant directly recovering cold of LNG. (Drawing includes non-English language text).    LNG evaporator and heater (16)    LNG bypass valve (17)    After heater (18)    LNG (20)    Evaporator (25)
NOVELTY - The utility model is new type supply have one kind energy saving type compost, provided with one crushing component and one hot pump component, the crushing component with the one body, at least one hinge crushing knife, at least one turn stirring room and at least one turn stirring pole, the main body is hollow and provided with at least one internal enter port, the at least one enter port connected on upper surface of the main body, the at least one hinge crushing knife is rotatably and setting on the main body, the at least one stirring room forming in turn on the the body, bottom of the stirring room is formed with one discharging mouth, the at least one stirring pole rotatably setting in turn in turn the stirring room, the heat pump module set in crushing component outside side and set with one heater, one heat circulation tank and one hot water tank, the heater respectively connected the hot water tank and the heat circulation tank, the heat pump module is for heating the air and water, and to maintain the environmental temperature and humidity in the body by switching the hot air and hot water.
NOVELTY - The new type utility claims have one plant coal comprehensive using manganese slag compound fertilizer production system, including coal generating system and fertilizer production system, the coal generating system comprises two-section coal, tar collector, cyclone dust collector, cutter and urgency before furnace water seal tank, the compound fertilizer production system comprises combustion furnace draught fan, a combustion furnace, weigh burdening system, a mixer, pulverizer raw material, the compound fertilizer dryer, fertilizer cooling machine, cold air draught fan, a sieving machine, a coating machine and a metering package machine. The utility model is new type using manganese slag as raw material, by adding each kind nitrogen, P, potassium base fertilizer prepared compound fertilizer production, have not only solves discharge problem of the waste, but also full use resource waste as treasure. In addition, the utility model is new type using two-section coal gas as heat source device, increase have gas and gasification efficiency, and reducing have pollute environment.
NOVELTY - The utility model is new type relates to biomass gasification cogeneration of multi-technology field. The utility model is new type by charcoal and gasification furnace produced using indirect cooling method for cooling the biological fuel gas cooling process of gasification furnace and generate, using wood tar oil and condensed for collection, and biological fuel gas transport process for sum liquid separation, for separating out the oil coke carry out collecting the burner and condensing out a little wood tar and oil carry out collection, will separate from the biological fuel gas boiler for burning wood tar collecting and holding at temperature of 100 to 120 degrees C centigrade. The utility model is new type of advantage wherein the sum by wind through wind cooling pre-heating, increase have heat efficiency of biomass gasification furnace, produced charcoal is low water charcoal, charcoal water less than 15%, need not consume energy in addition to the drying process, large increase and have economic value produced the charcoal, the production because of wood tar with steam heater for heat preservation, keeping good fluidity is good.
NOVELTY - The utility model is new type relates to biological fuel gas supply system, especially claims a biological fuel gas boiler for the system device. Gasification furnace of the system device in mounted with matched gasification fan of corresponding type, gasification furnace through fuel gas pipe connected to the combustion device, the combustion device front set with tar collecting tank, fuel gas pipe holding one of downward incline angle, comprising connecting sum in one end position high furnace, burning device connected one end location low, after biological fuel gas through cooling device from gasification furnace from the temperature is lowered to 100 to 250 degrees C degrees centigrade and sending to biomass fuel gas burner special for processing. A liquid film layer water vapour and tar series biological fuel gas carry and in transport course of substance would form in the gas pipe wall, a fan scroll casing and impeller equal to the, the exist film make liquid transport pipe and transport equipment comprises bear corrosion and wear resistance, heat preservation and characteristics from the clean, for pipe, a fan, a combustion device of long-term and continuous, stable operation aspect has a greatly.
NOVELTY - The utility model claims a continue production marsh gas pool, belongs to technology field. Above include fermentation pool (1), a fermentation pool (1) one end side wall equipped with the feedstock mouth (2), fermentation pool (1) wherein another end side wall bottom is set with (3), fermentation pool (1) is set with the sum room (4), and fermentation pool (1) are formed and by discharging mouth (3) connected the water chamber (5) and is set in water chamber (5) biogas residue extraction device (6), extracting device (7) and stirring device (8), the residue extraction device (7) and stirring device (8) and lower end from the discharging mouth (3) to enter into the fermentation pool (1) lower part. The biogas pool structure is simple, suitable mounting, can be any feedstock, at any time, not affect gas discharging, which greatly increase have gas production efficiency, not use dedicated machine, not consume energy, environment protection and energy saving implementation have classify discharging, realize have circulation for discharging.
NOVELTY - The utility model claims a fuel gas generating set for preparing fuel gas by using domestic garbage, comprising transmission belt wheel group, smashing room and marsh gas pool, a conveying belt wheel group lower side enter connected with material funnel, material enter the following side connected with the crushing hopper, a crushing lower side connected with fermentation chamber, the fermentation chamber under side connected with a filter liquor pool, fermentation chamber bottom provided with a filter screen, the utility model is new type household garbage for fuel gas and combustion sum generation device can use domestic garbage is fermented marsh gas and a marsh gas power generation use, using smashing device for processing domestic garbage smashing, increase have effect and efficiency, filter screen and a fine filter network and domestic garbage fermentation can greatly reduce the filter pool entering into the garbage before in fermentation, when at the same time can reduce blockage condition of waste gate valve, reducing safety accident hidden danger of marsh gas pool, and using a gas turbine producing work and heat for effective use, increasing energy using efficiency and saving energy and protecting environment.
NOVELTY - Hydrogen generating apparatus (10) produces hydrogen-containing-gas using raw material. The hydrogen generating apparatus comprises hydrodesulfurization device (1) which removes the sulfur compound in raw material from the upstream so that temperature increases toward downstream.    USE - Hydrogen generating apparatus is used for fuel cell system (claimed).    ADVANTAGE - The compact and economical hydrogen generating apparatus is operated efficiently and easily.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell system; and    (2) operation method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrodesulfurization device (1)    Hydrogen generation portion (2)    Heater (4)    Hydrogen generating apparatus (10)
NOVELTY - The utility model is new type is A kind environment-friendly fuel economizer, the bottom water tank (4) bottom, the top and the bottom water tank (4) is connected with fluorin pipe (11), (11) position is equipped with the middle oxidization generator (9), oxidization generator (9) and constant flow power source back plate (8), a constant flow source power plate (8) side is equipped with the radiating fan (3), a cathode water box (2) and bottom layer water tank (4) by connector (13) connected with the connector (13) is set on constant flow electric source plate (8) and between electrochemical oxidation generator (9), a cathode water tank (2) on the top part is provided with the funnel (10) and air pump (12), anode water box (1) and outside is equipped with water level meter (14), of each component after mounting are fixed on mounting panel (7) above. The utility model is new type of it is: 1, add have speed ignition and combustion of hydrogen production of heat can, add have power. 2, active oxygen main component of ozone 25% and 75% oxygen, the combustion is more complete, increase the heat can have value after fuel combustion, and more clean in tail sum over discharge.
NOVELTY - The new type utility claims have one kind based on air conditioner system is methyl alcohol water hydrogen generation system, comprising methyl alcohol water hydrogen production by reforming device, fuel cell and thermoelectric mixed air conditioner device, methanol water hydrogen production by reforming device, methyl alcohol and water for generating hydrogen by reforming reaction, the reforming reaction prepared hydrogen and hydrogen transport give fuel cell, process reaction wherein reforming and preparing hydrogen, discharging the waste of the heat transport give sum-absorption refrigeration unit, fuel cell, hydrogen and oxygen for generating electrochemical reaction producing electric energy, the electric energy production is power type air conditioner unit with power supply, electric mixed air conditioner device, comprising absorption refrigeration unit and uses power type air conditioner unit, absorption refrigeration unit can absorb methanol water hydrogen production by reforming device discharging waste and sum of heat and then cooling, for power type air conditioner unit may consume fuel cell generating electric energy and then cooling. The utility model is new type environment-friendly, energy saving, convenient, and environment influence are small, methyl alcohol and water raw material energy use rate high.
NOVELTY - Organic production seedling matrix comprises 45-50 wt.% vermiculite, 30-35 wt.% peat, and 20-25 wt.% sheep manure.    USE - Organic production seedling matrix is useful for solanberry, melon and vegetable containing tomato, pepper and cucumber, reducing soil-borne diseases, promoting seedling growth, and improving seedling quality.    ADVANTAGE - The organic production seedling matrix has excellent disease resistance, and prolonged service life.
NOVELTY - The utility model is new type supply have one plant for production biological organic fertilizer and powder fungus bacteria adding device, the device comprises bacteria adding device and fungus material mixing device, the bacteria adding device comprises hopper, the upper part of the hopper with bacteria adding mouth, lower part of the hopper with out fungus wherein, in the hopper set with one end used for control the first kick-out device and amount of fungus, the first kick-out device comprises transverse pulling pole through out of the hopper lumen and fixed one group shifting teeth on the stirring stick on the, the shifting pole position is outside the hopper and the first rotary drive mechanism connected with the said fungus material mixing device comprises roller, the bacteria outlet mouth through bacteria adding pipe and the connected expansion cylinder, the expansion cylinder of the second rotary driving mechanism in driving movement, the utility model is new type using kick-out for bacillus subtilis dialing and fungus pipe, accuracy and can control bacillus subtilis and adding amount, adding the bacillus subtilis can and organic fertilizer in fungus material mixing device in full mixing, production quality high.
NOVELTY - The utility model is new type category in compost fermentation facility construction technology field, relating to one kind rural household garbage bin compost reaction device. It comprises, compost, gas exchanger, ventilating pipe, a cabin body is house shape cover top side of sealed square cabin structure, gas exchanger is air pipeline, waste gas pipeline and the controller is composed of a cross shape gas pipeline control device, ventilating pipe is a pipe laying formed by the square pipe side, the ventilating pipe is equipped with cabin body inner side bottom middle location, stacking for compost side and ventilating pipe on the seat bottom in cabin body, gas exchanger is equipped with right outside seat cabin and waste gas pipeline for through series cabin body inner wall form and cabin body upper part connected with the air pipeline lower end bent to form ventilating pipe outwards and connected with connecting head. The utility model is new type comprises following characteristics: facility construction is simple and with cost; from organic garbage organic fertilizer and become circle. waste gas recovery process can, avoid to pollute environment.
NOVELTY - The utility model is new type category rural agricultural compost production equipment manufacturing technology field, relating to one kind of cooling device for preparing compost process. It is of metal material manufacture, comprising tube, feedstock room, discharge room, for hopper, wind, to pump out, front baffle supporting wheel device, rear baffle supporting wheel device, transmission gear, driving system, stand, tube as left high right low in incline set, feedstock room is equipped with left end tube seat, a discharging room is set with tube right end position, for hopper is equipped with feedstock room on the left position, to pump member equipped with wind discharging room is on the middle position, come equipped with material discharging room at the right position as follows, two group divided height each one group bracket, high bracket is set with seat, low bracket as follows feedstock room set at position as follows the discharge room. The utility model is new type comprises following characteristics: cooling speed fast, production capacity is strong, can further reduce material water, increase particle strength, fit scale compost production use.
NOVELTY - The utility model is new type supply have one plant biological organic fertilizer production system, which comprises orderly connected with the raw material crushing machine, mixing stirring device, hoisting machine, machine, circular machine, dryer, a sieving machine and packing machine, the machine comprises machine frame, along the vertical direction orderly equipped with two end has rolling roller group, crushing roller group and screen, rolling roller group comprises rolling roller I and rolling roller II, crushing roller group and reverse rotating comprises crushing roller I and crushing roller II, a rolling roller I and crushing roller I is respectively through mounting frame I and machine frame fixedly connected on machine frame, two end rolling roller II and crushing roller II is mounted on mounting frame II respectively upper, lower end of two mounting bracket II formed with guide convex strip, machine frame set on and guide convex strip matched with the horizontal guide rail, upper machine frame mounted with motor, motor drive connected with lead screw, a lead screw through the U-shaped bracket, two end U-shaped bracket is respectively connected with two mounting frame II and fixed, production cost of the production system compared with the existing technology low.
NOVELTY - A methanol fuel additive comprises 100-150 parts mass dimethyl carbonate, 100-150 parts mass dimethoxyethane, 150-200 parts mass diphenyl dimethoxy silane, 50-80 parts mass cyclohexane, 50-80 parts mass isopropanol, 10-20 parts mass acid amide, 10-20 parts mass trans-fatty acid, 2-5 parts mass ammonium chloride, 2-5 parts mass sodium chloride, 8-10 parts mass ethyl tert-butyl ether, and 8-10 parts mass tert-amyl methyl ether.    USE - Methanol fuel additive (claimed).    ADVANTAGE - The methanol fuel additive has high calorific value, high heat efficiency, high latent heat of vaporization, high combustion efficiency and excellent corrosion resistance.
NOVELTY - A energy biomass pellets comprise 40-60 pts. wt. corn stover, 10-20 pts. wt. pine needles, 10-20 pts. wt. sawdust, 5-15 pts. wt. Populus tree branch extract, 10-15 pts. wt. willow tree branch extract, 5-15 pts. wt. cassia tree branch extract, 5-10 pts. wt. elm tree branch extract, 5-10 pts. wt. carbonaceous shale, and 10-20 pts. wt. chicken parts.    USE - Energy biomass pellets (claimed).    ADVANTAGE - The energy biomass pellets have high calorific value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of energy biomass pellets.
NOVELTY - A palm oil biodiesel is fractionated using a fractional distillation system by filling biodiesel (methyl ester) into boiling vessel, heating at medium heat until methyl ester reaches certain temperature and pressure to separate into desired fractions, and condensing fractionated fractions to obtain dominant palmate methyl esters.    USE - The drawing shows an image of a fractional distillation system.    ADVANTAGE - The method allows separation of methyl ester fraction of palmate as a potential dominant surfactant feedstock methyl ester sulfate which has high detergency and residual fraction of methyl ester fraction of oleate as a potential dominant biodiesel fuel that is resistant to cold temperature.    DESCRIPTION OF DRAWING(S) - The drawing shows an image of a fractional distillation system.
NOVELTY - A microbial compost shown in the following figures: (i) Figure 1 shows the Trichoderma sp. on Potato Dextrose Agar (PDA) culture medium, (ii) Figure 2 shows the Trichoderma sp. seen under the microscope at a magnification of 100X, (iii) Figure 3 shows the results of the isolation of microbial Actinomycetes compost, (iv) Figure 4 shows the results of the isolation of Pseudomonas sp. compost, and (v) Figure 5 shows the results of the isolation of Bacillus sp. compost.    USE - The microbial compost or organic compost extract is used as biopesticide or biofertilizer or is used for controlling rotting of cocoa plants caused by Phytophthora palmivora.    ADVANTAGE - The microbial compost or organic compost extract can be produced at low cost, can effectively control the bud-rot of cocoa plants, can be stored in a relatively long time, and can be transported and applied easily.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing organic waste compost extract formulations in the form of pellets by (a) arranging rice straw alternately with a starter of organic material (household waste) in 250-L container, (b) placing the straw and organic material inside a burlap sack, (c) filling the 250-L container with ground water until it covers the burlap sack, (d) treating the straw and organic material with sugar solution as a food source for microbes, (e) isolating the microbes from the container, (f) once the compost has matured, extracting the compost in a machine and mixing with a solution outside of the burlap sack, (g) making the pellets by adding green bean flour with 1:10 ratio between green bean and compost extract, and (h) adding sodium alginate.
NOVELTY - The flexible fuel cell comprises an anode having an anode end plate structure made of a polymer material and having a hydrogen flow channel formed in the node end plate structure. A current collector is provided with a conductive layer deposited on the structure. A cathode has a cathode end plate structure made of a polymer material and has an air flow channel. A membrane electrode assembly is provided with a polymer electrolyte membrane having a catalyst layer attached to the surface of the polymer electrolyte membrane.    USE - Flexible fuel cell for portable electronic devices.    ADVANTAGE - The flexible fuel cell is provided with excellent clamping force by using a material having high flexibility for the anode end plate and the cathode end plate, thus ensuring higher stability, durability, efficiency and excellent quality even under bent condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing a flexible fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a method for producing a flexible fuel cell.
NOVELTY - A A binding beer factory waste water treatment device, comprising: decontaminating, water storage tank, a sediment regulating pool, retention type Anaerobic reactor, liquid, gas storage tank, vertical flow precipitate pool, an aerobic reaction pool, air blower, biological absorbing, collected mud well, concentration pool, mud storage pool and dewatering. Said binding beer factory waste water processing device can effective reduce binding of beer factory waste water and the COD value and BOD value and TN value, besides, said binding beer factory waste water processing device and biogas storing tank formed by upper guide wheel and lower guide wheel, cover body and balance weight block not only can be marsh gas to realize automatic pressurizing removing wet operation, and also can ensure the safety, make better recovery using marsh gas.
NOVELTY - The new type utility claims have one kind aerobic compost device, including compost material cabin, an electric stirring machine and fine hole sieve pore sieve plate located on the stack in material chamber and fertilizer and the compost material cabin bottom between air inlet buffer layer composed of, compost material storehouse set discharging window, air inlet pipe, a drain pipe and discharge pipe, left part of fertilizer material storehouse with feeding bin is set with sealing cover, an electric stirring machine with six individual, wherein two individual electric mechanism arranged on left part of stack fertilizer material chamber close to the middle position, in addition of four electric mechanism arranged at right part of the fertilizer stack material cabin, a pore plate incline set on the compost material in cabin, lower end of fine sieve plate located on the stack right is fertilizer material chamber, a discharging window located on the stack right side face of fertilizer material chamber and lower end joint and the fine sieve plate. The utility model is new type stirring efficiency is high, the organic garbage for disposable processing amount large and full reaction, and after reaction can easily discharging material, which greatly increase and have treatment efficiency of organic garbage.
NOVELTY - The new type utility claims have one plant for organic waste aerobic fermentation roller, in the sum for the system including the fan air supply pipeline, the air supply pipeline divided air supply dry pipe and the gas supplying branched pipe, the air supply dry pipe and connected with fan, on the air supply dry tube formed with pipe adjusting valve, the gas supplying branch pipe from the air supply dry pipe are out, the upper gas supplying branch pipe install branch pipe with adjusting valve distributing device, said distributing device set with set data of fermentation process of fermented material in roller for monitoring oxygen in the aerobic fermentation roller at on end of the gas supplying branch pipe, monitoring device, the monitoring device, controller, the monitoring device set in the aerobic roller in the inside the two multi-section and at least one function of function section, the controller connected to the main pipe adjusting valve, a branch pipe adjusting valve, a gas distribution device and of the at least one of the fan.
NOVELTY - The new type utility claims have one kind aerobic compost device, comprising bottom base bracket, shell, a clapboard, a blower and water nozzel, said shell set up on the stand pedestal, on the clapboard set with multiple air holes, the clapboard of the shell for separating for compost chamber and gas distributing room, side wall of the air distribution room set up with air inlet, the fan set up in the air inlet, the water nozzel set at bottom of the compost chamber, upper end of the compost cabin side wall set with air outlet nozzle on bottom of the gas distribution room set with water discharging mouth. The utility model is new type aerobic compost device by using gas distribution room set in the compost cabin bottom, again by fan blowing air, realize adequate oxygen supply to the compost chamber, at the same time can be through water outlet and air hole and bottom of clapboard in time using a filter liquid generated by compost discharging.
NOVELTY - The utility model is a reaction system for producing a azoxystrobin pesticide intermediate 4, 6-dichloropyrimidine, composed of a feedstock, reaction, separation and catalyst recovery system; a reaction still is used as a reaction container, and at the same time as hydrolysis, water washing container, one multi-kettle using, no need to add the hydrolysis tank and water washing tank, device comprehensive using rate high, using system construction cost greatly reduce, 4, 6 production yield and high dichloropyrimidine is more than 96%, solvent, catalyst and water can repeat use, three-waste discharge small, production process pollute small, process is green.
NOVELTY - The utility model is new type relates to one plant biological diesel deacidification decolouring device, comprising the first adsorption column, the second adsorption column, third adsorption column, finished product tank and the raw material tank, the outlet of the raw material tank connected with the first adsorption column connected entrance, the first absorbing column outlet pipeline connected connected with finished product tank, one branch pipe 4 on the upper pipe, a branch pipe connected with the second adsorption column connected entrance, the second absorbing column outlet pipeline connected connected with another finished product tank, one branch pipe is provided in the upper pipe, a branch pipe connected with third absorbing column entrance connected, third absorbing column outlet pipeline connected connected with another finished product tank. The biological diesel oil processing after the application adsorption effect, in adsorption column adsorbent for biological diesel oil with a certain of decolouring effect, can desalting biological diesel oil colour, biological diesel oil increase stability, acid value reach to complete state standard GB/T20828-2007.
NOVELTY - The utility model is new type provide photoelectric catalytic decomposing hydrogen production reaction device, it comprises: reactor, a jacket and cover, the reactor and the jacket internal space, used for containing reaction solution, set with water inlet on bottom of the jacket, water outlet is set at the top part of the jacket, cap by screw thread and connected with sealing reactor, equipped with cover has two air outlet of the upper rotary cover also set with three individual electrode columns, respectively as work electrode, electrode and reference electrode providing bias voltage, provided with illumination window on side wall of reactor, to illumination window with light is set with sealing piece, through illumination window for semiconductor catalytic material can be applied to illumination, to realize light catalytic process, and through to the water inlet and water outlet of the jacket circulation water condensing can for reaction system provide keeping and regulating temperature. The utility model is new type construction is simple, the reactor volume is small, controllable temperature, suitable.
NOVELTY - The new type utility claims have one kind portable solar energy stove, comprising water storage tank and ignition device, then the water storage tank bottom is relative set with two of the whole plate, solar energy solar panels positive and negative respectively connected with two plate of the water storage tank and the water storage tank top form the vertical direction of air outlet pipe, an air outlet pipe connected ignition device. The utility model is new type with the advantages and positive effect is electric energy by solar energy and generating, electrolytic water producing hydrogen and oxygen, igniting for cooker.
NOVELTY - Preparing liquid and/or solid hydrocarbon compound containing carbon dioxide and methane, comprises desulfurizing gas mixture obtained by anaerobic fermentation of biomass, performing reformation stage including steam reformation and/or partial oxidation with water and/or air, supplying carbon dioxide, hydrogen and water vapor containing gaseous mixture of Fischer Tropsch synthesis, stripping synthesized liquid and/or solid hydrocarbon compound, where synthesized water vapor, carbon dioxide and gaseous hydrocarbon compounds and additional gases) air and/or water is subjected to reformation.    USE - The method is useful for preparing liquid and/or solid hydrocarbon compound containing carbon dioxide and methane (claimed).    ADVANTAGE - The method: is cost-effective; and utilizes natural resources.    DETAILED DESCRIPTION - Preparing liquid and/or solid hydrocarbon compound containing carbon dioxide and methane, comprises desulfurizing gas mixture obtained by anaerobic fermentation of biomass, performing reformation stage (2) including steam reformation and/or partial oxidation with water and/or air, supplying carbon dioxide, hydrogen and water vapor containing gaseous mixture of Fischer Tropsch synthesis, stripping the synthesized liquid and/or solid hydrocarbon compound, where the synthesized water vapor, carbon dioxide and gaseous hydrocarbon compounds and additional gases) air and/or water is subjected to the reformation stage, separating water vapor of short-chain hydrocarbon compounds with up to 4 carbon atoms (1-4C) and supplying to the stage (4) for complete oxidation.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the process flow for preparing liquid and/or solid hydrocarbon compound containing carbon dioxide and methane.    Reactor (1)    Reformation stage (2)    Stage 3 (3)    Stage 4 (4)    Heat exchanger (5)
NOVELTY - Biomass feedstock and an organic solvent are mixed, heated, in-situ hot-filtered, extracted, cooled and filtered, to obtain high-molecular-weight biomass extract. The resulting filtrate is distilled, to obtain low-molecular-weight biomass extract. Blended coal feedstock is added to high-molecular-weight biomass extract and low-molecular-weight biomass extract. The raw materials are mixed with coal and coke and adhesion of coal feed is improved, and strength of coke is increased.    USE - Extraction of biomass (claimed).    ADVANTAGE - The method provides coal and coke with excellent strength and reduced coking cost.    DETAILED DESCRIPTION - Biomass feedstock and an organic solvent in mass ratio of 1:10-1:15 are mixed, to obtain mixture. The mixture is heated at 250-350 degrees C and in-situ hot-filtered. The residue is extracted, to obtain liquid product. The liquid product is cooled to room temperature and filtered, to obtain filtered residue and filtrate. The filtered residue is high-molecular-weight biomass extract. The resulting filtrate is distilled under reduced pressure, to obtain low-molecular-weight biomass extract. 0.5-3 %mass Blended coal feedstock is added to high-molecular-weight biomass extract and low-molecular-weight biomass extract. The raw materials are mixed with coal and coke. and adhesion of coal feed is improved, and strength of coke is increased.
NOVELTY - Producing bio-coal from biomass material such as de-oiled palm fiber, palm oil empty fruit branch, palm kernel shell or other carbon containing botanical substances by using torrefaction reactor, comprises continuously carbonizing the biomass material by using direct heating and indirect heating simultaneously in the torrefaction reactor at 270-650 degrees C and heated nitrogen gas.    USE - The method is useful for producing bio-coal.
NOVELTY - The system (100) has a load that is connected to a fuel cell. A power supply to the load is adjusted by changing the predetermined width of an output current of fuel cell at the time of warming-up of the fuel cell. An IV estimation unit estimates the IV characteristic of a fuel cell based on two pairs of output current and voltage values detected while making change. An IV estimation stop unit is provided to stop implementation of IV estimation unit during implementation of IV estimation unit based on the output of fuel cell.    USE - System for supplying anode and cathode gases to fuel cell for generating electric-power.    ADVANTAGE - The current-voltage (IV) estimation unit estimates the IV characteristic of a fuel cell based on two pairs of output current and voltage values detected while making change and the IV estimation stop unit is provided to stop implementation of IV estimation unit during implementation of IV estimation unit based on the output of fuel cell. Thus, the worsening of power generation characteristic estimated by originating in changing the output current of fuel cell is avoided effectively while improving the fluctuating fixed quantity of output current by amplitude for estimated precision. Hence, the output current is not reduced from target electric current for warming-up to promote warming-up while suppressing the deterioration of warming-up performance by reducing the calculation load of controller.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for controlling fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell system. (Drawing includes non-English language text)    Cathode gas supply-discharge apparatus (2)    Anode gas supply-discharge apparatus (3)    Stack cooling device (4)    Electric power system (5)    System for supplying anode and cathode gases to fuel cell (100)
NOVELTY - A gas-separation composite film (10) has a gas-separation layer (3) formed using polyimide compound, on a gas-permeable support (1). The solubility of polyimide compound with respect to dimethylacetamide is 20 mg/100 g or less at 20 degrees C. The thickness of the gas-separation layer is 0.1-5 mu m.    USE - Gas-separation composite film is used in module for apparatus used in separation of gas e.g. carbon dioxide (all claimed).    ADVANTAGE - The gas-separation composite film has excellent carbon dioxide transmission rate, gas-separation selectivity and durability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of gas-separation composite film, which involves forming a film using polyimide compound (which is insolubilized when heated at 200 degrees C or more) or its precursor on heat-resistant base material and heat-processing at 200 degrees C or more, bonding a gas-permeable support on the formed film, and peeling the heat-resistant base material;    (2) gas-separation module, which comprises the gas-separation composite film;    (3) gas-separation apparatus, which is provided with the gas-separation module; and    (4) gas-separation method, which involves selectively transmitting carbon dioxide from gas containing carbon dioxide and methane using the gas-separation composite film.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gas-separation composite film.    Gas-permeable support (1)    Contact bonding layer (2)    Gas-separation layer (3)    Gas-separation composite film (10)
NOVELTY - Method for transforming a biomass, involves (a) subjecting the biomass to a treatment to increase its hydro lytic power, (b) simultaneously with or subsequently to step (a), exposing the biomass to an enzymatic activity that degrades polysaccharides in the biomass, preferably cellulose, hemicellulase, amylase, oxidoreductase and/or esterase, and (c) simultaneously with or subsequently to step (b), exposing the biomass to a Deinococcus or its extract.    USE - The method is useful for transforming a biomass which is used for producing an alcohol and product of interest from a lignocellulosic biomass (all claimed). The product is biofuel, isoprenoid or organic acid.    ADVANTAGE - The method is suitable for generation of valuable products under industrially-effective conditions.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing an alcohol; and    (2) method for producing a product of interest from a lignocellulosic biomass.
NOVELTY - Preparing triglycidyl isocyanurate (I) comprises reacting cyanuric acid (III) with 3-7 molar equivalents of epichlorohydrin using a phase transfer catalyst in an autoclave at 80-100 degrees C for 1 hour to obtain a reaction mixture, and extracting the reaction mixture with a chlorinated solvent and adding an alkali lot wise to the chlorinated solvent at 10-15 degrees C to obtain (I).    USE - The process is useful for preparing triglycidyl isocyanurate (claimed) which is useful: in the synthesis of metaxalone that is a muscle relaxant; and as a crosslinker in the manufacture of laminated sheets, printed circuits, electrical insulations, inks, adhesives and lining materials.    ADVANTAGE - The process: provides (I) in cost effective manner; avoids the contact with toxic vapors of epichlorohydrin, thus rendering the process safe and environment friendly; and reduces the chances of explosion and fire, thus rendering the process industrially viable.    DETAILED DESCRIPTION - Preparing triglycidyl isocyanurate of formula (I) comprises reacting cyanuric acid of formula (III) with 3-7 molar equivalents of epichlorohydrin using a phase transfer catalyst in an autoclave at 80-100 degrees C for 1 hour to obtain a reaction mixture, and extracting the reaction mixture with a chlorinated solvent and adding an alkali lot wise to the chlorinated solvent at 10-15 degrees C to obtain (I).
NOVELTY - The cell (118) has an anode electrode (206), a cathode electrode (207) and a reference electrode electronically connected to each other and to an external electric current. A first microbial biocatalyst is located in an anode chamber (204) and has a fermentative organism for fermenting biomass to produce a fermentation product. A second microbial biocatalyst located in the anode chamber and has an electricigen for transferring electrons present in fermentation products to the anode electrode to produce hydrogen at the cathode.    USE - Microbial electrolysis cell for producing electricity and bioproducts.    ADVANTAGE - Performance of the microbial electrolysis cell is improved by enhancing the capacity of the anode biofilms to remove electron donors such as acetate to prevent feedback inhibition and shifts in the fermentative metabolism away from ethanol production. Adding components simultaneously minimizes disruptions to the bioprocessing reaction and reduces costs associated with the set-up of the bioreactor. Production of ethanol from glycerol wastewater eliminates the need to dispose of the glycerin wastewater for a fee, reduce costs and carbon emissions associated with the use of petrochemical methanol, and increases biodiesel productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method of using a microbial electrolysis cell; and    (2) a bioelectrochemical system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a microbial fuel cell.    Cell (118)    Anode chamber (204)    Cathode chamber (205)    Anode electrode (206)    Cathode electrode (207)
NOVELTY - Producing organic waste e.g. biomass and waste water, for further processing, preferably for a gasification, comprises (a) introducing organic wastes into an anaerobic fermenter, and adding an inoculum, and (b) supplying carbon dioxide obtained in the fermenter and optionally methane to a gas reformer to convert into methane gas.    USE - The method is useful for producing organic waste e.g. biomass and waste water, for further processing, preferably for a gasification (claimed).    ADVANTAGE - The method produces biogas containing 90% methane.
NOVELTY - The utility model is new type relates to one plant domestic garbage rotten efficient device, belonging to environment protection technology field and solves the have the technology of household garbage processing complex technique, high cost and problem. The efficient household garbage composting device comprises smashing mechanism, hopper, clinker cylinder, a smashing machine for domestic garbage after carrying out pre-processing enter into hopper, the domestic garbage after hopper by one transport mechanism for smashing transport to cylinder inner corrosion clinker, the clinker barrel inside set with assistant heating mechanism, upper cylinder is also provided with corrosion clinker to corrosion clinker in garbage barrel for stirring process of stirring machine, clinker cylinder top end also provided with rotten waste sum collection mechanism, the top of the clinker is also set with medicine-adding machine. The efficient household garbage composting device by smashing machine for processing domestic garbage pre crushing process, then send to corrosion clinker cylinder in processing process, can effective for domestic garbage fermentation conversion into organic fertilizer, waste reach to re-utilize the goal.
NOVELTY - The new type utility claims one kind amino acid liquid fertilizer is fermentation device, comprising liquid delivery system, an oxygen supply system and fermentation system, wherein, fermentation system of fermentation kettle and discharging wherein one, equipped with discharging valve on the discharging mouth in the fermentation kettle material is comprising of the polyethylene, polypropylene, polyvinylidene fluoride, polytetrafluoroethylene at least one composed of A, and set with liquid inlet and gas inlet, liquid delivery system by pressure pump, transport pipe and regulating valve make up, comprising transport pipe insert fermentation kettle upper end face of liquid inlet in upper end face of fermentation kettle, oxygen system of oxygen tank, pipeline and composed of a flow meter, comprising oxygen obtained amino acid variety and amount of stable, high quality products, with high economic benefit.
NOVELTY - Invention relates to a method of operating a solid-polymer water electrolyser, which includes applying dc supply voltage and feeding reaction water into the electrolyser, heating the solid-polymer electrolyser and the reaction water to operating temperature which corresponds to a given electrolysis current while monitoring the present electrolysis current and temperature values, measuring the operating temperature of the solid-polymer water electrolyser which provides the given electrolysis current value, and breaking down water at said temperature and electrolysis current into hydrogen and oxygen. The method is characterised by that measurement of the operating temperature of the solid-polymer water electrolyser is carried out once the electrolysis current during heating reaches its maximum value and begins to fall, having reached the given value.    USE - Chemistry.    ADVANTAGE - Use of the present invention provides high-speed thermal stabilisation of the electrolysis cell.1 dwg
NOVELTY - The system (100) has a heat generation unit (4) that generates heat using the hydrogen obtained by an electrolysis unit (3). A distillation unit (2) vaporizes the treated water obtained by a sewage-treatment unit (1) using the heat which is generated from the heat generation unit. A vaporization portion (21) generates water vapor. The water vapor generated in the vaporization portion is cooled using the treated water (W1) obtained by the sewage-treatment unit. A liquefaction portion (20) is provided to liquefy the water vapor and obtain the distilled water (W2).    USE - Sewage-treatment system for treating sewage such as domestic waste water, excrement waste water, general industrial waste water, mixing water and rain water sent to sewage works.    ADVANTAGE - Since the sewage-treatment system ensures the energy which is needed for vaporization of treated water or liquefaction of water vapor, the cost reduction is achieved. Hence the treated water which is obtained by purifying the sewage is effectively utilized.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage-treatment system. (Drawing includes non-English language text)    Sewage-treatment unit (1)    Distillation unit (2)    Electrolysis unit (3)    Heat generation unit (4)    Liquefaction portion (20)    Vaporization portion (21)    Treated water (W1)    Distilled water (W2)
NOVELTY - The membrane electrode assembly manufacturing method involves forming top and bottom electrode catalyst layers (M1,M2) on opposite sides of a strip-shaped electrolytic membrane (EM). The defect of at least one of electrolytic membrane and top electrode catalyst layer is detected. At least one electrode catalyst layer is formed at location of electrolytic membrane without defect.    USE - Manufacturing method of membrane electrode assembly for fuel cell.    ADVANTAGE - Uselessness of electrode catalyst layer is suppressed by forming at defect-free location of electrolytic membrane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a membrane electrode assembly manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the membrane electrode assembly manufacturing apparatus. (Drawing includes non-English language text).    Back sheet (1)    Electrolytic membrane (EM)    Membrane electrode assembly (M0)    Top and bottom electrode catalyst layers (M1,M2)    Product sheet (W5)
NOVELTY - Strip-shaped dehydration woven bag comprises strip-shaped small diameter nylon as main body, two-ports arranged annular fastening device, an annular buckle, a first terminal port arranged concave groove and another port arranged I-shaped groove.    USE - The woven bag is useful in biomass gas production process.    ADVANTAGE - The woven bag: achieves rural domestic fuel gas requirements; can achieve industrialization and mass production; and has low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the strip-shaped dehydration woven bag.
NOVELTY - Preparation of tetrabromobisphenol A flame retardant comprises adding bisphenol A and 95% ethanol in bottle, stirring, heating to dissolve bisphenol A completely, cooling to room temperature, adding sodium bromide and concentrated hydrochloric acid, adding dropwise potassium bromide water solution; reacting at room temperature, adding hydrogen peroxide, reacting at room temperature for 2 hours, heating under reflux for 2 hours, dropping sodium bisulfite to system until color becomes white; and distilling to recover ethanol, cooling, filtering, and drying to obtain faint yellow product.    USE - Method for preparing tetrabromobisphenol A flame retardant (claimed).    ADVANTAGE - The low cost, safe and economic method ensures easy recovery of solvent, small toxicity, and no pollution.    DETAILED DESCRIPTION - Preparation of tetrabromobisphenol A flame retardant comprises, in bottle equipped with electric stirrer and condensing pipe, adding bisphenol A and 95% alcohol, stirring, heating to dissolve bisphenol A completely, cooling to room temperature, adding sodium bromide and concentrated hydrochloric acid, adding dropwise potassium bromide water solution; reacting at room temperature, adding hydrogen peroxide, reacting at room temperature for 2 hours, heating under reflux for 2 hours, dropping sodium bisulfite to system until color becomes white; and distilling to recover alcohol, cooling, filtering, and drying to obtain faint yellow product.
NOVELTY - The extraction method of hesperidin from dried orange peel involves adding distilled water in solid-liquid ratio of 1:8-40 g/ml, adding 0-3% pectinase, adding dilute hydrochloric acid to liquid for adjusting pH value to 3-5, placing liquid in water bath for carrying out hydrolysis at 40-55 degrees C for O-3 hours, filtering, concentrating filtrate and placing into vacuum oven for drying.    USE - The method is useful for extraction of hesperidin from dried orange peel (claimed).    ADVANTAGE - The method is simple to operate without using special equipment, and ensures low organic solvent residue, high production safety, non- polluting environment, high extraction rate, and large scale production.
NOVELTY - The method involves obtaining a biomass fuel feeding gasification furnace function. A hot fuel gas is entered into a biomass burner. Paper making heat preservation or quenching process is performed. A Kiln furnace discharging temperature is obtained for about 700 degrees Celsius. Hot wind furnace heat exchanging process is performed according to the biomass fuel feeding gasification furnace function. An air heat exchanger is fixed with a heating warm air cooler. The biomass burner is made of wood leftover material, glass, ceramic, casting, food and paper making material.    USE - High temperature hot biomass fuel gas combustion tail sum generating wind cleaning method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a high temperature hot biomass fuel gas combustion tail sum generating wind cleaning method. '(Drawing includes non-English language text)'
NOVELTY - Improving soil compaction comprises crushing 650-750 pts. wt. crop straw, 220-280 pts. wt. peat and 50-90 pts. wt. livestock manure, mixing, covering with plastic film, and naturally fermenting to obtain organic fertilizer; mixing 0.1-0.3 pt. wt. Lactobacillales powder, 0.1-0.4 pt. wt. Nitrobacter powder and 0.1-0.2 pt. wt. Rhizobium powder to obtain mixed fertilizer; taking 1-5 pts. wt. microbial water-retaining agent powder; and mixing organic fertilizer, mixed fertilizer and microbial water-retaining agent powder, applying to soil, and compacting.    USE - Method for improving soil compaction (claimed).    ADVANTAGE - The method solves the problem of fast water evaporation of soil, lack of organic matter, and weak soil fertility.
NOVELTY - Biological cultivation of earthworm comprises using culture medium which is prepared by mixing corn stover or straw, peanut, 38% rapeseed and 62% pig manure.    USE - Method for biological cultivation of earthworm.    ADVANTAGE - The method increases earthworm yield.
NOVELTY - Biological pesticide composition comprises 12 wt.% pyrimidine nucleotides, 15 wt.% polyoxin A, 11 wt.% polyoxin B, 44 wt.% wettable powder and 23 wt.% fungicide.    USE - Biological pesticide composition used for preventing and controlling fungal and bacterial diseases in plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological pesticide composition comprising taking raw materials, adding 5-10 g water and drying at 25-35 degrees C.
NOVELTY - Extracting antistaling agent involves grinding traditional Chinese medicine to obtain particles of 50-100 mesh. Soaking traditional Chinese medicine in water in a ratio of 1:(2-4) for 2-4 hours. Soaked product is boiled for 30-60 minutes to obtain extract. Obtained extract is filtered and filtrate is stored at 2-4 degrees C. Obtained residue is again soaked in water in a ratio of 1:(1-2) for 2-4 hours for 30-60 minutes to obtain another extract. Obtained extract is filtered to obtain another filtrate. Obtained filtrates are combined and stored at 2-4 degrees C.    USE - Method for extracting antistaling agent for strawberry, grape, cherry, raspberry, blueberry or cherry (claimed).    ADVANTAGE - The method enables to prepare antistaling agent, which is non-toxic, and eco-friendly, and replaces chemical preservative.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for applying antistaling agent on fruits, which involves soaking fruits in antistaling agent for 3-5 minutes, and packing them in polyethylene bags at 1 plus minus 0.5, and relative humidity 90-95%.
NOVELTY - The system has a biomass sum room provided with a circular tank body. An upper layer of the circular tank body is connected with a gasification room. A water channel is connected with a main pipe. A dry-type filter room is connected with a smoke exhaust pipe. A water ring vacuum pump is connected with a power supply unit. A pipeline is connected with the dry-type filter room that is provided with a gas flow meter. A storage tank is connected with a transport pipe. A decompression valve is connected with a stove. A filtering device is connected with a sewage discharge valve.    USE - Integrated biomass gas storing system.    ADVANTAGE - The system has high purification and production efficiency, and improves gas transmitting stability, removes ash, impure slag and tar in an effective manner and realizes dry purification and compression biomass gas storage operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an integrated biomass gas storing system.
NOVELTY - The system has a baking reactor (3) provided with a reactor main body (3a). A rotating shaft (3b) is mounted on the reactor main body. A driving component (3c) is connected with the rotating shaft. A tower plate (3d) and a scraping plate are connected with each other. A tray (3g) is fixed with the tower plate. The tray is mounted with a baking medium input pipe (3f) that is connected with an input terminal. The input terminal is fixed with an air outlet of a wind cap (3h) that is connected to the tower plate.    USE - Air flow bed gasification biomass pre-processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an air flow bed gasification biomass pre-processing system.    Baking reactor (3)    Reactor main body (3a)    Rotating shaft (3b)    Driving component (3c)    Tower plate (3d)    Baking medium input pipe (3f)    Tray (3g)    Air outlet cap (3h)
NOVELTY - The device has a smoke pipe (14) connected with a draught fan. U-shaped foam dust-removing pipe (12) is connected between a fume entrance (15) and a smoke outlet unit (1). An end of the fume entrance is provided with a foam pipe (11) and a foam nozzle (13). An end of the smoke outlet unit is connected with another foam pipe (4) and a foam outlet (3). A bottom part of another smoke pipe (10) is connected with a knife gate valve (9). A lower end part of the foam outlet is connected with a flange unit (16).    USE - U-shaped biomass gasification furnace foam dust removing device.    ADVANTAGE - The device performs foam dust removing process with high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a U-shaped biomass gasification furnace foam dust removing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a U-shaped biomass gasification furnace foam dust removing device.    Smoke outlet unit (1)    Foam outlet (3)    Foam pipes (4, 11)    Knife gate valve (9)    Smoke pipes (10, 14)    U-shaped foam dust-removing pipe (12)    Foam nozzle (13)    Fume entrance (15)    Flange unit (16)
NOVELTY - The fermentation device has a cloth bacteria pipe that is connected with circular pipe fixing cloth and fermented annular inner side wall pipe. The cloth bacteria pipe is set with cloth fungus in multiple vertical upper directions through hole. The discharging water pipe and cloth bacteria device are equipped with the biogas slurry on one-way valve with water pressure portion. The feedstock pipe (10) and discharging pipe (20) are set with water pressure portion (40). The water discharging pipe is set with the one-way valve of one-way liquid control outlet pipe.    USE - Unordered type biogas slurry and marsh gas fermentation device.    ADVANTAGE - The operation of the multiple area annular fermentation system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the unordered type biogas slurry and marsh gas fermentation device.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipeline (30)    Air guide pipe (36)    Water pressure portion (40)
NOVELTY - The system has a gas-guide tube (36) that is set with an upper valve. A cloth bacteria device is comprised with a drain pipe (44). The drain pipe and cloth bacteria device set the water level and lowest point of water pressure which is higher than drain pipe. The drain pipe is located on a horizontal plane. The discharging water pipe is provided to discharge the control liquid from a discharge pipe (20) into a one-way valve. The discharging water pipe is provided to discharge liquid from a hydraulic control one-way flow into feedstock tube and one-way valve.    USE - Multi-fermentation region biogas liquid turbulent flow stirred energy fermentation system.    ADVANTAGE - The flow of fermentation material is ensured so that the fermentation efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the multi-fermentation region biogas liquid turbulent flow stirred energy fermentation system.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipe (30)    Gas-guide tube (36)    Drain pipe (44)
NOVELTY - The disordered turbulent flow type super-efficient biogas sum fermentation system has setting annular fermentation pipeline which is provided at top portion of annular pipeline with opening. The water pressure and feedstock pipe (10) is connected with drain pipe (20). A gas-guide tube is provided with valve on fermentation system. The cloth bacteria pipe is connected to annular cloth bacteria fermentation pipe (30). Each cloth bacteria pipe is formed with through out holes along vertical upper direction.    USE - Disordered turbulent flow type super-efficient biogas sum fermentation system.    ADVANTAGE - The efficient of the biogas sum fermentation system is improved. The heat preservation effect of the system is ensured. The labor intensity required for operating the system is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the disordered turbulent flow type super-efficient biogas sum fermentation system.    Feedstock pipe (10)    Drain pipe (20)    Annular cloth bacteria fermentation pipe (30)    Water connecting portion (40)    Discharging tube (42)
NOVELTY - The device has a material cylinder that is provided with a feedstock pipe (10). A discharging pipe plate is arranged between a fermentation pipe (30) and a discharging pipe (20). A cloth bacteria device is comprised with a drain pipe (44). The cloth fungus hole is formed on the on cloth bacteria pipe in vertical upper direction. A feedstock pipe (10) is set with a water discharging pipe (42) for controlling the water pressure and marsh liquid which flows into feedstock pipe and one-way valve, and biogas slurry which flows into the one-way check valve.    USE - Pressure disturbance mixed flow biogas generating device.    ADVANTAGE - The multi-fermentation efficiency is increased so that the biogas slurry is uniformly distributed in the fermentation system easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the pressure disturbance mixed flow biogas generating device.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipe (30)    Water discharging pipe (42)    Drain pipe (44)
NOVELTY - The method involves taking fermentation raw material and pouring the fermentation raw material into feedstock tube (10). A marsh liquid is pushed in the direction adjacent to the fermentation area. The fermentation biogas is continuously generated from a fermentation system. The fermentation area is arranged adjacent to the biogas fermentation slurry transport area. The backflow pressure is provided in inner annular slurry pipeline to reduce methane fermentation space. The rest of the stored methane fermentation area is used.    USE - Method for generating biogas using dismountable type generating device.    ADVANTAGE - The bad influence caused by fungus liquid for generating biogas is prevented, and the generating of biogas is performed in short time. The labor resource is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the dis-mountable type generating device.    Feedstock tube (10)    Discharge pipe (20)    Fermentation pipeline (30)    Air guide pipe (36)    Exhaust pipe (46)
NOVELTY - The method involves providing a raw material from a fermentation feedstock pipe (10) into an U-type fermentation pipe (30), and producing the marsh gas in U-type fermentation pipe. The marsh gas for collecting/discharging pipe (20) side wall and adjacent blocking plate, is passed into the fermentation area. The biogas liquid of the water pressure pipe is reached to the drain pipe (12). The water pressure portion is connected with a connecting position of lowest cloth bacteria device (50). The fermented biogas slurry is flowed into water pressure pipe via cloth bacteria device .    USE - Biogas preparation method for several section disturbance promoted uniform strain distribution anaerobic fermentation system.    ADVANTAGE - The preparation of the biogas is enhanced efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic fermentation system.    Feedstock pipe (10)    Drain pipe (12)    Discharge pipe (20)    Fermentation pipe (30)    Cloth bacteria device (50)
NOVELTY - The biogas pool has annular pipe that is connected with fermentation feedstock pipe to install with feedstock tube plate. The annular fermentation pipe is connected with a discharging pipe to set with discharging pipe plate. The plate portion is arranged between pipe blocking plate and feedstock material blocking plate. The fermentation area top portion is set with mutually independent air pipe. The air pipe is set up with valve. The water discharging pipe is set with control discharging pipe. The biogas slurry is flowed into the one-way check valve in water pressure portion.    USE - Channel-type biogas pool.    ADVANTAGE - The environment-friendly and energy-saving effect of the biogas pool are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biogas pool.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipeline (30)    Air guide pipe (36)    Water pressure portion (40)
NOVELTY - The method involves taking fermentation raw material, and passing the feedstock through a pipe. Continuous flow fermentation marsh gas is generated in the fermentation area, and the biogas fermented in pipe extrusion is passed through the feedstock tube. A discharging pipe is configured for draining the lowest liquid level. A gas-guide tube is installed in the top portion of the fermentation area.    USE - Method for generating energy using pressure disturbance type energy generating device.    ADVANTAGE - The precipitation operation is carried out easily, and the fermentation efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the pressure disturbance type energy generating device.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipeline (30)    Discharging pipe blocking plate (36)    Fermentation area (40)
NOVELTY - The method involves generating continuous flow fermentation marsh gas with a fermentation cell. An annular pipe is provided to flow the fermented biogas liquid to a side wall. The continuous fermentation biogas is generated from the overflow side of fermentation system. The water is flowed through a drain pipe using the gas-guide tube (36). The marsh gas in a fermentation area is reduced, and the liquid feedstock (10) is stored through drain pipe.    USE - Method for generating marsh gas of disordered turbulent flow type biogas fermentation system.    ADVANTAGE - The fermentation is ensured, and the flow of fermentation material is promoted effectively. The fermentation efficiency is increased effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for generating marsh gas of disordered turbulent flow type biogas fermentation system.    Feedstock (10)    Discharge pipe (20)    Fermentation pipeline (30)    Air guide pipe (36)    Discharge pipe (46)
NOVELTY - The device has a gas-guide tube (36) that is set with a valve on a fermentation system. A water pipe and a cloth bacteria device are formed with an annular fermentation pipeline (30). A discharge pipe (20) is set with a control discharging pipe for controlling the biogas slurry flow into the one-way check valve. A feedstock pipe (10) is connected with a drain pipe (44). The lowest point cloth bacteria level of discharge pipe is provided higher than the drain pipe. The drain pipe is connected with a water pressure device.    USE - Device for lifting biogas liquid turbulent flow effect using multi-area annular super-efficient biogas fermentation system.    ADVANTAGE - The flow of fermentation material is ensured so that the fermentation efficiency is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the device for lifting biogas liquid turbulent flow effect.    Feedstock pipe (10)    Discharge pipe (20)    Annular fermentation pipeline (30)    Gas-guide tube (36)    Drain pipe (44)
NOVELTY - The method involves pouring the fermentation raw material into a feedstock pipe (10). The marsh liquid pushing direction adjacent fermentation cell is generated when thick of the cell is to-be increased with fermentation biogas. The continuous fermentation biogas in flow direction is generated when thickness is not required. An annular pipe of biogas fermentation liquid feedstock pipe or discharge pipe (20) is reached to the lowest position. The continuous fermentation biogas is generated from fermentation system.    USE - Method for generating biogas for biogas liquid turbulent in multiple area annular fermentation system lifting device.    ADVANTAGE - The operation of the multiple area annular fermentation system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the multiple area annular fermentation system.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipeline (30)    Air guide pipe (36)    Water pressure portion (40)
NOVELTY - Microecological fertilizer comprises 5-10 pts. wt. Aspergillus niger (CGMCC 7927) culture, 3-8 pts. wt. Bacillus mucilaginosus culture, 3-8 pts. wt. B.megaterium culture, 5-12 pts. wt. B.subtilis culture, 4-7 pts. wt. A.awamori culture, and 2-4 pts. wt. Lactobacillus culture.    USE - The microecological fertilizer is used for promoting growth of crops.    ADVANTAGE - The microecological fertilizer improves microecological environment of soil for growth of crops, and has high organic matter content.
NOVELTY - The method involves generating the continuous fermentation biogas from the fermentation system. The inner annular pipe production fermentation process of marsh gas is performed. The marsh liquid in the liquid level is reached to feedstock pipe (10) and discharging pipe (20) to most low point. The transport and storage of hydraulic liquid is performed through feedstock pipe. The relux in reducing water pressure of the marsh gas is supplied to annular fermentation pipeline (30).    USE - Method for generating marsh gas in biogas liquid turbulent flow stirring super-efficient biogas fermentation system.    ADVANTAGE - The operation of the multiple area annular fermentation system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biogas liquid turbulent flow stirring super-efficient biogas fermentation system.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipeline (30)    Air guide pipe (36)    Water pressure portion (40)
NOVELTY - The method involves obtaining the fermentation raw material. The continuous flow fermentation marsh gas is generated. The biogas slurry inside a fermentation pipe (30) is extruded through bacteria device. The marsh gas is input into the top portion of fermentation area using gas-guide pipe. The pressure inside fermentation area is reduced. The biogas is sent to a feedstock pipe (10) through a drain pipe. The fungus device is provided in the biogas fermentation area to supplement the loss of marsh gas in space. The fermented marsh gas is stored in the rest of area.    USE - Method for generating marsh gas using superefficient biogas fermentation system.    ADVANTAGE - The multi-fermentation efficiency is increased so that the biogas slurry is uniformly distributed in the fermentation system easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view illustrating the process for generating marsh gas using superefficient biogas fermentation system.    Feedstock pipe (10)    Discharge pipe (20)    Fermentation pipe (30)    Air pipe (36)    Discharge hole (46)
NOVELTY - Microalgae comprising 50% phosphoenolpyruvate carboxylase and 50% acetyl-coenzyme A carboxylase, is new.    USE - New microalgae is useful for extraction of biodiesel (claimed).    ADVANTAGE - The microalgae has excellent production rate, and promotes photosynthesis effect and lipid content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for extraction of biodiesel involving taking microalgae and genetically modifying.
NOVELTY - Preparation of transition metal chalcogenide hydrogen evolution reaction electrode comprises dispersing two-dimensional transition metal chalcogenide nanochips to mixed liquid of water and anhydrous ethanol to obtain transition metal chalcogenide nanosuspension with concentration of 0.01-5 g/L, performing electrophoresis deposition to carbon cloth using stainless steel plate connected to negative direct current power supply at 50-200 V, drying at 55-70 degrees C for 12-24 hours and sintering at 140-160 degrees C for 0.5-5 hours.    USE - Method for preparing transition metal chalcogenide hydrogen evolution reaction electrode used for solar water electrolysis (claimed).    ADVANTAGE - The simple and easy method has low production cost.
NOVELTY - Methanol synthesizing device comprises a synthetic gas generating unit (100) for generating synthetic gas containing hydrogen and carbon monoxide by gasifying the raw materials, a methanol synthesizing (200) unit for synthesizing the synthetic gas into methanol, and a hydrogen circulating unit for separating hydrogen remain in the synthetic gas from the synthetic gas without synthesizing methanol and secondarily adjusting the molecules ratio of hydrogen/carbon monoxide by participating for synthesizing methanol through resupplying by the methanol synthesizing unit.    USE - Used as methanol synthesizing device.    ADVANTAGE - The device easily controls the ratio of hydrogen and carbon monoxide, economically synthesizes methanol without using expensive water gas shift apparatus, and has high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for synthesizing methanol, comprising (a) generating synthetic gas containing hydrogen and carbon monoxide by gasifying the raw materials, (b) synthesizing the obtained synthetic gas into methanol, (c) separating hydrogen which remain in the synthetic gas from the synthetic gas without synthesizing methanol, and (d) determining whether the molecules ratio of hydrogen/carbon monoxide is deviated from 2.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methanol synthesizing device (Drawing includes non-English language text).    Synthetic gas generating unit (100)    Methanol synthesizing unit (200)    Synthetic gas compressing unit (210)    Methanol purification unit (230)    Methanol storage unit (240)
NOVELTY - Method for producing a biofuel, involves (a) culturing an Acetobacter lovaniensis bacterium in a growth medium containing phosphate at a level which is more than 1 g/l and separating product from the growth medium, or (b) providing an aqueous medium containing a cell-free extract of an A.lovaniensis bacterium cultured in a growth medium containing phosphate at a level which is more than 1 g/l, where the biofuel is produced in the aqueous medium, and optionally separating the biofuel from the aqueous medium.    USE - The method is useful for producing biofuel or its component, preferably volatile alcohols, esters and monoterpenes which is useful as an additive (all claimed).    ADVANTAGE - The method produces biofuel simply using waste substrates. The biofuel is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for aqueous medium which comprises a cell-free extract of an A.lovaniensis bacterium cultured in a growth medium containing phosphate at a level which is more than 1 g/l.
NOVELTY - Manufacture of 1-(4-hydroxy-3-methoxyphenyl)-1,3-propanediol involves contacting 3-hydroxy-1-(4-hydroxy-3-methoxyphenyl)-1-propanone-containing solution and borohydride compound, and obtaining 1-(4-hydroxy-3-methoxyphenyl)-1,3-propanediol containing material by reducing 3-hydroxy-1-(4-hydroxy-3-methoxyphenyl)-1-propanone.    USE - Manufacture of 1-4-hydroxy-3-methoxyphenyl-1,3-propanediol used for manufacturing resin, adhesive agent, resist material, and pharmaceutical products.    ADVANTAGE - The method enables safe and environmentally-friendly manufacture of 1-4-hydroxy-3-methoxyphenyl-1,3-propanediol.
NOVELTY - The new type utility claims have one full time domain A of rural sewage treatment system, comprising inner cylinder by three area of two clapboards divide into the two, wherein Anaerobic zone comprises sewage pipe is connected with deposition water bending head, time domain biochemical treatment area including spiral wound hollow telescopic pole and chain filler, ground source heat pump and is connected heat-conducting tube, dissolved in sum pre-hanging slag area set with bracket connected with cylinder bottom by the solution engine and sum for pre-hanging slag machine connected with the cylinder top part, corresponding to the hanging machine provided with slag discharge groove is connected with end cover. The utility model is new type by using septic tank is divided into a precipitation zone, a full time domain Anaerobic biochemical treatment area, sum pre-hanging slag area of three are implementation have, waste liquid solid-liquid separating, the waste liquid until, second time using the technology goal, at the same time use heat source of pump technology increase full time local biochemical treatment area and treatment temperature reach to the system and all full-area.
NOVELTY - The new type utility claims have one plant for organic biological fertilizer production fermentation material turning the turning plate and the turning machine, belonging to agricultural machine equipment technology field, the turning plate comprises taking axis as plate leaves the symmetrical strip structure, the plate leaves with two end part width less than width of work face middle part, axis seat and plate leaves is set with assembly hole, plate leaves the working face formed with a reinforcing rib, reinforcing rib and the axis A section of height greater than height of two end part, the utility model is new type of turning plate by the unique structure design, in turning process and high depth of plate leaves the stress condition is good, process make the turning plate can be applied in organic biological fertilizer production and fermentation material is middle, turning with high efficiency, reliability and the machine, turning machine of the utility model is new type by turning plate in the special composite method, make turning machine process whole stress condition is good, and turning operation transition is stable, especially fit for large square meter in stacking and turning cooling process.
NOVELTY - Fuel cell comprises an anode and a cathode. The fuel cell being capable of operating in power delivery mode in which it generates electrochemical power by reaction of electrochemically active species at anode. The fuel cell comprises a Lewis acid (A1), a Lewis base (A2) and hydrogen. The electrochemically active species at anode is Lewis acid hydride formed via heterolytic cleavage of hydrogen with Lewis acid, and Lewis base along with Lewis base hydride and the redox reaction of Lewis acid hydride gives proton, Lewis acid and 2 electrons at anode when fuel cell is in power delivery mode.    USE - The fuel cell is useful: for oxidation of hydrogen; for generating electrochemical power (all claimed); and as energy generating device and as energy storage device including battery or capacitor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) electrocatalytically oxidising hydrogen using a Lewis acid, a Lewis base and at least one electrode comprising introducing hydrogen to the Lewis acid and Lewis base and heterolytically cleaving hydrogen to produce an electrochemicaily active Lewis acid hydride, and electrochemicaily oxidising the electrochemicaily active Lewis acid hydride; and    (2) an electrode in combination with a lewis acid, where the lewis acid can form a hydride via the heterolytic cleavage of hydrogen using a Lewis base.
NOVELTY - Fermentatively producing biogas from biomass, comprises providing biomass in a fermentation reactor, and adding 0.01-1.5 vol.% ethanol to the biomass, based on the total volume of the biomass in the fermentation reactor.    USE - The method is useful for fermentatively producing biogas from biomass (claimed).    ADVANTAGE - The method produces biogas with improved methane yield in cost-efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of ethanol, preferably ethanol-containing solution or ethanol-containing fermentation material to increase the yield of the fermentative generation of biogas from biomass.
NOVELTY - Garbage environment-friendly system comprises straw sludge pretreatment device (11), sludge and coarse particulate dust pretreatment device (12), waste mixture manufacturing device (13), and system earth-moving device (14).    USE - Garbage environment-friendly system used for paving, farmland, and soil fertilization of straw (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of garbage environment-friendly system (Drawing includes non-English language text).    Straw sludge pretreatment device (11)    Sludge and coarse particulate dust pretreatment device (12)    Waste mixture manufacturing device (13)    System earth-moving device (14)
NOVELTY - Constructed wetland filler matrix comprises 1-10% polyurethane microorganism support material with respect to total weight of the constructed wetland filler matrix, and inorganic matrix, where the inorganic matrix comprises fine gravel, vermiculite and blast furnace residue in a weight ratio of 1-4:1-2:1-5, and the polyurethane microorganism support material is uniformly distributed on the inorganic matrix.    USE - The constructed wetland filler matrix is useful for sewage treatment (claimed).    ADVANTAGE - The constructed wetland filler matrix has excellent adhesiveness with respect to microorganism, and accelerates generation of biofilm.
NOVELTY - Recycling processing system comprises incineration boiler, first residual fume heat exchanger, sludge storage tank, alkali refining room, heat cracking room, dehydration room, second residual fume heat exchanger, heat drying room, anaerobic fermentation tank, alkali storage room, sealed heat treatment tank, snake-shaped steam disk pipe and stirring device.    USE - Recycling processing system used for dewatered sludge (claimed).    ADVANTAGE - The system easily removes sludge moisture, promotes removal of sludge biochemical degradation characteristics, achieves sludge stabilization and efficient separation of sludge, and solves the problem of low drying efficiency and prone to explosion problem.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recycling processing of dewatered sludge comprising pouring dewatered sludge into reservoir tank, transporting to alkali refining room, carrying out alkali refining; transporting alkali sludge to heat cracking room, carrying heat cracking; dehydrating to obtain solid phase and liquid phase; drying solid phase to obtain sludge, entering liquid phase into anaerobic fermentation tank, heating to produce methane; entering dried sludge into incineration boiler as fuel, and burning.
NOVELTY - An intensive cattle excrement anaerobic reaction tank comprises outer jacket (9) and internal stirring plate (13). The stirring plate comprises main rod, stirring plate port, support rod, and fin rod. The stirring plate main rod is fixed on rotating shaft (25). The included angle between main rod and rotating shaft is 30-90 degrees . The rotating shaft is provided with sealing ring (26) on two ends and connected to tank body through bearing.    USE - Anaerobic reaction tank for intensive cattle excrement processing.    ADVANTAGE - The reaction tank allows for uniform heating of materials and improves mixing efficiency, thus, enabling thorough metabolism of organic materials.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of anaerobic reaction tank.    Outer jacket (9)    Thermometer detection hole (10)    Stirring plate (13)    Rotating shaft (25)    Sealing ring (26)
NOVELTY - Preparation of biological fertilizer involves taking residual straw obtain from biogas fermentation, drying 25 pts. wt. straw, crushing into powder, drying 60 pts. wt. cow manure and 8 pts. wt. plant ash, crushing, adding 7-13 pts. wt. bryophyte, drying, crushing and mixing.    USE - Method for preparing biological fertilizer.
NOVELTY - Preparation of chicken manure organic fertilizer involves adjusting moisture content of chicken manure to 45-50%, adding rice straw, rice husk, humic acid, peanut shells, melon seed shell and rice bran, mixing, adding complex microbial agent, fermenting at 35 degrees C, stirring, curing, drying and crushing.    USE - Method for preparing chicken manure organic fertilizer.
NOVELTY - Preparation of beanstalk fiber organic fertilizer involves cutting beanstalk into 6 cm long, placing in pot, adding 38-52 wt.% ammonium bicarbonate, 38-52 wt.% potassium acetate and 7.5-10 wt.% calcium oxide, mixing, adding water, heating at 80 degrees C, stirring for 45 minutes, heating at 175-205 degrees C and 0.5-0.7 MPa for 1.5-2.5 hours, pulping mixture, filter pressing to obtain black liquor and pulp, bleaching black liquor, concentrating, spray-drying, solidifying to obtain powder, rinsing pulp, and recycling pulp into paper.    USE - Method for preparing beanstalk fiber organic fertilizer.    ADVANTAGE - The method is environmental-friendly and has simple operation.
NOVELTY - Preparation of pig manure processing plant involves remodeling pig barn, collecting pig manure into fermentation bed, performing ecological farming and cleaning piggery.    USE - Method for preparing pig manure processing plant used for decontaminating and recycling pig manure and producing organic fertilizer.    ADVANTAGE - The method is simple, and reduces waste discharge.
NOVELTY - Fermentation livestock manure involves performing pretreatment of manure, fermenting at 55-65 degrees C with fermenting agent, controlling moisture content to 45-60%, aerating, drying and sieving.    USE - Method for preparing livestock manure.    ADVANTAGE - The method is environmental-friendly, inexpensive and simple.
NOVELTY - Biological organic fertilizer comprises 100-200 pts. wt. natural red loam, 50-150 pts. wt. rice straw, 30-60 pts. wt. green waste, 5-15 pts. wt. ash, 5-10 pts. wt. chicken manure and 0.01-0.1 pt. wt. organic decomposing inoculant.    USE - Biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer is environmental-friendly, and has low production cost.
NOVELTY - Preparation of fertilizer involves weighing 15-20 pts. wt. traditional Chinese medicine, 5-10 pts. wt. bone meal, 2-5 pts. wt. shrimp and crab shell, 2-3 pts. wt. copper sulfate, 80-100 pts. wt. rice water and 2-3 pts. wt. yeast, crushing shrimp and crab shell into 20-30 mesh powder, adding traditional Chinese medicine, bone meal, copper sulfate, yeast and rice water, stirring, fermenting at 50-60 degrees C for 48-60 hours, controlling humidity to 60-65%, drying, and packaging.    USE - Method for preparing fertilizer.    ADVANTAGE - The fertilizer is inexpensive and has simple preparation.
NOVELTY - Fermented cotton straw composite microbial agent comprises 25-45 wt.% white-rot fungus, 5-20 wt.% Trichoderma viride bacteria broth, 10-40 wt.% Pleurotus ostreatus bacteria broth, 5-20 wt.% Streptococcus bacteria and 5-20 wt.% Bacillus.    USE - Fermented cotton straw composite microbial agent.    ADVANTAGE - The fermented cotton straw composite microbial agent increases soil fertility and increases plant root absorbing capacity.
NOVELTY - Preparation of chalcone compound comprises grinding benzaldehyde and acetophenone and subjecting to solid phase aldol condensation under no solvent condition and using sodium hydroxide and potassium carbonate mixed alkali as catalyst.    USE - Preparation of chalcone compound (claimed).    ADVANTAGE - The method has relative higher yield, simple operation and short response time, avoids the use of organic solvent, thus, reducing environmental pollution and simplifying the reaction and post-processing operation, reduces production cost, and uses convenient ball-milling method.
NOVELTY - Environment-friendly deicing agent comprises 40-50 wt.% organic acid salt, 30-40 wt.% biochar, 1.5-2 wt.% diammonium hydrogen phosphate, 5-12 wt.% urea, 4-6 wt.% silicate and 2-5 wt.% hydroxycellulose.    USE - Environment-friendly deicing agent.    ADVANTAGE - The deicing agent with 55 plus minus 1 degrees C thermal phase transition temperature, 80% stearic acid degree of saturation and 169 J/g latent heat can absorb solar energy, and has fast melting speed and wide temperature range.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of environment-friendly deicing agent comprising mixing organic acid salt, diammonium phosphate, urea and silicate, adding biochar, mixing, adding hydroxycellulose, mixing and extruding into 6-8 mm.
NOVELTY - Plant biomass processing involves taking biomass and water according to mass ratio of 1:5-1:15 in anoxic atmosphere, and then heating at 205-235 degrees C for 10-30 minutes. The obtained reaction mixture is cooled to form a solid liquid mixture product, which is filtered in vacuum to obtain liquefied product and carbonizing material. The liquefied product is separated by dialysis, electrodialysis or nanometer filtration. The separated liquid is mixed with 0-10% water in a reaction kettle with a carbonizing material at 255-345 degrees C in oxygen atmosphere for 180-240 minutes to obtain liquefied product.    USE - Method for processing plant biomass (claimed).    ADVANTAGE - The method processes plant biomass in a simple manner with increased conversion rate.
NOVELTY - The cover has bottom plate and supporting plate. An opening of the bottom plate is provided with several circular through holes. The supporting plate is provided with multiple waist-shaped opening through holes on the supporting plate is provided with multiple waist-shaped through holes whose lengths are more than circular through hole diameter. The waist-shaped through hole is exposed from the bottom plate for supporting the bottom of the bottle cover. The same portion of circular through hole and the waist-shaped through hole is used for bottle cover.    USE - Biochemical analyzer agent assistant cover used in hospital laboratory.    ADVANTAGE - The insulation effect is improved, and the exchange of heat is reduced. The consumption of energy is reduced so that the energy saving effect is improved. The environment friendly reagent cabin cover is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biochemical analyzer agent assistant cover.    Top plate (3)    Pressing plate (4)    Reagent bottle (5)    Nut (7)    Lug boss (23)
NOVELTY - Herba cistanche green tea beverage comprises (based on 1000 pts. wt.) 20-30 pts. wt. green tea fresh leaf, 15-25 pts. wt. herba cistanche, 15-25 pts. wt. hawthorn, 10-15 pts. wt. gingko leaf, 5-10 pts. wt. buckwheat, 5-10 pts. wt. radix puerariae, 5-10 pts. wt. pear freeze-dried powder, 5-10 pts. wt. isomaltooligosaccharide, 1-5 pts. wt. taurine, 1-3 pts. wt. xylitol, 1-2 pts. wt. sodium erythorbate, 1-5 pts. wt. lucid ganoderma polysaccharide and balance water.    USE - Herba cistanche green tea beverage used for promoting fluid, quenching thirst, improving intelligence, providing anti-aging and anti-fatigue effects, enhancing immunity, supplementing kidney, strengthening yang cold resistance and relaxing the bowels.    ADVANTAGE - The herba cistanche green tea beverage has increased active substance extraction rate, nutritional value, wide material sources, increased healthcare effect, simple preparation and low device requirements, is convenient for large-scale industrial production and green and environment-friendly and improves user life quality.
NOVELTY - Processing fish product leftovers and low value fish waste comprises taking raw material which is fish head, bone, skin, flake, fin, tail, fat, internal organs (gills, guts excluded) and edible low value fish waste raw material, rinsing raw materials, draining, before decocting, impregnating with spice, where the impregnating process specifically comprises smashing ginger, clove, fennel, and trinaphthyl spice, adding water to decoct, dry and mixing raw material uniformly, and impregnating for 25 minutes so as to remove the fishy smell.    USE - The method is useful for processing fish product leftovers and low value fish waste (claimed).
NOVELTY - A foot healthcare product comprises 11.3-15.8 g thorny jujube tree, 7.3-12.5 g Heracleum hemsleyanum, 4.3-8.6 g teasel root, 5.8-10.4 g corydalis tuber, 12.4-16.8 g wormwood, 13.8-18.5 g Cynomorium songaricum, 6.3-11.9 g Angelica, 5.9-7.6 g dandelion, 10.6-15.9 g Chinese yam, and 14.5-19.6 g radix paeoniae alba.    USE - Foot healthcare product used for regulating foot blood, strengthening bones and muscles, and expelling wind.    ADVANTAGE - The foot healthcare product is pure and environment-friendly.
NOVELTY - Preparation of nutritional extract involves extracting Astragalus, Atractylodes, Poria, licorice, Citrus, parsley, peony and yam in water, filtering to obtain extract A, extracting Amomum, Saposhnikovia, buckthorn, rhizoma ligustici wallichii, herba epimedii, fried malt, hawthorn, radix bupleuri, Rehmannia, wheat and jujube in water, filtering to obtain extract B, mixing extracts, standing and cooling.    USE - Method for preparing nutritional extract used for promoting abdominal delivery.    ADVANTAGE - The method is environmental-friendly and has wide social and economic use.
NOVELTY - An MRI contrast agent is prepared by preparing raw materials, preparing primary agent and purifying.    USE - Method for preparing MRI contrast agent used for drug carrier and drug controlled release fields (claimed).    ADVANTAGE - The environment-friendly method has simple operation, low cost, and excellent pH and temperature sensibility.
NOVELTY - A sanitary napkin includes medicinal layer between surface layer and absorbent layer. The medicinal layer comprises 3-5 g radix scrophulariae, 4-6 g Gardenia jasminoides, 5-6 g rhizoma coptidis, 3-5 g Phellodendron, 2-4 g indigo, 3-5 g radix sophorae flavescentis, 4-6 g radix bupleuri, 3-4 g radix scutellariae, 2-3 g caulis sinomenii, 2-3 g Achyranthes, 3-4 g Erythrina indica, 2-4 g radix aconiti carmichaeli, 3-5 g large-headed atractylodes rhizome, 4-6 g stiff silkworm, 5-7 g radix stemonae, 5-6 g myrrh, and 3-5 g rhizoma Corydalis.    USE - Sanitary napkin used for preventing and treating vaginitis (claimed).    ADVANTAGE - The napkin is simple to manufacture, environment-friendly and easy and comfortable to use, and has no toxic and side effects.    DETAILED DESCRIPTION - A sanitary napkin comprises surface layer, absorbent layer, bottom layer, and medicinal layer between surface layer and absorbent layer. The medicinal layer comprises 3-5 g radix scrophulariae, 4-6 g G. jasminoides, 5-6 g rhizoma coptidis, 3-5 g Phellodendron, 2-4 g indigo, 3-5 g radix sophorae flavescentis, 4-6 g radix bupleuri, 3-4 g radix scutellariae, 2-3 g caulis sinomenii, 2-3 g Achyranthes, 3-4 g E. indica, 2-4 g radix aconiti carmichaeli, 3-5 g large-headed atractylodes rhizome, 4-6 g stiff silkworm, 5-7 g radix stemonae, 5-6 g myrrh, and 3-5 g rhizoma Corydalis. An INDEPENDENT CLAIM is included for manufacture of sanitary napkin by screening medicinal raw materials, washing, cutting into pieces, drying, and grinding into powder; using cotton, cloth and paper pulp material to manufacture surface layer, absorbent layer and bottom layer; and providing medicinal powder between surface layer and absorbent layer.
NOVELTY - The catheter has a needle tube protective sleeve provided with a long hollow shell. A front end of a groove joint is opened with an opening. A rear part of the needle tube protective sleeve is connected with a needle base and a needle base slide sleeve. The needle tube protective sleeve is sleeved with a coaxial limiting ring. A conduit module is extended outward of a remaining channel. The needle base is fixed with an operation fin. Another groove joint is formed in the remaining channel. The coaxial limiting ring is fixed on an outer periphery of the conduit module.    USE - Dual chamber clinical indwelling needle protective sleeve blood catheter.    ADVANTAGE - The catheter avoids hurt of human and pollution of environment. The catheter has strong practicability, and is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a dual chamber clinical indwelling needle protective sleeve blood catheter.
NOVELTY - Preparation of valsartan (salt) involves reacting 2-((2'-cyano-biphenyl-4-yl-methyl)-amino)-3-methyl-butyric acid methyl ester hydrochloride (I) with valeryl chloride, obtaining 2-((2'-cyano-biphenyl-4-yl-methyl)pentanoylamino)-3-methyl-butyric acid methyl ester (II), reacting 2-((2'-cyano-biphenyl-4-yl-methyl)pentanoylamino)-3-methyl-butyric acid methyl ester with metal azide in the presence of trialkyltin chloride, and hydrolyzing obtained 3-methyl-2-(pentanoyl-(2'-(1H-tetrazol-5-y1)-biphenyl-4-yl-methyl)-amino)-butyric acid methyl ester.    USE - Preparation of valsartan (salt) used in pharmaceutical composition for treating high blood pressure and cardiac insufficiency.    ADVANTAGE - The method enables preparation of valsartan with high purity, by simple, economical, and environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of valsartan (salt) involves reacting 2-((2'-cyano-biphenyl-4-yl-methyl)-amino)-3-methyl-butyric acid methyl ester hydrochloride of formula (I) with valeryl chloride in presence of a base and a solvent, obtaining 2-((2'-cyano-biphenyl-4-yl-methyl)pentanoylamino)-3-methyl-butyric acid methyl ester of formula (II), reacting 2-((2'-cyano-biphenyl-4-yl-methyl)pentanoylamino)-3-methyl-butyric acid methyl ester with metal azide in the presence of trialkyltin chloride, obtaining 3-methyl-2-(pentanoyl-(2'-(1H-tetrazol-5-yl)-biphenyl-4-yl-methyl)amino)-butyric acid methyl ester of formula (III), hydrolyzing 3-methyl-2-(pentanoyl-(2'-(1H-tetrazol-5-y1)-biphenyl-4-yl-methyl)amino)-butyric acid methyl ester in the presence of a base under pressure, obtaining valsartan without isolating the intermediates, and converting valsartan to its salt.
NOVELTY - Preparation of bromhexine hydrochloride comprises carrying out reductive amination step synthesis-bromhexine free alkali of 2-amino-3,5-dibromobenzaldehyde and N-methylcyclohexyl amine as raw materials in the presence of a catalyst and a reducing agent; and reacting bromhexine salt into the free alkali with hydrogen chloride salt formation reagent to prepare bromhexine hydrochloride.    USE - Method for preparing bromhexine hydrochloride (claimed).    ADVANTAGE - The method reduces reaction steps, shortens production period, increases reaction yield, reduces production cost, has mild reaction condition, and is environment-friendly.
NOVELTY - The utility model is new type provides one kind cutting, fermentation, sterilization and integrated animal corpse treatment device, it can use again in processing animal corpse and at the same time. The device comprises tube, two end respectively connected tube and left end plate and right end plate, upper tube side wall set with feed opening, also comprises heating system and the connection oil slot, inner tube provided with cutting knife, cutting knife comprises bucket wall and tube inside wall connected cutter and the cutter set on the main shaft on the main shaft. The utility model is new type bucket wall by knife and cutter main shaft body for cutting, wherein in tube added with biological fungus, through oil groove to carry out heating tube, make biological fungus start work, at last taking corpse decomposing as can use the efficient organic fertilizer. At the same time in process of body, it can make body obtained using again, and process of smoke, odour, accord with environment-friendly new standard.
NOVELTY - The new type utility claims have one kind animal excrement treatment device, comprises excrement collected pool, collected urine pool, regulating pool, urine separating machine, fermentation room, drying tank, and outlet end of collected manure pool and inlet end of separating machine connected with urine, stool and urine separating machine and solid-phase outlet terminal and inlet terminal of regulating pool connected, outlet end of regulating pool and inlet end of fermentation room connected with the outlet end of fermentation room and inlet end of drying tank connected with the outlet end of drying tank and inlet end of cd machine connected with the urine separating machine and liquid phase outlet end and inlet end of urine collecting pool connected, outlet end of urine collecting pool and bottom inlet end of fermentation room connected with. The utility model is new type through to carry out fermentation and livestock excrement particle drying treatment after, make the conversion as can use the organic matter wastes is used as soil improvement agent use, simple technique, easy operation, no season limit, no second time pollute, production period short, with the obvious economic benefit, finish have vibration livestock excrement by weight and resource for the target.
NOVELTY - The utility model is new type supply one kind animal corpse harmless treatment device of heating system, using heat conducting oil for heating, heating performance, small floor space small. The heating system comprises tube, temperature sensor and liquid level switch, tube top part and bucket cover connected and lower tube part is connected with supporting leg and bucket plate, inner tube provided with the heat conducting oil, the tube inner cavity body set with heater and filter, filter and discharge oil pipe connection, after the inner oil pipe and oil pipe through carrying on bucket cover extends into the tube, for oil pipe through oil pump and oil sending pipe connection, oil sending pipe formed in an upper plate. The utility model is new type internal fill heat conducting oil as heat medium, heating uniformly, main component integrated on internal tube, small volume, and the utility of new type set have heat preservation cotton, make heat preservation property is enhanced tube, it can save energy.
NOVELTY - The new type utility claims have one plant soft capsule drying device, comprising motor, dehumidifying device, drying room, an exhaust fan, a housing, said housing provided with several internal dry room, on the drying room set with several yarn disc, housing top part and wind wind channel phase connection, another end wind channel and wind and dehumidifying device connected with each, the wind in wind channel provided with an exhaust fan, the dehumidifying device and the return air channel connected with each, the return air channel end and another housing connected with the motor and the dehumidifying device connected with each, the housing upper inner wall mounted with radiator. The utility model is new type by drying room, wind channel wind, dehumidifying device, the return air channel form one of air flow loop, the plant using dry method and air loop, simple operation, small noise, high percent of pass, low energy consumption, capsule drying device is one kind of environment-friendly energy saving.
NOVELTY - The new type utility claims have one kind novel straw fermentation pool, is square and comprises pool body, the pool body frontage provided with open mouth, adjacent two side opening is opened with an air inlet and an air outlet respectively, the inner side the pool body top part fixed with out water device and temperature control device, the pool body wall provided with inner insulating layer and a data phase corresponding to the strip groove, in groove insert clapboard, pool body bottom fixedly connected with roller. The utility model is new type can full utilize earthworm, for cultivation waste and crop straw by biodegradation and conversion of earthworm, become can directly use the organic agricultural fertilizer, and automatic degree high, suitable, simple use, fit in rural popularization and use.
NOVELTY - The new type utility claims one kind biologic organic fertilizer manure, wherein comprising a machine body, a perforated plate vibration, air distribution pipe, fan and hoisting machine, the upper machine body of internal spring base connected with fixed punched by vibration, upper spring seat set with vibration motor, the machine body has set with discharging mouth, the discharging mouth to set with gate valve, feed hopper and hoisting machine and discharging mouth connected with the blanking pipe is connected with hoisting machine to shake blanking punching plate upper part, a machine body also set with internal annular bellows and centre pipe, annular air box and centre pipe through air distribution pipe and connected with the fan. The utility model is new type structure is simple, suitable operation, turning completely, small square meter small, manufacturing cost low, fit in small type organic fertilizer turning process use.
NOVELTY - An organic fertilizer producing device, wherein A comprises a tank body, the tank body one end has cover and equipped with transmission teeth, said cover set with an air outlet pipe, the transmission teeth connect with one of transmission pedestal, shaft base tank body another end through the support shaft mounted on the whole can go up and down and one up, the tank body is double-layer hollow structure, the tank body side wall set with interlayer and connected with the infusion pipe, inside the tank body set with one of said tank body and fixedly connected with the stirring shaft, the stirring shaft formed with a inclined guide multi-blade. A plant organic fertilizer production device the utility new type of supply is, no need to use the special turning device, greatly reducing production cost, and can avoid the pollute gas.
NOVELTY - A plant organic fertilizer fermentation tank, comprising one of the tank body, the tank body one end has cover and equipped with transmission teeth, said cover set with an air outlet pipe, the transmission teeth connect with one of transmission pedestal, shaft base tank body another end through the support shaft mounted on the whole can go up and down and one up, the tank body is double-layer hollow structure, the tank body side wall set with interlayer and connected with the infusion pipe, inside the tank body set with one of said tank body and fixedly connected with the stirring shaft, the stirring shaft set with S-shaped stirring leaf. The utility model is new type of providing one kind of organic fertilizer fermentation tank, no need to use the special turning device, greatly reducing production cost, and can avoid the pollute gas.
NOVELTY - A plant organic fertilizer production device, it comprises one of stainless steel tank body, the tank body one end has cover and equipped with transmission teeth, said cover set with an air outlet pipe, the transmission teeth connect with one of transmission pedestal, shaft base tank body another end through the support shaft mounted on the whole can go up and down and one up, the tank body is double-layer hollow structure, the tank body side wall formed with one pair and interlayer connected with the infusion pipe, inside the tank body set with one of said tank body and fixedly connected with the stirring shaft, the stirring shaft with multi-set with one inclined guide blade. A plant organic fertilizer production device the utility new type of supply is, no need to use the special turning device, greatly reducing production cost, and can avoid the pollute gas.
NOVELTY - The utility model relates to a fermentation method and device, especially relates to an integrated high concentration dry anaerobic fermentation device, the bottom discharging machine (1) mounted in inner chamber (9), the spiral transport device (2) by movable bottom discharging machine (1) drive, one end set in the upper storage bin (9) is inner groove, another end set in dry fermentation pool (3) and the terminal enter material mouth, dry fermentation pool (3) bottom end of collecting groove (31) through pipeline connected to the vacuum continuous discharging device (6) enter the inlet, continuous vacuum discharging device (6) and discharging mouth connected to solid-liquid separating machine (10), the solid-liquid separating machine (10) is connected below the marsh liquid pool (11) equal characteristic. Using the utility new type marsh gas fermentation, increase have yield tank, saves. square meter floor space and investment cost of fermentation device, reducing maintenance operation cost, steady, and raw material reaction complete after marsh liquid amount less, reducing have post treatment and biogas slurry;
NOVELTY - The utility model relates to straw cutting device, specifically a straw cutting device for marsh gas producing, comprising working chamber (1), heater (2), conveyor belt (3), belt pulley (4), bracket (5), motor (6), roller (7); said working chamber (1), specifically is opening structure, one end set with bracket (5), said working chamber (1), the internal set with heater (2), conveying belt (3), roller (7), thereof heater (2) set with one end upper wall of working chamber (1), conveyor belt (3) located lower part of heater (2), roller (7) equipped with one end of conveyor belt (3), another end of conveyor belt (3) extending out entrance of working chamber (1) set on bracket (5), and the main shaft and belt pulley (4) matching connected, lower part of said bracket (5) equipped with motor (6), and main shaft of motor (6) through belt and belt wheel (4) matching connected.
NOVELTY - A biomass steam blasting device, belonging to biomass energy technology field, the device comprises steam-exploded tank, steam-exploded tank upper part set with material inlet, lower part set with steam inlet and material outlet, a steam inlet and steam tank through pipeline connected with the steam generator, material outlet of steam tank through pipeline connected with receiving tank, receiving tank is cyclone separator, a cyclone separator comprises tube and the gas phase outlet tube of upper part, a solid phase outlet, upper tube side wall and provided with material outlet of each steam tank connected the material inlet, the lower tube and provided with solid phase outlet corresponding the washing tank. The structure is simple, the design is reasonable, the gas phase after finish have the mixture after steam explosion finish sum solid separation and separating to obtain full of circulation use, effective to avoid have pollute and energy waste for the environment, reach to have energy saving, water saving, emission reduction and goal.
NOVELTY - The utility model claims a novel angle relux mixing type anaerobic fermentation tank, belonging to fermentation equipment field, said device comprises the tank body, an exhaust port, a stirring device, driving device, spray device, conduit, a discharging mouth, a screw rod pump, extraction tube, heating coil, a feeding port, equipped with strong cutting action with mechanical stirring in the fermentation tank, large particle diameter object and dispersing solid and liquid and the full mixing, and avoid generating crust. biogas slurry extraction tank bottom tube and tank body to force the liquid product flow of internal circle direction in the following extraction function of screw pump, forming liquid stirring, strong cutting effect small, which avoids the damage to methane fungus have the mechanical stirring and the slurry extraction tube stirrer extraction liquid form the liquid relux stirring effect together, forming full mixing stirring, increase have stirring effect, effective reduce have stirring consume power, the utility model is new type structure is simple, suitable operation, which is good for popularization.
NOVELTY - The utility model claims an integrated straw marsh gas pool with closeness pipe feeding, comprising an aggregate pool, a straw pre-processing pool and a straw Anaerobic digestion pool; the aggregate pool is formed at the external side of the anaerobic straw digestion pool, equipped with an inner solid-liquid mixed ejector at the solid-liquid mixed ejector with a biogas slurry inlet A, B inlet and mixed material outlet C, biogas slurry inlet A is connected with biogas slurry pipe, upper part of biogas slurry pipe in straw Anaerobic digestion pool and clean water layer, rear lower part connected with the straw Anaerobic digestion pool outside the pipeline pump connected with biogas slurry inlet A, B and collected material inlet pool connected, mixed material outlet C connected with feeding pipe, another feeding pipe is connected with on end of straw pre-processing pool and loading releasing mouth, straw pre-processing pool at internal upper part setting pool of Anaerobic digestion. The biogas pool structure is simple, it saves energy and operation cost low, fermentation period short, efficiency is high, can effective solve the straw marsh gas pool problem crust.
NOVELTY - The utility model claims a marsh gas automatic monitoring controller, belonging to new energy technology field. The marsh gas automatic monitoring controller comprises a main control unit, an alarm system, a touching screen, a check device and a valve pump system, wherein the alarm system, the touching screen, the check device and the valve system are respectively connected with pump and main control unit, the detecting device comprises a temperature sensor, PH value sensor, oxidation-reduction potential sensor, flow rate sensor and methane concentration sensor, the valve pump system comprises solenoid valve, the raw material pump, hot water pump and neutralizing agent pump, and marsh gas fermentation tank by pipeline are connected. The utility model is new type finish have marsh gas production full process is automatic control, can increase production rate, reduce use cost, ensuring safe production, by use of touching screen, using operation is simple and clear.
NOVELTY - Production of granular microbial organic fertilizer comprises grinding peat coal into particles with size of 2-5 mm, removing impurities, drying at 70 degrees C for 2 hours until water content is 20%, and reducing toxins in peat coal; activating with 10% hydrochloric acid solution to acidify insoluble humate salts into humic acids, and neutralizing with 28% ammonium hydroxide solution to alkalize humic acids into water-soluble ammonium humate; and adding microbial composition, mixing, and granulating.    USE - Method for producing granular microbial organic fertilizer from peat coal.
NOVELTY - A low carbon vehicle fuel comprises 900 pts. wt. methanol, 2 pts. wt. isopropyl ether, 3 pts. wt. isopropyl alcohol used as anti-cryogenic agent, 5 pts. wt. ethylene glycol used as activator, 20 pts. wt. butyl acetate, 50 pts. wt. methyl tert-butyl ether used as uprising solvent, 5 pts. wt. sodium hydroxide used as denaturant, 5 pts. wt. tetrachloroethylene used as cleaning agent, 0.5 pts. wt. benzotriazole used as preservative, 0.5 pts. wt. antioxidant, 2 pts. wt. refined castor oil used as lubricant, 2 pts. wt. ethanolamine and 5 pts. wt. catalyst.    USE - Environmentally-friendly low carbon vehicle fuel (claimed).    ADVANTAGE - The low carbon vehicle fuel is economical and environmentally-friendly, and has excellent combustion effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of low carbon vehicle fuel, which involves adding 900 pts. wt. methanol into reactor, adding catalyst, curing agent and other raw materials, stirring for 2 hours and adding additive to reaction vessel.
NOVELTY - Preparing biodiesel involves mixing 50-90 a1 biological diesel oil, 10-30 a1 methanol, 0-20 a1 standard diesel oil, 5-30 a1 auxiliary agent, biologic diesel oil and 1-5 a1 alicyclic alcohol to obtain mixture. Isopropyl acid, hydrochloric acid and potassium permanganate are added to mixture, and then processed to obtain the desired product.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method enables to prepare biodiesel in a simple and cost-effective manner.
NOVELTY - Method for preparing bio-organic fertilizer, involves crushing straw, adjusting carbon and nitrogen ratio to 20 and moisture content to 60%, sprinkling strain on the straw, mixing, forming the mixture into pile to width of 1.5-2 m, height of 0.8-1 m, and suitable length, fermenting at 60 degrees C or more for 12-15 days, turning once every 6-7 days, adjusting moisture content to 30-40%, sieving, adding trace elements, biological agents and nitrogen, phosphorus and potassium (NPK)-35%, granulating the mixture and forming the granules into ball shape.    USE - The method is used for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method consumes less time. The fertilizer has effective viable cell count of more than 50 million/g, and high humic acid content.
NOVELTY - Biomass briquette comprises 50-75 pts. wt. bituminous coal, 20-40 pts. wt. clay, 5-10 pts. wt. pine, 2-4 pts. wt. dispersing agent and 1-2 pts. wt. curing agent.    USE - Biomass briquette.    ADVANTAGE - The biomass briquette is prepared on large scale.
NOVELTY - Biomass pellet fuel comprises biomass raw material and additive, where the additive is mixture of calcium carbonate and magnesium carbonate.    USE - Biomass pellet fuel.    ADVANTAGE - The biomass pellet fuel ensures good combustion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass pellet fuel, which involves using biomass raw material and additive.
NOVELTY - Gasoline composition comprises 40-50 pts. wt. ethanol, 20-30 pts. wt. methanol, 5-10 pts. wt. potassium chloride, 10-15 pts. wt. octane, 1-5 pts. wt. benzyl alcohol and 5-10 pts. wt. aromatic hydrocarbon.    USE - Gasoline composition.    ADVANTAGE - The gasoline composition ensures complete combustion, and increases heat efficiency and reduces oil consumption.
NOVELTY - The utility model is new type providing one kind environment-friendly odourless organic fertilizer production line, comprising fermentation device, package device, wherein also comprising the raw material storage pool, closeness transport device, fermentation device, second time oxygen fermentation device and waste sum processing device. The utility model is new type supply and production line, have smell raw material storage pool, fermentation and second time fermentation device can complete the raw material fermentation, closeness transport device can ensure that the smell of the raw material transport process, in addition also comprise have waste gas processing system, will smell and harmful gas by discharging processing production line, make whole strip production line smell and environment-friendly.
NOVELTY - Preparation of black fruit wolfberry biological fertilizer comprises taking Bacillus subtilis (CICC: 10339) with 109-1010 density; and taking black fruit wolfberry, cutting into small pieces, spraying bacterial suspension, and fermenting.    USE - Method for preparing black fruit wolfberry biological fertilizer used for preventing pathological fungi (claimed).    ADVANTAGE - The simple method increases yield, ensures no wastewater discharge and easy operation, and fits industrial large scale production. It has low investment requirement, low energy consumption, and good economic benefit.
NOVELTY - Preparation of biologic fertilizer comprises taking Bacillus subtilis (CICC: 10339) culture with 109-1010 cfu/ml density to get high density fungus suspension liquid; and cutting red fruit medlar plant into small sections, spraying high density fungus suspension liquid, and fermenting.    USE - Method for preparing biologic fertilizer used for inhibiting medlar pathology fungi (claimed).    ADVANTAGE - The simple method has no wastewater discharge, low investment, low energy consumption, easy operation, and good economic benefit and wide application. It fits for industrial large scale production.
NOVELTY - Special fertilizer comprises nitrogen-phosphorus pentoxide-potassium oxide at mass ratio of 5:5:5, 100 kg/ton oil, 150 kg fermented distillers grains, 500 kg organic fertilizer, 50 kg urea, 150 kg calcium superphosphate and 50 kg potassium sulfate.    USE - Special fertilizer for Dendrobium nobile (claimed).    ADVANTAGE - The product promotes nutrient absorption of seedlings.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of special fertilizer comprising preparing the planting site with elevation of 300-800 m, relative humidity of 75-80%, shading area of 55-70% with water near the national secondary standard, planting from March 10th to April 10th with spacing of 30 cm by 30 cm, preparing 50 lbs. fresh cow dung, planted seedlings with density of 30 cm by 30 cm, pulling off moss, seedling roots and surface stone where seedling stem base is above 1.5-2.5 cm, diluting cow dung with water to obtain manure slurry, brushing around the roots, affixing live moss to the plant roots and cow dung slurry, germinating, allowing growth of new roots, installing stone with surface slope of greater than or equal to 30? to prevent slipping moss, stabilizing temperature at greater than or equal to 16 degrees C to allow Dendrobium rapid growth and development, spraying with foliar fertilizer A or B every 15 days to promote plant germination and new shoots, applying high nitrogen content fertilizer every 15 days, applying special fertilizer to improve every 10 days and continuously spraying for 3-4 times.
NOVELTY - Production of bifenthrin (I) comprises reacting 3-(2-chloro-3,3,3-trifluoro-1-propenyl)-2,2-dimethyl-cyclopropanecarboxylic acid halide (Ia) and 2-methyl-3-biphenylmethanol (Ib) with halogenated hydrogen solvent or mixed solvent, vacuumizing, cooling, and crystallizing.    USE - Method for producing bifenthrin (claimed).    ADVANTAGE - The method is simple and reduces waste emissions.    DETAILED DESCRIPTION - Production of bifenthrin of formula (I) comprises reacting 3-(2-chloro-3,3,3-trifluoro-1-propenyl)-2,2-dimethyl-cyclopropanecarboxylic acid halide of formula (Ia) and 2-methyl-3-biphenylmethanol of formula (Ib) with halogenated hydrogen solvent or mixed solvent, vacuumizing, cooling, and crystallizing.    X=Cl or Br.
NOVELTY - A taurine separation and extraction method comprises removing ammonia, adding neutralizing agent, reacting, carrying out low temperature crystallization, separating, filtering, producing sodium sulfite or sodium bisulfite, and recycling.    USE - Method for separation and extraction of taurine (claimed).    ADVANTAGE - The method is environment-friendly, energy efficient and suitable for industrialization. It has high product yield and quality.
NOVELTY - A desvenlafaxine hydrochloride is prepared by dissolving venlafaxine hydrochloride into methanesulfonic acid, and adding demethylation reagent methionine.    USE - Method for preparing desvenlafaxine hydrochloride (claimed).    ADVANTAGE - The method is green and environment-friendly, has no high temperature, less by-product, good product quality, yield of more than 88% and purity of 99.9%.
NOVELTY - Synthesis of scopolamine comprises taking toluene derivative (IV), carrying out acylation reaction with methylnitrene derivative (III) to obtain scopolamine compound (II) where scopolamine compound (II) is obtained by epoxidation of L-scopolamine, hydrochloride, hydrobromide or p-toluenesulfonate.    USE - Method for synthesizing scopolamine (claimed).    ADVANTAGE - The method is simple and has high yield and produces less harmful substances. The product has high purity.    DETAILED DESCRIPTION - Synthesis of scopolamine comprises taking toluene derivative of formula (IV), carrying out acylation reaction with methylnitrene derivative of formula (III) to obtain scopolamine compound of formula (II) where scopolamine compound of formula (II) is obtained by epoxidation of L-scopolamine, hydrochloride, hydrobromide or p-toluenesulfonate.
NOVELTY - Downstream fluidized bed reactor (1) has high aspect ratio of 20-100, average gas velocity of 3-18 meter per second, and comprises catalyst inlet (2), heavy oil injection port (3), multiple light hydrocarbons inlets (4a,4b,4c,4d,4e) and reactor outlet (5). The distance between the first heavy oil reactor and light hydrocarbon injection port is 3-10 times the diameter. The distance from the entrance between different light hydrocarbons is 2-10 times the reactor diameter.    USE - Downstream fluidized bed reactor used in heavy oil reactor (claimed).    ADVANTAGE - The downstream fluidized bed reactor is simple, cost-effective, has high product value and low catalyst coke rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a downstream fluidized bed reactor. (Drawing includes non-English language text).    Fluidized bed reactor (1)    Catalyst inlet (2)    Injection port (3)    Light hydrocarbons inlets (4a,4b,4c,4d,4e)    Reactor outlet (5)
NOVELTY - The preparation method of biodiesel using quaternary phosphonium-based ionic liquid as catalyst involves preprocessing ionic liquid, adding sodium methylate to preprocessed ionic liquid, vigorously stirring, adding methanol and soybean oil to stirred mixture, stirring and distilling methanol using distilling device.    USE - The method is useful for preparation of biodiesel using quaternary phosphonium-based ionic liquid as catalyst (claimed).    ADVANTAGE - The method enables simple and energy-efficient preparation of biodiesel at high rate using ionic liquid catalyst having excellent catalytic effect.
NOVELTY - Processing municipal wastewater and producing grease by (a) expanding microalgae in culture medium and increasing cell density of microalgae, (b) immobilizing cultured microalgae in log phase in solvent mixture, adding calcium chloride dropwise to mixture to obtain immobilized alginate beads, (c) adding immobilized alginate beads to municipal wastewater and culturing in two stages, where the first stage culturing process is semi-continuous culture, and the second stage culturing process is batch culture, inducing microalgae grease accumulation, and recovering alginate beads.    USE - The method is useful for processing municipal wastewater and producing grease (claimed).    ADVANTAGE - The method extracts nutrients from wastewater.    DETAILED DESCRIPTION - Processing municipal wastewater and producing grease by (a) expanding microalgae in culture medium and increasing cell density of microalgae, (b) immobilizing cultured microalgae in log phase in solvent mixture, adding calcium chloride dropwise to mixture to obtain immobilized alginate beads, (c) adding immobilized alginate beads to municipal wastewater and culturing in two stages, where the first stage culturing process is semi-continuous culture, wastewater is updated, and microalgae production rate is increased, and the second stage culturing process is batch culture, inducing microalgae grease accumulation, and recovering alginate beads.
NOVELTY - The preparation method of oxysophoridine using microbial strain involves adding microbial strain under a preservation number of CCTCC M 2014660 to alkali, uniformly mixing, and reacting. The microbial strain is deposited in China type culture collection.    USE - The method is useful for preparation of oxysophoridine using microbial strain (claimed).    ADVANTAGE - The method enables simple and economical preparation of oxysophoridine with excellent catalytic performance and selectivity in an environmentally-friendly manner.
NOVELTY - The new type utility claims have one kind reusing garbage organics, comprising frame, smashing treatment device, extrusion dehydration device, a distribution box, oil water separating device and fermentation chamber, the smashing treatment device is in place and frame position is close to the position of the top part, the extrusion dehydration device set under the smashing processing device, set with oil water separation device and fermentation chamber, smashing treatment device for garbage pre-processing process, and later for smashing garbage is sent to the extrusion dehydration device at lower part of extrusion dehydration device, separate the extrusion dehydration device out of the oil water mixture enter into oil water separating device, after extrusion of solid garbage to enter into fermentation chamber, oil water mixture from oil water mixture inlet to enter into the box body in the oil liquid from oil liquid discharging outlet, then waste water and waste water discharging outlet, that have oil water separation problem from the box body bottom.
NOVELTY - A roller type aerobic compost reactor plant, comprises roller main body, roller main shaft, machine frame, motor, speed reducer and transmission mechanism, tube inner side set with the inside lining layer is divided to be multiple partition of inside lining layer, and each individual compartment respectively provided with corresponding to the air inlet pipe, discharge pipe and water outlet. Two end provided with ventilating tube and the drainage pipeline system, through air inlet pipe to control and valve on the discharge pipe, realize ventilating direction is always blown from stacking in the following side roller, roller on discharging side. At the same time, anti-relux design of lining layer of compartment in roller, reducing compost process of stacking would produce water and the subsequent discharging roller rotate then the stack material in relux. Using roller reactor of the plant design, it can make the ventilating roller reactor more uniform full, using material and in compost process property is more uniform, so as to increase quality and effect and compost product is compost treatment.
NOVELTY - The utility model claims a dual-cylinder binding straw marsh gas pool, feedstock tube, discharging tube, fermentation pipeline, composed of marsh gas pool main body, pipe horizontal placing for fermentation, feedstock pipe incline set and fermentation pipeline and connected with discharging pipe vertical well and placing for fermentation pipeline connected with, in a double end connected and the pipe centre axis direction set fermented fermentation pipeline at the top of the water pressure and feedstock pipe side wall and discharge tube side wall connected, on fermentation pipeline connected with gas-guide tube, straw more suitable feedstock, straight cylinder pipe make fermented fermentation route of straw to obtain enlargement, the whole multi-pipe air removing gas and ensure smooth, not easy to be blocked, the utility model is new type reasonable structure, the whole marsh gas pool can use glass steel material is made of PVC pipe or connection.
NOVELTY - A bio-fuel composition comprises 15-25 wt.% bio-oil, 50-60 wt.% 1-5C lower alcohol and 18-26 wt.% cetane number improver.    USE - Bio-fuel composition is used for bio crude oil for diesel engine.
NOVELTY - The utility model is new type relates to one kind organic fertilizer type dumper comprises the top steel frame, a chain wheel base, chain wheel, driving, bracket, a transverse moving wheel, a driven chain wheel, a track and turning device, said top steel frame bottom welding with connecting beam, the connecting beam part mounting surface with number one chain wheel base, on the number one chain wheel base mounted with driving chain wheel, the lower part connected with the welding beam has, below the top of the steel frame is fixedly connected with bracket, the bracket and the right side suspension, said stand number as number four, and the right part of bottom bracket provided with number two chain wheel base and the second wheel base mounted with the driven chain wheel, the lower part the bracket mounted with the transverse moving wheel, the transverse moving wheel lower part set with track, the track number is two, the middle part mounted with suspension beam turning device. The utility model is new type can make organic fertilizer completely, using fungus and raw material full contact, so as to promote fermentation completely decomposed.
NOVELTY - Mycorrhizae-based biofertilizer consortium comprises (a) air dried roots colonized with mycelia of ectomycorrhiza and arbuscular mycorrhizal fungus (AMF), and vesicles of AM, (b) air dried mycelia of AMF and ectomycorrhizae, and (c) air dried spores of AMF.    USE - The mycorrhizae-based biofertilizer consortium is useful as biofetilizing agent, plant growth enhancer, plant growth promoter, and biocontrol agent (claimed). The mycorrhizae-based biofertilizer consortium is useful for reclamation of industrially created wastelands.    ADVANTAGE - The mycorrhizae-based biofertilizer consortium is cost-effective and environmentally-friendly, and enables to increase tolerance against soil stresses such as heavy metal toxicity, salinity, drought, and high soil temperatures in plants, and increases survival rate of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biofertilizer consortium, which involves (a) isolating and selecting pregrown ectomycorrhizae, (b) performing transformation, (c) adding AM to the hairy roots, (d) adding pregrown ectomycorrhizae obtained from the step (a) to colonized hairy roots obtained from the step (c), (e) incubating mixture, (f) regularly subculturing plates containing the hairy roots, the AM and the ectomycorrhizae to obtain multiple copies, (g) harvesting, and (e) air drying to obtain the product.
NOVELTY - A refinery gas 2-3C components light hydrocarbon and hydrogen recovery method comprises taking refinery dry gas, condensing at - 15 to 0 degrees C, recovering liquid light hydrocarbon component, passing non-condensed refinery dry gas into temperature swing adsorption column, absorbing 4-6C components, passing into pressure swing adsorption column, absorbing 2-3C components, entering into separation device, separating, and purifying.    USE - Refinery gas 2-3C components light hydrocarbon and hydrogen recovery method (claimed).
NOVELTY - Processing kitchen waste involves separating food waste using solid-liquid separating apparatus. The solids are separated from liquid. The liquid is collected in a container. The solid is crushed in crusher.    USE - Method for processing kitchen waste (claimed).    ADVANTAGE - The method enables to process kitchen waste in effective manner without polluting environment.
NOVELTY - Kitchen garbage anaerobic fermentation bucket comprises outer bucket (1), inner bucket (2) and solar energy panel (3). The outer bucket bottom is set with low pressure sheet (4), constant temperature controller (5) and radiating fan. The solar energy panel provides electric energy to low pressure electric heat piece. The radiating fan adjusts the outer jacket temperature. The inner bucket cover is set with discharging on inner bucket and internal gas exhaust valve.    USE - Kitchen garbage anaerobic fermentation bucket.    ADVANTAGE - The kitchen garbage anaerobic fermentation bucket converts kitchen waste into resource ensures reduced pollutant discharge and simple operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a kitchen garbage anaerobic fermentation bucket.    Outer bucket (1)    Inner bucket (2)    Solar energy panel (3)    Low pressure sheet (4)    Constant temperature controller (5)
NOVELTY - Biological fertilizer comprises 8-10 pts. wt. edible mushroom, 15-20 pts. wt. plant fiber, 12-15 pts. wt. chicken manure, 25-30 pts. wt. cow dung, 5-7 pts. wt. cotton seed hull powder, 4-6 pts. wt. biogas residue, 1.5-2.5 pts. wt. Trichoderma, 0.5-1.5 pts. wt. Aeromonas, 18-20 pts. wt. humic acid, 14-16 pts. wt. aqueous solution of trace elements and 1.5-2 pts. wt. complex biological bacterial composition.    USE - Biological fertilizer used for cultivating field crop, vegetable, melon, fruit, tea, Chinese herbal medicine, flower and nursery.    ADVANTAGE - The biological fertilizer reduces crop pest and weed generation, increases production and improves product quality in green and environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological fertilizer, which involves;    (A) fermenting mixture of edible fungus, cellulose, dairy manure, cotton seed hull powder, biogas residue, Trichoderma fungus and Aeromonas at 50-65 degrees C for 28-32 days;    (B) drying fermented materials at 28-32 degrees C;    (C) crushing dry materials;    (D) mixing humic acid, trace element solution and composite biological bacterial composition;    (E) fermenting obtained mixture for 6-8 days at 30-40 degrees C; and    (F) drying, mixing and granulating fermented materials to obtain product.    .
NOVELTY - Preparing organic fertilizer involves mixing 30-50 pts. wt. dairy manure, 30-50 pts. wt. chicken manure, 60-70 pts. wt. cassava residue, 10-15 pts. wt. beef, 10-15 pts. wt. mud filtrate, 2-5 pts. wt. tea cypress, bactericide and metal passivating agent uniformly for 1-24 hours. The obtained mixture is fermented with microbial inoculum and brown sugar aerobically in summer for 15-20 days, and in winter for 25-30 days. The fermented material is further fermented in anaerobically for 5-9 days. The fermented material is crushed and sieved to obtain granular organic fertilizer powder.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that kills pathogen, eliminates odor and reduces water content, volume and weight, and ensures increased nutrient content and quick action.
NOVELTY - Organic material heating transport device comprises heating device and transport device connected with pipe (11). The transport device comprises groove (1) and internal cylinder that is provided with stirring device (2) and terminal device. The groove bottom is connected with pipe. The lower output transport device is provided with multiple fermentation groove (6). The heating device also comprises hot air furnace (8) connected with pressurizing device (9) and check valve.    USE - Organic material heating transport device used in winter season for fermentation.    ADVANTAGE - The organic material heating transport device is effective and simple, and ensures uniform and efficient heating.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a organic material heating transport device.    Groove (1)    Stirring device (2)    Fermentation groove (6)    Hot air furnace (8)    Pressurizing device (9)    Pipe (11)
NOVELTY - Compound microbial fertilizer comprises microbial fermentation agent, complex nutrient, pullulan and polyglutamic acid, where microbial fermentation agent is Bacillus megaterium, Bacillus amyloliquefaciens, Bacillus thuringiensis, Bacillus subtilis and Azotobacter broth in mass ratio of 1:1:1:1:1. The complex nutrient includes nitrogen, phosphorus, potassium, trace elements, organic matter and complex amino acids.    USE - Compound microbial fertilizer.    ADVANTAGE - The compound microbial fertilizer is environment-friendly and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing compound microbial fertilizer, which involves;    (A) mixing raw materials in appropriate mass ratio thoroughly;    (B) UV-sterilizing obtained mixture to obtain product;    (C) labelling plastic bottle; and    (D) filling obtained product in labeled plastic bottle.    .
NOVELTY - A carbonized straw flower fertilizer comprises 5-10 pts. wt. gypsum powder, 1-2 pts. wt. urea, 10-15 pts. wt. attapulgite, 30-40 pts. wt. castor husk, 20-25 pts. wt. rapeseed cake, 30-50 pts. wt. pig feces, 20-30 pts. wt. reed stalk, 25-40 pts. wt. rice straw, 10-15 pts. wt. ammonium sulfate, 20-25 pts. wt. phosphorus pentoxide, 25-40 pts. wt. phosphate rock, 15-20 pts. wt. potassium chloride, 4-5 pts. wt. crosslinking agent and remainder of water.    USE - Carbonized straw flower fertilizer (claimed).    ADVANTAGE - The carbonized straw flower fertilizer improves water retention and permeability of fertilizer package, and regulates soil temperature and humidity.    DETAILED DESCRIPTION - A carbonized straw flower fertilizer comprises 5-10 pts. wt. gypsum powder, 1-2 pts. wt. urea, 10-15 pts. wt. attapulgite, 30-40 pts. wt. castor husk, 20-25 pts. wt. rapeseed cake, 30-50 pts. wt. pig feces, 20-30 pts. wt. reed stalk, 25-40 pts. wt. rice straw, 10-15 pts. wt. ammonium sulfate, 20-25 pts. wt. phosphorus pentoxide, 25-40 pts. wt. phosphate rock, 15-20 pts. wt. potassium chloride, 4-5 pts. wt. crosslinking agent and remainder of water. The crosslinking agent comprises 8-10 pts. wt. acrylamide, 2-3 pts. wt. ethylene glycol dimethacrylate, 2-4 pts. wt. glycerin, 10-15 pts. wt. limestone, 5-8 pts. wt. ethanol, 2-4 pts. wt. sodium dodecyl sulfate, 12-16 pts. wt. industrial castor oil and remainder of water. The crosslinking agent is prepared by dissolving ethylene glycol dimethacrylate in ethanol diluted with water, adding limestone powder having particle size of 200-250 mesh, glycerin, sodium dodecyl sulfate, industrial castor oil and water, stirring for 20-30 minutes, adding solution of acrylamide to the obtained emulsion, and stirring at 70-90 degrees C for 30-40 minutes. An INDEPENDENT CLAIM is included for preparation of carbonized straw flower fertilizer.
NOVELTY - Preparing horticulture matrix involves crushing Amorpha branches to obtain powder that is mixed with organic fertilizer, urea and enzyme carboxymethyl cellulose enzyme uniformly at 10-40 degrees C. The obtained mixture is fermented, and then mixed with perlite and vermiculite to obtain product.    USE - Method for preparing horticulture matrix (claimed).    ADVANTAGE - The method enables to prepare horticulture matrix in low cost.
NOVELTY - Nutrient soil composition comprises 1200-1400 pts. wt. red soil and 400-500 pts. wt. Pennisetum litter powder.    USE - Nutrient soil composition used for planting Paris polyphylla (claimed).    ADVANTAGE - The method enables to prepare nutrient soil composition that protects farmland environment, and ensures low cost preparation and large scale industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutrient soil composition, which involves;    (A) drying and crushing Pennisetum to obtain powder;    (B) basking red soil in sunlight for 2-3 days;    (C) mixing water, salt solution, gray mold fungicide to obtain fungicide aqueous solution preparation;    (D) mixing red soil, Pennisetum litter powder, salt aqueous solution, gray mold fungicide aqueous solution and lime uniformly to obtain mixed nutrient soil;    (E) covering mixed nutrition soil for 3-5 days;    (F) fermenting nutrient soil; and    (G) regulating pH of fermented materials to 7.5-8.0 to obtain product.    .
NOVELTY - Preparing slow release organic fertilizer involves dissolving 1kg sodium alginate in 60L phosphoric acid buffer solution (pH=7.0) to obtain sodium alginate solution that is reacted with methanolic solution of n-hexylamine or n-heptyl amine at 70-90 degrees C for 3-5 hours. Sodium cyanoborohydride (0.1lkg) is stirred with obtained solution at room temperature for 0.5 hours. The reaction product is precipitated with methanol. The precipitate is dissolved in water, and then freeze-dried. An organic amine-modified alginate synergist, 1-1.5kg calcium carbonate, 10-20kg urea and 1-3kg pine needle powder.    USE - Method for preparing slow release organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare slow release organic fertilizer that increases utilization rate of fertilizer, reduces fertilizer loss and restrains nitrite and harmful substance absorption by crop, and ensures synergistic effect, no environment pollution and pollution free crops.    DETAILED DESCRIPTION - Preparing slow release organic fertilizer involves dissolving 1kg sodium alginate in 60L phosphoric acid buffer solution (pH=7.0) to obtain sodium alginate solution that is reacted with methanolic solution of n-hexylamine or n-heptyl amine at 70-90 degrees C for 3-5 hours. Sodium cyanoborohydride (0.1lkg) is stirred with obtained solution at room temperature for 0.5 hours. The reaction product is precipitated with methanol. The precipitate is dissolved in water, and then freeze-dried. An organic amine-modified alginate synergist, 1-1.5kg calcium carbonate powder, 10-20kg urea, 1-3kg pine needle powder, binder and balanced amount of water are mixed with sodium alginate solution. The obtained mixture is granulated using granulator. The obtained granule is dried at 140 degrees C in oven for 26 minutes to obtain slow release organic fertilizer granule.
NOVELTY - An alginic acid synergistic agent-containing active microbial fertilizer comprises 10-15 pts. wt. alginic acid synergistic agent, 20-40 pts. wt. minerals, 15-35 pts. wt. plant material, 10-20 pts. wt. nutrition material and 5-15 pts. wt. biological bacteria.    USE - Alginic acid synergistic agent-containing active microbial fertilizer (claimed).    ADVANTAGE - The alginic acid synergistic agent-containing active microbial fertilizer improves microbial viability, soil fertility, plant disease and insect resistance, drought tolerance effect and crop quality with reduced usage amount of fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alginic acid synergistic agent-containing active microbial fertilizer.
NOVELTY - A slow-release fertilizer comprises 4-10 pts. wt. Zhugen mud, 3-6 pts. wt. leaf mold, 3-6 pts. wt. sandy soil, 10-16 pts. wt. cow dung, 28-34 pts. wt. urea, 4-8 pts. wt. ammonium sulfate, 12-16 pts. wt. monoammonium phosphate, 8-14 pts. wt. potassium chloride, 2-4 pts. wt. citric acid, 1-2 pts. wt. carboxymethyl cellulose, 1-2 pts. wt. borax, 1-2 pts. wt. calcium carbonate, 1-2 pts. wt. iron ore, 1-2 pts. wt. agar and 1-6 pts. wt. additive.    USE - Slow-release fertilizer is used for floriculture.    ADVANTAGE - The slow-release fertilizer has excellent fertilizer effect for long period of time, improves quality and stress resistance of flower, and saves water and labor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of slow-release fertilizer.
NOVELTY - Bio-organic fertilizer comprises 30-80 wt.% sugar refinery waste fermented powder, 10-60 wt.% micro-organism pesticide, 2-16 wt.% wetting agent and 2-16 wt.% dispersing agent.    USE - Bio-organic fertilizer used for growing sugarcane (claimed).    ADVANTAGE - The bio-organic fertilizer improves chlorophyll content and increases stem diameter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves mixing sugar refinery waste fermented powder, micro-organism pesticide, wetting agent and dispersing agent uniformly to obtain product that is packaged.
NOVELTY - Biological composite fertilizer comprises component A, component B, component C and component D in ratio of 0.05-1:3-8:0.05-1:1-5. Component A comprises Bacillus subtilis, Paenibacillus polymyxa, phosphate-solubilizing bacteria and potassium bacteria in mass ratio of 1-5:1-5:0.1-3:0.1-3. Component B comprises humic acid, rapeseed cake, organic fertilizer and lignin in mass ratio of 1-6:1-6:1-6:0.01-3. Component C comprises hydroquinone, isobutylene diurea and N- butylthio triamide in mass ratio of 0.01-3:0.01-3:0.02-8. Component D comprises urea and ammonium polyphosphate.    USE - Biological composite fertilizer used for reducing nitrate content in soil and vegetable (claimed).    ADVANTAGE - The biological composite fertilizer has obvious effect.    DETAILED DESCRIPTION - Biological composite fertilizer comprises component A, component B, component C and component D in ratio of 0.05-1:3-8:0.05-1:1-5. Component A comprises Bacillus subtilis, Paenibacillus polymyxa, phosphate-solubilizing bacteria and potassium bacteria in mass ratio of 1-5:1-5:0.1-3:0.1-3. Component B comprises humic acid, rapeseed cake, organic fertilizer and lignin in mass ratio of 1-6:1-6:1-6:0.01-3. Component C comprises hydroquinone, isobutylene diurea and N- butylthio triamide in mass ratio of 0.01-3:0.01-3:0.02-8. Component D comprises urea, ammonium polyphosphate and potassium tripolyphosphate in mass ratio of 0.1-3:0.1-5:0.1-5.
NOVELTY - Processing acetamiprid mother liquor comprises adding ethyl acetate to ethanol-free acetamiprid mother liquor, stirring, filtering at less than or equal to 0 degrees C, washing filter cake with ethyl acetate, drying to obtain acetamiprid and vacuum evaporating filtrate at 90-100 degrees C and - 0.09 MPa to obtain ethyl N-cyanoethylimidoate.    USE - Processing acetamiprid mother liquor used for increasing recovery rate of acetamiprid and ethyl N-cyanoethylimidoate (claimed).    ADVANTAGE - The method is environment-friendly and energy-saving, and reduces processing costs.
NOVELTY - Preparation of telmisartan comprises taking 3-methyl-4-nitrobenzoic acid, adding 1-butyl-3-methylimidazolium tetrafluoroborate, N-ethylpyridinium tetrafluoroborate, 1-butyl-3-methylimidazolium hexafluorophosphate or 1-hydroxyethyl-2,3-dimethylimidazolium chloride as ionic liquid, esterifying, performing primary reduction, acylating, performing nitration, performing secondary reduction, performing cyclization, adding N-methyl-o-phenylenediamine dihydrochloride, primary condensing, adding 4'-bromomethyl biphenyl-2-carboxylate and secondary condensing.    USE - Method for preparing telmisartan.    ADVANTAGE - The method is simple and environment-friendly, has high safety, yield and purity, and is suitable for industrial production.
NOVELTY - Producing low-carbon ethanol, comprises (i) pressing sugar cane once, to obtain sugarcane juice and bagasse, purifying sugarcane juice, concentrating, and crystallizing, to obtain sucrose and molasses; (ii) mixing molasses and bagasse, and carrying out solid state fermentation in a fermentation device by inoculating yeast strain, to obtain ethanol; and (iii) carrying out distillation of solid-state fermented sugar cane, to obtain ethanol and a fermentation slag, and converting remaining molasses and bagasse sugar into ethanol from the steps (i) to (iii).    USE - The ethanol is useful in the production of candy, and fuel alcohol (claimed).    ADVANTAGE - The method is environmental friendly (claimed), and economical; has low energy consumption, and high production quantity; produces high quality cane sugar; reduces the production of organic sewage while carrying out solid fermentation process; and utilizes carbon dioxide, fermentation slag, and other waste steam by-products in equivalent amount.
NOVELTY - A Myriophyllum aquaticum propagating method involves selecting growth robust, bright green color and pest free stem segments as explants, soaking the explants in detergent and rinsing in tap, and repeatedly washing with distilled water and placing in sterile environment. The treated explant is sterilized aseptically with ethanol and sodium chloride and rinsed. Leaves in the Myriophyllum aquaticum explants are removed and placed in an induction medium. The induced explant is placed in a proliferation culture medium. The proliferated explant is hardened and transplanted.    USE - Method for propagating Myriophyllum aquaticum.    ADVANTAGE - The method enables propagating the Myriophyllum aquaticum in a rapid and eco-friendly manner.    DETAILED DESCRIPTION - A Myriophyllum aquaticum propagating method involves selecting growth robust, bright green color and pest free stem segments as explants, soaking the explants in detergent for 30 minutes and rinsing in tap for 2 hours, and repeatedly washing with distilled water for 4-5 times, repeatedly washing with sterile water for 4-5 times and placing in sterile environment. The treated explant is sterilized aseptically with 70% ethanol for 15 seconds and rinsed with sterile water for 4-5 times, and sterilized with 0.1% sodium chloride for 2-5minutes and rinsed with sterile water for 4-5 times. Leaves in the 5-2 cm Myriophyllum aquaticum explants are removed and placed in an induction medium for culturing callus and shoots, where the induction medium comprises MS solid culture base, 0.50-1.50 mg/l 6-benzylaminopurine (6-BA), 0.25-0.50 mg/l naphthaleneacetic acid (NAA) and 3% sucrose. The induced explant is placed in a proliferation culture medium comprising 1/2 MS broth, 0.50-1.50 mg/l 6-BA, 0.25-0.50 mg/l NAA and 1.5% sugar. The proliferated explant is hardened at room temperature for 1-2 days for removing shoots. The culture of roots is washed and transplanted.
NOVELTY - The preparation method of paracetamol and amantadine hydrochloride particles involves mixing chlorpheniramine maleate, caffeine, artificial bezoar, amantadine hydrochloride and acetaminophen to obtain mixture, grinding the mixture to obtain pre-mixed material, granulating the pre-mixed material in a granulator, then adding additive to obtain drug particles, drying the drug particles, then mixing and packaging in bag.    USE - The method is useful for preparing paracetamol and amantadine hydrochloride particles for children.    ADVANTAGE - The method enables simple and economical preparation of paracetamol and amantadine hydrochloride particles with high efficiency and purity in an environmentally-friendly manner.
NOVELTY - Anaerobic reactor comprises container body (1), water distribution system (2), three phase separator (3), sludge reaction zone (4), storage tank (5), high-pressure air compressor (6), valve (7), pressure sensor (8), controller (9), gas chamber (31), water clarification area (32), precipitation zone (33), sludge bed zone (41), sludge suspension zone (42), water distribution channel (410) and baffles (411).    USE - Anaerobic reactor used for treating sewage containing sludge (claimed).    ADVANTAGE - The device has high sewage treatment efficiency and good operation stability.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of anaerobic reactor.    Container body (1)    Water distribution system (2)    Three phase separator (3)    Sludge reaction zone (4)    Storage tank (5)    High-pressure air compressor (6)    Valve (7)    Pressure sensor (8)    Controller (9)    Gas chamber (31)    Water clarification area (32)    Precipitation zone (33)    Sludge bed zone (41)    Sludge suspension zone (42)    Water distribution channel (410)    Baffles (411)
NOVELTY - Synthesis of potassium dihydrogen phosphate involves hydrolyzing condensed phosphate as raw material, crystallizing and separating.    USE - Synthesis of potassium dihydrogen phosphate (claimed).    ADVANTAGE - The method efficiently provides high-quality potassium dihydrogen phosphate without affecting the environment.
NOVELTY - Paraquat (RTM: N,N'-dimethyl-4,4'-bipyridinium dichloride) alkylation chloromethane compression recovery involves alkylating chloromethane and pyridine to obtain chloromethylpyridine hydrochloride, passing excess chloromethane gas into upper portion of alkylation reactor and through a pipeline into a buffer tank and then into a low-pressure compressor, flowing lower chloromethane liquid from buffer tank through a pipe into alkylation reactor, continuing alkylation, compressing chloromethane gas, and passing the high-pressure gas through a pipe for alkylation.    USE - Paraquat (RTM: N,N'-dimethyl-4,4'-bipyridinium dichloride) alkylation chloromethane compression recovery (claimed).    ADVANTAGE - The method enables recovery of unreacted chloromethane, is safe, economical and environmentally-friendly, and reduces discharge of waste gas.    DETAILED DESCRIPTION - Paraquat (RTM: N,N'-dimethyl-4,4'-bipyridinium dichloride) alkylation chloromethane compression recovery involves alkylating chloromethane and pyridine to obtain chloromethylpyridine hydrochloride, passing excess methyl chloride gas into the upper portion of alkylation reactor and through a pipeline into a buffer tank and then into a low-pressure compressor, flowing lower chloromethane liquid from buffer tank through a pipe into alkylation reactor, continuing alkylation, compressing chloromethane gas in low-pressure compressor to a final high pressure of 0.6-0.85 MPa, and passing the high-pressure chloromethane gas through pipe for alkylation.
NOVELTY - Method of production of organic mineral fertiliser from sediments of urban wastewaters is reactant treatment of urban wastewater sediments followed by composting the mixture, and the reagent is used as the organic mineral composition containing calcium oxide and lowland peat in a weight ratio to the sediments of urban wastewater equal to (25-75):(2-3.5):10, respectively, the sediments of urban wastewaters: calcium oxide: lowland peat, and the treated sediments are composted for at least 7 days in air.    USE - Agriculture.    ADVANTAGE - Invention enables to reduce the potential hazard of environmental contamination with heavy metals during sediment storage, to obtain organic mineral fertiliser at lower cost, to involve the wastes into secondary use.4 tbl, 4 ex
NOVELTY - The equipment has a main module (100) that is equipped at lower portion of main module housing (110). Hot air supplying apparatus (120,130) is set to supply hot air within module housing. Exhaust passage is formed in one side of main module housing. Stirring unit (140) is provided for mixing food waste ingredient and ejects recycling product. The annex module (200) removes moisture and dust of exhaust air processed according to increment of food waste treatment quantity or feed pump. The main module injects food waste for fermentation and drying.    USE - Modular food waste recycling equipment.    ADVANTAGE - The food waste is provided to main module and annex module so that active management is performed efficiently according to the capacity change at the problem area unit. The generation of drain water is prevented while maximizing the odor removal capability and preventing the environmental pollution about the surrounding environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the modular food waste recycling equipment. (Drawing includes non-English language text)    Main module (100)    Mai module housing (110)    Hot air supplying apparatus (120,130)    Stirring unit (140)    Annex module (200)
NOVELTY - Purifying an amino acid from a starting mixture, in which the amino acid comprises an aromatic ring and has an acidity constant (Ka), comprises: (a) contacting the starting mixture with a strong cationic resin at a pH of greater than or equal to pKa; and (b) eluting with an aqueous eluting solution having a pH greater than the pH of the step (a), to collect a stream enriched in amino acid.    USE - The method is useful for purifying an amino acid from a starting mixture including salts and sugars, where the amino acid is tryptophan, phenylalanine, tyrosine or histidine (claimed).    ADVANTAGE - The method: eliminates the need of intermediate rinsing after step (a) and before step (b); allows separation between the target amino acid and impurities including salts, sugars and pigments, with high purity and by minimal consumption of chemical products or elution solution; and avoids large fluctuations in yield and purity of amino acid products.
NOVELTY - A methanation reaction catalyst comprises metal foam, and metal (II), where metal (II) is coated on surface of metal foam. The metal (II) is magnesium, vanadium, manganese, iron, cobalt, nickel, molybdenum, ruthenium, cerium and/or tungsten.    USE - Catalyst is used for manufacturing methane (claimed).    ADVANTAGE - The methanation reaction catalyst has high carbon monoxide conversion rate and methane selectivity due to the metal foam structure, and excellent thermal stability. The usage amount of catalyst is reduced, during manufacture of methane. The reactor internal temperature is regularly controlled by the reaction gas flow and heat of reaction dispersion effect, during manufacture of methane using the catalyst.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of methanation reaction catalyst; and    (2) manufacture of methane.
NOVELTY - Organic fertilizer comprises 20-30 pts. wt. dry chicken manure, 10-20 pts. wt. urea, 6-8 pts. wt. calcium superphosphate, 6-8 pts. wt. potassium chloride, 5-6 pts. wt. active silica sol, 3-5 pts. wt. silica, 3-5 pts. wt. sulfuric acid, 1.5-2.5 pts. wt. alkyl polyglycoside, 3-5 pts. wt. humic acid, 3-5 pts. wt. sugar waste liquid, 3-5 pts. wt. gypsum, and balance water.    USE - Organic fertilizer used for improving soil yield (claimed).    ADVANTAGE - The method is simple and has shortened heating time, no pollution and low cost. The organic fertilizer is environment-friendly, reduces long-term use of chemical fertilizer, and improves agricultural compost quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising adding alkyl polyglycoside to water, adding sugar waste liquid and humic acid, putting into reaction kettle, mixing, and stirring for 30-50 minutes to obtain suspension; adding dry chicken manure, urea, calcium superphosphate, potassium chloride, active silica sol, silica and sulfuric acid into reaction kettle, mixing, reacting at 70-85 degrees C, stirring for 30-50 minutes, stacking, and fermenting for 10-20 days; and uniformly mixing with suspension, drying, crushing, sieving through 60-80 meshes sieve, drying, and packaging.
NOVELTY - Brick type planting matrix comprises 40-50 wt.% edible fungi residues, 40-50 wt.% bonding material and 10 wt.% organic fertilizer. The bonding material is yellow clay, brown soil, red soil and/or yellow soil. The amount of bonding material per kg is 1 g fertilizer (15-15-15). The organic fertilizer is decomposed chicken manure or pig manure.    USE - Used as brick type planting matrix.    ADVANTAGE - The planting matrix realizes utilization of edible fungus waste resources and is environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the brick type planting matrix, comprising (i) taking edible fungi slag, removing covered plastic film, piling, drying, smashing in a pulverizer and sieving to obtain edible fungi slag material of 1 mm particle size, (ii) mixing edible fungi slag material and organic fertilizer, stacking uniformly and placing for 10-15 days, (iii) mixing bonding material and complex fertilizer, and then mixing uniformly with mixed edible fungus slag material, and (iv) adding resulting material into mold of 10-20 cm length, 10 cm width and 1 cm thickness, uniformly scattering grass seeds on surface, compressing and molding in a compressor form matrix with size as follows: the length is 10-20 cm, the width is 10 cm and the thickness is 5 cm; and    (2) use method of the brick type planting matrix, comprising paving brick type planting matrix on flat or slope surface with gap of 2 cm, spraying water on surface, swelling, pressing and forming brick type body, and forming a layer of root plate structure.
NOVELTY - The utility model is new type relates to a formulated a prescription fertilizer production system, comprising in turn connected with the a first site and a second site, the first cylinder, a third site, the first hoisting machine, pulverizer, a storage hopper, a mixing cylinder, a hoisting machine, round disc pelletizer, a vibration separating sieve, drying a, a vibration separating sieve, a, a storage hopper, packing and finished product base, also comprising with inorganic material warehouse, in a third site a mobile tripper, a vibration separating sieve, a vibration separating sieve through a conveying belt connected to the second hoisting machine, a hoisting machine, third storage hopper, third hoisting machine, extrusion pelleting machine connected in turn, extrusion granulator connected with a packing machine. The production system full fermentation organic material, a, out of a finished product fertilizer with different slow release effect, and classify a sieving is not qualified and organic material and a fit and the inorganic material, automatic degree high and strong practicability.
NOVELTY - Method of growing grass involves mixing grass seed and soil mixture obtained by mixing sand with peat moss and pearlite in a ratio of 1:0.07:0.03, and growing grass.    USE - Method of growing grass (claimed).    ADVANTAGE - The method enables growing of grass with excellent water holding capacity and reduced energy consumption, by environmentally-friendly process.
NOVELTY - New copolymer is a block copolymer (III) comprising a hydrophobic portion (I) and a hydrophilic portion (II).    USE - New copolymer is used for manufacturing membrane of fuel cell.    DETAILED DESCRIPTION - New copolymer is a block copolymer of formula (III) comprising a hydrophobic portion of formula (I) and a hydrophilic portion of formula (II).    Q1,Q2=single bond, -CH2- or -C(R1)(R2)-;    x,y=1 or more;    R1,R2=1-3C alkyl;    M1,M2=monovalent cation;    A1=hydrophobic portion (I);    A2=hydrophilic portion (II);    D1=group of formula (IV);    D2=group of formula (V);    n=integer;    Q3,Q4=single bond, -CH2- or -C(R3)(R4)-;and    R3,R4=R1.    An INDEPENDENT CLAIM is included for manufacture of copolymer.
NOVELTY - A composite plant fertilizer comprises 7-10 pts. wt. Chinese trumpet creeper, 8-15 pts. wt. milk vetch, 5-10 pts. wt. alfalfa, 2-5 pts. wt. sweet clover, 3-6 pts. wt. sunn hemp, 1-5 pts. wt. Sesbania cannabina, 3-6 pts. wt. Amorpha, 0-4 pts. wt. Azolla, 2-8 pts. wt. hyacinth, 4-9 pts. wt. Alternanthera philoxeroides, 3-8 pts. wt. soybean, 4-8 pts. wt. tea, 1-4 pts. wt. plant ash, 4-8 pts. wt. pea, 6-12 pts. wt. horsebean, 10-15 pts. wt. wheat bran straw stick, effective microorganism leavening agent and mountain spring water.    USE - Composite plant fertilizer.    ADVANTAGE - The fertilizer uses natural green plant raw material, is safe environment-friendly, has air environmental protection and no additive, does not pollute, sets with rich protein, vitamin and carotene, and enhances soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite plant fertilizer comprising drying medicinal materials, putting into pulverizer, crushing, placing into stirrer, stirring, adding remaining materials, stirring uniformly, high temperature fermenting, drying, sieving, measuring, and storing.
NOVELTY - High nutrient microorganism complex fertilizer comprises 16-190 pts. wt. double wall layer composite microbial microcapsules, 150-450 pts. wt. monoammonium phosphate, 0-400 pts. wt. urea powder, 100-200 pts. wt. potassium chloride, 200-350 pts. wt. ammonium chloride, 20-100 pts. wt. ammonium bicarbonate, 0-150 pts. wt. ammonium sulfate and 0-50 pts. wt. attapulgite. The composite microbial strain is composed of Bacillus subtilis, Bacillus laterosporus, Bacillus megaterium, Bacillus cereus, Bacillus circulans and Bacillus mucilaginosus.    USE - High nutrient microorganism complex fertilizer.    ADVANTAGE - The product increases yield of crop production and reduces incidence of pests.    DETAILED DESCRIPTION - High nutrient microorganism complex fertilizer comprises 16-190 pts. wt. double wall layer composite microbial microcapsules, 150-450 pts. wt. monoammonium phosphate, 0-400 pts. wt. urea powder, 100-200 pts. wt. potassium chloride, 200-350 pts. wt. ammonium chloride, 20-100 pts. wt. ammonium bicarbonate, 0-150 pts. wt. ammonium sulfate and 0-50 pts. wt. attapulgite. The double-wall layer composite microbial microcapsules contain 3-5 pts. wt. composite microbial strains. The composite microbial strain is composed of Bacillus subtilis, Bacillus laterosporus, Bacillus megaterium, Bacillus cereus, Bacillus circulans and Bacillus mucilaginosus where each strain has total viable count of greater than or equal to 30000000000 colony-forming unit/g. An INDEPENDENT CLAIM is included for preparation of high nutrient microorganism complex fertilizer comprising crushing monoammonium phosphate, urea powder, potassium chloride, ammonium chloride, ammonium bicarbonate, ammonium sulfate and attapulgite, mixing, granulating, drying, cooling to obtain chemical fertilizer particles, introducing double-wall layer composite microbial microcapsules into the coating machine by screw conveyor, uniformly coating on the surface of chemical fertilizer and packaging.
NOVELTY - Dimethyl carbonate and ammonia are produced by taking carbon dioxide and methyl alcohol as initial raw material, and performing esterification and addition, ester exchange. The first step is reacting urea and propylene glycol at 160 degrees C and 33-47 KPa in the presence of lead carbonate catalyst for 5-7 hours to obtain propylene carbonate and ammonia gas.    USE - Method for production of dimethyl carbonate and ammonia (claimed).    ADVANTAGE - The method is convenient to implement and is safe. It has zero waste discharge making it environment-friendly.    DETAILED DESCRIPTION - Production of dimethyl carbonate and ammonia comprises taking carbon dioxide and methyl alcohol as initial raw material, and performing esterification and addition, ester exchange. The first step is reacting urea and propylene glycol at 160 degrees C and 33-47 KPa in the presence of lead carbonate catalyst for 5-7 hours to obtain propylene carbonate and ammonia gas. The second step comprises reacting ammonia with carbon dioxide and water at high temperature in the presence of catalyst for preparing propylene and carbon raw material. The third step comprises reacting propylene carbonate and methanol at 64-80 degrees C in the presence of potassium titanate catalyst, and separating and purifying product.
NOVELTY - Preparing acid sensitive degradable modified dextran involves obtaining hydrophobic polymer acetal compound.    USE - Method for preparing acid sensitive modified dextran (claimed) used in targeted therapy and diagnostics.    ADVANTAGE - The method enables to prepare acid sensitive modified dextran that ensures biocompatibility, biological degradability and good research value and application prospect.
NOVELTY - Preparation of biomass briquette fuel comprises steam drying biomass raw material and sludge raw material; crushing sludge raw material and biomass raw material; baking biomass raw material and cooling; crushing cooled baked biomass; and uniformly mixing sludge raw material powder and baked biomass powder, regulating water content, extruding and molding.    USE - Method for preparing biomass briquette fuel (claimed).    ADVANTAGE - The method has low system operation cost, small molding equipment loss, mild molding condition, and high thermal efficiency. The product is easy to mold, and has anti-absorbing ability and high strength.    DETAILED DESCRIPTION - Preparation of biomass briquette fuel comprises steam drying biomass raw material and sludge raw material at 160-200 degrees C to biomass raw material water content of less than or equal to 10% and sludge raw material water content of 25-35%; crushing sludge raw material to less than or equal to 5 mm, and biomass raw material to 5-20 mm; baking biomass raw material at 200-280 degrees C, flue gas inlet temperature of 220-300 degrees C and outlet temperature of 150-200 degrees C under anaerobic condition for 10-40 minutes, and cooling; and crushing cooled baked biomass to less than or equal to 3mm; uniformly mixing sludge raw material powder and baked biomass powder, regulating water content to 12-18%, extruding and molding. An INDEPENDENT CLAIM is included for fuel preparation system comprising raw material processing system, molding system, and boiler system, biomass raw material and sludge raw material processing system, biomass drying device, biomass crushing device, baking device, biomass powder device, storage hopper, sludge drying device, sludge crushing device, sludge storage hopper, mixing device, molding machine, cooling device, biomass boiler, high temperature steam pipe, dust remover, blower, and discharge system.
NOVELTY - Fatty acid methyl ester is prepared by subjecting kitchen waste oil and methanol to esterification reaction in presence of concentrated sulfuric acid as catalyst; after esterification reaction, distilling and recovering remaining methanol; adding esterification reaction crude product methyl ester with sodium hydroxide as catalyst and methanol and carrying out transesterification reaction to produce soap; and adding soap with glycerin and entering mixture into reduced pressure rectifying tower, raising temperature to 250-290 degrees C, rectifying and refining to obtain fatty acid methyl ester.    USE - Method for preparing fatty acid methyl ester (claimed) used as biodiesel.    ADVANTAGE - The method can fully utilize kitchen waste oil, and thus reducing environment pollution. It involves two-step method of esterification reaction and transesterification in which the method is simple and has high conversion rate.    DETAILED DESCRIPTION - Preparation of fatty acid methyl ester comprises:    (A) pumping kitchen waste oil to an esterification reactor, adding concentrated sulfuric acid as catalyst, then pumping methyl alcohol to reactor, and carrying out esterification reaction;    (B) after esterification reaction, distilling and recovering remaining methanol, and discharging remaining sulfuric acid and water from the reactor;    (C) adding esterification reaction crude product methyl ester with sodium hydroxide as catalyst and methyl alcohol and carrying out transesterification reaction to produce soap; and    (D) adding soap with glycerin and entering mixture into reduced pressure rectifying tower, raising temperature to 250-290 degrees C, rectifying and refining to obtain fatty acid methyl ester.
NOVELTY - The separating type methane biogas generator has a feedstock pipe (10) and a discharging pipe (20) which are detachably connected with a straight pipe (30). A discharging tube plate (34) is connected with the discharging pipe. The baffle plates are respectively provided in the inner side walls of the feedstock pipe and discharging pipe. One-way valve is provided to the feedstock pipe for feeding the biogas fluid. One-way valve is provided in the discharging pipe for discharging the biogas fluid.    USE - Separating type methane biogas generator for use in agricultural field.    ADVANTAGE - The biogas slurry circulation flow stirring performance is improved, and the uniform distribution of strain is promoted using stirring biogas slurry circulation flow. The gas production is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the separating type methane biogas generator.    Feedstock pipe (10)    Discharging pipe (20)    Straight pipe (30)    Hydraulic chamber (40)    Drain pipe (51)
NOVELTY - Eco-friendly toilet comprises a toilet pedestal pan (2), toilet room (1) and biodegradable chamber (3). The toilet pedestal pan is provided with a door (4), floor (5) and ventilating chamber. The ventilating chamber is located on side wall or top part of the toilet pedestal pan, which is fixed on floor of the toilet room. Biodegradable chamber is provided in toilet indoor floor, and the biodegradable chamber comprises Hermetia illucens larva and auxiliary material.    USE - Eco-friendly toilet.    ADVANTAGE - The eco-friendly toilet decomposes toilet excrement residue that used for manufacturing fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an eco-friendly toilet.    Toilet room (1)    Toilet pedestal pan (2)    Biodegradable chamber (3)    Door (4)    Floor (5)
NOVELTY - The utility model provides a clean feeding device in glyphosate raw material production process, vacuum conveying pipe, a air input channel pipe respectively connected with material for vacuum, vacuum feeding machine by channel reverse blow pipe in turn and glycine closeness storage hopper, storage hopper a closeness, low vacuum feeding machine also equipped with a part in a kettle with vacuum feeding machine set with filter, filter on the lower part set with a vacuum feeding machine side wall between t a, a filter formed with a feedstock tube, lower hopper has a circle is set with bin door. The utility model is new type can eliminate a feeding caused by the dust flying, which avoids material waste cause the proportion unbalance, and solves the problem that the dust flying caused by the environmental pollute, relieving the environmental pressure.
NOVELTY - Manufacture of moisture adjusting agent involves mixing granulated pellets of coal ash material and organic sludge obtained by drying and distilling starch from food factory, adding saw dust, mixing and dying obtained mixture.    USE - Manufacture of moisture adjusting agent used for producing compost (claimed) for organic rice.    ADVANTAGE - The compost manufactured using the moisture adjusting agent improves acidity of soil, by environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of additive.
NOVELTY - Preparing manure by biological treatment method using Pseudomonas aeruginosa involves culturing P.aeruginosa at a temperature of 37 degrees C in an incubator until density reaches 5000 colony forming units (CFU), inoculating 500 g culture in compost, and culturing P.aeruginosa in proliferation culture medium for 168 hours or 7 days.    USE - The method is useful for preparing manure by biological treatment method using P.aeruginosa (claimed).
NOVELTY - A low-carbon alcohol synthesis system comprises feed gas processing module, low-carbon alcohol synthesis module, and product processing module in which feed gas processing module comprises feed gas compressor (11) and feed gas heating component, low-carbon alcohol synthesis module comprises low-carbon alcohol synthesis component (21), product processing module comprises low-carbon alcohol separation component, and low-carbon alcohol separation component comprises low-carbon alcohol separator (311).    USE - A low-carbon alcohol synthesis system.    ADVANTAGE - Low-carbon alcohol synthesis system reduces oil dependence and has high efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for low-carbon alcohol synthesis which involves sending feed gas to low-carbon alcohol synthesis system, pressurizing, heating, performing low-carbon alcohol synthesis to produce synthesis mixture, and separating low-carbon alcohol products.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of low-carbon alcohol synthesis system. (Drawing includes non-English language text).    Feed gas compressor (11)    Feed gas heater (12)    Desulfurizing groove (13)    Low-carbon alcohol synthesis component (21)    Low-carbon alcohol separator (311)
NOVELTY - In situ modification of nano magnesium hydroxide comprises mixing ore tailings, 1-30 wt.% concentrated sulfuric acid and copper sulfate, carrying out acidolysis and filtering; adding filter liquid with oxidizing agent, oxidizing, adding sodium hydroxide or ammonia water until 6.5-8, stirring, and filtering; mixing 1-5 wt.% silane coupling agent, 2-6 wt.% dispersing agent and refined magnesium-copper sulfate solution, fully stirring, slowly inletting ammonia gas, aging, filtering, washing, and drying; and extracting ammonia, and removing ammonium sulfate by acidolysis.    USE - Method of in situ modification of nano magnesium hydroxide (claimed) used in rubber and paint.    ADVANTAGE - The method produces with good interface bonding and dispersibility in polymer matrix, and is environment-friendly.    DETAILED DESCRIPTION - In situ modification of nano magnesium hydroxide comprises mixing ore tailings, 1-30 wt.% concentrated sulfuric acid and copper sulfate, carrying out acidolysis reaction at 50-80 degrees C for 2-4 hours and filtering; adding filter liquid with oxidizing agent, oxidizing, adding sodium hydroxide or ammonia water until 6.5-8, stirring, and filtering precipitate to obtain refined magnesium-copper sulfate solution; mixing 1-5 wt.% silane coupling agent, 2-6 wt.% dispersing agent and refined magnesium-copper sulfate solution, fully stirring, slowly inletting ammonia gas to obtain mixed solution through crystal sediment reaction at 25-50 degrees C for 1-3 hours at pH 10-11, aging, filtering, washing, and drying prepare surface modified nano magnesium hydroxide; and extracting ammonia, and removing ammonium sulfate by acidolysis reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the in situ modification of nano magnesium hydroxide (Drawing includes non-English language text).
NOVELTY - One-step synthesis of terpineol comprises taking 1-3 pts. wt. carbon-based solid acid catalyst, 10-25 pts. wt. distilled water, 10 pts. wt. turpentine and 25-125 pts. wt. solvent, carrying out hydration of turpentine using carbon-based solid acid catalyst and separating.    USE - Method for carrying out one-step synthesis of terpineol (claimed).    ADVANTAGE - The method is environment-friendly and has conversion rate of 95-98% and terpineol yield of 35-42%.
NOVELTY - Non-chloro preparation of acetazolamide intermediate i.e. 2-acetylamino-5-chloro-sulfonyl-1,3,4-thiadiazole involves adding 15-36 mass% hydrochloric acid into reactor; dropping 10-30 mass% hydrogen peroxide; reacting at - 5-15 degrees C for 0.5-3.0 hours to obtain reaction liquid; adding reaction liquid with 2-acetylamino-5-mercapto-1,3,4-thiadiazole via batch addition; reacting at - 5-15 degrees C for 2-20 hours; subjecting reaction mixture into suction filtration; washing filter cake with water for 2-3 times to obtain 2-acetylamino-5-chloro-sulfonyl-1,3,4-thiadiazole intermediate; and drying.    USE - Non-chloro preparation of acetazolamide intermediate i.e. 2-acetylamino-5-chloro-sulfonyl-1,3,4-thiadiazole.    ADVANTAGE - The method has moderate operation, is more environmentally friendly, and produces 2-acetylamino-5-chloro-sulfonyl-1,3,4-thiadiazole with good color and high purity.    DETAILED DESCRIPTION - Non-chloro preparation of acetazolamide intermediate i.e. 2-acetylamino-5-chloro-sulfonyl-1,3,4-thiadiazole comprises adding 15-36 mass% hydrochloric acid into reactor; dropping 10-30 mass% hydrogen peroxide in ice salt bath to control reaction system at - 5-15 degrees C; reacting at 5-15 degrees C for 0.5-3.0 hours to obtain reaction liquid, in which hydrochloric acid and hydrogen peroxide have molar ratio of (5-40):50; adding reaction liquid with 2-acetylamino-5-mercapto-1,3,4-thiadiazole via batch addition, such that 2-acetylamino-5-mercapto-1,3,4-thiadiazole is suspended in reaction system; reacting at - 5-15 degrees C for 2-20 hours to obtain reaction mixture, in which molar ratio of 2-acetylamino-5-mercapto-1,3,4-thiadiazole and hydrogen peroxide is 1:(1-100); subjecting reaction mixture into suction filtration; washing filter cake with water for 2-3 times to obtain 2-acetylamino-5-chloro-sulfonyl-1,3,4-thiadiazole intermediate; and drying to obtain acetazolamide 2-acetylamino-5-chloro-sulfonyl-1,3,4-thiadiazole intermediate.
NOVELTY - Preparation method of animal and plant type organic fertilizer involves (a) leavening animal raw material and drying to obtain animal manure, (b) fermenting plant material and drying to obtain plant manure, and (c) stir-mixing manure obtained from step (a) and step (b), extruding and granulating, polishing, drying, cooling, sieving, measuring, and packaging.    USE - The method is useful for preparing animal and plant type organic fertilizer for improving soil fertility, providing plant nutrition and improving quality of crops.    ADVANTAGE - The method increases crop yield and pest resistance, and is environmentally-friendly.
NOVELTY - The new type utility claims a a hydraulic crawler-type dumper using a crawler-type process, wherein a motor speed reducer driving a crawler driving wheel, the driven crawler movement following a match of crawler supporting wheel, through a hydraulic pipeline of a left right two strip crawler single control movement, not only is a no easy happen fault, and two strip crawler can independently carry out forward and backward, and no interference, the turning semi-diameter is small; the dumper also apply to a roller transfer power gear, transmission efficiency is high, use a life.
NOVELTY - Microbial functional microbial agent is prepared by eliminating air in production line, adding liquid, adding strain (A) to seed tank (6), inoculating, propagating, storing, and filling in which production line comprises seed tank, fermentation tank (5), storage tank (9), metering filling tank (10), steamer (2), steam filter (16), air compressor (8), air storage tank (7), freeze-drying device (12), oil-water separator (11), air coarse filter (13), decompressing valve (14), air fine filter (15), pure water tank (1), circulating water tank (4), and water pump (B).    USE - Preparation of microbial functional microbial agent for fertilizer.    ADVANTAGE - Microbial functional microbial agent is non-toxic, harmless, and environment-friendly, prevents and treats plant diseases and insect pests, improves soil structure, high fertilizing effect, and promotes crop production yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of production line.    Pure water tank (1)    Steamer (2)    Circulating water tank (4)    Fermentation tank (5)    Seed tank (6)    Air storage tank (7)    Air compressor (8)    Storage tank (9)    Metering filling tank (10)    Oil-water separator (11)    Freeze-drying device (12)    Air coarse filter (13)    Decompressing valve (14)    Air fine filter (15)    Steam filter (16)    Strain (A)    Water pump (B)
NOVELTY - A biofertilizer comprises 99.53 %mass inorganic fertilizer, 0.28 %mass bioculture and 0.19 %mass nutrition protective agent. The inorganic fertilizer contains 23.26 %mass potassium chloride, 22.33 %mass monoammonium phosphate, 6.51 %mass ammonium bicarbonate, 42.78 %mass ammonium chloride and 4.65 %mass attapulgite clay. The bioculture is Bacillus subtilis powdered inoculant. The nutrition protective agent is easily degradable spreading agent prepared using vegetable oil.    USE - Biofertilizer (claimed).    ADVANTAGE - The biofertilizer has low bacteria content and high concentration bioculture having excellent activity, and is rich in nutrients.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of biofertilizer.
NOVELTY - A green vegetable bio-organic fertilizer comprises 90-110 pts. wt. crop residue, 30-40 pts. wt. poultry manure, 4-6 pts. wt. yeast, 4-6 pts. wt. brassin, 8-12 pts. wt. glutamate mother liquor, 9-11 pts. wt. urea, 4-6 pts. wt. purple potato skin, 2-4 pts. wt. zinc carbonate, 1-3 pts. wt. tea saponin, 1-3 pts. wt. green tea water extract, 2-4 pts. wt. date stone powder, 0.5-2 pts. wt. chlorophyll, 2-4 pts. wt. sawdust, 1-3 pts. wt. maltogenic amylase, 7-9 pts. wt. sodium selenite, 0.5-2 pts. wt. tea alkaloid, 1-3 pts. wt. seaweed powder, 1-3 pts. wt. chelated iron, and 1-3 pts. wt. selenium yeast.    USE - Green vegetable bio-organic fertilizer (claimed).    ADVANTAGE - The green vegetable bio-organic fertilizer contains 16 nutrients necessary for crop growth and elements of other beneficial crop growth, and increases farmer's income, promotes plant growth and reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of green vegetable bio-organic fertilizer.
NOVELTY - An organic seaweed fertilizer comprises Sargassum, Enteromorpha, cow dung, avermectin dregs, phosphocitric acid residue, calcium phosphate, guano phosphate, papermaking wastewater, high-temperature Halomonas, Sporotrichum thermophile, marine Nocardia, Bacillus megaterium, glial Bacillus and Streptomyces.    USE - Organic seaweed fertilizer is used for corn.    ADVANTAGE - The organic seaweed fertilizer promotes thickening of corn stalk, improves ear weight and grain weight of corn and sugar content and taste of corn and can effectively reduces generation of corn smut.    DETAILED DESCRIPTION - An organic seaweed fertilizer comprises 55-65 pts. wt. Sargassum, 70-80 pts. wt. Enteromorpha, 40-50 pts. wt. cow dung, 13-16 pts. wt. avermectin dregs, 13-16 pts. wt. phosphocitric acid residue, 10-12 pts. wt. calcium phosphate, 21-25 pts. wt. guano phosphate, 100-120 pts. wt. papermaking wastewater, 1-1.2 pts. wt. high-temperature Halomonas, 1.5-1.8 pts. wt. Sporotrichum thermophile, 1.2-1.5 pts. wt. marine Nocardia, 1.5-1.8 pts. wt. Bacillus megaterium, 0.8-1 pt. wt. glial Bacillus, and 0.8-1 pt. wt. Streptomyces.    An INDEPENDENT CLAIM is included for preparation of organic seaweed fertilizer which comprises weighing 60 pts. wt. Sargassum, 75 pts. wt. Enteromorpha, 45 pts. wt. cow dung and 50 pts. wt. papermaking waste water, crushing, controlling the temperature to 50-55 degrees C, stirring, adding 1. pts wt. Halomonas, reacting for 10-14 days, controlling the temperature at 33-35 degrees C, adding 0.9 pts. wt. marine Nocardia, 1.2 parts wt. Bacillus megaterium, and 0.3 pts. wt. Streptomyces, reacting for 15-18 days, adding 14 pts. wt. avermectin dregs, 15 pts. wt. phosphocitric acid residue, 11 pts. wt. calcium phosphate and 24 pts. wt. guano phosphate, heating to 95-100 degrees C, boiling for 3-4 hours, controlling the temperature at 30-33 degrees C, stirring at 29-36 degrees C for 15-20 days and granulating.
NOVELTY - The utility model is new type relates to biological fuel gas purification waste water processing equipment technology field, especially relates to one kind biological fuel gas purification waste water comprehensive using device, the utility model is new type using following technology scheme: comprising fuel gas purification system, heating type evaporator, heating type evaporator provided with sewage inlet, a sewage outlet, gas purification system is discharging mouth connected heating water inlet of sewage type evaporator, the utility model is new type of advantage wherein the biological fuel gas purification waste water through heating the evaporator for evaporation, to realize substance of waste water and to carry out effective separation, biological fuel gas purification waste water by evaporator for evaporation of generating the second time steam directly by mixing gasification furnace and sum for sending wind participate gasification reaction, steam no second time via condensing, then using equipment is simple, quadratic steam obtained waste heat recovery use, increase whole efficiency of system.
NOVELTY - The new type utility claims have one plant modified manganese slag clean compound fertilizer production system, comprising prefabricate manganese slag system, production system of compound fertilizer and compound fertilizer drying cooling exhaust sum processing system, the prefabricate manganese slag system comprises combustion furnace draught fan I, a combustion furnace I, a slag dryer, modified device acidification and neutralization reactor, the 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, fertilizer cooling machine, cold air draught fan, a sieving machine, a coating machine and measuring machine, the compound fertilizer drying cooling exhaust sum processing system comprises settling chamber, a washing tower, a sediment pool and clear water tank. The utility model is new type adopts high temperature decomposing and preparing phosphoric acid and treatment method for carrying out modified manganese slag, modified manganese slag as raw material for prepare compound fertilizer product, the waste as treasure. In addition, the utility model is new type compound fertilizer drying cooling exhaust sum to carry out have full process, which can ensure the environment-friendly clean production.
NOVELTY - The new type utility claims have one kind environment-friendly clean coal and comprehensive using manganese slag compound fertilizer production system, including coal generating system, production system of compound fertilizer and compound fertilizer drying cooling exhaust sum processing system, the coal generating system comprises two-section coal gas, tar collector, cyclone dust collector, cutter and urgency before furnace water seal tank, the compound fertilizer production system comprises combustion furnace draught fan, a combustion furnace, weigh burdening system, a mixer, pulverizer raw material, the compound fertilizer dryer, fertilizer cooling machine, cold air draught fan, a sieving machine, a coating machine and a metering package machine. The utility model is new type using manganese slag as raw material, by adding each kind nitrogen, P, potassium base fertilizer prepared compound fertilizer product, the waste as treasure. In addition, the utility model is new type using two-section coal gas as heat source device, increase have gas and gasification efficiency, the utility model is new type cooling tail sum processing also have full process for compound fertilizer drying, which can ensure the environment-friendly clean production.
NOVELTY - The new type utility claims have one plant environment clean and prefabricate manganese slag system, comprising prefabricate system manganese slag and manganese slag drying tail sum processing system, the prefabricate manganese slag system comprises combustion furnace draught fan, a combustion furnace, slag dryer, modified device acidification and neutralization reactor, the manganese slag drying tail sum processing system comprises heat exchanger, buffer tank, washing tower, a sediment pool and clear water tank. The utility model is new type manganese slag to exist and the strong oxidizing substance potassium permanganate and alkaline substance KOH, it adopts high temperature decomposing and preparing phosphoric acid and processing method for processing the modified, manganese slag satisfy using compound fertilizer production requirement, not to crops and soil would cause dangerous not only solves have discharge problem of the waste, but also full use resource waste is; and the utility new type drying tail sum processing to have full process, which can ensure the environment-friendly clean production.
NOVELTY - Strain of bacteria Bacillus stratosphericus RNCIM B-11677, producing ethanol from lignocellulosic biomass, is proposed.    USE - Biotechnology.    ADVANTAGE - Strain represents strong growth in the lignocellulosic biomass and has resistance to the toxic components of lignocellulosic hydrolyzate.2 ex
NOVELTY - The utility model discloses a feeding cloth device suitable for forming straw particle, comprising forming machine, a connecting base fixedly connected on molding machine rotate on base, base connected with bottom through material pipe, the upper joint is connected with standing base, standing joint upper part periphery provided with upper cover, lower part set with sealing, as follows upper cover set with bearing, bearing as follows provided with retainer ring, standing through shaft joint and connecting base connected with, the utility new type beneficial effect is: raw material to ensure uniform thickness is paved on upper flat die, using biomass is full grinding, increase production efficiency, reduce energy consumption, particle forming more uniform, it is suitable for flat model biomass granule forming machine.
NOVELTY - The new type utility claims have recovery synthesis ammonia tail sum LNG production and device, it comprises circulation nitrogen compressor, the first condenser, the second condenser, third cooler and set in the pre-cooling heat exchanger in cool tank, a booster turbine expansion machine, a gas-liquid separator, rectifying tower and methane rectifying tower, the pre-cooling heat exchange device comprises carbon dioxide cooler and main heat exchanger. With the following advantages: using cryogenic separation synthesis ammonia tail sum technology, for synthesis ammonia production useful and hydrogen to obtain recovered at the same time and carry out have full extract for methane, and liquefied as LNG and high added value, reducing ammonia synthesis cost, full recovery on use and environmental protection problem in synthesis ammonia tail sum resource so.
NOVELTY - The utility model is new type provides one kind died animal corpse harmless treatment device, that have animal corpse treatment in the existing technology would generate second time pollute, body can not get to use the problem. Said processing device comprises control box, bracket, heating system and reaction cylinder, bracket top part set with slide rail and box cover, bracket lower part set with driving bracket and bucket base plate, tube and reaction cylinder set on bucket body base plate above, the response also comprises cylinder set is connected with discharging nozzle, tube outside wall at feed opening to the left end plate on the two end and right end tube plate, tube side wall provided with and heating system connected on the oil slot, inner tube provided with cutting knife, cutting knife comprises bucket wall and tube inside wall connected cutter and the cutter set on the main shaft on the main shaft, main shaft and driving device connected. The invention not exist the whole process of incineration, would not pollute environment, but also is with smell of smoke, and the raw material after reaction can be again using time, it can save the full resource.
NOVELTY - The utility model is new type relates to biomass gasification field, especially relates to one kind of biomass gasification system, comprising to use for carrying out the first stage gasification reaction waste biomass flow and generating the first gasification furnace, the gasification furnace comprises first drying area, pyrogenation, gasification area and combustion area, and the second gasification used for absorbing the first stage after gasification reaction is tar and carbon for the second stage reaction and gasification furnace, the second gasification furnace and the gasification furnace connected with the first. The utility model is new type set by the second gasification furnace used for to the tar after the first stage gasification reaction, carrying out the second stage carbon gasification reaction, using resource to obtain have circulation use, saves have resource.
NOVELTY - The new type utility claims have one plant biomass fuel gas cooling system, one grade of cooling tower, a gas-liquid separator A grade, second grade cooling tower and second level gas-liquid separator composed of a first-stage cooling tower and tar outlet of first-stage gas-liquid separator respectively and spray water entrance and one grade cooling tower by pipeline connected, and on the pipeline mounting oil filter and oil pump. Because of the first-stage spray directly to separate out the high temperature gas containing tar, the tar product not containing water, using tar as one grade cooling tower spray medium is replaced with tar water, saves have water resource, but also reducing have stock of tar and processing difficulty.
NOVELTY - The utility model supplies one kind of vertical type biomass particle machine box body, comprising four support and one of the whole cuboid box body, four of the support fixed at four angle to bottom of lower box body is cuboid, the cuboid box body bottom to the bottom left side set with one central line of the round hole, the round hole vertical to the upper bottom set with corresponding one of large circular hole, the circular hole right side formed with one of small circular hole, the rectangular box at bottom vertical corresponding to small round hole set with symmetrical and same size on bottom of small circular hole. The utility model is new type can be further increase particle machine box body structure compactness, increase body of high strength, high hardness and, realize versatility of particle machine box body, set with motor fixing plate can be directly and motor fixed on the box body on the granule machine, can be further reducing biomass granulator of the occupied space, the utility model is new type structure is compact, using suitable, small square meter, use is worth to be popularized.
NOVELTY - A lignocellulosic biomass which is substrate, and aqueous ammonia are mixed in reaction container (2) to obtain substrate mixture. The lignin is dissociated from the substrate, or substrate is swollen, in order to obtain ammonia-containing saccharification preprocessed material by heating the substrate at preset temperature and maintained for predetermined time. During formation of substrate mixture, the substrate is accommodated in reaction container, and after pressure-reducing reaction container by exhausting air in reaction container, the aqueous ammonia is added and mixed.    USE - Saccharification pre-processing of lignocellulosic biomass used for producing bioethanol used as automotive fuel.    ADVANTAGE - The method enables efficient saccharification pre-processing of lignocellulosic biomass by enabling favorable penetration of ammonia into the substrate, and suppressing expansion of substrate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus structure enforcing pre-processing method.    Preprocessor (1)    Reaction container (2)    Ammonia collection units (3,4)    Exhaust gas pipes (8,30,32,36)    Vacuum pump (33)
NOVELTY - A hydrogen-producing catalyst comprises solid solution of complex oxide containing rhodium, zirconium and rare-earth metal.    USE - Catalyst is used for producing hydrogen used for fuel cell system (all claimed) used for electric power generation.    ADVANTAGE - The catalyst enables efficient manufacture of hydrogen, even at low temperature, and reduces usage of noble metal. Anode oxidation of electrodes of power generation cell maintained in reducing atmosphere at low temperature zone is suppressed. By suppressing the slip occurrence of the unreformed fuel in reformer outlet, coking generation at the power generation unit of reformer downstream is suppressed. By suppressing deterioration of the power generation cell of fuel cell system, the durability of the fuel cell system is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of hydrogen-producing catalyst, which involves obtaining complex oxide by baking precipitate obtained by adding nitrate aqueous solution of zirconium and rare-earth metal to aqueous ammonia;    (2) production of hydrogen, which involves steam reforming hydrogen raw material-containing hydrocarbon compound using the hydrogen-producing catalyst;    (3) hydrogen production apparatus, which consists of modification portion, and supply portion which supplies gas containing steam in modification portion containing hydrogen-producing catalyst; and    (4) fuel cell system, which consists of the hydrogen production apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Water tank (1)    Water pump (2)    Fuel tank (3)    Fuel feed pump (4)    Desulfurizer (5)
NOVELTY - The system (1000) has a preheat hot tub (10) that is provided to heat the moisture content organic raw material including the food waste preliminarily, and is installed in and out of the carbonization reactor (20). The carbonization reactor is provided to carbonize the moisture content organic raw material according to the hydrothermal pressurization carbonizing method. An indirect heating device (30) is provided for heating the carbonization reactor through the heating pipes in which the heated insulating oil is indirectly flowed into the inside.    USE - System for producing biochar from food waste and organic waste such as sewage sludge.    ADVANTAGE - The percentage of water content of the biochar is minimized and the solid fuel in which the calorific value is high is generated. The bad smell generated in the reactor is prevented. The combustible gas is recycled to the heating energy and the energy consumption is minimized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the method for producing biochar.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for producing biochar.    Preheat hot tub (10)    Carbonization reactor (20)    Indirect heating device (30)    Bio liquid tank (50)    System for producing biochar (1000)
NOVELTY - The new type utility claims have one kind two-section combined type coal, comprising coal for device, a clapboard, a furnace body, a dust removing device, furnace wall, centre pipe, furnace bottom blast, water cool body and steam drum water box body, wherein: the furnace body set with outside furnace wall, the clapboard is located between the coal for device and a furnace body, the furnace wall outside set with dust-removing device, the water cool body and water cool body connected with steam drum, the utility model is new type provided with two of the same for coal device on the furnace body of the upper part, forming two-section combined type coal furnace, it can add coal for more and more, when one time of carrying on coal device need maintain, for the detachable and starting clapboard, switching into another one for using coal device replaces work, maintain at the same time and not affect the normal work and greatly increase work efficiency, use vertical integrated design, which greatly reduce square meter floor space of device, reducing production cost.
NOVELTY - A plant biomass material gasification clean energy conversion device, comprising splitting furnace, first-stage purification device, second level purification device, the first-stage separation device, second level separating device and blower, the splitting furnace comprises temperature control system, and by internal connecting pipe in turn connected with one level purification device, second level purification device, the first-stage separation device, second level separating device, a Roots blower. The utility model is new type having the following characteristics: energy conversion quickly, 5 minutes and that can generate clean gas, directly used for industrial supply heat, using equal. Reducing can storage device investment, at the same time because there is no air storage tank, can eliminate have safety hidden danger of flammable and explosive gas. There is no smoke dust discharge, at the same time producing gas and charcoal double A clean energy. With no pollute, zero discharge, low cost, large yield, suitable with equal. Charcoal variety, can directly use burning.
NOVELTY - A lower plant gasification furnace used for the connected double lock coal feedstock comprises coal lock device (1), a coal lock at valve (2), a coal lock lower valve (3), for (14), transition cavity (4) and coal (13), a coal lock (1) with 2 number, of each coal lock (1) is for (14), for (14) is coal lock at valve (2), a coal lock (1) and bottom connecting pipe (7) is connected on connecting pipe (7) on the top part is equipped with coal lock lower valve (3), a connecting pipe (7) and transition cavity (4) bottom connected with the transition cavity (4) and bottom is coal (13), 2 of coal lock (1) between through at least 1 of coal lock sum channel (5) connected. The utility model is new type with coal lock pressing coal consume low, operation cost is low.
NOVELTY - The new type utility claims have one plant alcohol ether fuel synthesis device, by using methyl alcohol and additive mixture after adding gas dimethyl ether, again by the first ultrasonic wave generator 2 time/second and the second ultrasonic wave generator 4 time/second, to let methyl alcohol and dimethyl ether, additive synthesis high heat value liquid fuel, then again enter into sum liquid separating tank, not entirely dissolve the dimethyl ether recovery processing, not reach alcohol ether solution and mixing concentration returning to the first channel process to process, to make dimethyl ether can be stable to dissolve in methanol, increase methanol, methanol can make full combustion, reducing have fuel cost.
NOVELTY - The method involves passing a gas mixture across a separation membrane including a feed side and a permeate side, where the separation membrane includes a selective layer comprising copolymer with two perfluorodioxolane monomers. Driving force is provided for transmembrane permeation. A permeate stream enriched in a component compared to a gas mixture is withdrawn from the permeate side of the separation membrane. A residue stream depleted in the component compared to the gas mixture is withdrawn from the feed side of the separation membrane.    USE - Method for separating two components such as hydrogen, carbon dioxide, nitrogen, helium, methane and organic compounds (all claimed), of a gas mixture i.e. natural gas, using gas-separation copolymer membranes.    ADVANTAGE - The method enables using oxygen to enhance combustion of fuels so as to achieve improved burning zone control and reduce emissions.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating a relationship between pure gas hydrogen permeance and hydrogen/methane selectivity as function of Monomer H content for membranes with selective layers composed of copolymers of Monomers D and H.
NOVELTY - Producing high purity carbon material by thermal decomposition natural gas, comprises introducing natural gas into a reactor, purifying transition metal and alkali metal with unknown suspended material and iron contained in the natural gas through combination of mash filter and magnetic filter (1), a water scrubber (2) and a moisture filter (3), and depositing waste deposition material.    USE - The method is useful for producing high purity carbon material (claimed).    ADVANTAGE - The method reduces time and installation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the high purity carbon material production apparatus (Drawing includes non-English language text).    Mash filter and magnetic filter (1)    Water scrubber (2)    Moisture filter (3)    Carbon fiber preform (5)    Vacuum pump (7)
NOVELTY - Aerosol-type cosmetics comprise undiluted solution containing compound (a) chosen from lecithin, N-acyl glutamic acid, amino-modified silicone, and ceramide, metal oxide powder (b), partially crosslinked organopolysiloxane polymer (c) and liquid oil (d), and propellant.    USE - Aerosol-type cosmetics used as make-up cosmetics, such as foundation, concealer, rouge, makeup base, eye-shadow, sunscreen cosmetics, and cosmetics for bodies and hair.    ADVANTAGE - Spilling and clogging of cosmetics are prevented. Cosmetics have good usability.
NOVELTY - A use one manufacturing biomass fuel and bark, comprising pressing cage, a screw rod, a pressure pole, the lower part of cage formed with funnel shaped collected material cylinder, the funnel shaped material cylinder lower end close to the collected pressure pole, inner screw of said auger pressing block extends into the funnel-shaped collecting cylinder, the utility model is new type of advantages is material pressing after material is compact, not easy breaking loose.
NOVELTY - An electrode consists of a substrate, and a catalyst portion containing copper-containing particles having particle diameter of 50-500 nm on portion(s) of the surface of the substrate.    USE - Electrode is used in electrochemical reduction of water and carbon dioxide, and hydrogen and carbon for manufacture of electrochemical reduction product (all claimed).    ADVANTAGE - The electrochemical reduction product can be economically manufactured using the electrode with high energy efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of electrode;    (2) electrochemical reduction method, which involves decomposing water and carbon dioxide, or hydrogen and carbon using the electrode; and    (3) manufacture of electrochemical reduction product.
NOVELTY - Preparing humus comprises taking 60-70 pts. wt. processed soy sauce residue, 15-25 pts. wt. straw stick, and 5-10 pts. wt. oyster powder, mixing and smashing, then adding 5-10 pts. wt. water, mixing uniformly, adding 0.1-0.2 pts. wt. strain, at 32-36 degrees C, boiling for 3-5 days, subjecting to thermal sterilization, taking 100-150 pts. wt. resulting product, adding 30-50 pts. wt. ammonium bicarbonate, heating at 80-100 degrees C, and sealing for 6-10 days to obtain the finished product.    USE - The method is useful for preparing humus (claimed).    ADVANTAGE - The method is simple, and has high humus yielding rate.
NOVELTY - Dissolved air-flotation oilfield wastewater is biological-degreased and pretreated in joint station. The oilfield wastewater is supplied to aerobic biological treatment system. The treated oilfield wastewater is supplied to microalgae culture system, and flue gas is supplied, and microalgae are grown in track-type microalgae culture system, to obtain treated oilfield wastewater. The treated oilfield wastewater is supplied to carbon filter system, and microalgae are collected. The sludge is filtered with press filter and carbon filter and sterilized water is cleaned and deoxygenated.    USE - Processing of oilfield wastewater (claimed).    DETAILED DESCRIPTION - Dissolved air-flotation oilfield wastewater is biological-degreased and pretreated in joint station. The oilfield wastewater is supplied to aerobic biological treatment system to remove crude oil. The oilfield wastewater is aerobic biological degreased by adding nitrogen and phosphorus and pressed to form mixture having total organic carbon, nitrogen and phosphorus in weight ratio of 100:5-10:1. The treated oilfield wastewater has crude oil content of less than 2 mg/L. The treated oilfield wastewater is supplied to microalgae culture system, and flue gas with carbon dioxide content of 3-15% is supplied, and microalgae are grown in track-type microalgae culture system for 5-15 days to density 107/ml, to obtain treated oilfield wastewater containing lipid content of more than 20% and microalgae. The treated oilfield wastewater is supplied to carbon filter system, and microalgae are collected. The sludge is filtered with press filter and carbon filter and sterilized water is cleaned and deoxygenated to low permeability.
NOVELTY - Method for producing vermicompost, involves mixing substrate components, moisturizing, placing the mixture in a container having height of 1.2-1.5 m, maintaining for 15-20 days, colonizing the mixture using mature worms, moisturizing the mixture until moisture content reaches 70% and maintaining for 4-4.5 months, where the substrate comprises 40 wt.% buckwheat husk, organic feedstock comprising 35 wt.% purified sugar juice, and mineral feedstock comprising 15 wt.% aluminum salt slag and 10 wt.% zeolite.    USE - The method is used for producing vermicompost (claimed).
NOVELTY - The utility model claims a municipal garbage and sludge comprehensive treatment system, including classify plant, on sow classify connected with sewage treatment device and marsh gas generating device, also connected with marsh gas collecting device and carbide reducing device, wherein carbide reduction device above also connected with dust removing device and water circulation device on in marsh gas generating device. The utility model is new type supply one A municipal garbage and sludge comprehensive treatment system, waste treatment slag and fume realize zero discharge, which completely avoids have second time pollute and discharge of harmful gas, and the protection have land and water resource, atomphere environment and human body health, at the same time solves world difficult to have low cost method for dehydrating and resource circulation using the above problem in domestic sludge treatment, increase have efficiency and economic benefit of treatment, further reducing have government to work into the economic burden and atomphere greenhouse effect reducing burden, further increase have social and economic benefit of state, increase have development competition of enterprise.
NOVELTY - The composition fuel includes mixing the water electrolysis gas and liquid fossil fuel vaporized. The fossil fuel is petroleum, gasoline, diesel, kerosene, bunker oil or biodiesel.    USE - Composition fuel for use in internal combustion engine (Claimed).    ADVANTAGE - The composition fuel includes mixing the water electrolysis gas and liquid fossil fuel, and thus enables reducing the pollution element. The fire is reduced due to the fast reaction of combustion. The water electrolysis gas generation efficiency is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for internal combustion engine combustion; and    (2) an internal combustion engine comprises a fuel tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an internal combustion engine.    Fuel tank (100)    Water electrolysis gas manufacturing device (200)    Mixer (300)    Engine (400)
NOVELTY - A methane/nitrogen separation adsorbent comprises KX-type zeolite/activated carbon composite material obtained by placing X-type zeolite/activated carbon composite material in potassium ion solution, and exchanging sodium ions with potassium ions.    USE - Methane/nitrogen separation adsorbent (claimed).    ADVANTAGE - The methane/nitrogen separation adsorbent has finely regulated pores with a pore size distribution of 0.48-0.57 nm, and has excellent absorption capacity with respect to methane and low absorption capacity with respect to nitrogen, thus exhibiting excellent methane/nitrogen adsorption separation performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methane/nitrogen separation adsorbent, which involves taking X-type zeolite/activated carbon composite material and 0.1-1.5 mol/L potassium ion solution in a ratio of 1:20-30, impregnating the composite material with the solution, carrying out ion-exchange at 60-90 degrees C for 40-60 minutes, and drying.
NOVELTY - Gene construct comprising a polynucleotide encoding polypeptide comprising SEQ ID NO: 43, and a polynucleotide encoding polypeptide comprising SEQ ID NO: 44, is new. Sequences not defined here may be defined at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The gene construct is useful for preparing enzymatic composition used for producing fermentable sugar; and for degrading cellulosic biomass, where degradation of cellulosic biomass takes place for producing by-product, where the by-product is a biofuel, e.g. ethanol (all claimed).    ADVANTAGE - The polysaccharide monooxygenases have the advantage that they are able to increase the efficiency of saccharification of cellulosic biomass by an increase in the amount of fermentable sugars produced at the end of the hydrolysis process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) host cell comprising the gene construct;    (2) an enzymatic composition comprising a polypeptide comprising SEQ ID NO: 43 and a polypeptide comprising SEQ ID NO: 44 and, preferably, other cellulolytic enzyme selected from endoglucanase, beta-glucosidase, cellobiohydrolase, beta-xylosidase, endoxylanase, endoxyloglucanase, monooxygenase polysaccharide and its combination;    (3) a method for producing fermentable sugar comprising: (a) incubating cellulosic biomass with the enzymatic composition; and (b) recovering the fermentable sugars obtained after incubation in step (a); and    (4) a process for producing a by-product from cellulosic biomass comprising: (a) incubating cellulosic biomass with the enzymatic composition; (b) fermenting the fermentable sugars obtained after incubation in step (a) with at least a fermenting microorganism, and (c) recovering the by-product obtained after fermentation of step (b).
NOVELTY - Manufacture of sugar liquid involves filtering saccharified liquid of cellulose-containing biomass through nanofiltration membrane and/or reverse-osmosis membrane, washing nano-membrane filter and/or reverse-osmosis membrane after filtration using acid wash purified liquid, and washing nano-membrane filter and/or reverse-osmosis membrane washed with acid wash purified liquid using alkali wash liquid.    USE - Manufacture of sugar liquid used for fermentation.    ADVANTAGE - The method enables manufacture of sugar liquid with suppressed clogging of nanofiltration membrane or reverse-osmosis membrane by an impurity derived from saccharified liquid.
NOVELTY - The new type utility claims have one plant mixing device, especially one kind organic fertilizer biological microbial inoculum online quantitative adding device, belonging to agricultural equipment technology field, and the organic fertilizer biological microbial inoculum online quantitative adding device comprises orderly connected with the smashing device and sieving device and sieving material transmission device composed of, on the screen material transmission device set with continuous add material device, the screen material transmission device is belt transport machine, the utility model is new type of organic fertilizer biological agent quantitative adding device is online, by continuous add material device and material transmitting device and realize have online quantitative biological microbial inoculum is added, compared for adding traditional method, which greatly increase the have added efficiency and add the homogeneity, at the same time reduce have manual cost and device cost investment, low cost and is good for biological organic fertilizer, in addition, the utility model is new type method after first sieving material by adding biological microbial inoculum is to avoid have the biological waste, further reducing have production cost.
NOVELTY - The new type utility claims one kind of biomass gasification furnace fuel gas preparation system, internal space of the furnace body through the first sieve plate is divided as gasification reaction area and feedstock discharge mixeduse district. The top wall of the furnace body set with biomass material inlet, the bottom wall of the furnace body set with water steam entrance and hot air entrance, the first sieve plate provided with biomass discharging mouth. Feedstock discharge mixeduse district through separation barrel for biomass feedstock channel and gas collecting discharging channel, and the top of the channel for discharging fuel gas collecting on the top wall in the furnace body set with fuel gas outlet. Gas collecting discharging channel is located on surface of the first sieve plate, space outside surface and inner surface of furnace body of material surrounded by the inner cylinder. Wherein, biomass discharging mouth is set with lower part used for using biomass material of dispersing uniformly to the material cone and gasification reaction area, and rotation driving device further provided with for driving the cone circle of material.
NOVELTY - The new type utility claims one kind from pre-heating biomass gasification furnace, internal space of the furnace body through the first sieve plate is divided as gasification reaction area and feedstock discharge mixeduse district. The top wall of the furnace body set with biomass material inlet, the bottom wall of the furnace body set with water steam entrance and hot air entrance, the first sieve plate provided with biomass discharging mouth. Feedstock discharge mixeduse district through separation barrel for biomass feedstock channel and gas collecting discharging channel, and the top of the channel for discharging fuel gas collecting on the top wall in the furnace body set with fuel gas outlet. Gas collecting discharging channel is located on surface of the first sieve plate, space outside surface and inner surface of furnace body of material surrounded by the inner cylinder. Wherein, in discharging at gas collection channel provided with the pipe, and set with water jacket around the outside wall of the furnace body at outside of gasification reaction area.
NOVELTY - The new type utility claims one kind of biomass gasification furnace waste heat comprehensively using system, internal space of the furnace body through the first sieve plate is divided as gasification reaction area and feedstock discharge mixeduse district. The top wall of the furnace body set with biomass material inlet, the bottom wall of the furnace body set with water steam entrance and hot air entrance, the first sieve plate provided with biomass discharging mouth. Feedstock discharge mixeduse district through separation barrel for biomass feedstock channel and gas collecting discharging channel, and the top of the channel for discharging fuel gas collecting on the top wall in the furnace body set with fuel gas outlet. Gas collecting discharging channel is located on surface of the first sieve plate, space outside surface and inner surface of furnace body of material surrounded by the inner cylinder. Surrounding set with wind shell, wherein the outside wall of the furnace body at outside of feedstock discharge mixeduse district, upper part of wind shell provided with cold air entrance, lower part of shell set with heat air outlet wind, cold air entrance through pipeline connected to draught fan, hot air outlet through bottom wall of pipeline and furnace body on the hot air entrance connected.
NOVELTY - The new type utility claims one kind of biomass gasification furnace is set with second grade tar filter, the internal space of the furnace body through the first sieve plate is divided as gasification reaction area and feedstock discharge mixeduse district. The top wall of the furnace body set with biomass material inlet, the bottom wall of the furnace body set with water steam entrance and hot air entrance, the first sieve plate provided with biomass discharging mouth. Feedstock discharge mixeduse district through separation barrel for biomass feedstock channel and gas collecting discharging channel, and the top of the channel for discharging fuel gas collecting on the top wall in the furnace body set with fuel gas outlet. Gas collecting discharging channel is located on surface of the first sieve plate, space outside surface and inner surface of furnace body of material surrounded by the inner cylinder, wherein, the first sieve plate is set with ceramic ball filter layer above the biomass fuel gas to carry out first-stage tar filter. The biomass gasification furnace further comprises second grade filtering device for biomass fuel gas by second grade tar filter.
NOVELTY - The new type utility claims have one plant biomass making sum furnace U-shaped foam dust-removing device. A plant biomass making sum furnace U-shaped foam dust-removing device comprises fume pipe and the draught fan, fume entrance and smoke sum between outlet provided with U-shaped foam dust-removing pipe, U-shaped foam dust-removing pipe close to one end entrance is set with fume and the first foam pipe connected the foam nozzel, U-shaped foam dust-removing pipe close to one end sum smoke outlet of the second foam and the foam outlet pipe connected, the first foam tube and between the second foam tube provided with foam and foam storage tank, bottom tube and U-shaped foam dust-removing pipe is connected, the bottom tube provided with belt flange knife gate valve and the lower flange, U-shaped foam dust-removing pipe at lower end of the foam outlet set with round filter screen frame, U-shaped foam dust-removing pipe is foam outlet and upper end set with dustproof ventilating film round frame. The utility model is new type suitable for dust removing and biomass for making sum furnace, can reach to efficient and lasting and dust-removing effect.
NOVELTY - The new type utility claims one plant purifying device of biological diesel oil, category lipid chemical industry technology field, the utility model is new type device comprises the feeding port I, port II, port III, a conveyor belt, a mixer, a valve I, a reaction tank, pump I, a pipeline I, a valve II, a valve III, pump II, a press, a mixer, a pipeline II, a pump III, pipeline III, buffer tank, granulator, upper level sediment tank, outlet I, outlet II, two level sediment tank, valve IV, valve V, the lower sediment tank, valve VI, valve VII, filter, the utility model is new type preparation to obtain the biological diesel oil purity is more than 98.2%, the heat value of fuel for more than 3000kcal/kg, biology diesel oil purifying middle and later period are non pollutant production, with simple technique, suitable operation, high efficiency, no pollute, low energy consumption, clean and semi continuous process of production.
NOVELTY - This utility model claims a device using acorn lees to prepare biologic diesel oil and feed, belonging to biological energy field,device of the utility model comprises separator I,evaporator I, extracting device, evaporator II,evaporator III, separator II, reactor, separator III, rectifier.Separator I provided with one entrance and two outlet respectively connecting with evaporator I and extracting device.Bottom end of extracting device connected with evaporator II,upper end of extraction device connected with evaporator III.Lower end of evaporator III connected with separator II,separator II, reactor, separator III and rectifier connected in turn, alcohol steam pipe respectively connected with extracting device,evaporator III, reactor and rectifier.Decice using acorn lees to prepare biologic diesel oil and feed of the utility model is featured by suitable operation, high efficiency, no pollute, low energy consumption andgood product market.
NOVELTY - The utility model is new type relates to carry out automatic family biology diesel oil and soap by the synthesis device, especially one kind family automatic fertilizer soap and biological diesel oil synthesis device. The lower part in the lower part it is: comprising shell (3), wherein the shell (3) has mounting pedestal (7), wherein the shell (3) mounted with reaction container (4), wherein the reaction container (4) is mounted with heating plate (2), the heating plate (2) and control temperature device mounted in shell (3) and upper (6) connected, on the said shell (3) is mounted with motor (10), the motor (10) through transmission mechanism and the agitator blade in into reaction container (4) connected with, the motor (10) is also connected with motor and control device mounted in shell (3) and above. The utility model is new type of beneficial effect is, for reasonable use of catering waste oil supply have one of simple structure, and suitable processing device, can reduce catering waste oil to ecological environment and food safety cause the dangerous state.
NOVELTY - Alkaline catalytic film comprises a polymeric material and an inorganic solid alkali as a catalyst, where the solid alkali is linked to polymeric material by chemical grafting process using a linking agent.    USE - The catalytic film is useful in catalytic transesterification of oils and low carbon alcohol for preparing biodiesel oil (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing , comprising (i) dissolving inorganic solid alkali in deionized water, adding linking agent, heating at 50-90 degrees C, and magnetically stirring for 2-4 hours, to obtain a modified solid alkali solution; (ii) dissolving polymeric material in deionized water, and ultrasonically mixing, to obtain solution; (iii) mixing the products obtained in the steps (i) and (ii) added in equivalent volumes, and heating while magnetically stirring for 2-6 hours at 50-75 degrees C, to obtain viscous film casting solution; (iv) allowing the film casting solution to stand for de-foaming, casting on a glass plate, placing in an oven at 50 degrees C under vacuum of 1.33 kpa, and drying for 2 hours, to obtain polymeric material and solid alkali hetero compound-based catalytic membrane; and (v) washing unreacted linking agent and excess particulate which are physically adsorbed on solid alkali catalyst by using ethanol, and drying for 3 hours at 50 degrees C under vacuum (1.33 kPa), to obtain the final product.
NOVELTY - The system has compression mechanism (X1) that is provided to receive exhaust pressure of each component. A rectification mechanism (Y) is provided to receive output flow of compression mechanism, and recover the propylene oxide mixed flow (2) and residual gas stream. The compression mechanism is provided to receive the remaining tail gas stream from rectification mechanism and to output remaining tail gas stream (4). A cryogenic unit (Z) is provided to receive the remaining tail gas stream from compression mechanism, and to separate non-condensable gas for recovering propylene and propane.    USE - Butyl octanol tail gas recovery system.    ADVANTAGE - The energy consumption is reduced, the high recovery rate is achieved and the propylene and propane mixture is obtained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for butyl octanol tail gas recovery method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the butyl octanol tail gas recovery system. (Drawing includes non-English language text)    Propylene oxide mixed flow (2)    Remaining tail gas stream (4)    Compression mechanism (X1)    Rectification mechanism (Y)    Cryogenic unit (Z)
NOVELTY - Ethylhexyl salicylate is synthesized by adding salicylic acid in esterification kettle, stirring and raising temperature to 160 degrees C, then slowly dripping mixture of isooctyl acrylate and phosphotungstic acid to the kettle, and separating out water generated in reaction system; after dripping is finished, preserving heat and continuously stirring until no water is generated in reaction process; and stopping reaction, cooling reaction product in esterification kettle to room temperature, crystallizing and centrifuging to obtain ethylhexyl salicylate finished product.    USE - Method for synthesis of ethylhexyl salicylate (claimed).    ADVANTAGE - The method has simple operation and easy to control synthesis process condition, little reaction by-product, and low production cost, and is green and environment-friendly.
NOVELTY - Olmesartan medoxomil condensate (I) is purified by dissolving olmesartan medoxomil crude condensate in mixed solvent of dichloromethane and acetonitrile, and carrying out low temperature crystallization to obtain high purity olmesartan medoxomil condensate.    USE - Method for purifying olmesartan medoxomil condensate (claimed).    ADVANTAGE - The method has high yield, low device requirement, simple operation, and less wastewater generation, and is environment-friendly and suitable for industrial large production. The crystallization solvent can be directly applied to a next crystallization. The purity of the olmesartan medoxomil condensate is greater than or equal to 98%.    DETAILED DESCRIPTION - Purification of olmesartan medoxomil condensate of formula (I) comprises dissolving olmesartan medoxomil crude condensate in mixed solvent of dichloromethane and acetonitrile, and carrying out low temperature crystallization to obtain high purity olmesartan medoxomil condensate.
NOVELTY - The preparation method of rivaroxaban (I) involves reacting 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one compound (II) with 5-chloro-thiophene-2-carboxylic acid compound (III) in the presence of a condensing agent containing 2,4,6-trichloro-1,3,5-triazine, 2-chloro-4,6-dimethoxy-1,3,5-triazine, 2,4-dichloro-6-methoxy-1,3,5-triazine and 2-chloro-4,6-diphenyl-1,3,5-triazine, and organic alkali.    USE - The method is useful for preparation of rivaroxaban (I) (claimed).    ADVANTAGE - The method enables simple and economical preparation of rivaroxaban (I) with high yield and purity in an environmentally-friendly manner.    DETAILED DESCRIPTION - The preparation method of rivaroxaban of formula (I) involves reacting 4-(4-((5S)-5-(aminomethyl)-2-oxo-1,3-oxazolidin-3-yl)phenyl)morpholin-3-one compound of formula (II) or its salt with 5-chloro-thiophene-2-carboxylic acid compound of formula (III) in the presence of a condensing agent containing 2,4,6-trichloro-1,3,5-triazine, 2-chloro-4,6-dimethoxy-1,3,5-triazine, 2,4-dichloro-6-methoxy-1,3,5-triazine and 2-chloro-4,6-diphenyl-1,3,5-triazine, and organic alkali.
NOVELTY - The furnace has a furnace unit (2) whose upper portion is provided with an electric heating unit (1) that is formed with a sum layer. The furnace unit is provided with an internal furnace unit. A furnace liner is fixedly connected with a furnace liner support (3). A lower end of a spiral input device (5) is fixedly provided with a tar catalytic splitting room (6). The spiral input device is sleeved on a furnace frame (4). A biomass gasification furnace catalyst portion (7) is arranged between the spiral input device and the furnace unit.    USE - Low temperature-type multi-functional industrial integrated biomass furnace.    ADVANTAGE - The furnace is simple in structure and easy to operate, and has high heating speed, low production cost, better heat transfer effect, low heat loss, high heating efficiency and prolonged service life. The furnace saves water resources, avoids environment pollution and ensures integrated catalytic splitting and purification filtering performance.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the low temperature-type multi-functional industrial integrated biomass furnace.    Electric heating unit (1)    Furnace unit (2)    Furnace liner support (3)    Furnace frame (4)    Spiral input device (5)    Tar catalytic splitting room (6)    Biomass gasification furnace catalyst portion (7)
NOVELTY - The anti-odor flushing-free toilet (1) has main portion which multi-row toilet pits (2) which are provided with parallel discharging through-holes (13). The storage tank (6) is provided below one row or two rows of toilet pit. The stirrer (5) and filler (4) are provided inside the storage tank.The transmission mechanism is connected with the power machine (9). A discharging door (3) is set in drainage port of storage tank. The power machine is electrically connected with the controller (10).    USE - Anti-odor flushing-free toilet.    ADVANTAGE - The storage tank is provided at the lower portion of toilet pit, and stirrer/filler is provided inside the tank, so that the excrement can directly enter in the storage tank. The filler can be changed easily. The excrement can be absorbed easily. The generation of peculiar smell is prevented. The need to use water for flushing is prevented, so that precious water resources can be saved. The filler is used as the agricultural fertilizer effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anti-odor flushing-free toilet.    Anti-odor flushing-free toilet (1)    Discharging door (3)    Filler (4)    Stirrer (5)    Storage tank (6)    Power machine (9)    Controller (10)    Discharging through-hole (13)
NOVELTY - The utility model is new type relates to vehicle tail sum purification equipment field, especially relates to one kind hydrodynamic machine vehicle system can solve the problem that the exist of vehicle engine combustion efficiency and low problem comprises: high frequency resonance pulse electric control device, water power saving oil device, safe water supply isolator, filter and electric source line and sum pipe, water power saving device on oil provided with positive and negative connector, power supply line respectively by positive and negative electrode of vehicular power supply system connected with the high frequency resonance pulse electric control device is connected with power source line connected in series of positive pole above the water power saving device on oil provided with water inlet and water outlet, water separator and safe to be electrolytic water, upper side wall provided with the water mouth, electrolytic mixture entrance and fuel gas outlet, by sum pipe, and water power saving oil device on the connected water inlet, a water outlet and electrolytic mixture entrance connected, entrance at the fuel gas outlet and connected filter, filter on the upper outlet and is set with air inlet pipe on vehicle engine connected the sum tube.
NOVELTY - The new type utility claims have one plant biology diesel oil synthesis technique and device, the goal is that in order to overcome the defect that the traditional biologic diesel oil preparation technology device needed multi-one more step to finish the reaction, providing have utility new type of raw material oil pre-processing reaction kettle " and " one step method catalytic esterification and crosslinking esterification reaction kettle " process equipment. Wherein technology scheme of the utility model is new type of the process device, the characteristic comprising one platform cylindrical jacketed electrification heating rod and stirring reaction kettle, the reaction kettle is set with internal layer blade of stirrer, wherein the top and bottom as butterfly; side wall with plate pipe, cylinder upper part set with feedstock mouth, lower part provided with a discharging mouth, kettle top center set with planet cycloidal-pin wheel speed reducer, stirring shaft, stirring motor, the reaction kettle bottom formed with and material extracting liquid; A method catalytic esterification and crosslinking step esterification reaction kettle and the fractionation column, a condenser, connected, the utility model is new type process equipment than the traditional device is simple and practical.
NOVELTY - The new type utility claims have one kind structure is simple, the environment-friendly stool and urine separating type ecological toilet. Three large part the toilet comprising control system, flushing system and microorganism purification system, control system comprises infrared sensor, rotate speed controller and liquid level meter, microorganism purification system comprises solid liquid separating device, a solid microorganism decomposing groove, sewage buffer groove, water pump, an aeration and aerobic biological filter chamber, flushing system comprises water storage tank, water pump, depth purification tank and water closet flushing pool, solid-liquid separating device and water closet flushing pool, a solid microorganism decomposing groove and sewage buffer groove connected with the aerobic biological filter pool by water pump and sewage buffer slot and depth purification tank connected, and the aeration and aerobic biological filter chamber connected, depth purification tank by water pump and water storage tank connected, water storage tank and water closet flushing pool connected, water closet flushing pool and control system by infrared sensor connected with. The ecological toilet has simple structure, operation cost low, which is good for environmental protection and resource regeneration use.
NOVELTY - A municipal sewage plant sludge composite type biological processing system, comprising mixer, hydrolysis acidification tank, Anaerobic fermentation tank, solid-liquid separating system, an aerobic fermentation tank, heat exchanger, odor treatment system. Sewage sludge through sludge pump sending into mixer, adding after smashing the straw regulate solid-containing rate,, adjust and mix the material pump enter hydrolysis acidification tank, material pump after the hydrolysis acidification enter Anaerobic fermentation tank by Anaerobic fermentation. By pH, temperature, ORP sensor control biogas relux quantity, stirring material, accelerate fermentation. Fermentation production of methane gas into the storage tank, after solid-liquid separation liquid through heat exchanger after heating for hydrolysis acidification tank, Anaerobic fermentation tank and aerobic fermentation tank and carrying out heat preservation. Biogas residue by sending feeder to aerobic fermentation tank, after adding smashing straw for aerobic fermentation by sensor control temperature, oxygen content, material stirring. In easy to produce stench section equipped with odour collection device, after using ozone to process purification discharge system. The utility model is new type combined have Anaerobic digestion method and aerobic composting advantages and fertilizer method, treatment efficiency high, low investment operation cost is low, it can root up from municipal sewage treatment plant sludge and solves the resource use and second time pollute problem.
NOVELTY - A plant organic fertilizer fermentation device, comprising one of the tank body, the tank body one end has cover and equipped with transmission teeth, said cover set with an air outlet pipe, the transmission teeth connect with one of transmission pedestal, shaft base tank body another end through the support shaft mounted on the whole can go up and down and one up, the tank body is double-layer hollow structure, the tank body side wall formed with one pair and interlayer connected with the infusion pipe, inside the tank body set with one of said tank body and fixedly connected with the stirring shaft. The utility model is new type of providing one kind of organic fertilizer fermentation device, no need to use the special turning device, greatly reducing production cost, and can avoid the pollute gas.
NOVELTY - The new type utility claims have one plant nitrogen-enriched biomass pyrolysis cogeneration containing chemicals and nitrogen-doped nitrogen coke and system, including nitrogen-enriched pyrolysis sub-system, nitrogen-doped sub-system, a nitrogen element into sub-system, nitrogen gas condensing sub-system. Nitrogen-rich pyrolysis sub-system generating high temperature smoke sum, and cause biomass and exogenous nitrogen element generating reaction, enriched nitrogen gas condensing sub-system for pyrolysis gas by condensing separating out enriched nitrogen containing chemicals and liquid product and for storing the coke nitrogen-doped sub-system generating high temperature gasification sum, and coke by deep processing process and to save the coke product after cooling, exogenous nitrogen element into sub-system to nitrogen pyrolysis sub-system and coke-doped nitrogen sub system providing exogenous nitrogen, capturing and absorbing the NOx in fume. The utility model is new type can be continuous production nitrogen-enriched oil and rich nitrogen, finish one step method in high value containing nitrogen chemicals and super capacitor carbon material, active pushing biomass efficient high quality conversion.
NOVELTY - The new type utility claims have one kind firewood bar carbonization process special for replacement, comprising upper supporting ring and lower supporting ring bottom, upright post, a retainer ring, a lifting lug and cage, fixedly mounted on upright post in lower support ring, upper support ring is fixedly mounted with upper sleeve, sleeve is sleeved on upright post up and through opening pin and upright post connected with fixed, moving steamer mounted on lower support ring above. The utility model is new type for upright post and sleeve adopt moving connection, which not only realize have replacement cage height is adjustable, satisfying have no loading requirement of length for firewood bar, when using according to length of firewood bar can properly adjust the height, and the replacement cage structure is simple, easy to operate, can further control and have made carbon and cost, at the same time and lower steamer supporting ring adopt moving connection, discharging comparison suitable, but also reduce have manual taking material and working amount, low labour low intensity, large amplitude and increase have working efficiency, is continuous for the mechanism to create coal have condition, and it is easy to popularize use.
NOVELTY - The utility model is new type device relates to carbon dioxide is one kind of removing methane, especially relates to one kind marsh gas low temperature compressor decarburization device, comprising compressor (1), wind cooling radiator (2), the first heat exchanger (3), the second heat exchanger (4), a refrigerator (5) and high pressure storage tank (6), the first heat exchanger (3) and the second heat exchanger (4) are provided with heat medium entrance, heat medium exit, cold medium entrance, cold medium outlet of four terminal. The utility model is new type device used less amount, reduce the maintenance cost and have each part operation, decarburization effect stable, reliability without added chemistry absorbing substance and physical adsorption substance, reducing have investment, small square meter small, according to scale and operation project and determining each exchanger, size, can the maximum effect of reducing occupied square meter.
NOVELTY - The new type utility claims have one plant for waste wood material as raw material and mechanism coal production system, including carbonizing furnace and drying furnace, carbonization of the carbonization room and lower combustion chamber is composed of upper layer, carbonization chamber top part of combustion gas outlet tube may end in installation with square and waste heat, waste heat recovery device set with heat-absorbing, drying furnace through the gas outlet bottom horizontal pipe and waste heat recovery device connected, on the combustible gas outlet pipe also set and combustion room connected with the combustion gas circulation can input pipe, burning room and smoke exhaust pipe of drying furnace through smoke sum input pipe connecting water dust remover. The utility model is new type formed by waste heat recycling and dust-removing processing device, greatly reducing have system heat loss, active control have sum of waste discharge system, and implementation have the recovery resource again using, variable waste as treasure, with the good social benefit and economic benefit, and it is easy to popularize use.
NOVELTY - A municipal solid organic waste dry Anaerobic digestion device, wherein A has one vertical feedstock cabin, lower end of vertical feedstock cabin connected with one transverse mixing of feedstock cylinder, wherein bottom of one end face of transverse mixture feedstock is cylinder, set with one transverse mixing of feedstock cylinder discharge pipe, a transverse mixing feedstock cylinder discharge pipe connected with one of the plunger pump, the plunger pump connected with one outlet of the tank body feedstock tube, upper tank body feedstock tube pipe opening, respectively connecting two of feedstock tube, two feedstock pipe through bottom of the dry Anaerobic digestion tank, bottom of dry Anaerobic digestion tank connected with one of inverted cone, inverted cone lower part connected with one of vertical out slag pipe, a vertical out slag pipe connected with three transverse slag A, transverse slag... relux. The utility model is new type has simple structure, install. feedstock mixing device, which ensures. municipal solid organic waste and dry Anaerobic digestion efficiency. The device can be widely applied for feedstock municipal solid organic waste dry-type Anaerobic digestion.
NOVELTY - The new type utility claims have one plant sludge compost production line, including feedstock mouth is set with stirring device, sludge into the stirring device for feedstock wherein the continuous transport device and agent pump sending device to sludge and microorganism microbial inoculum is added, the agent pump sending device comprises liquid storage tank, the continuous transport device end and the shower nozzle is located above the feeding port and can make the microorganism microbial inoculum in the liquid storage tank pump to feeding pump and the shower nozzle. The sludge compost production line for adding microorganism and selecting position at end of continuous transport device, the transport device to continue feeding the above blanking in stirring device, using feeding pump to let microorganism microbial inoculum with two strip high pressure network management send to end blanking of continuous transport device, the shower nozzle and shower nozzle direction alignment for blanking direction spray. Make the using rate of microorganism increase, and uniform contact.
NOVELTY - The new type utility claims have one A biological processor for kitchen garbage, comprising box body, the top part of the box body provided with the feeding port, the internal box body provided with the fermentation tank, the feeding and fermentation tank connected phase, the fermentation tank provided with internal stirring shaft, said stirring shaft and equipped with connected stirring motor in transmission and the fermentation tank outside the fermentation tank and the micro biodegradable fungus liquid phase tank connected, the top part of the fermentation tank provided with supplement water mouth, bottom set with water outlet, the utility model is new type of advantages wherein: can effective degradation of dangerous substance, degradation time of garbage short, as organic fertilizer can return farmland to avoid have addressing to large garbage treatment plant and construction and high the converying, protection have environmental, economic and efficient.
NOVELTY - The new type utility claims have one kind of fertilizer granulation drying system, comprising pelletizer, roller transfer device to the inner transport fertilizer granulator and drier and the granulator and is connected, said granulator comprises internal provided with crushing device and driving the roller of the rotating electrical machine, the drying machine comprises drying cylinder and drying furnace and said drying cylinder is connected, the drying furnace at set with water tank, the upper water tank provided with the hot water tube extends into the inner roller, the hot water pipe provided with multiple nozzles in on roller. The fertilizer pelleting drying system, in drying furnace obtained by hot water and using hot water into pelletizer water tank replaced with substitute steam boiler, granulating into ball faster and at the same time make the hot air drying furnace in drying cylinder, fertilizer and energy saving environment-friendly use drying furnace heating after drying and granulating the waste heat water tank, reducing production line manufacturing cost, reducing pollute environment.
NOVELTY - The utility model claims a distributed rural domestic waste plant resource use device, comprising a waste pre-processing system device, sewage Anaerobic fermentation pool and second level sewage treatment pool, wherein the waste pre-processing system comprises household garbage, stirring system, organic garbage hydrolysis pool and inorganic garbage storage pool. The utility model is new type A and A scattered type rural household waste resource use device and its application and existing technology compared to fermentation with raw material adaptability, disposable investment, simple operation suitable, protection operation cost low and can recovery part clean energy, realize have equal source decrement and domestic garbage and domestic garbage reducing weight by rate is more than 40%, greatly reducing of have household garbage collection, converying cost, realize have domestic sewage and can process and of, without laying to multi-pipeline too, suitable distributed rural domestic waste processing and low investment, requirement of low maintenance cost, with good popularization and use value.
NOVELTY - The utility model claims a composite fermentation tank, belonging to fermentation equipment field, comprising: a tank body, a stirring device, driving device, spraying device, relux device and filter device, wherein the set paddle stirring leaves can generate radial acting force with strong cutting effect, to promote large particle diameter of solid object dispersing and mixing with biogas slurry fullly, at the same time avoiding the crusting, the push type stirring leaves can produce axial force, with small cutting force, wherein the harm to methane fungus damage is small; bottom of the tank body to force liquid biogas production circle direction flow, forming an annular liquid circulation stirring the following in relux screw rod pump extraction effect, mechanical stirring and liquid stirring relux common function, increase stirring effect, reducing stirring power consume, equipped with two of a discharging port, effectively in the fermentation tank and biogas slag discharge, increase fermentation efficiency, filter device and material again producing fermentation, saves effective fermentation raw material, further reducing cost.
NOVELTY - The invention claims have one vehicle hydrogen gas manufacturing system and the electrolyte container, the electrolyte container comprises box body, said box body holding electrolyte is set with containing cavity, the box body also comprises a liquid outlet, gas inlet and gas outlet, the gas outlet is higher than gas inlet, the electrolyte container at the same time containing electrolyte as the container, and cooling and filtering as hydrogen and oxygen and device, compared with the existing technology separately set with electrolytic groove, cooling tank and filtering tank, the structure is simple, the volume is small, it saves space. The system because of using have the electrolyte container, to make the whole system volume is variable and is small, which is more convenient for mounting to motor vehicle above.
NOVELTY - The invention claims have one vehicle A hydrogen oxygen gas manufacturing device and system, the device and electric conduction plate is equipped with anode plate and cathode plate between, wherein between adjacent plate body by insulation sealing element, and each surrounded by sealing the cell in, an anode plate, a cathode plate and upper electric conduction plate respectively provided with connecting hole for each cell in connected. Hydrogen and oxygen and the device belongs to the immunizing for the electrolytic production of hydrogen and oxygen by instant transmission pipeline input to internal combustion engine and combustion, in the whole process of hydrogen and oxygen only exist for the transfer pipeline between device and internal combustion engine gas entrance in the hydrogen and oxygen amount of the one part relative then communication is compare small and, therefore, no need to worry about hydrogen-oxygen mixed gas explosion cause dangerous accidents. And the inner combustion engine and combustion room in the full fuel combustion, waste is in the combustion process of the fuel, also for reducing waste sum discharge, especially reducing carbon monoxide and discharge amount of nitrogen monoxide, which is good for environmental protection.
NOVELTY - Method for controlling rot disease in apple, involves detecting lesion of 0.5 cm, scrapping the lesion from outer skin of the apple to 2 cm, and applying mixture comprising garlic and vinegar in a weight ratio of 1:1 for 3-4 times and once a week on scrapped portion.    USE - The method is useful for controlling rot disease in apple (claimed).    ADVANTAGE - The method is natural and environmentally-friendly, and produces organic fruit.
NOVELTY - Producing liquid fertilizer, comprises (a) liquefying environmentally friendly water-soluble chemical composition, (b) weighing the crab byproduct, (c) calculating the optimum reaction weight of the liquefied composition based on the weight ratio of the crab byproduct, (d) spraying the optimal weight of the liquefied composition on byproduct, and (e) decomposing the byproduct.    USE - The fertilizer is useful as composition and food additive.    ADVANTAGE - The method is environmentally friendly and stable, reduces energy, cost and time, does not require processing plants and use strong acids or strong bases, and produces environmentally friendly liquid fertilizer regardless of the type of the crab by-product.
NOVELTY - alpha -Ferric oxide-graphene inverse opal structure has three-dimensional- alpha -ferric oxide-graphene inverse opal laminated on substrate.    USE - alpha -Ferric oxide-graphene inverse opal structure is used for fabricating electrode for water-splitting device (claimed).    ADVANTAGE - The alpha -ferric oxide-graphene inverse opal structure has high photocurrent density and low sheet resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of alpha -ferric oxide-graphene inverse opal structure, which involves electrodepositing nickel, adding polystyrene particles, polyol, solvent, etchant and aqueous ferric chloride solution.
NOVELTY - The device has a lifting device (2) that is set with head located along axial direction of a vertical fixed shaft (3), and hinged upwards on fermentation bag housing (1). A moving buckle (4) is connected with tail portion of the tray located along axial direction of folding type supporting frame. A fixing portion (6) is fixedly set on upper portion of tray. A folding portion (7) is rotated around the fixing portion connected with a square horn opening portion. The fermentation bag housing and the tail portion are connected with pallet (5) through folding type supporting frame.    USE - Device for fermenting agricultural crop waste material.    ADVANTAGE - The energy consumption required for fermenting the agricultural crop waste material is reduced. Convenient operation of the fermenting device is ensured. The manufacturing cost of the fermenting device is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the device for fermenting agricultural crop waste material.    Fermentation bag housing (1)    Lifting device (2)    Vertical fixed shaft (3)    Moving buckle (4)    Pallet (5)    Fixing portion (6)    Folding portion (7)
NOVELTY - The invention claims a treatment device for recovering glycerin from the biologic diesel oil comprising the reaction kettle, methanol recovery device and glycerol process tank composed, where in the reaction kettle is provided with a stirrer and the methanol gas outlet equipped on the top part of the reaction kettle equipped is connected to the methanol recovery device; the heating jacket used for infusing steam is set on the outside wall of the reaction kettle; the discharge port is connected to the glycerol process tank through the pipe; the glycerol process tank is set with the vent nozzle and alkali adding port; and the glycerol process tank is also set with a circulation pump for ciculating the materials in the glycerol treatment tank; the end part of the circulation pump is connected to the bottom of glycerol treatment tank through the pipe and is connected to the side wall of the glycerol treatment tank through the pipe; the outlet for the finished glycerol is set bettween the end part of the circulation pump and the glycerol process tank. This device has simple structure and fast processing speed which can separate out many kinds of product so as to increase the production benefit of enterprise.
NOVELTY - The utility model is new type relates to the field of coal chemical industry, especially claims a solar energy electric aluminum fertilizer coal carbon oil paper integrated carbon hydrogen circulation device, comprising the solar energy air can wind can power generation system, intelligent sending coal, coal catalytic device, filter, power generation system of fly ash, electric melting solid-liquid separator, solar energy aluminum electrolyzer, CO2, CO2 separator, a remote anti-explosion monitoring centre, said intelligent sending and the catalytic device connected with coal, coal catalytic device and power generation system, connected with filter, filter and CO2 catcher connected with the power generation system and power fly ash melting solid-liquid separator, aluminum electrolyzer connected with solar energy of fly ash, electric melting solid-liquid separator and aluminum electrolyzer connected with solar energy, solar energy aluminum electrolyzer and CO2, solar energy air can wind can power generation system connected with, CO2 and collector CO2 connected with separator. The utility model is new type of beneficial effect wherein: it can carry out integrated unite production, saves resource, increase heat can use rate, water discharge.
NOVELTY - The method involves taking process of sludge by gravity sedimentation and concentration in a concentration pool (1). The anaerobic treatment temperature is maintained at 20 to 37 degrees C. The releasing of anti-gene such as sulfonamide anti-gene and tetracycline anti-gene, and quantity of sludge are detected by a real time fluorescence quantitative polymerase chain reaction (PCR) instrument (4). The pH value of alkali liquid is controlled in the range 9.0 to 11.0 by the anaerobic treatment process, using feedback regulating amount, according to detecting result of anti-gene release amount.    USE - Method for reducing anti-gene released in sludge anaerobic treatment process, for use in sewage processing plant.    ADVANTAGE - The reduction of supernatant anti gene releasing amount of the sludge residual is achieved. The anti gene reduction process is simplified, and the reduction effect is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process of reducing anti-gene released in sludge anaerobic treatment process. (Drawing includes non-English language text)    Concentration pool (1)    Ultrasonic preprocessing device (2)    Real time fluorescence quantitative PCR instrument (4)    Computer (5)    Alkali pool (6)
NOVELTY - Production of special organic fertilizer involves mixing humic acid raw materials and 3.0 mol/L sodium hydroxide solution, heating, stirring, filtering, collecting filtrate, mixing humic acid raw materials and 3.0 mol/L sodium hydroxide solution, heating, stirring, filtering, combining filtrates, adjusting filtrate pH value to obtain humic acid, mixing with animal manure where mass ratio of animal manure, humic acid and leavening agent is 91-97:1-15:2-4, grinding, stirring, sieving, adding minerals, crushing, adding water, stirring, stacking, fermenting, granulating, drying and cooling.    USE - Method for producing special organic fertilizer for vegetables (claimed).    ADVANTAGE - The method is environment-friendly.    DETAILED DESCRIPTION - Production of special organic fertilizer comprises mixing humic acid raw materials and 3.0 mol/L sodium hydroxide solution at ratio of 1:3-4, heating at 40-45 degrees C for 2-3 hours, stirring, filtering, collecting filtrate, mixing humic acid raw materials and 3.0 mol/L sodium hydroxide solution at ratio of 1:3-4, heating, stirring, filtering, combining filtrates, adjusting filtrate pH value to 6.0-6.7 using inorganic acid to obtain humic acid, mixing with animal manure where mass ratio of animal manure, humic acid and leavening agent is 91-97:1-15:2-4, grinding, stirring, sieving, adding minerals at ratio of 85-92:8-15 where minerals are 8 wt.% monoammonium phosphate, 5 wt.% ammonium sulfate, 15 wt.% urea, 8 wt.% calcium magnesium phosphate, 16 wt.% potassium chloride or potassium sulfate, 14 wt.% iron ore slag waste, 25 wt.% humic acid and 9 wt.% phosphogypsum, crushing, adding water, stirring, stacking, fermenting at 75 degrees C for 15-18 days, granulating, drying and cooling.
NOVELTY - Livestock and poultry excrement deodorizing decomposition agent comprises 9-12 pts. wt. ferrous sulfate, 2-4 pts. wt. magnesium sulfate, 95-110 pts. wt. calcium superphosphate, 15-18 pts. wt. potassium oxide ore powder, 17-20 pts. wt. phosphorus pentoxide rock powder, 30-45 pts. wt. peppermint extract, 15-20 pts. wt. laurel extract, 12-15 pts. wt. Ammopiptanthus nanus extract, 0.3-0.8 pt. wt. gelling agent, 4-8 pts. wt. boric acid or borax, 10-35 pts. wt. natural zeolite powder, 6-15 pts. wt. microbial deodorizing agent and 200-250 pts. wt. water.    USE - Livestock and poultry excrement deodorizing decomposition agent used for livestock and poultry manure processing and deodorizing method to prepare odorless active ecological organic fertilizer raw material (all claimed).    ADVANTAGE - The livestock and poultry excrement deodorizing decomposition agent achieves convenient disposal of livestock and poultry excrement, reduces insect eggs and germs contamination and environmental pollution, and has simple operation and good deodorization effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for livestock and poultry manure processing and deodorizing method using livestock and poultry excrement deodorizing decomposition agent comprising weighing the components, dissolving magnesium sulfate and boric acid or borax in water, adding ferrous sulfate, stirring to completely dissolve, adding calcium superphosphate, potassium oxide ore powder and phosphorus pentoxide rock powder, continuously stirring, adding peppermint extract, laurel extract and A. nanus extract, stirring to obtain manure treatment agent, mixing (based on 1000 kg manure) 15-20 kg manure treatment agent and 0.2-0.7 kg microbial deodorizing agent, diluting with 5-10 times water, spraying to livestock and poultry excrement, stirring uniformly and naturally standing for 5-7 days to obtain odorless active ecological organic fertilizer raw material.
NOVELTY - Preparing p-anisaldehyde, comprises (i) dissolving p-hydroxybenzaldehyde in an organic solvent, in presence of a catalyst composition, and carrying out methylation reaction of dimethyl carbonate, to obtain a reaction liquid, then filtering the reaction liquid, and distilling, to obtain the final product, where catalyst composition includes a first catalyst and a second catalyst, and first catalyst is a phase transfer catalyst, and the second catalyst is an alkaline catalyst, an acidic catalyst or biological enzyme catalyst, and the phase transfer catalyst is e.g. tetrabutylammonium bromide.    USE - The method is useful for preparing p-anisaldehyde (claimed).    ADVANTAGE - The method has target product yield reaching up to more than 90%, product purity reaching up to more than 99%, and dimethyl carbonate utilization rate of 61%; and is economical, and environmental friendly.    DETAILED DESCRIPTION - Preparing p-anisaldehyde, comprises (i) dissolving p-hydroxybenzaldehyde in an organic solvent, in presence of a catalyst composition, and carrying out methylation reaction of dimethyl carbonate, to obtain a reaction liquid, then filtering the reaction liquid, and distilling, to obtain the final product, where the catalyst composition includes a first catalyst and a second catalyst, and the first catalyst is a phase transfer catalyst, and the second catalyst is an alkaline catalyst, an acidic catalyst or biological enzyme catalyst, and the mol ratio of p-hydroxybenzaldehyde, dimethyl carbonate, first catalyst and the second catalyst, is 0.5-1:1.24:0.05-0.1:0.2-0.75, and the phase transfer catalyst is tetramethylammonium chloride, tetramethylammonium bromide or tetrabutylammonium bromide.
NOVELTY - Preparation method of photosynthetic bacteria fertilizer involves (a) inoculating Thiocapsa roseopersicina into semi-solid culture medium and culturing, and activating strains from the culture, (b) inoculating activated strain into liquid medium, and anaerobically culturing liquid culture for 7-10 days, and (c) mixing seed culture obtained in step (a), fermentation culture medium and inoculum obtained in step (b) in a ratio of 1:1-2:5, anaerobically culturing mixture for 7-10 days and stirring at 120 revolutions/minute, and filling and packing product.    USE - The method is useful for preparing photosynthetic bacteria fertilizer (claimed).    ADVANTAGE - The method prepares photosynthetic bacteria fertilizer which prevents hydrogen sulfide poisoning by rapidly degrading hydrogen sulfide, promotes root development in rice, repairs soil, reduces culture time, and is cost-effective and not required in large quantity e.g 100 ml/acre.    DETAILED DESCRIPTION - Preparation method of photosynthetic bacteria fertilizer involves (a) inoculating Thiocapsa roseopersicina into semi-solid culture medium and culturing at 25-35 degrees C under light for 7-10 days, and activating strains from the culture, (b) inoculating activated strain into liquid culture medium, and anaerobically culturing liquid culture at 25-35 degrees C and 1000-3000 lux for 7-10 days until optical density of culture reaches not less than 1.2 at 650 nm and concentration of bacteria reaches not less than 6 hundred million colony forming units (cfu)/ml broth, and (c) mixing seed culture obtained in step (a), fermentation culture medium and inoculum obtained in step (b) in a ratio of 1:1-2:5, anaerobically culturing mixture at 25-35 degrees C and 1000-4000 lux for 7-10 days and stirring at 120 revolutions/minute until optical density of culture reaches not less than 4 at 650 nm and concentration of bacteria reaches not less than 20 hundred million cfu/ml broth, and filling and packing product.
NOVELTY - Garden waste treatment method comprises digging in the garden plants between line width 0.2-0.5 m and 0.2-0.5 m deep earth ditch; taking garden plant leaves, trim branches, harvesting weeds, pulverizing, mixing with nitrogen, phosphorus, potassium, trace elements and microbial inoculum to obtain a mixture of organic matter mixture; carrying out soil excavation trenches, and laying a thickness of 0.1-0.15 m; spraying water on the mixture of organic matter; and covering the organic matter mixture of 0.05-0.1 m soil layer.    USE - Garden waste treatment method.    ADVANTAGE - The method improves soil compaction conditions, and reduces garbage dumps.
NOVELTY - Special fertilizer comprises 26-30 pts. wt. dairy manure, 22-25 pts. wt. straw, 10-15 pts. wt. corn straw, 3-5 pts. wt. borax, 4-6 pts. wt. chitosan, 20-24 pts. wt. urea, 10-15 pts. wt. hydrated lime, 8-12 pts. wt. potassium humate, 2-4 pts. wt. sodium selenite, 4-7 pts. wt. composite amino acid, 0.3-0.5 pt. wt. carbendazim and 0.1-0.3 pt. wt. effective microorganisms (EM).    USE - Special fertilizer used for preventing pepper anthracnose disease (claimed).    ADVANTAGE - The special fertilizer increases the yield and quality of product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of special fertilizer comprising mixing dairy manure, straw, corn straw and chitosan, fermenting to obtain fermented material, adding into pulverizer, crushing, indoor airing to water content of less than 60%, taking borax, urea, hydrated lime and potassium humate, crushing, adding composite amino acid, carbendazim and EM, adding into fermented material, stirring uniformly and packaging.
NOVELTY - A drumstick mushroom cultivation covering material comprises 100 pts. wt. humus, 100-120 pts. wt. sandy soil, 3-5 pts. wt. lime, and 3-5 pts. wt. pesticidal fungicidal agent. The humus comprises crop straw, reed powder, bran, and cotton seed hull at ratio of 1:3-5:0.3-0.5:1-1.5.    USE - Drumstick mushroom cultivation covering material.    ADVANTAGE - The covering material is high in nutrient content, has good air permeability, strong water absorption, and high water retention property, and can improve physicochemical property of soil material and loosen soil structure so as to increase mushroom fruiting rate, yield and quality of drumstick mushroom.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the covering material, comprising mixing crop straw, reed powder, bran and cotton seed hull, adding water to the mixture, uniformly stirring, then stacking and fermenting, keeping material temperature at 60-70 degrees C, stirring for 3-5 times to form humus substance mixture, and then drying; and adding the humus with sandy soil, lime and insecticidal bactericide, uniformly stirring, and regulating pH value to 8-9 to obtain the covering material.
NOVELTY - Preparation of avanafil comprises hydrolyzing 4-((3-chloro-4-methoxybenzyl)amino)-5-(ethoxycarbonyl)-2-(methylthio)pyrimidine, reacting with condensing agent in the presence of acid binding agent and 2-(aminomethyl)pyrimidine hydrochloride, reacting with meta-chloroperoxybenzoic acid, carrying out oxidation reaction at less than or equal to 0 degrees C, reacting with L-prolinol and performing condensation reaction.    USE - Method for preparing avanafil (claimed).    ADVANTAGE - The method is environment-friendly and simple.
NOVELTY - Extraction of aerobic particle sludge total protein comprises centrifuging aerobic particle sludge with clean deionized water; grinding aerobic granular sludge with liquid nitrogen; regulating the pH value of aerobic particle sludge at 11-14; regulating the pH of the aerobic particle sludge, digesting at 45-55 degrees C, and controlling the digesting time for 9-12 hours; and digesting the aerobic particle sludge, and taking the supernatant to obtain the aerobic particle sludge total protein.    USE - Method for extracting aerobic particle sludge total protein (claimed).    ADVANTAGE - The method is simple, and has high efficiency.
NOVELTY - Apixaban synthesis involves performing ammonolysis of ethoxy compound (I) to give the finished compound apixaban, where the ammonolysis is carried out by using ammonia solution.    USE - Method for synthesizing apixaban (claimed).    ADVANTAGE - The method synthesizes apixaban in a simple, safe, cost-effective and eco-friendly manner with high purity greater than 97% and high yield under mild reaction condition on industrial scale.    DETAILED DESCRIPTION - Apixaban synthesis involves performing ammonolysis of ethoxy compound of formula (I) to give the finished compound apixaban, where the ammonolysis is carried out by using ammonia solution.
NOVELTY - And A composting plant is suitable for straw and livestock excrement mixing, belonging to technology field of compost, compost device relates to one kind is suitable for straw and livestock excrement and mixing. The utility model is new type supply one kind is suitable for straw and mixing the livestock manure compost, the compost device that have the manual turning not in time caused by the temperature, humidity and oxygen supply stable and no problem to ensure stability of compost system. The utility model is new type using following technology scheme: one kind is suitable for straw and livestock excrement mixing and composting device comprises stack layer, insulating layer, heating device, an aeration pump and aeration plate, carrying out heat preservation layer set on outside side wall of stack layer above, heating device set on insulating layer inside, with aeration plate set at inner layer stack, formed with the waste liquid outlet on the bottom stack layer, stacking layer of the aeration pump and aeration plate under each connected.
NOVELTY - The new type utility claims have one plant biomass can not condensed sum using system, comprising drying furnace, circulation fluidization bed reactor, a gas-solid separator, double grade spray tower and secondary reactor, double grade spray tower is respectively connected with the air outlet pipeline and the air and drying furnace hearth of circulation fluidization bed reactor between. By using no coagulation sum circulation recovery input may give circulation fluidization bed reactor participate biomass splitting reaction, not only effective recovery can not condensed sum then not waste, and because of no coagulation sum not containing oxygen may then make gasification reaction process keeping inert gas environment, increase the safety of system, then the redundant and not condensed sum can then give drying furnace combustion using, implementation may not condensed sum circulation use.
NOVELTY - Preparing methyl or ethyl ethers of glycerol comprises reacting glycerol fraction from transesterification of triglycerides of fatty acids with methyl or ethyl alcohol containing methyl or ethyl esters of fatty acids, unreacted alcohol and water, and alcohol in presence of acid catalyst. The process comprises reacting glycerol with methyl or ethyl alcohol at 140-200 degrees C under a pressure of 5-90 bar, optionally in presence of an electromagnetic field over a catalyst comprising an active sulfonic acid, cooling, degassing and removal of acid catalyst, and isolating ethers and fractionation.    USE - The process is useful for preparation of methyl or ethyl ethers of glycerol, that are used as a component for improving the performance of diesel fuels in diesel engines and in manufacturing of polyurethanes.    DETAILED DESCRIPTION - Preparation of methyl or ethyl ethers of glycerol comprises reacting glycerol fraction from the transesterification of triglycerides of fatty acids with methyl alcohol or ethyl alcohol containing methyl or ethyl esters of fatty acids, unreacted alcohol and water, with an alcohol in the presence of an acid catalyst, in a closed pressurized system. The process comprises reacting 90 wt.% glycerol having a pH of 0-7 with methyl alcohol or ethyl alcohol at 140-200 degrees C under a pressure of 5-90 bar, optionally in the presence of an electromagnetic field over a catalyst comprising an active sulfonic acid, cooling the reaction mixture to a temperature below 60 degrees C, degassing and removal of the acid catalyst, isolating glycerol ethers and subjecting to potential fractionation to obtain mono-, di- or tri glycerols.
NOVELTY - Cultivating organic selenium-enriched blueberry comprises (a) preparing selenium-rich organic substrate composition by mixing 1-3 pts. selenium containing cardamine, 20-40 pts. straw fermentation material,10-30 pts. composting manure, and piling; (b) sowing blueberry nursery, and placing selenium-rich organic substrate having thickness of 0.5 cm; (c) prior to transplantating blueberry, administering base fertilizer on the selenium-rich organic substrate; (d) administering selenium-rich organic matrix as top dressing on blossoming and fruit setting blueberries.    USE - The method is useful for curing cultivating organic selenium-enriched blueberry (claimed).    ADVANTAGE - The method is economical and efficient, non-polluting, increases selenium level, and has positive significance in preventing and curing diseases.    DETAILED DESCRIPTION - Cultivating organic selenium-enriched blueberry comprises (a) preparing selenium-rich organic substrate composition by mixing 1-3 pts. selenium containing cardamine, 20-40 pts. straw fermentation material,10-30 pts. composting manure, and piling; (b) sowing blueberry nursery at 200 m2, and placing selenium-rich organic substrate having thickness of 0.5 cm; (c) prior to transplantating blueberry, administering 120-150 kg/acre base fertilizer on the selenium-rich organic substrate; (d) administering selenium-rich organic matrix as top dressing on blossoming and fruit setting blueberries, where the application rate is 100-120 kg/acre.
NOVELTY - Biologically controlling barley disease resistance and promoting growth comprises (i) culturing Bacillus subtilis CICC 10339, where the density of high density bacterial suspension is 109-1010 colony forming unit (cfu)/ml; (ii) cutting the barley straw into small pieces, composting by spraying high density bacterial suspension, fermenting to obtain fertilizer, which is capable of inhibiting and killing the pathological fungi of barley, and using the fertilizer for controlling the disease resistance of barley and promoting growth.    USE - The method is useful for biologically controlling barley disease resistance and promoting growth (claimed).    ADVANTAGE - The method is simple and easy to operate, economical, does not discharge wastewater, consumes less energy, is suitable for large scale industrial production, and has good economic benefit.
NOVELTY - Cultivating oyster mushroom using mulberry stalk comprises processing mulberry, preparing culture medium, packaging, sterilized inoculating, culturing hyphae, fruiting management and harvesting. The raw materials comprises 40-80% mulberry branch cuttings, 0-20% cottonseed core, 15-25% saw dust, 10-15% bran and 2% lime powder.    USE - The method is useful in cultivating oyster mushroom using mulberry stalk (claimed).    ADVANTAGE - The method utilizes agricultural waste e.g. mulberry sericulture cuttings as its raw materials, solves the problem of mulberry raw material resource waste, realizes the resource optimization, and promotes industrial rapid development of oyster mushroom.
NOVELTY - Preparing bacitracin zinc premix, comprises (i) adding zinc sulfate into a fermentation liquid, adding a flavoring agent, a flocculating agent and an auxiliary material, and stirring; (ii) filtering the obtained mixed liquid; (iii) sieving the filter cake through a sieve having pore size of 0.6-1.2 mm, and rotating while mixing, and pelletizing, and controlling the rotating speed at 500-1000 rotations/minute, to obtain wet particles; (iv) placing the wet particles into a vibration-type fluidization bed, and drying; and (v) detecting, and packaging the finished product.    USE - The method is useful for preparing bacitracin zinc premix (claimed).    ADVANTAGE - The method can reduce energy consumption while drying; does not produce bad odor; produces product with uniform particle size, and good liquidity; utilizes easily available raw materials; has easy operation procedure; and is suitable for large-scale production.    DETAILED DESCRIPTION - Preparing bacitracin zinc premix, comprises (i) adding zinc sulfate into a fermentation liquid added into a fermentation tank, and simultaneously adding a flavoring agent, a flocculating agent and an auxiliary material, then stirring for 0.5-2 hours, and allowing to stand for 1-3 hours, to obtain mixed liquid; (ii) filtering the obtained mixed liquid through a diaphragm plate-frame filter press, and taking out the filter cake; (iii) sieving the filter cake through a sieve having pore size of 0.6-1.2 mm, and rotating while mixing, and pelletizing, and controlling the rotating speed at 500-1000 rotations/minute, to obtain wet particles; (iv) placing the wet particles into a vibration-type fluidization bed, and drying, to obtain the final product; and (v) detecting, and packaging the finished product.
NOVELTY - An apparatus (1) consists of an adsorption-and-desorption tank (2) which is filled with ammonia-adsorption fiber (3) obtained by introducing carboxyl group into a fiber, which is capable of absorbing and desorbing ammonia from supplied aqueous solution of ammonia.    USE - Apparatus is used for processing ammonia (claimed) used as raw material of nitric acid, urea, ammonium chloride, ammonium sulfate, ammonium nitrate, and other chemical industry products.    ADVANTAGE - The ammonia is efficiently and economical recovered from the aqueous solution using the apparatus, without performing frequent activation treatment, deterioration waste processing and exchange process, by simple method. The chloride compound byproduct produced during processing of ammonia is nontoxic, safe with respect to human body and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing of ammonia, which involves adsorbing ammonia in the aqueous solution using ammonia-adsorption fiber, dehydrating by blowing air (C), desorbing ammonia from the ammonia-adsorption fiber by blowing water vapor (B), condensing water vapor-containing desorbed ammonia by cooling, and recovering aqueous ammonia.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of apparatus for processing ammonia in aqueous solution.    Processing apparatus (1)    Adsorption-and-desorption tank (2)    Ammonia adsorption fiber (3)    Air supply portion (5)    Water vapor (B)    Air (C)
NOVELTY - Preparing fertilizer involves treating biomass in digester to obtain semi-liquid biogas effluent that is separated and pyrolyzed to obtain fertilizer.    USE - Method for preparing fertilizer used as soil conditioner (claimed).    ADVANTAGE - The method enables to prepare fertilizer that reduces greenhouse gases effect and pathogens, and increases pH, organic materials and cationic exchange capacity of soil, and ensures slow release of nutrients, improved soil bio-diversity and productivity, high nutrient concentration and fast carbon dioxide fixation without pollution.
NOVELTY - The new type utility claims have one kind negative pressure under environment of gas circulation purification device, comprising circulation pipeline orderly connected by the peristaltic pump, titanium pump and negative pressure working system, a peristaltic pump depend on two section with baffle and corrugated pipe do compression, action and realize stretching gas transport, limiting switch control tube compress and travel after the stretching, the limiting switch is touched on function to the one for interlock relay, control motor positive rotation, rotating the motor by coupling to transfer, transfer again give corrugated tube, corrugated tube realize the compression and stretching movement of titanium pump inner part is equipped with sponge titanium, heating silk to it by heating, and forming titanium film to absorb nitrogen, hydrogen, oxygen in wall titanium pump equal in impurity gas. The new type utility is aiming at the negative pressure environment in the following using protective gas for longer time and working operation, can be low in condition not damage system negative pressure environment of the inert gas to the internal for purification purifying system, which not only increase have working efficiency, but also reducing have working cost.
NOVELTY - The utility model is new type fermentation device field, especially relates to one kind of horizontal organic fertilizer fermentation device, comprising insulating layer with the tube, stirring device, support frame and heat conducting device, tube mounted on support frame above, stirring device set in inside tube, wherein the heat guide device set in tube outside of the hot oil tube connecting tube, wherein, the heat device of high temperature oil furnace, an oil pump, a heating plate and heat conducting oil pipe composed of the above high temperature oil furnace equipped with oil pump, a high temperature oil furnace bottom equipped with heating plate, high temperature furnace and oil pump by oil guide heat oil pipe connecting cylinder body in the guide heat oil pipe; the device using full-closeness structure, can in high temperature high pressure lower operation to prevent the loss of nutrient, environment protection, stirring way is vertical, stirring resistance is reduced, can reduce consume, and stirring arm can disassemble, provided with external heat preservation material, reducing heat loss and can use heat-conducting oil pipe heat sending, realize oil way by the oil pump and circulation of heat can is convenient to heat can transfer, control temperature, increase product quality, suitable maintenance at the same time.
NOVELTY - The utility model is new type one plant inclined dynamic sludge aerobic compost device of main control room, compost chamber, supporting frame, a crawler transmission device, stirring device, heating system, an aeration system equal part one. Control room placing automatic control device. The compost cabin mounting support frame is on, the internal upper side arrangement have temperature humidity sensor for monitoring temperature, uniform arrangement have aeration head for aeration, compost chamber set with double layer side wall, inside outside wall can pass in heat water, ground source heat pump and temperature depend on humidity sensor to carry out the automatic heating heat preservation, compost chamber left right side arrangement and motor through shaft drive stack in fertilizer cabin and spiral stirring device, compost chamber lower part placing have aeration device, compost chamber at left upper angle and right upper angle part lower part respectively provided with feedstock mouth and discharging mouth, the lower part discharging mouth set with crawler conveyor belt device to collect fertilizer. at the internal lower side
NOVELTY - The new type utility claims have tank sludge continuous aerobic fermentation complete equipment, belonging to municipal sludge located technology field, comprising orderly connected and can move elevating conveyer, a mixer, a feeding device, an aerobic ferment device, an air inducing device, washing tower and biological filter chamber, said mixer set with weighing device, the washing tower set with spray device, the aerobic ferment device comprises full-closed and tank body, equipped with layered rotating aeration device in the tank body in the layered rotating aeration device and connection transmission device and the blowing device, realize have feeding, ventilating, automatic control of temperature, and fermentation process with penetrating fluid, 100 % of odour collecting processing, the aerobic fermentation time short, small square meter, bacteriostat ability is strong, the investment cost low equal.
NOVELTY - A novel crop planting base material production, comprising hot fermentation room and cold removing fungus room, the hot fermentation room in the cold removing fungus room, the cold and removing fungus room between set with insulating plate, the insulating plate one end through turning shaft and production house main body frame connected with, the hot fermentation room top end middle position is provided with one ventilating mouth, also mounted to make base material with the hot air in the hot air drying fermented indoor top through scientific and reasonable in the design, reducing manpower participate, reduce labour cost, fermentation room automatically stir, make fermentation more uniformly, by skill and air discharging effect and toxic gas in fermentation room, but also can through air drying the base material to carry out primary , wherein by effect of cold and fungus room, base material for freezing, carrying out further ultraviolet sterilizing processing, to obtain high-efficient base material, which greatly increase crop yield.
NOVELTY - Planting method of Zizania latifolia involves (a) selecting clay soiled field, ploughing soil, mixing soil with organic fertilizer, and irrigating the field, (b) selecting high-quality variety of Z.latifolia, (c) transferring seedlings to field mentioned in step (a) and maintaining surface water height of 3-5 cm, and applying urea, and (d) applying organic fertilizer and maintaining surface water height of 10 cm, applying chemical fertilizer and maintaining surface water height of 20 cm, and finally maintaining the surface water height at 20 cm.    USE - The method is useful for planting Z.latifolia (claimed).    ADVANTAGE - The method achieves best result of fertilizer, avoids misuse of fertilizer, reduces excess use of resources, provides nutrients rapidly, enhances vitality of seedlings, kills weeds, and is environmentally-friendly.    DETAILED DESCRIPTION - Planting method of Zizania latifolia involves (a) selecting clay soiled field where Z.latifolia has not grown, ploughing soil to a depth of 25-30 cm, mixing soil with 50-70 kg organic fertilizer/acre, irrigating the field, and maintaining soil in paste condition, (b) selecting high-quality variety of Z.latifolia of previous year, taking 2-3 seedlings in a cluster as one unit, cutting not greater than 5 cm of hard parts, and shifting the units into a container filled with nutritious solution, (c) transferring units to the field mentioned in step (a) at a depth of 5 cm and maintaining a gap 60x 90 cm between units and surface water height of 3-5 cm, and applying 25 kg urea/acre to promote rooting, and (d) applying 10-15 kg organic fertilizer/acre and maintaining surface water height of 10 cm after 10 days, applying 20 kg chemical fertilizer/acre and maintaining surface water height of 20 cm after 25 days, and finally maintaining the surface water height at 20 cm.
NOVELTY - Manufacture of refrigerator deodorant and disinfectant comprises using tea residue, crushing, and adding bamboo activated carbon block as deodorant.    USE - Method for manufacturing refrigerator deodorant and disinfectant (claimed).    ADVANTAGE - The product is energy-saving, environment-friendly and convenient to use, removes bacteria, preserves fresh food, has easy to obtain natural materials, and can restore performance by periodic exposure to sunlight.
NOVELTY - A vardenafil hydrochloride detecting method involves taking right amount of product to be tested, adding extracting solvent mixture, shaking or dissolving ultrasonically to obtain a mixed test solution. The mixed test solution is measured by using electric field directional movement according to electrochemical principle for determining electrochemical parameters of the test solution, followed by determining the size of products according to electrochemical parameters and judging whether the sample added with vardenafil hydrochloride.    USE - Method for detecting vardenafil hydrochloride.    ADVANTAGE - The method enables detecting vardenafil hydrochloride with high sensitivity, in simple, fast, safe and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a complete detection device.
NOVELTY - A chitosan modified mesoporous silicon dioxide filled hybrid membrane comprises 60-98 wt.% polyoxyethylene-polycaprolactam block copolymers and chitosan modified mesoporous silicon dioxide, where the content of poly (ethylene oxide) - polycaprolactam block copolymer, poly (ethylene oxide) segments is 55-60 wt.%, and polycaprolactam chain segment is 40-45 wt.% and membrane has thickness of 70-105 mu m.    USE - Chitosan modified mesoporous silicon dioxide filled hybrid membrane for separating carbon dioxide/methane mixture with CO2 flux of 450-1835barrer, CO2/CH4 separation factor of 15-36, and carbon dioxide/nitrogen mixture with flux of 460-1943barrer, CO2/ N2 separation factor of 49-85 (all claimed).    ADVANTAGE - The membrane is excellent in membrane separation performance and can be prepared in easy and cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing chitosan modified mesoporous silicon dioxide filled hybrid membrane.
NOVELTY - Preparing flower nutrient liquid involves electrolysing nitric acid as electrolyte, carbon glue solution and other raw materials using graphite plate as anode and cathode for 12-50 hours to obtain flower nutrient liquid. The flower nutrient liquid comprises 20-100mL carbon glue, 20-120g potassium dihydrogen phosphate, 0-20g potassium nitrate, 40-80g urea, 0.6-1.0g zinc sulfate, 0.2-0.4g ferrous sulfate, 0.1-0.2g boric acid, 0.8-1.2g magnesium sulfate, 0.1-0.3g calcium chloride and 1000mL pure water.    USE - Method for preparing flower nutrient liquid (claimed).    ADVANTAGE - The method enables to prepare flower nutrient liquid in simple, cost-effective, eco-friendly and efficient manner.
NOVELTY - Synthesis of acetylated resveratrol comprises taking 3,4',5-trimethoxystilbene as raw material and aluminum chloride and triethylamine complex as demethylation agent, conducting demethylation reaction under the action of inorganic salt to prepare resveratrol, acetylation reacting with acetic anhydride under the action of triethylamine, and obtaining the product.    USE - Synthesis of acetylated resveratrol (claimed).    ADVANTAGE - The method has high yield, improved product quality and low cost, is environment-friendly, suitable for industrial operation, and simple, and reduces product impurities.
NOVELTY - Preparation of oteracil potassium comprises dissolving potassium hydroxide or potassium carbonate in purified water, adding potassium iodide and allantoin, stirring, adding potassium persulfate, and reacting to 0-100 degrees C while stirring; and filtering insolubles, adjusting pH to 5.5-6.5, precipitating solid, and drying.    USE - Method for preparation of oteracil potassium (claimed).    ADVANTAGE - The method is simple and suitable for industrial production, utilizes inexpensive and environment-friendly oxidizing agent, and it has mild reaction condition, and high yield and purity. The oteracil potassium has purity of 99.8% and single impurity of less than 0.1%.
NOVELTY - Xanthene-1,8-dione derivatives (I), are new.    USE - New compound (I) are useful for preparation of ketone-acridine intermediate (claimed).    ADVANTAGE - The compound (I) can be prepared with high yield under mild reaction conditions and reduced time consumption, and without using catalyst in an economical and an environmentally-friendly manner.    DETAILED DESCRIPTION - Xanthene-1,8-dione derivatives of formula (I), are new. (CN104610218A-001-skc)    R1=-H, 4-OCH3, 2-Cl, 3,4-(OCH3)2, 4-CH3 or 3-NO2.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of compound (I); and    (2) use of compound (I) for preparation of ketone-acridine intermediate.
NOVELTY - The preparation method of cephalothin involves reacting 2-thiopheneacetic acid with trifluoro-acetic acid 2,5-dioxo-pyrrolidin-1-yl ester compound (I) in the presence of organic alkali at -20 degrees C to 40 degrees C to obtain thiophen-2-yl-acetic acid 2,5-dioxo-pyrrolidin-1-yl ester compound (II), and performing condensation reaction of compound (II) with 7-aminocephalosporanic acid at 10-35 degrees C.    USE - The method is useful for preparation of cephalothin (claimed).    ADVANTAGE - The method enables simple preparation of cephalothin with reduced environmental pollution under mild reaction conditions, and without causing degradation of amide compound.    DETAILED DESCRIPTION - The preparation method of cephalothin involves reacting 2-thiopheneacetic acid with trifluoro-acetic acid 2,5-dioxo-pyrrolidin-1-yl ester compound of formula (I) in the presence of organic alkali at -20 degrees C to 40 degrees C to obtain thiophen-2-yl-acetic acid 2,5-dioxo-pyrrolidin-1-yl ester compound of formula (II), and performing condensation reaction of compound (II) with 7-aminocephalosporanic acid at 10-35 degrees C.
NOVELTY - Commercial production of Lepista sordida comprises taking Lepista sordida strain, sowing in 45-74 wt.% strain and crop straw, 20-49 wt.% livestock manure, 0.5-5 wt.% lime and 0.5-5 wt.% gypsum mixture, and fermenting.    USE - Method for commercial production of Lepista sordida (claimed).    ADVANTAGE - The method has low cost, wide raw material source, and high yield.
NOVELTY - Cultivation of Hericium erinaceus comprises crushing corn cob, drying shiitake mushroom, and crushing; adding water, soaking at room temperature, uniformly mixing with corn cob powder and soybean cake, piling, adding culture medium, stacking, inserting with stick, covering with grass, and naturally fermenting; turning, adding gypsum, turning, adding potassium dihydrogen phosphate, and turning to obtain planting material with moisture content of 63-65%; cooling, sowing, covering with mycelium, and fruiting; and harvesting and spraying with shiitake mushroom extract.    USE - Method for cultivation of Hericium erinaceus (claimed).    ADVANTAGE - The Hericium erinaceus has low carbon content, high activity, strong bacterial resistance, and high bioconversion rate. The method is environment-friendly, saves manpower and coal and other resources, and reduces environmental pollution.    DETAILED DESCRIPTION - Cultivation of Hericium erinaceus comprises crushing 74-80 wt.% corn cob into 3-5 mm diameter, drying 3-4 wt.% shiitake mushroom, and crushing into 2-3 mm diameter; adding 20-30 times water, soaking at room temperature for 18-24 hours, uniformly mixing with 74-80 wt.% corn cob powder and 16-20 wt.% soybean cake, piling at 1-1.2 m height and 2-3 m width, adding 300-500 kg culture medium, stacking, inserting with 10-15 cm diameter stick, covering with grass, and naturally fermenting; turning at 60 degrees C for 24 hours, adding 1.4 wt.% gypsum, turning, adding 0.1 wt.% potassium dihydrogen phosphate, and turning for 3-4 times for 5-6 days to obtain planting material with moisture content of 63-65%; cooling, sowing, covering with 2-2.5 cm mycelium, and fruiting; and harvesting and spraying with 0.01-0.02 g/ml 4-6 kg/m2 shiitake mushroom extract.
NOVELTY - Cultivation of Pleurotus geesteranus comprises crushing 72-80 wt.% bagasse, drying shiitake mushroom, and crushing; adding water, soaking, uniformly mixing with bagasse powder and soybean cake, piling, adding culture medium, stacking, inserting with stick, covering with grass, and naturally fermenting; turning, adding lime, turning, adding gypsum, and turning to obtain planting material; cooling, sowing, covering with mycelium, and fruiting; and harvesting and spraying with shiitake mushroom extract.    USE - Method for cultivation of Pleurotus geesteranus (claimed).    ADVANTAGE - The Pleurotus geesteranus has low carbon content, high activity, strong bacterial resistance, and high bioconversion rate. The method is environment-friendly, saves manpower and coal and other resources, and reduces environmental pollution.    DETAILED DESCRIPTION - Cultivation of Pleurotus geesteranus comprises crushing 72-80 wt.% bagasse into 3-5 mm diameter, drying 3-4 wt.% shiitake mushroom, and crushing into 2-3 mm diameter; adding 20-30 times water, soaking at room temperature for 18-24 hours, uniformly mixing with 72-80 wt.% bagasse powder and 14-18 wt.% soybean cake, piling at 1-1.2 m height and 2-3 m width, adding 300-500 kg culture medium, stacking, inserting with 10-15 cm diameter stick, covering with grass, naturally fermenting, turning at 60 degrees C for 24 hours, adding 3-4 wt.% lime, turning, adding 1 wt.% gypsum, and turning for 3-4 times for 5-6 days to obtain planting material with moisture content of 63-65%; cooling, sowing, covering with 2-2.5 cm mycelium, and fruiting; and harvesting and spraying with 0.01-0.02 g/ml 4-6 kg/m2 shiitake mushroom extract.
NOVELTY - Preparation of Sophora flower quercetin by pot boiling method comprises crushing Sophora flower bud, preparing extracting liquid, concentrating extracting liquid, removing impurities, centrifuging, washing and drying.    USE - Preparation of Sophora flower quercetin (claimed).    ADVANTAGE - The method provides high purity quercetin, is simple and environment-friendly, has low cost and high yield, provides no acid water pollution of the prior art, and saves resources.
NOVELTY - Fermentation system comprises body (1) comprising top wall (2) and side wall (3). The top wall is connected with side wall from inner side by equidistant support (4). A vent pipe (5) on top wall is provided in drawer type box body (6). The drawer type box body is set on the support in fermentation room that is provided with vent hole.    USE - Fermentation system used for treating organic solid waste (claimed).    ADVANTAGE - The fermentation system reduces ammonia organic solid waste and increases fertilizer effect and organic fertilizer nitrogen content by more than 2 times.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic drawing of a fermentation system.    Body (1)    Top wall (2)    Side wall (3)    Support (4)    Vent pipe (5)    Drawer type box body (6)
NOVELTY - Preparing biological controlled release fertilizer involves reacting 15-18 pts. wt. humate, 5-8 pts. wt. citric acid and 5-8 pts. wt. urea-formaldehyde with 120 pts. wt. water in a reaction kettle at 70-80 degrees C to obtain urea formaldehyde sustained release liquid. 2-3 pts. wt. Effective microorganism microbial inoculums, 3-5 pts. wt. fungus and 20-30 pts. wt. poultry manure are mixed, and then fermented at 50-60 degrees C for 5-7 days. 15-18 pts. wt. Boron and magnesium residue and 5-8 pts. wt. attapulgite are mixed and granulated to obtain granules.    USE - Method for preparing biological controlled release fertilizer (claimed).    ADVANTAGE - The method enables to prepare eco-friendly biological controlled release fertilizer.    DETAILED DESCRIPTION - Preparing biological controlled release fertilizer involves reacting 15-18 pts. wt. humate, 5-8 pts. wt. citric acid and 5-8 pts. wt. urea-formaldehyde with 120 pts. wt. water in a reaction kettle at 70-80 degrees C to obtain urea formaldehyde sustained release liquid. 2-3 pts. wt. Effective microorganism microbial inoculums, 3-5 pts. wt. fungus and 20-30 pts. wt. poultry manure are mixed, and then fermented at 50-60 degrees C for 5-7 days. 15-18 pts. wt. Boron and magnesium residue and 5-8 pts. wt. attapulgite are mixed and granulated to obtain granules. 1-2 pts. wt. Urea formaldehyde sustained release liquid, 1-2 pts. wt. fermented product and 1-2 pts. wt. granules are mixed, and then 10-12 pts. wt. light clay is coated on the product.
NOVELTY - Manufacturing organic fertilizer involves utilizing 15-20 pts. wt. polyphenol carboxylic acid compound, 10-15 pts. wt. rapeseed cake fermented solution, 3-6 pts. wt. ferrous sulfate, 0.3-0.6 pts. wt. pyrethroid, 2-5 pts. wt. wheat husk fermented solution, 4-8 pts. wt. fallen leaves humus and 10-15 pts. wt. silicon oxide. Polyhydric carboxylic acid compound, rapeseed cake fermented solution, silicon oxide and fallen leaves humus are mixed and stirred in a bucket. The bucket is sealed and fermented at 40 degrees C for 48-72 hours.    USE - Method for manufacturing organic fertilizer used for flowering (claimed).    ADVANTAGE - The method is simple and cost-effective, and ensures disease resistant ability and vigorous growth of flower.    DETAILED DESCRIPTION - Manufacturing organic fertilizer involves utilizing 15-20 pts. wt. polyphenol carboxylic acid compound, 10-15 pts. wt. rapeseed cake fermented solution, 3-6 pts. wt. ferrous sulfate, 0.3-0.6 pts. wt. pyrethroid, 2-5 pts. wt. wheat husk fermented solution, 4-8 pts. wt. fallen leaves humus and 10-15 pts. wt. silicon oxide. Polyhydric carboxylic acid compound, rapeseed cake fermented solution, silicon oxide and fallen leaves humus are mixed and stirred in a bucket. The bucket is sealed and fermented at 40 degrees C for 48-72 hours. The fermented product is dried at 45 degrees C and crushed through a pulverizer and sieved with 35-40 meshes. Remaining components are mixed with the powder, and then crushed through the pulverizer and sieved with 40-50 meshes.
NOVELTY - The synthesis method of 1-(isopropylsulfonyl)-2-nitrobenzene involves reacting o-fluoronitrobenzene with sodium hydride in the presence of dimethylformamide as solvent and adding isopropyl mercaptan to obtain 2-(isopropyl thioether)nitrobenzene reaction solution, dripping acetic acid to the 2-(isopropyl thioether)nitrobenzene reaction solution and oxidizing with hydrogen peroxide.    USE - The method is useful for synthesizing 1-(isopropylsulfonyl)-2-nitrobenzene, which is useful as intermediate for ceritinib for treating cancer.    ADVANTAGE - The method enables easy, economical and environmentally-friendly one-pot synthesis of 1-(isopropylsulfonyl)-2-nitrobenzene under low reaction temperature, high reaction rate and without foul odor.
NOVELTY - Preparation of solid fuel from biomass liquefaction residue, involves mixing biomass liquefaction residue, binder and fuel additive, adjusting moisture content of the resulting mixed raw material to 10-20%, and extruding.    USE - Preparation of solid fuel from biomass liquefaction residue (claimed).    ADVANTAGE - The method enables economical preparation of energy-saving and environmentally-friendly solid fuel with high density and strength, low water-absorption property. Solid waste and biomass are effectively utilized.
NOVELTY - Coal or biomass, and oxygen and/or hydrogen are reacted with carbon monoxide, to obtain synthesis gas. Heat is recovered from produced synthesis gas, and impurities containing hydrogen sulfide and dust are removed and desulfurized. Obtained mixed gas is supplied to adiabatic reactor (I), and primary methane synthesis and water gas shift processes are carried out simultaneously. Methane gas discharged from adiabatic reactor (I) is supplied to adiabatic reactor (II). Gas discharged from adiabatic reactor (II) is water-cooled, and isothermally reacting to obtain synthetic natural gas.    USE - Manufacture of synthetic natural gas (claimed).    ADVANTAGE - The method provides synthetic natural gas with high efficiency.    DETAILED DESCRIPTION - Coal or biomass, and oxygen and/or hydrogen are reacted with carbon monoxide, to obtain synthesis gas containing carbon dioxide and hydrogen. Heat is recovered from produced synthesis gas, and impurities containing hydrogen sulfide and dust are removed and desulfurized. The obtained mixed gas is supplied to adiabatic reactor (I), and primary methane synthesis and water gas shift processes are carried out simultaneously. Supersaturated steam is produced through heat exchange with hot gases discharged from adiabatic reactor (I). Methane gas discharged from adiabatic reactor (I) is supplied to bottom of adiabatic reactor (II). Gas discharged from adiabatic reactor (II) is water-cooled, and water and carbon dioxide is removed by supplying resultant gas to an isothermal reactor to obtain synthetic natural gas. An INDEPENDENT CLAIM is included for synthetic natural gas manufacturing device.
NOVELTY - Invention relates to the field of processing wastes into compost. The processing line comprises devices of receiving, humidification, unloading, and modules made of heat-insulating enclosure panels. The modules are mounted sequentially in cascade coming down from the first to the final. The output part of the previous module is mounted above the inlet part of the next module. At the end of each module a stirring device is mounted in the form of horizontal shafts with beaters, and a hopper with dispenser of additives. The modules are equipped with conveyors and individual ventilation system with the ability of automatic regulation of the exchange and temperature of the air. The terminal devices of the ventilating system are made in the form of perforated air ducts. The air ducts are arranged along the conveyors and in the side walls of the modules with the descend to the final relative to each other. The modules comprise the moulding and the working chambers. The chambers are integrated by conveyors and blocked off by the valves-flanges. At least two modules are formed as modules of composting and germination of mycelium. The line comprises at least two modules of composting. At the beginning of the modules of composting the alignment devices are mounted.    USE - Agriculture.    ADVANTAGE - Reduction of time of composting and increase in the efficiency of waste processing is ensured.2 cl, 2 dwg
NOVELTY - Method for preparing bio-fertilizer, involves (a) mixing 40-50 wt.% earthworm, 30-40 wt.% rice bran, 10-20 wt.% fish cake, 5-15 wt.% molasses and 3-8 wt.% microbial agent, adding water to obtained mixture, stirring the mixture, and fermenting the mixture, where the microbial agent is carrier, (b) granulating fermented product, and (c) drying obtained product at low temperature.    USE - The method is useful for preparing the bio-fertilizer which is useful for supplying nutritional components to plant, controlling insect pests of plant and growth of weeds, promoting plant growth and soil improvement. The bio-fertilizer is used in herbicidal composition and soil conditioner. The soil conditioner is used for restoring soil microorganisms (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) bio-fertilizer prepared by above-mentioned method;    (2) herbicidal composition comprising the bio-fertilizer as an active component;    (3) soil conditioner comprising the bio-fertilizer as an active component; and    (4) method for soil improvement, involves applying the soil conditioner to soil.
NOVELTY - Producing fertilizer involves mixing grass carbon soil with microbial agent and water in seed pot using slant test tubes and flasks to obtain product that is tested, weighed and packed.    USE - Method for producing fertilizer (claimed).
NOVELTY - Method for producing bioorganic fertilizer, involves (a) preparing seaweed fermentation broth by subjecting the squeezed seaweed to anaerobic fermentation, adding manure or biogas residue and ventilating the mixture, (b) crushing wheat and rice, adding potassium hydroxide to the crushed wheat and rice, stacking the mixture and adjusting pH of the mixture, (c) mixing Bacillus subtilis and B.cereus, adding adsorption agent to the mixture and crushing the mixture, and (d) mixing the products obtained in the steps (a)-(c), and stirring the mixture.    USE - The method is useful for producing bioorganic fertilizer (claimed).    ADVANTAGE - The method produces bioorganic fertilizer which is rich in nutrients, organic substance, amino acid, and produces crop having excellent resistant drought and disease, and conditions soil.    DETAILED DESCRIPTION - Method for producing bioorganic fertilizer, involves (a) preparing seaweed fermentation broth by crushing and squeezing seaweed, subjecting the squeezed seaweed to anaerobic fermentation for 25-30 days, adding manure or biogas residue and ventilating and standing the mixture for 1-2 days, (b) crushing wheat and rice to mesh size of 80-120, adding 5-7% potassium hydroxide to the crushed wheat and rice, stacking the mixture for 8-12 hours and adjusting pH of the stacked mixture to 7-8, (c) mixing Bacillus subtilis and B.cereus in a ratio of 1:3-5, adding adsorption agent to the mixture in a ratio of 1:2 and crushing the mixture to mesh size of 80-120, and (d) mixing the products obtained in the steps (a)-(c), organic fertilizer, and stirring the mixture.
NOVELTY - Cultivating Pleurotus nebrodensis involves utilizing 80-86% cotton stalk shell, 8-12% cake, 3-4% tang, 2.5% lime and 1% stone bone, where raw materials are dried and crushed into granules that are soaked in water for 18-24 hours at room temperature. The soaked material is fermented at 60 degrees C for 24 hours. The fermentation is continued for 5-6 days to obtain planting material. The Pleurotus body is planted on obtained material. The Pleurotus nebrodensis is harvested after required growth.    USE - Method for cultivating Pleurotus nebrodensis (claimed).    ADVANTAGE - The method enables to cultivate Pleurotus nebrodensis that promotes beneficial micro-organism flora, increases yield, overcomes long-term pesticide use, improves quality, saves labor and reduces environmental pollution in environment friendly manner.
NOVELTY - Cultivating potted chive comprises: (i) taking a ceramic pot and disinfecting by sterilization; (ii) drying the sandy soil, spraying carbendazim wettable powder on sand, then adding sand into ceramic pot, mixing the sand with rapeseed cake as base fertilizer; (iii) soaking the bulb stem in carbendazim wettable powder liquid, then drying; (iv) planting the green onion seed in sand soil, irrigating, covering using a thin film; and (v) watering once for every 5-6 days, spreading rape seed cake fertilizer once for every 30-40 days, then administering 1% Sudan insecticide after 50 days of planting.    USE - The method is useful for cultivating potted chive (claimed).    ADVANTAGE - The method is environmentally-friendly and shortens the germination time of chive.    DETAILED DESCRIPTION - Cultivating potted chive comprises: (i) taking a ceramic pot having a depth of 15-20 cm and radial opening of 30-40 cm, then disinfecting by sterilization; (ii) drying the sandy soil, spraying 35-40% carbendazim wettable powder on sand, then adding sand into the ceramic pot, mixing the sand with 3-5% rapeseed cake as base fertilizer; (iii) taking full bulb green onion seed, soaking the bulb stem 400 times amount of 40-45% carbendazim wettable powder liquid for 15 minutes, then drying; (iv) planting the green onion seed in sand soil with an interval of 5-8 cm between two seeds, covering a layer of 2-3 cm thick ultraviolet sterilized sand soil, irrigating, covering the pot opening using a thin film for 8-10 days, then opening the thin film to observe the germination; and (v) watering once for every 5-6 days, spreading rape seed cake fertilizer once for every 30-40 days, then administering 1% Sudan insecticide once after 50 days of planting.
NOVELTY - A kind of city ecological restoration system, comprising underground drain pipe, the characteristic is a system including a micro-environment a woody plant, woody plant and a micro-environment device connected with the floor ecological restoration device, the woody plant growing micro-environment device comprises inner shell, shell periphery, said periphery shell side part is provided with a vertical spraying pipe, spraying pipe on the top provided with a atomization sprayer, a floor ecological restoration device comprises ecological restoration cloth, a cloth of a planting hole, the ecological restoration cloth by absorbing activated coal layer, montmorillonite mineral powder layer and non-woven soil engineering cloth layer composite composed of up to down in turn is absorbing activated coal layer, montmorillonite mineral powder layer and inner non-woven soil engineering cloth layer, a planting hole set with nutrient soil. The utility model is new type with high survival rate, strong practicability, and various repair. One aspect cleaning soil surface layer, keeping stable soil, another face blocking of a pollute soil and air.
NOVELTY - The system has an aeration tank (50) for aerating the liquid manure supplied from a reactor (40). A scrubber (60) is connected to the aeration tank, for processing the purified gas generated from the aeration tank. The manure is supplied to a liquefied fertilizer reservoir (70) from the aeration tank. The aeration tank is connected with the liquefied fertilizer reservoir. An oxygen supply source (90) is provided for supplying the oxygen within the aeration tank and liquefied fertilizer reservoir.    USE - System for manufacturing high efficiency liquefied fertilizer by recycling of livestock excretion.    ADVANTAGE - The efficiency of liquefied fertilizer manufacturing system is improved, and the high-quality liquefied fertilizer is produced within the short time. The load and consumable power of the centrifuge are saved, and the capacity and power consumption of the blower and scrubber are reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for manufacturing high efficiency liquefied fertilizer by recycling of livestock excretion.    Reactor (40)    Aeration tank (50)    Scrubber (60)    Liquefied fertilizer reservoir (70)    Oxygen supply source (90)
NOVELTY - Preparation of amino acid fertilizer involves carrying out solid-state fermentation of bean cake, mixing with nutrient supplement to form solid-state fermentation culture medium, inoculating Bacillus and actinomycete in the culture medium, and extracting.    USE - Preparation of amino acid fertilizer used for disease-resistant material.    ADVANTAGE - The method enables economical environmentally-friendly preparation of amino acid fertilizer with low energy consumption.
NOVELTY - An organic fertilizer comprises 25-40 pts. wt. corn rice straw, 10-25 pts. wt. manure, 10-15 pts. wt. oil cake, 0.1-0.6 pt. wt. urea and 0.1 pt. wt. inoculant.    USE - Organic fertilizer is used for tobacco cultivation.    ADVANTAGE - The organic fertilizer is manufactured by simple, economical and environmentally-friendly process, and effectively improves quality and excellent appearance of tobacco leaves.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer.
NOVELTY - 1-Chloro-1,2,2-trifluorobis(chloromethyl)ether and alkali metal fluoride in molar ratio of 1:3-8 are dissolved in a solvent and stirred uniformly. The obtained mixture is slowly warmed for 3-10 hours, cooled to less than 25 degrees C after distillation and fractions are collected at less than 60 degrees C to obtain enflurane. The alkali metal fluoride is potassium fluoride or sodium fluoride. The solvent is polyethylene glycol, polyethylene glycol 400, triethylene glycol, diethylene glycol or 18-crown-6 ether.    USE - Preparation of enflurane (claimed).    ADVANTAGE - The method efficiently and economically provides enflurane without using hydrogen fluoride and antimony salts which are highly corrosive and toxic, using simple equipment under controlled reaction conditions and without causing pollution to the environment.
NOVELTY - Preparation of nicotinic acid involves performing hydrolysis reaction of nicotinamide mother liquor, sodium hydroxide and water in a four-necked flask at 90-115 degrees C for 2.5-3.5 hours, obtaining 3-pyridyl-sodium formate, adding activated charcoal, decolorizing at 70-80 degrees C for 0.5-1.5 hours, filtering the resultant material to remove the activated carbon, adding hydrochloric acid, adjusting pH of the solution to 3.5-4, crystallizing, performing suction filtration process, washing the resultant mixture with water, obtaining wet product and drying in an oven at 105-100 degrees C.    USE - Preparation of nicotinic acid (claimed).    ADVANTAGE - The method provides nicotinic acid with high quality and reduced discharge of emissions.    DETAILED DESCRIPTION - Preparation of nicotinic acid involves performing hydrolysis reaction of nicotinamide mother liquor, sodium hydroxide and water in a four-necked flask at 90-115 degrees C for 2.5-3.5 hours, obtaining 3-pyridyl-sodium formate, adding activated charcoal, decolorizing at 70-80 degrees C for 0.5-1.5 hours, filtering the resultant material to remove the activated carbon, adding hydrochloric acid, adjusting pH of the solution to 3.5-4, crystallizing, performing suction filtration process, washing the resultant mixture with water, obtaining wet product and drying in an oven at 105-100 degrees C. The mass ratio of nicotinamide mother liquor, sodium hydroxide and water is 1:0.39-0.80:2-4.
NOVELTY - Use of punicalagin (I) for controlling pine wood nematode, is claimed. Concentration (for controlling pine wood nematode) of (I) is 200-1000 mu g/ml.    USE - (I) is useful for controlling pine wood nematode (claimed).    ADVANTAGE - The preparation method: has simple operation, low cost, and high efficiency; utilizes easily available raw materials; and is safe and environment-friendly.    DETAILED DESCRIPTION - Use of punicalagin of formula (I) for controlling pine wood nematode, is claimed. Concentration (for controlling pine wood nematode) of (I) is 200-1000 mu g/ml. An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - Liquid bio-organic fertilizer is prepared by mixing 1-50 pts. wt. amino acid liquid fertilizer uniformly with 1-50 pts. wt. lactic acid liquid fertilizer at room temperature. Total quantity of amino acid in amino acid liquid fertilizer is (200-220g/l). Viable lactic acid bacteria amount in lactic acid liquid fertilizer is (10 hundred million/ml).    USE - Liquid bio-organic fertilizer used for saline-alkali soil (claimed).    ADVANTAGE - The liquid bio-organic fertilizer provides nutrients to plant, and has synergistic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for applying liquid bio-organic fertilizer on saline-alkali soil, which involves:    (A) mixing liquid bio-organic fertilizer with water (1: 3000 times) fertilizer tank; and    (B) heating the mixture at 0.5-3 degrees C, and then applying in field during irrigation.
NOVELTY - The utility model is new type relates to a novel plant sludge fermentation device, specifically comprising: the aerobic fermentation storehouse 1, Anaerobic fermentation chamber 2, feeding opening 3, electrical machine 4, stirring device 5, pressure table 6, an aeration device 7, aeration pipe 8, gas absorbing processing device 9. The vent tube 10, electric discharging door opening and closing 11, wherein 12 a bracket 13. A with b solves the sludge compost reaction, using a equal rate problem. The utility model is new type with a novel, suitable and practical, a degradation degree of sludge deep, using rate v equal.
NOVELTY - Preparation of organic copper feed additive comprises filtering wastewater containing copper ions; passing through ion exchange resin at a flow rate of 1-2 BV/hour; eluting at 0.5-1 BV/hour to obtain copper ion concentration liquid; mixing copper ion concentration liquid, industrial and agricultural by-product and microbial inoculum, fermenting for 25-30 days at room temperature, stirring every 12 hours; drying fermentation product; and pelletizing.    USE - Method for preparing organic copper feed additive (claimed).    ADVANTAGE - The method solves the problems of water pollution and supplementary animal body trace element problem.    DETAILED DESCRIPTION - Preparation of organic copper feed additive comprises filtering wastewater containing copper ions; passing through ion exchange resin at a flow rate of 1-2 BV/hour, where the weight ratio of sample and resin is 6-10:1; eluting at 0.5-1 BV/hour to obtain copper ion concentration liquid, where the weight ratio of eluate and wastewater is 1:15-20; mixing copper ion concentration liquid, industrial and agricultural by-product and microbial inoculum at a weight ratio of 1:1000-2000:10-20, fermenting for 25-30 days at room temperature, stirring every 12 hours; drying fermentation product; and pelletizing to obtain organic copper feed additive.
NOVELTY - The utility model is new type provide the a. fertilizer production device, including, nitrogen purifier, a round disc pelletizer, a drier, a swing cooling machine, a draught fan. Wind absorption wind can provide a needed electric energy, a depth generator is led out a diameter a. nitrogen supply nitrogen purifier, a round disc pelleting machine incline installation, swing plate is 0.1-0.2 times of the incline angle of the plate is 30 degrees to-60 degrees, a round disc pelleting machine by arc track. machine a second time and granulating, drying, drying and cooling machine through bucket hoisting machine phase, draught fan. discharge wherein the swing cooling machine. The utility model is new type has simple structure, environment-friendly and energy-saving, at the same time increase the production benefit to ensure the product quality.
NOVELTY - Artificial soil composition comprises a mixture of ameliorated topsoil containing coffee grounds; and solidifying agent accounting for 0.1-3 wt.% based on the total weight of the ameliorated topsoil, where the solidifying agent is diluted in water in a predetermined ratio.    USE - The composition is useful for tree-planting in artificial soil (claimed).    ADVANTAGE - The composition improves the quality of the ameliorated topsoil by lowering the high coal dust (C/N) ratio of the coffee grounds and sawdust mixture which is fermented with EM fermentation broth and nitrogen; and avoids environmental contamination since it re-uses waste that is regenerated e.g., coffee residues, sawdust and bottom ash.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing an artificial soil composition, comprising (S10) mixing coffee grounds and saw dust in a ratio of 2:1-4:1; (S20) adding nitrogen and EM fermentation broth in the mixture of coffee grounds and sawdust, and fermenting at more than 60 degrees C and less than 70 degrees C for more than 14 days and less than 20 days; (S30) preparing ameliorated topsoil by adding bottom ash, coco pit, decomposition of granite, perlite and casting to the fermented mixture of coffee grounds and sawdust; and (S40) solidifying by mixing solidifying agent with the ameliorated topsoil.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow of the method for producing the artificial soil composition for tree-planting in artificial soil (Drawing includes non-English language text).    Mixing step (S10)    Fermentation step (S20)    Ameliorated topsoil preparing step (S30)    Solidifying step (S40)
NOVELTY - Chitosan-modified biochar-immobilized lipase prepared by decomposing biomass including peanut shell under limited oxygen conditions at high temperature into biochar having porous structure, modifying the biochar with chitosan having high biocompatibility, mutual crosslinking between chitosan macromolecules to form a substrate material having three-dimensional network structure, and immobilizing lipase in the substrate carrier, is claimed.    USE - The immobilized lipase is useful as a catalytic system for conversion of kitchen waste into biodiesel, preferably high acid value kitchen waste oil (claimed).    ADVANTAGE - The method: provides immobilized lipase having high catalytic activity and stability (claimed).
NOVELTY - A fertilizer comprises 22-24 pts. wt. ammonium hydroxide, 17-19 pts. wt. calcium ammonium nitrate, 13-15 pts. wt. phosphate rock, 11-13 pts. wt. potassium magnesium fertilizer, 10-12 pts. wt. green manure, 12-14 pts. wt. manure composting, 3-7 pts. wt. photosynthetic bacteria fertilizer, 7-9 pts. wt. yield fertilizer, 2-4 pts. wt. pine emulsion (sic), 1-3 pts. wt. acetophenate, 3-5 pts. wt. humic acid, 1-3 pts. wt. potassium salt of indole-3-butyric acid, 2-4 pts. wt. molybdenum trioxide and 40-50 pts. wt. water.    USE - Fertilizer is used for cultivating pepper.    ADVANTAGE - The fertilizer is manufactured by simple process, and effectively resists pest and improves quality of pepper.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer.
NOVELTY - Preparing isoprocarb, comprises (i) dispersing powder by using an organic solvent, to obtain wet product, mixing, distilling, and dehydrating; (ii) injecting solvent as a carrier while heating or passing through a film evaporator, distilling, and dehydrating, and carrying out wet grinding process, modulating, and packaging under continuous operation; and (iii) adding mancozeb and zinc into organic solvent, and simultaneously dehydrating to obtain product in the form of crystal complex.    USE - The method is useful for preparing isoprocarb (claimed).    ADVANTAGE - The method reduces the decomposition of products, and production of harmful impurities and dusts causing pollution; and prevents the product from fire accidents during the drying process (claimed).
NOVELTY - The invention relates to a process and a plant for treating urban solid waste. The claimed process consists of a stage for manually and mechanically sorting a flow of urban solid waste followed by a stage of biological treatment of the organic matters, comminuted and conditioned by anaerobic fermentation in a digestor and aerobic fermentation on a composting platform.    DETAILED DESCRIPTION - The claimed plant is of superposed type comprising some disc separators (8, 11, 12), with vibration screens (9), ballistic screens (13), magnetic screens (14), eddy-current screens (18), optical screens with ultrared spectrography (15, 19, 20), with rotary screens (21), a cyclone (22), a hydrocyclone (23) for manually and mechanically separating the waste, a comminuting area (24), a a digestor (28) for anaerobic fermentation and a composting platform (31) for aerobic fermentation in the stage of biological treatment.
NOVELTY - A low temperature plasma technology of device for processing acid waste gas, comprising plasma reaction room, said plasma reaction room comprises multiple hollow of the cathode tube, the centre of each cathode tube with one of emitting electrode tube through the cathode tube and emitting electrode tube spaced array, one array plasma or plasma parallel array, plasma reaction room framework, said plasma reaction room framework is metal frame, machine and electric connected with each of the cathode tube, emitting electrode tube skeleton, the emitting electrode tube skeleton for each emitting electrode tube of metal frame, machine and electrical connection, the whole multi-insulation device, the insulation device one end connected to the cathode tube framework, another end connect to emitting electrode tube skeleton, protection cover, the protection cover is alumina material. The utility model is new type according to the characteristics and can process industrial waste sum by connected in series or in parallel connected using, for purification of waste gas, dust and smoke equal peculiar smell or harmful gas effect obvious, and it is very fit industrial application.
NOVELTY - Synthesis of molecular sieves involves preparing seed solution comprising aluminosilicate zeolite ( beta ) nanocrystals, dealuminating nanocrystals, preparing suspension of the dealuminated nanocrystals without drying, preparing solution comprising structure directing agent and heteroatom source, adding the suspension of dealuminated nanocrystals to the solution, forming gel, heating gel at predetermined temperature and time to form solid, filtering, washing and drying solid, and calcining solid.    USE - Synthesis of molecular sieves used as catalyst in e.g. petrochemical processing and production of high-value chemicals and biofuels from naturally biomass.    ADVANTAGE - The method enables simple and rapid synthesis of molecular sieves having excellent catalytic activity and hydrothermal stability, in reduced period of time. Reactor and plant corrosions are reduced.
NOVELTY - Bulk gas-flotation oilfield wastewater is pretreated and degreased, and activated sludge or biofilm in oilfield wastewater is removed. The oilfield wastewater is subjected to aerobic biological-treated with flue gas, and supplied to track-type microalgae culture system containing microalgae species, and microalgae is grown, to form biological-treated water. The biological-treated water is flocculated, filtered with press filter, extracted, precipitated, filtered, sterilized and deoxidized. Thus, the processing of oilfield wastewater is carried out.    USE - Processing of oilfield wastewater (claimed).    DETAILED DESCRIPTION - Bulk gas-flotation oilfield wastewater is pretreated and degreased in joint station, and activated sludge or biofilm in oilfield wastewater is removed. The activated sludge or biofilm contains total organic carbon, nitrogen and phosphorus in weight ratio of 100:5-10:1, and has crude oil content of less than 1 mg/L. The wastewater has total organic carbon of less than 60 mg/L and chemical oxygen demand of less than 150 mg/L. The oilfield wastewater is subjected to aerobic biological-treated with flue gas having carbon dioxide content of 3-15%, and supplied to track-type microalgae culture system containing microalgae species, and microalgae is grown for 5-15 days to density of 107/ml, to form biological-treated water having lipid rate of more than 20% and microalgae. The biological-treated water containing microalgae is supplied into flocculation tank and flocculated. The flocculated sludge is filtered with press filter, extracted, precipitated, filtered, sterilized and deoxidized. Thus, the processing of oilfield wastewater is carried out.
NOVELTY - Converting biomass into solid fuel, comprises: (a) providing comminuted and dried biomass containing lignocellulosic biomass; (b) preheating the biomass at above 140 degrees C and below 300 degrees C in a gaseous atmosphere devoid of oxygen at a pressure of 1-40 bar; (c) heating the biomass at 220-350 degrees C in a gaseous atmosphere devoid of oxygen at a pressure of 1-40 bar; (d) allowing the reaction to proceed while maintaining the temperature at 300-700 degrees C and pressure of 1-40 bar; (e) cooling the biomass; and (f) recovering the calorific solid product.    USE - The process is useful for converting biomass into solid fuel.    ADVANTAGE - The process: can be implemented in the absence of any external supply of inert gas, and provides the solid fuel having high calorific value with high carbon content (greater than 85 wt.%) and less oxygen content ( less than or equal to 10 wt.%); is highly energy efficient and economical and allows to recover heat from the gas generated in steps (c) and (d) and optionally recycle the gas upstream in the process; has shorter reaction times.    DETAILED DESCRIPTION - Converting biomass into at least one solid fuel, comprises: (a) providing a comminuted and dried biomass, where the biomass contains at least 30 wt.% of lignocellulosic biomass; (b) subjecting the biomass to a preheating step at above 140 degrees C and below 300 degrees C in a gaseous atmosphere devoid of oxygen at a pressure of 1-40 bar; (c) heating the biomass at 220-350 degrees C in a gaseous atmosphere devoid of oxygen at a pressure of 1-40 bar; (d) allowing the reaction to proceed while maintaining the temperature at 300-700 degrees C and pressure of 1-40 bar; (e) cooling the biomass to a temperature of at most 100 degrees C in a gaseous atmosphere devoid of oxygen; and (f) recovering the calorific solid product.
NOVELTY - The utility model is new type relates to one kind disposable anesthesia sum tube cannula bag tray, comprising tray, the upper tray set with several respectively so as to sum holding pipe, suction pipe, suction, with a balloon device, laryngoscope, tooth and oral pharynx breathing channel of groove, the groove and put in general anesthesia sum tube cannula instrument outside outline and wherein each. The utility model is new type of goal wherein supply one A disposable anesthesia sum tube cannula bag tray, it can containing needed instrument and sum pipe intubation anesthesia operation to prevent the apparatus leakage to increase operation efficiency. The utility model has the following advantages: 1, Tray for starch base full biodegradable material is made of plastic, which is good for environmental protection and resource replaced and in preventing cross infection of medical goods. 2. Fetching groove is equipped with upper groove is convenient to fast take out and place the surgical instrument in groove in, increase the operation efficiency.
NOVELTY - The apparatus (1) has a hydrodesulfurization device (3) that removes sulfur component in raw material by hydrogenation reaction. A cooler (14) is provided to cool air flowing through hydrodesulfurization device. An aperture unit (17) is arranged on combustion air flow path. The cooling path is branched from upstream of squeeze unit of combustion air flow paths and merged with downstream of squeeze unit of combustion air flow path. A first valve (16) is arranged on cooling flow path. The controller (13) is configured to raise the opening degree of the first valve at predetermined timing.    USE - Hydrogen generating apparatus.    ADVANTAGE - The unstable combustion with a combustor is effectively suppressed. Thus, the hydrogen generating apparatus is operated stably. The starting time of the hydrogen generating apparatus is effectively reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an operating method of hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus.    Hydrogen generating apparatus (1)    Hydrodesulfurization device (3)    Controller (13)    Cooler (14)    First valve (16)    Aperture unit (17)
NOVELTY - The apparatus (100) has a modifier (1) which is provided to reform the raw material discharged from a hydrodesulfurization device (2), and provided to generate a hydrogen-containing-gas. An ejector (4) is provided in the merging unit of the material supply path and the recycle gas flow path (3) and provided to suck the hydrogen-containing-gas from the recycle gas flow path on the material supply path. A valve (5) is comprised so that the valve is closed when the raw material below predetermined flow volume flows into the ejector.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - The valve is comprised so that the valve is closed when the raw material below predetermined flow volume flows into the ejector. Thus, the reliability of the hydrogen generating apparatus is improved and operation of the hydrogen generating apparatus is stable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Hydrodesulfurization device (2)    Ejector (4)    Valve (5)    Hydrogen generating apparatus (100)
NOVELTY - The device has a micro-plasma reactor (1) which comprises a feeding port (3), a quartz container (4), polytetrafluoroethylene sealing rings (7,8), and polytetrafluoroethylene flanges (11,12). An upper electrode (5) and a lower electrode (6) are connected with a high voltage power source (2), and are made from same material. The polytetrafluoroethylene flange joint is provided in quartz container. The ethyl alcohol solution is passed through the feed inlet of the quartz container. The ethanol is fully exposed to the micro-micro-arc plasma region, when device works.    USE - Micro-plasma alcohol reforming hydrogen device for battery used for electronic system.    ADVANTAGE - The micro-plasma alcohol reforming hydrogen device is made as portable structure, and portable hydrogen supply source is used.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the micro-plasma alcohol reforming hydrogen device.    Micro-plasma reactor (1)    High voltage power source (2)    Feeding port (3)    Quartz container (4)    Upper electrode (5)    Lower electrode (6)    Polytetrafluoroethylene sealing rings (7,8)    Polytetrafluoroethylene flanges (11,12)
NOVELTY - The processing device has a fume tee joint (19) that is set with upper axial-flow alternating current (AC) fan (20) connected with a gradually reducing caliber (21) and PPR tee joint (24). A spray head (22) is provided with control ball valve (25), and connected with the magnetic force driving circulation pump (26) by soft pipe. The magnetic force driving circulation pump is connected with connecting ball valve. A collecting bucket (27) is connected with the wave pipe (23). A stainless steel frame (28) is set in a spiral collecting bucket portion (29).    USE - Device for processing crop straw.    ADVANTAGE - The crop straw is processed without smoke carbonization process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for processing crop straw.    Fume tee joint (19)    Axial-flow AC fan (20)    Caliber (21)    Spray head (22)    Wave pipe (23)    PPR tee joint (24)    Control ball valve (25)    Magnetic force driving circulation pump (26)    Collecting bucket (27)    Stainless steel frame (28)    Spiral collecting bucket (29)
NOVELTY - A fuel oil additive comprises 30-35 parts mass hydrocarbon oil, 20-25 parts mass bio-alcohol oil, 10-15 parts mass anhydrous ethanol, 5-10 parts mass isobutanol, 5-10 parts mass isooctanol, 5-10 parts mass methyl tert-butyl ether, 5-10 parts mass diethylene glycol, 2-5 parts mass thinner and 2-5 parts mass stabilizer.    USE - Fuel oil additive (claimed).    ADVANTAGE - The fuel oil provided using the additive is environmentally-friendly, and has high quality, excellent complete combustion property, reduced pour point and mechanical impurities content, and suppressed generation carbon monoxide emission and coke during combustion.
NOVELTY - Manufacture of synthesis gas involves using carbon monoxide obtained from converter of oxygen steel plant or electric furnace for melting scrap.    USE - Manufacture of synthesis gas used for producing methanol, formaldehyde and liquid fuel (all claimed).    ADVANTAGE - The method enables easy and quick manufacture of synthesis gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for assembly of iron and steel mill with coking plant and converter or electric furnace.
NOVELTY - Production of bio-oil involves introducing initial amount (q1) of biomass material into hopper (h1), transporting amount (q1) of biomass to hopper (h2), introducing final amount (q2) of biomass to hopper (h1), pressurizing hopper (h2) with gas when amount (q1) of biomass is located in hopper (h2), transporting amount (q2) of biomass from hopper (h2) to feed system, depressurizing hopper (h2), routing a portion of gas to hopper (h1), using gas routed from hopper (h2) to at least partially purge oxygen from amount (q2) of biomass and reacting.    USE - Production of bio-oil (claimed).    ADVANTAGE - The method enables efficient and reliable production of bio-oil using the biomass feed system.    DETAILED DESCRIPTION - Production of bio-oil involves introducing amount (q1) of biomass material into hopper (h1), transporting amount (q1) of biomass from hopper (h1) into hopper (h2), introducing amount (q2) of biomass into hopper (h1), pressurizing hopper (h2) with gas when amount (q1) of biomass is located in hopper (h2), transporting amount (q2) of biomass from hopper (h2) to a pressurized feed system, depressurizing hopper (h2) by releasing at least a portion of gas from hopper (h2), routing at least a portion of gas released by depressurizing to hopper (h1), using gas routed from hopper (h2) to at least partially purge oxygen from amount (q2) of biomass material inside hopper (h1) and reacting. An INDEPENDENT CLAIM is included for biomass conversion system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of various reactor inlets on a reactor.    Biomass conversion reactor (300)    Feed lines (302a,302b)    Reactor inlets (304a,304b)
NOVELTY - The assembly (1) has a fuel cell (2), and a set of gas generating devices (3, 4), that is connected to the fuel cell for feeding reactive gas for the fuel cell. The set of gas generating device is provided as exothermic gas generating devices, and a heat transport device arranged for the set of gas generating devices provides a coolant such as water-glycol mixture, other than the reactive gas to the set of gas generating devices. A thermal control circuit (9) is arranged for the fuel cell, and is provided with a heat exchanger (14) for evacuation of heat transmitted by the fuel cell.    USE - Electrical power assembly such as emergency electric power supply sources, for use in an electric supply system that is utilized for an aircraft.    ADVANTAGE - The heat transport device provides the coolant other than the reactive gas to the set of gas generating devices, thus allowing to quickly heat the fuel cell so as to allow the fuel cell to reach the operating temperature in a quick and simple manner in a stabilized mode without damages and without excessively increasing weight and avoiding obstruction of electrical power, and avoiding complete loss of electrical supply.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) an electric supply system    (2) a method for starting an electrical power assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electric power assembly.    Electrical power assembly (1)    Fuel cell (2)    Gas generating devices (3, 4)    Thermal control circuit (9)    Heat exchanger (14)
NOVELTY - A photocatalyst (20) comprises photoactive material (10) containing titanium dioxide particles having anatase to rutile ratio of greater than or equal to 2:1, and metal material (15) containing silver, palladium and gold in which molar ratio of gold to palladium is 0.1-5 and molar ratio of gold to silver is 0.1-3. Metal material is deposited on surface of photoactive material.    USE - Photocatalyst for composition used in water splitting system for photocatalytic electrolysis of water, photocatalytic oxidation of organic compound and production of hydrogen gas (all claimed).    ADVANTAGE - Efficiency of photocatalyst is improved, and complexity and costs are reduced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) composition comprising photocatalyst (20);    (2) water splitting system comprising transparent container which consists of the composition, and light source which irradiates the aqueous solution; and    (3) production of hydrogen gas by photocatalytic electrolysis which involves irradiating aqueous electrolyte solution containing the composition with light in electrolytic cell having anode and cathode in which anode contains photocatalyst and voltage between anode and cathode is produced and water (36) molecules are split to form hydrogen and oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water splitting system.    Photoactive material (10)    Metal material (15)    Photocatalyst (20)    Light source (31)    Water (36)
NOVELTY - Microorganisms cultivation process involves using water phase obtained by separating into solid and liquid the water containing mixture which processed foodstuff waste material or livestock excrement sediment with required amount of water, and arose as nutrient of micoorganisms.    USE - Cultivation process of microorganisms used for substance production which uses biomass as raw material.    ADVANTAGE - Production cost of inoculum and cost of useful substance production are reduced.
NOVELTY - The system has a solar energy heat collector (1) that is connected with hot water storage tank (2), hot water heat exchanger (3), biogas liquid tank (7), filter (8), a hot water circulation pump heat exchanger (11) and water pump (12). The high temperature side heat exchange loop is formed with multiphase flow marsh gas pool (4) connected to biogas liquid tank by valve. Low temperature side heat exchange loop is formed by filter, heating coil (9), and drain pump (14) set on outside wall in spiral shape. The heating coil end is connected to sewage factory.    USE - Solar energy heating system used for multiphase flow marsh gas pool.    ADVANTAGE - The water storage tank is used to reduce impact of weather on the solar collector system. The solar energy heating system with simple structure is provided and maintained easily. The fault point and fault rate can be reduced. The operation cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solar energy heating system used for multiphase flow marsh gas pool.    Solar energy heat collector (1)    Hot water storage tank (2)    Hot water heat exchanger (3)    Multiphase flow marsh gas pool (4)    Biogas liquid tank (7)    Filter (8)    Heating coil (9)    Hot water circulation pump heat exchanger (11)    Water pump (12)    Drain pump (14)
NOVELTY - The boiler burner has a burner housing (20) whose upper portion is connected with a fire burner (21). One end of water evaporator (4) is connected with a plasma arc catalytic ejector (3), and another end is connected with a water pump (15). An intelligent controller (1) is respectively connected with solenoid valve (9,13), water pump, oil pump (11), flame and temperature sensors (5,8), electronic lighter (7), high voltage power supply (2) and fan (6). The power supply is connected with ejector. The solenoid valves are respectively connected with the water tank and oil tank.    USE - Boiler burner for plasma decomposition of water into hydrogen and oxygen, used for fuel boiler and industrial boiler.    ADVANTAGE - The green and environment-friendly boiler burner is achieved, the energy and fuel saving effects are realized, and the emission is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the boiler burner.    Intelligent controller (1)    High voltage power supply (2)    Plasma arc catalytic ejector (3)    Water evaporator (4)    Temperature sensor (5)    Fan (6)    Electronic lighter (7)    Flame sensor (8)    Solenoid valves (9,13)    Oil pump (11)    Water pump (15)    Burner housing (20)    Fire burner (21)
NOVELTY - The compacted material comprises lignocellulosic biomass and foam. The lignocellulosic biomass includes wood waste.    USE - Compacted material for manufacturing briquettes for energy recovery.    ADVANTAGE - The compacted material increases electrical production, significantly reduces emission of greenhouse gases and acids, improves management of natural resources, and reduces costs in transport, handling and storage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing briquettes from waste furniture, which involves shredding wood waste and foam, and then pressing the obtained material.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting durability of the wood briquettes. (Drawing includes non-English language text).
NOVELTY - Method for treatment of lignocellulosic organic waste or biomass, by which carbohydrates are rendered more available for subsequent hydrolysis, involves adding enzymes or performing direct fermentation to one or more desired products.    USE - The method is useful for treatment of lignocellulosic organic waste or biomass (claimed).    ADVANTAGE - The method can be performed with undivided or only poorly divided substrate having high dry material concentration.
NOVELTY - The utility model claims a soil sterilizer for vegetable planting, belonging to soil improvement device field, comprising a cylindrical main body and medicament bottle, wherein the main body bottom is set with cone locating base, the locating base is internal hollow and connected with the body lumen, bottom of locating base is opening, top part of the medicament bottle is set with a sealing cover, below the medicament bottle bottom is connected with a sleeve, the medicament bottle is connected with the top part of the main body through connecting to the sleeve, bottom of the medicament bottle is set with at least one of cotton strip hole, in the cotton strip hole is clamped with a cotton strip guiding liquid, upper end of the cotton strip guiding liquid is in the medicine bottle and soaking in liquid medicine preparation, lower part of the cotton strip guiding liquid is contacting to the soil passing through the main body and the lumen of the locating base. The utility model is new type of vigetable plant soil sterilizer and existing technology, with reasonable design, simple structure, easy processing, using suitable equal, can effective of the medicine preparation is full use and improve have soil quality, and can reduce pollute environment.
NOVELTY - Device comprises a holder (10) equipped with positive and negative power supply terminals for supplying power into the positive and negative electrodes and a storage of a port (20) for delivering water at the bottom of a water storage, and reaction structure (24) for generating hydrogen water by vertically placing the positive electrode and the negative electrode at the center of an ion membrane which is interposed between an upper member (24a) and a lower member assembled by screwing.    USE - The device is useful for generating hydrogen water (claimed).    ADVANTAGE - The device produces pure hydrogen water instead of neutral hydrogen water, prevents the release of atmospheric ozone, improves product properties, avoids leakage, and ensures structural stability and durability.    DETAILED DESCRIPTION - Device comprises a holder (10) equipped with positive and negative power supply terminals for supplying power into the positive and negative electrodes and a storage of a port (20) for delivering water at the bottom of a water storage, and reaction structure (24) for generating hydrogen water by vertically placing the positive electrode and the negative electrode at the center of an ion membrane which is interposed between an upper member (24a) and a lower member assembled by screwing. The reaction structure is assembled with a coupling portion by screwing method and vertically penetrates the bottom of the port. The inner side of the port is arranged with the negative electrode of the reaction structure. The positive electrode is arranged on one side of the port    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device.    Holder (10)    Supporting stand (12)    Port (20)    Reaction structure (24)    Upper member (24a)
NOVELTY - The preparation method of alternative binder sludge biomass briquette involves: (1) taking 50-70 pts. wt. bituminous coal, 20-40 pts. wt. sludge, 5-10 pts. wt. pinewood, 2-4 pts. wt. dispersing agent and 1-2 pts. wt. curing agent; (2) crushing and screening bituminous coal and pinewood; (3) carrying out viscosity sludge treatment process; (4) uniformly mixing curing agent with product obtained in step (3); and (5) performing hot forming process.    USE - The method is useful for preparing alternative binder sludge biomass briquette (claimed).    ADVANTAGE - The method prepares alternative binder sludge biomass briquette with reduced cost and high yield and efficiency in a simple manner.    DETAILED DESCRIPTION - The preparation method of alternative binder sludge biomass briquette involves: (1) taking 50-70 pts. wt. bituminous coal, 20-40 pts. wt. sludge, 5-10 pts. wt. pinewood, 2-4 pts. wt. dispersing agent and 1-2 pts. wt. curing agent; (2) crushing and screening bituminous coal and pinewood so that bituminous coal has particle size of below 3 mm and pinewood has particle size of less than or equal to 5 mm; (3) carrying out viscosity sludge treatment process to reduce viscosity to 1200-1400 mPa.second; (4) uniformly mixing curing agent and dispersing agent with product obtained in step (3) using high-speed mixer and stirring for 8-12 minutes; and (5) performing dry hot forming process.
NOVELTY - The utility model is new type providing one kind of odourless organic fertilizer raw material storage pool comprises side wall and bottom is composed of pool body and upper cover, also comprising discharging mouth, set at bottom of the storage pool on the said discharging mouth connected with material transport device, stirring device, set at lower surface of said upper cover, motor, is equipped with the upper cover above the transmission mechanism driven by the upper cover connected with opened to realize opening and closing of the storage pool in the upper side wall. The utility model is new type supply and odourless organic fertilizer storage pool comprises side wall, upper cover and bottom, forming closeness space can not only storage of the raw material, but also reduce have raw material in natural condition the following stacking then produce the harmful gas and peculiar smell, protect have production environment.
NOVELTY - The utility model is new type supply one kind organic fertilizer fermentation device, comprising bracket, fermentation box body, said box body comprises shell, for mounting the bracket on the inner shell, set in the internal shell, and shell and between forming; in the jacket set with electric heating silk and cooling device is located in the shell and outside surface, feeding port, set at the top part of the box body and connected in the shell, the discharging mouth, set at bottom of the tank body, connected in the shell, two of stirring device, parallel mounted at the inner shell in one strip edge at the inner side of shell, and rotation direction opposite. The utility model is new type of goal is to provide one installation and add material A suitable, but also can increase fermentation device and fermentation efficiency.
NOVELTY - The utility model is new type category stirring device manufacturing technology field, relating to one kind used for compost material mixing the stirrer. It is of metal material manufacture, comprising stirring chamber, driving device, bracket, agitator blade, a discharging machine, driving device for driving shaft extending to side center position form in stirring room is equipped with bracket cross shaped middle cross position and on the bracket and fixedly connected with the two agitator blade as symmetry form is respectively equipped with horizontal stirring room at the inner side of lower driving device driving shaft end left right two seat and driving device and is fixedly connected with the discharging machine to level to the discharging mouth form stirring chamber is equipped with stirring room right side and below the seat. The utility model is new type comprises characteristics as follows: simple structure and low cost, suitable stirring and fast speed, mixing uniformity is not less than 90%.
NOVELTY - The utility model is new type category in compost fermentation facility construction technology field, relating to one kind used for compost fermentation and aeration pool simple. It comprises pool body, the vent plate, air room, compost, air inlet pipe, the pool body is square brick pool and upper opening, the vent plate is face plate provided with uniformly distributing the 16 vent hole of the square plate, air room is flat square room, air inlet pipe is circular pipe channel, horizontal plate is equipped with pool body inner side bottom close to upper position, to form the lower air room, the upper part in the compost, the air inlet pipe through series brick to form the transverse wall is equipped with pool body lower part right side inside the middle air room and the middle position. The utility model is new type comprises following characteristics: pool is easy and low cost, suitable compost and effect is good, the fit of farmer compost single use.
NOVELTY - A breeding site biogas engineering system comprises livestock and poultry building (1), anaerobic fermentation tank (3), air storage tank (8), stove air outlet (9), biogas tank generator (10), heat collector (5) and biogas slurry discharge field (11).    USE - Breeding site biogas engineering system.    ADVANTAGE - The system increases yield of biogas and soil fertility, and it has zero pollution discharge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of breeding site biogas engineering system.    Livestock and poultry building (1)    Anaerobic fermentation tank (3)    Heat collector (5)    Air storage tank (8)    Stove air outlet (9)    Biogas tank generator (10)    Biogas slurry discharge field (11)
NOVELTY - The device has a LNG pump (2) that is connected with a first distributor (3) connected with a plate-fin heat exchanger (4). A demethanizer (6) is connected with a reflux pump (13). The deethanizer (7) and fin heat exchanger are connected with a reflux tank (14), a first circulation device (5) and demethanizer. The reflux tank is connected with relux pump connected with a second distributor (12). The second distributor is connected with a second circulation device (10) connected with deethanizer connected with balancer (8).    USE - Device for recovering ethane from LNG.    ADVANTAGE - The structure of the recovering device is simplified. Separation of methane of LNG is realized. Ethane purity is reached to 94%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for recovering ethane from LNG.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the device for recovering ethane from LNG.    LNG pump (2)    Distributors (3,12)    Plate-fin heat exchanger (4)    Circulation devices (5,10)    Demethanizer (6)    Deethanizer (7)    Balancer (8)    Reflux pump (13)    Reflux tank (14)
NOVELTY - Supercritical methanol extraction cogeneration of clay and biodiesel includes adding oily waste clay powder and methanol into high-pressure reactor, extracting, and water-bath cooling; filtering to obtain liquid product, distilling, and recycling unreacted methanol; washing filtered solid clay with n-hexane, and drying regenerated clay; and adding distillation product with n-hexane washing solution, layering, taking upper liquid, and vacuum-distilling to obtain biodiesel.    USE - Method for supercritical methanol extraction cogeneration of clay and biodiesel (claimed).    ADVANTAGE - The method solves vegetable oil factory waste clay problems, achieves biodiesel yield of up to 90%, and it has easy recovery of biodiesel and inexpensive raw materials.    DETAILED DESCRIPTION - Supercritical methanol extraction cogeneration of clay and biodiesel comprises:    (A) adding oily waste clay powder and methanol at ratio of 1:2-1:5 into high-pressure reactor, extracting to 240-300 degrees C at 9-30 MPa while stirring at 500-1500 revolutions/minute, and water-bath cooling to room temperature for 0.5-4 hours when temperature and pressure are stable;    (B) filtering to obtain liquid product, distilling under reduced pressure, and recycling unreacted methanol;    (C) washing filtered solid clay with 2-5 times n-hexane until colorless, and drying regenerated clay; and    (D) adding distillation product with n-hexane washing solution, layering, taking upper liquid, and vacuum-distilling to obtain biodiesel.
NOVELTY - Recycling food waste comprises e.g. taking food waste, stirring and smashing, adding water so that the water content reaches 90%, adding alpha -amylase, glucoamylase, cellulase and lipase in processed food waste, mixing uniformly, adjusting the pH value, carrying out enzymolysis to obtain fermented raw material, after the enzymolysis, placing obtained raw material in a fermentation equipment, regulating temperature of fermentation raw material, carrying out continuous fermentation, every 5-10 days, flowing fermentation raw materials, and proceeding for continuous fermentation.    USE - The method is useful for recycling food waste (claimed).    ADVANTAGE - The method achieves continuous fermentation for processing food waste and generates gas e.g. methane used as biomass fuel.    DETAILED DESCRIPTION - Recycling food waste comprises (i) taking food waste, stirring and smashing, then adding water so that the water content reaches 90%, (ii) adding 20-25U alpha -amylase, 5-10 U glucoamylase, 60-100 U cellulase and 30-45U lipase in processed food waste, mixing uniformly, adjusting the pH value of mixture to 5-7, then at 60-65 degrees C, carrying out enzymolysis for 6-8 hours to obtain fermented raw material, (iii) after the enzymolysis, placing obtained raw material in a fermentation equipment, regulating temperature of fermentation raw material to 15-35 degrees C, carrying out continuous fermentation, (iv) after continuous fermentation process, for every 5-10 days, flowing fermentation raw materials, proceeding for continuous fermentation, every time the fermentation raw material adding amount is 5-8% according to the fermentation device capacity, and (v) collecting fermentation process produced gas.
NOVELTY - Preparation of metallic silver enhanced molybdenum disulfide modified silicon nanowire array photochemical hydrogen evolution electrode comprises cleaning silicon wafer, depositing catalyst, adding hydrogen peroxide and hydrofluoric acid, etching, soaking in silver nitrate solution, washing, drying, soaking in dimethylformamide and ammonium thiosulfate, drying at 60-80 degrees C, annealing at 400-500 degrees C for 5-8 hours and contacting.    USE - Method for preparing metallic silver enhanced molybdenum disulfide modified silicon nanowire array photochemical hydrogen evolution electrode.    ADVANTAGE - The method is simple, easy and economical.
NOVELTY - The utility model claims a buried Anaerobic fermentation device fit for cold region, belonging to marsh gas engineering technology field. It solves the problem that have existing technology of Anaerobic fermentation pool is easy to corrosion and leakage gas is difficult and not enough in winter, it main comprises feedstock pool, Anaerobic fermentation pool and water pressure in. Wherein, in Anaerobic fermentation pool wall is coated with anti-corrosive layer, with insulating layer outside. The utility model is new type main uses for northern cold medium of underground marsh gas engineering.
NOVELTY - The utility model claims a biogas digester backflush device, comprising on its periphery nozzel, nozzel set with cone head, cone head set with through hole, upper nozzel also formed with connection mouth, upper connecting at upper mouth welding with connecting pipe, connecting pipe set with welding stick and welding stick welding with operation pole, operating pole of bottom end is cone head at welding. The utility model has the following beneficial effects: formed by the nozzel, and periphery is equipped with nozzel with cone head, cone head welding with operation pole, further make the utility new type comprises the stirring effect, on nozzel welding with connecting pipe, upper cone head also set with through hole by the connecting tube and external sewage water pump connect to have make Anaerobic Microorganism fermentation and full contact of the raw material in the stirring process and effect, increase have fermentation efficiency, at the same time also can adjust length of pole for satisfying operation for operation of different marsh gas pool, further reach to have strong practicability and feature, the utility model is new type also comprises manufacture cost low, suitable utility feature equal.
NOVELTY - The utility model claims a high tightness biogas digester, comprising biogas pool, wherein the pool at internal part of marsh gas pool one side mounted feedstock feedstock gas and is connected with upper part of feedstock tube installation fixing cover, two side fixing cover is respectively mounted fixing plate, upper fixing plate is set vertical screw hole, in screw hole mounting bolt, upper part of marsh gas pool installation of two fixed tube, fixed tube and upper part inner side mounting fixing ring. The utility model is new type supply have A.. sealing marsh gas pool. The utility model is new type of cover can be fixed by bolt and feedstock pipe tightly matched, the marsh gas pool in entering into oxygen to prevent the marsh gas in the marsh gas pool produce explosion.
NOVELTY - The utility model relates to a high leak tightness of cell culture bag sampling tube, category biological medical material field. Comprises tube body, annular sealing convex ring, sealing wing, a supporting column, a sealing plug. The annular sealing convex ring set on pipe body outside, and one cell culture bag connected with the end, the tube body two side edge coaxially symmetrical set with seal wing, the pipe body set with support of weight symmetry at end part coaxial and cell culture bag internal. The pipe body far away from one terminal cell culture bag mouth is set with sealing plug. When the utility model is new type and cell culture bag sealing connected with character is good, which ensures cells in culture is different stage sampling detection, sample not be pollute.
NOVELTY - The utility model relates to self-locking sealing joint of cell culture bag inlet pipe, category biological medical material field. Comprising puncture channel, anti-dust seal, sealing base, sealing plug, sealing gasket. Said sealing base and cell culture bag inlet pipe spiral connection. Anti-dust seal set in the sealing base, the first layer protecting barrier as liquid inlet tube is. The sealing plug set with seal base at lower part of the liquid inlet tube and tube body internal connected. The sealing base and the middle set with sealing gasket, a sealing plug as the second layer protecting barrier liquid inlet tube is. The puncture channel, anti-dust seal, sealing base, sealing gasket, centre of sealing plug on one straight line on strip. The utility model is new type injector suitable repeatedly puncturing, and automatically close. When the cell culture is at different stage adding each kind of different maintenance liquid, sample is not pollute, and cell liquid would not relux.
NOVELTY - An artemisinin crystallizing tank, comprising evaporation room, heating room, crystallizing room, evaporation room top with solvent steam outlet, middle part side wall has sight glass, side wall with a liquid inlet, the lower evaporation room is fixedly connected with heating room, heating room with internal annular interlayer, the annular interlayer and uniformly provided with multiple annular of the annular upper part with interlayer steam inlet, lower part has water outlet condensing, crystallizing room is cone is fixedly connected with the lower part in heating room, lower crystallization room part provided with side, upper hand hole installation with closed door, crystallizing room bottom from falling over in turn provided with filter screen, upper unfolding valve, concentrated liquid outlet, the utility model is new type, whole concentrated crystallization process realizes have integrated, up in production operation is more convenient, at the same time to concentration crystallization process and prevent have concentrated liquid and air contact then caused by the risk on, in whole concentration, crystallizing and removing process have no necessary transfer time and production time and reducing relative, time reducing production, increase production efficiency have to avoid have pollute.
NOVELTY - The cover has a glue plug pressure pad fixed to a sealing rubber plug that is fixed with an upper surface of a polygon-shaped glue plug room. A side surface of the polygon-shaped glue plug room is coated a film e.g. aluminum foil and plastic film. The polygon-shaped glue plug room is divided into a rubber plug containing part and glue plug pressure pad containing part. An inner part of the polygon-shaped glue plug room is fixed to a fixing device. A middle part of the rubber plug is formed with rectangular groove. The glue plug pressure pad is made of PP material and isoprene rubber material.    USE - Transfusion bag single-head plug composite cover.    ADVANTAGE - The cover is eco-friendly, safe to use and easy to operate, and realizes glue plug pressure pad optimizing function.    DETAILED DESCRIPTION - The sealing rubber plug is provided with a transfusion part for adding traditional Chinese medicine.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a transfusion bag single-head plug composite cover.
NOVELTY - Producing biodiesel involves adding catalyst containing acid and basic centers with an oil and methanol mixture into an electrolytic cell and then heating the oil and methanol mixture. The heated material is subjected for magnetic agitation for the complete esterification of the free fatty acids. The solid catalyst is removed from the liquid mixture by decantation and then the lower liquid portion is separated from the liquid superior part. The residue of methanol and water is evaporated by heating in a reactor and then the obtained material is mixed with sodium hydroxide and methanol.    USE - Method for producing biodiesel (claimed).    DETAILED DESCRIPTION - Producing biodiesel involves adding catalyst containing acid and basic centers with an oil and methanol mixture into an electrolytic cell and then heating the oil and methanol mixture. The heated material is subjected for magnetic agitation for the complete esterification of the free fatty acids. The solid catalyst is removed from the liquid mixture by decantation and then the lower liquid portion is separated from the liquid superior part. The residue of methanol and water is evaporated by heating in a reactor and then the obtained material is mixed with sodium hydroxide and methanol. The mixed material is subjected for magnetic agitation by applying electric current and then the methyl esters of fatty acids are separated from the glycerol. The methyl esters of fatty acids are washed with aqueous buffer solution of pH 6.6 and then the washed material is dried in a reactor to obtain the desired product.
NOVELTY - The utility model is new type fermentation device field, especially relates to one kind of vertical organic fertilizer fermentation device, comprising tube, supporting frame and heating device, wherein the tube set on supporting frame on the heating device by carrying on heat guide oil tube and out the guide heat oil pipe connecting cylinder body bottom, wherein, shell and tube of outside wall, heat preservation material and three part composed of inner container, the heat preservation material is located between outside wall and inner container, and by nail fixing, heating device comprises high temperature furnace, an oil pump, for guiding heat oil pipe and out the guide heat oil pipe, upper high temperature oil furnace provided with an oil pump, for guiding heat oil pipe connected with the oil pump and oil tank supply heat, out heat guide oil pipe connected with high temperature oil furnace and supply heat oil tank, the high temperature oil furnace shell from outside wall and the heat preservation material composed of, the device adopt closed structure, reduces floor square meter, can in the following high pressure operation, vertical stirring arm can disassemble, reducing have resistance through the heat pipe for heating material, accelerate fermentation, realize heat source circulation, temperature control, heat preservation effect is good, increase have product quality.
NOVELTY - The new type utility claims have one kind novel controllable aerobic compost reaction treatment device, provided with feedstock hole on top part of reactor, stirring shaft, a water outlet, a compost reactor main body is double layer side wall design, in outside between double layer side wall by hot water, water inlet and outlet pipes and constant temperature water channel connected with then into constant temperature hot water, forming constant temperature hot water insulating layer, side of reactor provided with aeration device, a discharging hole, a water inlet, a gas flow meter and temperature display instrument, the reactor internal temperature probe and provided with micro-pore aeration pipe, provided with liquid discharging pipe for discharging waste liquid bottom in reactor, stirring device comprises motor and setting the stirrer at reactor in, stirring shaft through bearing mounted on stirring shaft hole in well and connected with motor, driven stirrer stirring, aeration system comprises air blower and vent-pipe, air blower through ventilating pipe and micro-pore aeration pipe connected with. The utility model is new type using hot water constant temperature heating, ventilating air flow control to obtain buffer layer in equal, with ventilating uniformity, high efficiency, small square meter small, compost effect and good application value equal wide.
NOVELTY - Multi-angle rotating roller and scarifying belongs to material and device, especially relates to one kind used for municipal sludge and processing and other organic solid waste treatment and multi-angle rotating roller turning device. It is the turning roller of hanger, rocker arm, a pin shaft, a fixed inner cylinder, a hydraulic motor, a roller rotating wheel disc and multi-angle rotating roller composed of the multi-angle rotating roller mounted on blade, the multi-angle rotating roller, between blade provided with regulating device. The advantages is: the turner connected with blade up in multi-angle rotating roller, can enlargement blade stability, and to adjust for the adjustment and change blade, blade length is to turn diversity of polishing material with good effect, to reach to adapt to different variety material and fermentation effect is needed turn polishing diversity.
NOVELTY - The new type utility claims microorganism for preparing device, specifically a circulation filling device of chlorella culture liquid, it comprises mixed gas storage room (1), an injection device (5), a diffusion device (6), the annular water collecting device (7), device (10), and the mixed gas storage room (1) is respectively set with left and right gas leading-in pipe (4), connecting pipe (8) and mixed gas storage room (1) and relative another end provided with annular water collecting device (7), and the said annular water collecting device (7) and spraying device (5) connected with the said injection device (5) provided with convergence device (10), device (10) two side lower part of injection device (5) is internal provided with left and right inclined pipe (9), the convergence device (10) lower end set with diffusion device (6), its beneficial effect wherein the use safe, suitable, circulation use effect is good, and it saves resource, without any waste, which is good for environment.
NOVELTY - Bamboo charcoal production device comprises furnace body (1), ignition platform (2), charcoal filter device (3), pulverizer (4), material bucket (5), lifting table, exhaust pipe, flue gas purification device, coal outlet port, coal inlet port, and discharging port.    USE - Bamboo charcoal production device.    ADVANTAGE - The device is simple, energy-saving and environment-friendly, has convenient maintenance, and improves production quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of bamboo charcoal production device.    Furnace body (1)    Ignition platform (2)    Charcoal filter device (3)    Pulverizer (4)    Material bucket (5)
NOVELTY - Organic soil formulation contains 100 pts. wt. natural red loam, 200 pts. wt. cow dung, 100 pts. wt. chicken manure, 100 pts. wt. wheat straw, 100 pts. wt. corn stover, 10-15 pts. wt. bean cake, 10-15 pts. wt. sesame dregs, 20 pts. wt. mushroom residue, 0.2 pts. wt. microbial inoculum and 0.1 pts. wt. fermented milk.    USE - The organic soil formulation is useful for preventing pest in crop.    ADVANTAGE - The organic soil formulation effectively prevents pest in crop, improves yield of crop and has high organic matter content, excellent water retention ability and soil stability, less harmful mineral, rich nutrition, microbial activity and high carbon-nitrogen ratio.
NOVELTY - Organic fertilizer comprises 5-10 pts. wt. edible fungus mushroom waste, 1-5 pts. wt. chicken manure, 2-5 pts. wt. furnace ash, 1-5 pts. wt. weathered coal and 2-5 pts. wt. additive.    USE - Organic fertilizer is useful for cultivation of fruit tree and flowering plant.    ADVANTAGE - The organic fertilizer is prepared from edible fungus mushroom waste in easy, inexpensive and environmentally-friendly manner, increases waste utilization and saves resources and energy.
NOVELTY - Use of roc-mediated ectomycorrhizae-based bio-inoculum, is claimed, in diverse applications.    USE - The roc-mediated ectomycorrhizae-based bio-inoculum is useful in diverse applications as a biofertilizing agent, plant growth enhancer, plant growth promoter or biocontrol agent (all claimed), and in soil fertilization, and reclamation of industrially created wastelands.    ADVANTAGE - The roc-mediated ectomycorrhizae-based bio-inoculum is environmentally-friendly, facilitates enhanced nutrient uptake in plants, and enhances plant productivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) mycorrhizae-based biofertilizer composition/biofertilizer formulation prepared using the roc-mediated ectomycorrhizae-based bio-inoculum; and    (2) method for obtaining roc-mediated ectomycorrhizae-based bio-inoculum, involves isolating, (b) transforming, (c) incubating, (d) sub-culturing, harvesting and air drying, and (e) packaging product.
NOVELTY - Kitchen garbage high-temperature aerobic fermentation treatment device comprises receiving device, breaking device (2), sorting device (4), first transport device (3), second transport device (5), storage hopper, skip and biochemical reaction device (9).    USE - Kitchen garbage high-temperature aerobic fermentation treatment device.    ADVANTAGE - The device controls kitchen waste water oil, and reduces kitchen waste disposal weight.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of kitchen garbage high-temperature aerobic fermentation treatment device.    Breaking device (2)    First transport device (3)    Sorting device (4)    Second transport device (5)    Biochemical reaction device (9)
NOVELTY - Production of poultry manure organic composite fertilizer comprises taking poultry manure, removing water, mixing with swelling agent, extruding, preparing into fecal pellets, crushing, mixing with wheat bran, biological humic acid, microflora, zinc sulfate, iron sulfate, ammonium nitrate, ammonium phosphate, boron, calcium chloride and fermented material, adding fermenting bacteria, fermenting and extruding.    USE - Method for producing poultry manure organic composite fertilizer (claimed).    ADVANTAGE - The green fertilizer ensures high survival rate, gives crop nutrition, eliminates chemical fertilizer, modifies soil, increases fertilizer using rate, reduces cost, enhances crop resistance to disease and lodging capacity, and increases crop heat resistant capacity. It has strong decomposing ability, and microorganism community and organic matter for crop root nutrition.    DETAILED DESCRIPTION - Production of poultry manure organic composite fertilizer comprises taking poultry manure, removing water until water content is 60-70%, separating excess water until particle diameter is 0.5 cm; mixing manure with 1.5-3.5 wt.% swelling agent, extruding at 200 degrees C and pressure of 10 kg/cm2, preparing into fecal pellets, crushing using grinder and sieving to get less than 1 mm puffed powders; mixing 40-55 wt.% puffed powders, 10-20 wt.% wheat bran, 0.4-0.6 wt.% biological humic acid, 10-20 wt.% microflora, 0.6-0.8 wt.% zinc sulfate, 0.6-0.8 wt.% iron sulfate, 1.5-3.5 wt.% ammonium nitrate, 0.7-0.9 wt.% ammonium phosphate, 0.2-0.4 wt.% boron, 0.02-0.04 wt.% calcium chloride and 0.02-0.04 wt.% fermented material; adding 0.3-0.5 wt.% fermenting bacteria, fermenting at pH of 5-7 for 10-15 days; and extruding. The poultry manure is cow dung, horse manure, pig manure, chicken manure and/or duck manure.
NOVELTY - A fuel comprises, in a ratio of, greater than 99.95 methanol content, 900 kg solvent oil No. 200, 80 kg methyl tert-butyl ether, 15 kg ethanolamine, 2 kg tetrachloroethylene, 1 kg benzotriazole derivative, 0.5 kg antioxidants and 0.5 kg vegetable acid.    USE - The fuel is useful for M90 linear heat generator.    ADVANTAGE - The fuel can be easily stored and transported, has low cost and excellent storage stability, and is safe to use and environmentally friendly.
NOVELTY - Hericium erinaceus cultivation comprises taking seed hulls, bean cake, mushroom, monopotassium phosphate, calcium superphosphate and calcium carbonate; taking mushroom, adding clean water, soaking at room temperature for 18-24 hours, mixing cotton hulls and soybean, stacking, covering with grass and fermenting; holding, turning, adding calcium carbonate, turning, adding potassium dihydrogen superphosphate, turning, fermenting; cooling, spreading in furrow bed, seeding hairy fungus, covering; and based on mycelial growth, spraying mushroom extract.    USE - Method for Hericium erinaceus cultivation (claimed).    ADVANTAGE - The method promotes microorganism breeding, improves microorganism flora, saves labor, and reduces environmental pollution.    DETAILED DESCRIPTION - Hericium erinaceus cultivation comprises taking 75-85 wt.% seed hulls, 14-16 wt.% bean cake, 3-4 wt.% mushroom, 0.1 wt.% monopotassium phosphate, 0.4 wt.% calcium superphosphate and 1 wt.% calcium carbonate; taking mushroom, adding 20-30 times clean water, soaking at room temperature for 18-24 hours, mixing cotton hulls and soybean, stacking at 1-2 m high and 2-3 m width, inserting stick in heap, covering with grass and fermenting; holding at 60 degrees C for 24 hours, turning once per day, adding calcium carbonate, turning, adding potassium dihydrogen superphosphate, turning 3-4 times, fermenting for 5-6 days, terminating to get material with 63-65 wt.% water content; cooling, spreading in furrow bed, seeding hairy fungus, heat covering, covering with soil at 2-3 cm thick, carrying out fruiting management; and based on mycelial growth, spraying 0.01-0.02 g/ml mushroom extract at 4-8 kg/m2. The extract is prepared by taking mushroom, adding 20 times water, soaking for 18-24 hours, removing filter slag, and adding water to dilute.
NOVELTY - The method involves providing ten valves, a quantitative pipe, three chromatographic columns, a nickel conversion furnace, a three-pass joint, a hydrogen flame ion detector and an electron capture detector. Each valve is switched at certain time for measuring gas sample. Chromatographic column sequence detection process is performed after gas sample.    USE - Gas phase chromatography analysis based method for realizing dual-valve system chromatographic sum way configuration of main greenhouse gas such as carbon dioxide, methane and oxidation sub-nitrogen.    ADVANTAGE - The method enables monitoring main greenhouse climate changes in different ecological systems based on atmosphere environment gas discharge condition.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a gas phase chromatography analysis based method for realizing dual-valve system chromatographic sum way configuration of main greenhouse gas.
NOVELTY - Method for performing desalination, involves using microbial fuel cell which comprises anion exchange membrane and cation exchange membrane with separate anode and cathode chambers instead of two cation exchange membranes, where protons can be easily transferred between anode chamber, desalting chamber and cathode chamber, and the anode chamber, desalting chamber and cathode chamber are maintained at stable pH.    USE - The method is used for performing desalination (claimed) in sewage water.
NOVELTY - Preparation of pemetrexed disodium sterile powder injection comprises dissolving pemetrexed disodium in water to prepare pemetrexed disodium solution, sterile filtering to obtain medicine liquid A, adding crystallization solvent, stirring, separating pemetrexed disodium crystals, filtering, decompression drying to obtain pemetrexed disodium sterile materials, recovering crystallization solvent in filtrate and subpackaging the pemetrexed disodium sterile materials to obtain pemetrexed disodium sterile powder injection.    USE - Preparation of pemetrexed disodium sterile powder injection (claimed).    ADVANTAGE - The method is carried out at room temperature, simple and easy for industrial production, provides product with stable quality and reduces energy consumption.
NOVELTY - The device has fermentation tank (1) which is provided in machine frame (2). Electric heating tube (5) is provided with heat insulating jacket (3). Electric control equipment box (6) is connected with heating device by connecting line. Speed reducing motor (7) is connected with box through connecting line. Filter material (11) is located in dehumidifier (10). Discharging port (15) is connected to feeding port. Discharging port and feeding port are automatically opened and closed. Units of electrical control system are unified and are connected to box for automatic control functions.    USE - Production device for high temperature rapid fermentation of agricultural waste organic fertilizer.    ADVANTAGE - The production device prevents environmental pollution. The common sanitary safety is provided at high temperature fermentation process. The nitrogen loss is reduced. The volatilization of ammonia is reduced in fermentation process. The fermentation time is shortened. The product fertilizer efficiency is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a production method for high temperature rapid fermentation of agricultural waste organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the production device.    Fermentation tank (1)    Machine frame (2)    Heat insulating jacket (3)    Electric heating tube (5)    Electric control equipment box (6)    Speed reducing motor (7)    Dehumidifier (10)    Filter material (11)    Discharging port (15)
NOVELTY - Preparing esomeprazole magnesium compound of polymorphic form, involves weighing 60 pts. wt. esomeprazole sodium, dissolving esomeprazole sodium in purified water, adding charcoal, stirring, filtering, dripping 0.5 N magnesium chloride solution in the filtrate, heat-preserving, centrifuging, vacuum-drying the filter cake, and crushing.    USE - Preparing esomeprazole magnesium compound of polymorphic form (claimed).    ADVANTAGE - The method enables preparation of esomeprazole magnesium compound with moisture content reduced by 6-8%, and improved stability, purity, quality and yield, without using organic solvent, in a rapid and simple manner.
NOVELTY - Toilet with environment-friendly compost processing device comprises toilet system, fermentation system, discharge system, air compressor, air storage tank, water tank, toilet bowl, fermentation tank, temperature control system, guide rail, sliding trolley, rotating shaft, agitator blade, transparent glass door, air inlet tank, sewage pipe, rotary valve, fan, biological filter, and activated carbon filter.    USE - Toilet with environment-friendly compost processing device.    ADVANTAGE - The device recycles organic waste, provides compost production system, and eliminates odor produced during fermentation.
NOVELTY - Cushion material flat cultivating chicken feces harmless treatment site fermentation comprises carrying out two batches culture, at the same time pad material batch fermentation, at the end of batch culture, spray microbial inoculum and supplementing pad, and carrying out stacking fermentation for 14 days at 60 degrees C or more.    USE - The method is useful for cushion material flat cultivating chicken feces harmless treatment site fermentation (claimed).    ADVANTAGE - The method does not need cleaning during each batch, reduces environmental pollution, can completely kill the pathogenic microorganism, and reduces farmers concern in reducing residual pathogen.
NOVELTY - Preparing Thalictrum plant extracts, comprises subjecting Thalictrum to extraction process by adding 40-100% ethanol as an extraction solvent in an amount of 10-40 times, where the extraction temperature is 40-60 degrees C, and the extraction time is 30-120 minutes, and extracting under ultrasonic frequency of 30-40 khz, and filtering, recovering ethanol, concentrating, and drying or not drying, to obtain the final product.    USE - The Thalictrum plant extract in useful in the preparation a medicinal composition for preventing and treating citrus postharvest pathogens, preferably Penicillium italicum, Geotrichum candidum and Alternaria citri and/or preservatives while post-harvesting citrus (claimed).    ADVANTAGE - The method produces product having strong pathogen inhibitory effect, and does not easily produce drug resistance; and does not produce chemical residues on fresh citrus; harm human health; and is environmental friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (I) Thalictrum plant extracts, prepared as mentioned above; (III) use of Thalictrum plant extract in the preparation a medicinal composition for preventing and treating citrus postharvest pathogens and/or preservatives used while post-harvesting citrus; and #(III) medicinal composition and preservative comprising Thalictrum plant extracts.
NOVELTY - Production of immunoactive feed for river crab comprises taking fish meal, soybean, vegetables, corn, garlic dry powder, calcium lactate, plant oil, monocalcium phosphate, and salt. The feed also comprises 0.8-2% cordycepin, 5-11.9% cordycepic acid, and 3-20% cordyceps polysaccharide.    USE - Production method for immunoactive feed for river crab used for regulating the immune function and providing disease resistance ability.    ADVANTAGE - The method avoids the abuse of antibiotic and other drugs, and avoids ecological environmental pollution. It increases feed using rate, promotes growth of river crab, improves meat quality taste, and provides good economic benefit. By recycling waste resource, the method has low cost, simple technique, wide using range, and is safe.
NOVELTY - Preparation method of sea cucumber feed involves using Cordyceps group, degummed kelp powder, gulfweed powder, soybean protein powder, sea greens powder, garlic dry powder, scallop meat powder, fish meal and shrimp shell meal, where feed also comprises 0.8-2% cordycepin, 5-11.9% cordycepic acid and 3-20% cordycepic polysaccharide.    USE - The method is useful for preparing sea cucumber feed which is useful for regulating immunocompetence (claimed), and providing anti-disease resistance.    ADVANTAGE - The method avoids overuse of antibiotics, is environmentally-friendly, cost-effective and simple, and prepares sea cucumber feed which promotes sea cucumber growth, and improves meat taste.
NOVELTY - Obtaining Citrus aurantium flavonoid involves grinding Citrus aurantium powder and shell with mortar to obtain solid mixture that is extracted using solid phase extracting column as fixed phase with ionic liquid as elution agent to carry out elution. The eluted liquid is collected and then centrifuged using vortex to obtain upper clear liquid as flavonoid extract.    USE - Method for obtaining Citrus aurantium flavonoid (claimed).    ADVANTAGE - The method enables to obtain Citrus aurantium flavonoid in efficient and environment-friendly manner.
NOVELTY - Treatment of glyphosate wastewater involves processing to-be-treated wastewater using reverse osmosis membrane, separating glyphosate, obtaining glyphosate solution and formaldehyde pale liquid, filtering glyphosate solution, recycling glyphosate, adjusting pH of filtrate to 7 or more, heating, obtaining pyrophosphate, oxidizing formaldehyde liquid and processing resultant formic acid to formate crystals.    USE - Treatment of glyphosate wastewater (claimed).    ADVANTAGE - The method enables treatment of glyphosate wastewater with suppressed generation of emission, by economical and environmentally-friendly process.    DETAILED DESCRIPTION - Treatment of glyphosate wastewater involves processing to-be-treated wastewater using reverse osmosis membrane, separating glyphosate, obtaining glyphosate solution and formaldehyde pale liquid, filtering glyphosate solution, recycling glyphosate, adjusting pH of filtrate to 7 or more, heating, obtaining pyrophosphate, oxidizing formaldehyde liquid such that formaldehyde is oxidized to formic acid occurs and oxidation of formic acid to water and carbon dioxide is suppressed, obtaining formic acid solution having concentration of 10-15 wt.%, recycling remainder solution for glyphosate production, converting 10-15 wt.% formic acid to formate brine, concentrating, filtering, obtaining formate crystals, filtering mother liquor and concentrating.
NOVELTY - Composite fertilizer comprises 20-50 pts. wt. inorganic fertilizer, 20-50 pts. wt. organic material, 2-6 pts. wt. polyglutamic acid, 5-15 pts. wt. kaolin and 5-15 pts. wt. bacterial strain. Inorganic fertilizer is selected from urea, sulfuric acid or potassium chloride. Organic material is selected from fermented residue, grape residue or plant ash. Microorganism bacterial strain is selected from Bacillus, Pseudomonas aeruginosa or actinomycetes.    USE - Composite fertilizer.    ADVANTAGE - The composite fertilizer ensures high nutrient, improves soil fertility and quality of the crop, promotes plant growth, and increases disease resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing composite fertilizer, which involves:    (A) mixing raw materials and granulating to obtain granules;    (B) drying the granules and cooling; and    (C) fermenting by adding microorganism bacterial strain, and packaging to obtain final product.
NOVELTY - Preparing mushroom cultivating material involves utilizing 38-44% corn core, 18-22% cotton seed hull, 12% sawdust, 20% rice bran, 3-4% mushroom residue, 2.5% lime and 1% calcium carbonate. The corn core and sawdust are crushed to obtain powder that is mixed with cotton seed hull, mushroom residue and water. The obtained mixture is fermented with lime, calcium carbonate and rice bran at 20-22 degrees C for 26-28 days to obtain product that is packaged in polypropylene plastic bag.    USE - Method for preparing mushroom cultivating material (claimed).    ADVANTAGE - The method enables to prepare mushroom cultivating material that promotes beneficial microbial growth, catalytic material decomposition and mushroom mycelium growth and vigor, and ensures strong anti-bacterial capacity by requiring low manpower and coal resources in eco-friendly manner.
NOVELTY - Nutrient soil comprises 50-80 pts. wt. garden soil, 25-30 pts. wt. white oak wooden meal, 10-20 pts. wt. cedar wood meal, 2-5 pts. wt. bone powder, 2-5 pts. wt. clam shell, 2-5 pts. wt. egg shell, 8-18 pts. wt. flour, 5-8 pts. wt. rice bran, 0.3-0.6 pts. wt. urea, 5-10 pts. wt. bean dregs, 5-10 pts. wt. lees, 8-12 pts. wt. walnut, 8-12 pts. wt. badam, 6-9 pts. wt. plant ash, 12-20 pts. wt. vermiculite, 10-15 pts. wt. metal stone, 8-10 pts. wt. deer marsh soil and 30-50 pts. wt. water.    USE - Nutrient soil used for cultivating potted vegetable plant (claimed).    ADVANTAGE - The nutrient soil is rich in nitrogen, phosphorus, potassium, aluminum, iron, magnesium and silicates, and ensures good ventilation property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutrient soil, which involves;    (A) grinding clam shell to obtain powder;    (B) mixing bone powder, flour and rice bran uniformly with obtained powder in a stirrer;    (C) stirring white oak wooden meal, cedar wood meal, urea and water for 10-20 minutes in container;    (D) keeping obtained mixture for 5-8 days to obtain wooden meal;    (E) crushing walnut shell, badam, vermiculite, metal stone and deer marsh soil to obtain mixture;    (F) stirring obtained powders and mixtures with garden soil, plant ash, bean dregs and lees; and    (G) fermenting obtained mixture for one month to obtain nutrient soil that is sterilized and then sprayed.
NOVELTY - Fertilizer comprises wood vinegar powder, mixed powder of cloves and nutmeg, sunflower cake, egg shell powder, Dipterex (RTM: Insecticides and fungicides), wheat bran, deionized water and potassium permanganate solution.    USE - Fertilizer used for flowering garden plant (claimed).    ADVANTAGE - The fertilizer ensures purification of indoor air, provides nutrient substance to each flower, and eliminates peculiar smell of flower.
NOVELTY - Multifunctional fertilizer comprises 600-820 pts. wt. straw, 300-400 pts. wt. animal feces, 10-12 pts. wt. urea, 10-12 pts. wt. calcium chloride, 3-4 pts. wt. ferrous sulfate, 2-3 pts. wt. zinc sulfate, 10-15 pts. wt. soil conditioning agent, 10-11 pts. wt. modified epoxy resin coated diammonium phosphate, 10-12 pts. wt. modified epoxy resin envelope potassium nitrate, 5-10 pts. wt. pesticides and 30 pts. wt. biological microorganism.    USE - Multifunctional fertilizer used for nursery stock (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing multifunctional fertilizer, which involves:    (A) grinding rice stick and combustioning to obtain plant ash;    (B) mixing animal excrement with plant ash and heating at 80 degrees C;    (C) adding Streptococcus, Bacillus or yeast with the mixture and fermenting at 40-50 degrees C for 30-45 days and then adding lactic acid (106 colony forming unit/mg); and    (D) adding remaining components with the fermented product, coating it, and then granulating to obtain granules.
NOVELTY - Preparing bio-organic fertilizer involves mixing microbial agent and ingredient A at 30 degrees C for 12 hours. The obtained mixture is mixed with ingredient B and C for 3 minutes. The obtained mixture is dried at low temperature and then granulated. The weight ratio of ingredients A, ingredient B, ingredient C and microbial agent is 10-12:4-6:3-5:1-2.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-organic fertilizer in simple and cost-effective manner.
NOVELTY - Extraction of urine ammonia involves collecting human urine, distilling, cooling, refluxing at 178-220 degrees C and 2.15 MPa, heating in preheating tower, performing dehydrogenation, conveying into carbon dioxide stripper, placing unreacted urea in carbamate condenser, granulating urea, performing two-stage evaporation, molding at 20-25 degrees C, screening and packaging.    USE - Method for extracting urine ammonia used for synthesizing urea.    ADVANTAGE - The method is energy-saving, environmental-friendly, inexpensive, and has no agglomeration and production of irritant odor.
NOVELTY - Composting vegetable residue involves crushing vegetable residues, where crushed materials has water content of 80-85%. The crushed material is fermented for 10-12 days at not less than 15 degrees C, where carbon and nitrogen ratio of fermented material is regulated to 25-30. Plastic thin film is utilized to cover fermenting medium. The fermenting medium is turned after every 1-2 days.    USE - Method for composting vegetable residue (claimed).    ADVANTAGE - The method enables to compost vegetable residue that kills pathogenic fungus and inhibits diseases in efficient, economic, safe and eco-friendly manner.
NOVELTY - Preparing biological fertilizer involves dissolving 1-2 pts. wt. Rhizobium, 0.5-1 pts. wt. actinomycetes, 5-7 pts. wt. Bacillus natto, 0.5-1 pts. wt. photosynthetic bacteria, 5-6 pts. wt. vitamin C and 12-15 pts. wt. brown sugar with 150 pts. wt. water, and then fermented at room temperature for 3-5 days to obtain a mixed fermentation liquid. 5-8 pts. wt. Sodium humate, 20-30 pts. wt. urea, 15-20 pts. wt. plant straw, 5-10 pts. wt. animal excrement and 20-30 pts. wt. soybean are mixed with mixed fermentation liquid, and then carried out aerobic fermentation.    USE - Method for preparing biological fertilizer (claimed) used as base fertilizer and foliar fertilizer.    ADVANTAGE - The method enbles to prepare biological fertilizer that increases yield and quality of crops. Biological fertilizer is enriched with biological active component and organic nitrogen, reduces soil compaction, and increases quality of slow release organic fertilzer.    DETAILED DESCRIPTION - Preparing biological fertilizer involves dissolving 1-2 pts. wt. Rhizobium, 0.5-1 pts. wt. actinomycetes, 5-7 pts. wt. Bacillus natto, 0.5-1 pts. wt. photosynthetic bacteria, 5-6 pts. wt. vitamin C and 12-15 pts. wt. brown sugar with 150 pts. wt. water, and then fermented at room temperature for 3-5 days to obtain a mixed fermentation liquid. 5-8 pts. wt. Sodium humate, 20-30 pts. wt. urea, 15-20 pts. wt. plant straw, 5-10 pts. wt. animal excrement and 20-30 pts. wt. soybean are mixed with mixed fermentation liquid, and then carried out aerobic fermentation at room temperature for 1-2 days. The aerobic fermented product is subjected to anaerobic fermentation at 30-40 degrees C for 12-15 hours.
NOVELTY - Bio-organic fertilizer comprises 40-50 wt.% biomass straw coal powder, 45-50 wt.% biogas residue, 0.05-0.1 wt.% bentonite, 0.5-2 wt.% nitrogenous fertilizer, 0.5-2 wt.% phosphate fertilizer, 0.5-2 wt.% potassium fertilizer, 0.1-0.3 wt.% biological deodorizing agent and 0.5-1.5 wt.% pyroligneous acid. Bio-organic fertilizer is prepared by cutting crop straw into 1-5cm and crushed it through device. The powder is heated at 300-1100 degrees C and sieved with 60-100 meshes. The biomass straw coal powder and biological deodorizing agent are mixed and kept for 7-10 days to obtain block-shaped mixture.    USE - Bio-organic fertilizer.    ADVANTAGE - The bio-organic fertilizer is cost-effective and eco-friendly, increases yield of crop, and has socio-economic benefit.    DETAILED DESCRIPTION - Bio-organic fertilizer comprises 40-50 wt.% biomass straw coal powder, 45-50 wt.% biogas residue, 0.05-0.1 wt.% bentonite, 0.5-2 wt.% nitrogenous fertilizer, 0.5-2 wt.% phosphate fertilizer, 0.5-2 wt.% potassium fertilizer, 0.1-0.3 wt.% biological deodorizing agent and 0.5-1.5 wt.% pyroligneous acid. Bio-organic fertilizer is prepared by cutting crop straw into 1-5cm and crushed it through device. The powder is heated at 300-1100 degrees C and sieved with 60-100 meshes. The biomass straw coal powder and biological deodorizing agent are mixed and kept for 7-10 days to obtain block-shaped mixture. The block-shaped mixture is crushed through 40 meshes sieve, and then remaining components and auxiliary agent are added. Pyroligneous acid is sprinkled on the obtained mixture, mixed it, and then granulated.
NOVELTY - Manufacturing fertilizer involves utilizing 15-20 pts. wt. fermented residue solution, 10-15 pts. wt. rapeseed cake fermented solution, 3-6 pts. wt. bovine heart core powder, 0.3-0.6 pts. wt. pyrethroid, 2-5 pts. wt. potassium permanganate solution, 4-8 pts. wt. fallen leaves humus and 10-15 pts. wt. diluted beer. Fermented residue solution, rapeseed cake fermented solution and fallen leaves humus are mixed and stirred with diluted beer in a bucket. The bucket is sealed and fermented 40 degrees C for 48-72 hours. The fermented product is dried at 45 degrees C and crushed through a pulverizer.    USE - Method for manufacturing fertilizer used for flowering of garden plant (claimed).    ADVANTAGE - The method is simple and cost-effective, and ensures disease resistant ability and vigorous growth of flower.    DETAILED DESCRIPTION - Manufacturing fertilizer involves utilizing 15-20 pts. wt. fermented residue solution, 10-15 pts. wt. rapeseed cake fermented solution, 3-6 pts. wt. bovine heart core powder, 0.3-0.6 pts. wt. pyrethroid, 2-5 pts. wt. potassium permanganate solution, 4-8 pts. wt. fallen leaves humus and 10-15 pts. wt. diluted beer. Fermented residue solution, rapeseed cake fermented solution and fallen leaves humus are mixed and stirred with diluted beer in a bucket. The bucket is sealed and fermented 40 degrees C for 48-72 hours. The fermented product is dried at 45 degrees C and crushed through a pulverizer and sieved with 35-40 meshes. Remaining components are mixed with the powder, and then crushed through the pulverizer and sieved with 40-50 meshes.
NOVELTY - Manufacturing organic fertilizer involves utilizing 10-15 pts. wt. monoammonium phosphate, 3-6 pts. wt. rice water, 4-8 pts. wt. surface active agent, 6-10 pts. wt. egg shell powder, 1-1.5 pts. wt. chlorothalonil, 2-4 pts. wt. histidine, 15-20 pts. wt. deionized water and 2-3 pts. wt. yeast. Monoammonium phosphate, rice water, yeast and egg shell powder are mixed with 5-10 pts. wt. deionized water. The mixture is covered with a plastic thin film and fermented at 40 degrees C for 48-72 hours. The fermented product is dried at 45 degrees C and crushed through a pulverizer and sieved with 35-40 meshes.    USE - Method for manufacturing organic fertilizer used for plant (claimed).    ADVANTAGE - The method enables to manufacture phosphoric acid and nutrient substances enriched biodegradable organic fertilizer, kills harmful bacteria and pest in garden flowers, and reduces peculiar smell of fertilizer through histidine.    DETAILED DESCRIPTION - Manufacturing organic fertilizer involves utilizing 10-15 pts. wt. monoammonium phosphate, 3-6 pts. wt. rice water, 4-8 pts. wt. surface active agent, 6-10 pts. wt. egg shell powder, 1-1.5 pts. wt. chlorothalonil, 2-4 pts. wt. histidine, 15-20 pts. wt. deionized water and 2-3 pts. wt. yeast. Monoammonium phosphate, rice water, yeast and egg shell powder are mixed with 5-10 pts. wt. deionized water. The mixture is covered with a plastic thin film and fermented at 40 degrees C for 48-72 hours. The fermented product is dried at 45 degrees C and crushed through a pulverizer and sieved with 35-40 meshes. Remaining components are mixed with the powder, and then crushed through the pulverizer and sieved with 40 meshes to obtain granules.
NOVELTY - Bio-organic fertilizer comprises 10-12 pts. wt. component A, 4-6 pts. wt. component B, 3-5 pts. wt. component C and 1-2 pts. wt. microorganism preparation.    USE - Bio-organic fertilizer used for soil repairing (claimed).    ADVANTAGE - The bio-organic fertilizer is eco-friendly, ensures improved fertilizer effect, and removes pesticidal residue from soil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing component A, which involves mixing uniformly wheat bran and soybean meal in ratio of 1:1, adding 0.1 mol/l hydrochloric acid solution and leaching for 12 hours, drying it at 80 degrees C and crushing into powder, drying peanut shell dry and crushing into a pulverizer to obtain peanut shell powder, mixing powder, peanut shell powder and water in ratio of 1:1:1 and stirring in a tank with speed of 500 revolutions per minute for 15 minutes, heating the obtained material in a reactor with water steam at 95 degrees C for 30 minutes, and then naturally cooling to obtain component A;    (2) a method for preparing component B, which involves crushing calcite into calcite powder, and then mixing uniformly potassium chloride, humic acid and grass peat in ratio of 1:1:1:1 to obtain component B;    (3) a method for preparing component C, which involves crushing chitosan through 50-100 meshes, and then mixing chitosan powder uniformly with glycerol in ratio of 1:1 to obtain component C; and    (4) a method for preparing microorganism preparation, which involves mixing and stirring Bacillus, Pseudomonas, Enterococcus fecalis, Micrococcus luteus and Azotobacter in ratio of 3:3:2:1:1, and culturing to obtain microorganism preparation.
NOVELTY - The utility model is a new type relates to a plant fertilizer collecting processing device, specifically is a fertilizer production with a kitchen garbage primary treatment device, comprising box body (1), a temperature table (2), the electric control box (3), a panel (4), entrance (5), heater (6), back door (7), a pull ring (8), a guide plate (9), a depot (10), a clapboard (11), outlet (12), a collecting chamber (13), bushing (14), liquid collecting tank (15), the box body (1), wherein one end on a set with entrance (5), another end set with heater (6), the box body (1), one side equipped with the electric control box (3), the electric control box (3) equipped with a temperature table (2) and a panel (4), a box body (1) and another side set with rear door (7), door (7) equipped with a pull ring (8), the utility model is new type structure is simple, using suitable to solve have kitchen garbage use rate., problem of pollute environment.
NOVELTY - The utility model is new type supply have a animal body and a mini-a method for harmless treatment unit, belongs to harmless process device technology field, aiming at that existing died to animal body and process device of waste material of slaughtering, large harmless treatment device by the structure of limit square meter large floor space, the investment is high cost, complex operation problem equal. It comprises supply heat system, lifting system, made by a waste gas processing system, control system, made in a respectively connected with material lifting system, supply heat system, a waste gas processing system and control system, control system of control cabinet is respectively connected with power supply heat system, lifting system, made by a waste gas treatment system. The structure is simple and practical, operation is simple, it can complete kill the pathogen and reducing environmental pollute is suitable for farm, slaughterhouse, hatching site equal for each type of processing animal corpse died and slaughtering waste harmless treatment.
NOVELTY - A catalyst comprises carrier, and magnesium, nickel, calcium and iron supported on carrier.    USE - Catalyst is used for synthesizing methane from synthesis gas.    ADVANTAGE - The catalyst has excellent durability and workability, and is exposed to moisture at high-temperature environment of more than 700 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite catalyst, which involves injecting ammonia solution, dispersing catalyst precursor in water, and heat-treating.
NOVELTY - The device has a bracket (4) which is connected with a heating system (1). The bracket is provided with slide rail (4-1) and slide box cover (4-2). A lower portion of bracket is provided with driving bracket and bucket base plate. A reaction tube (2) is equipped with left and right end plates. A side wall of a cylindrical portion is connected with a discharging nozzle. An outside wall of cylindrical portion is connected oil groove. The cylindrical portion is provided with a cutting knife comprising a main shaft. The main shaft is connected with a driving device.    USE - Harmless processing device used for processing of dead animal corpse.    ADVANTAGE - The need to perform the incineration process is eliminated. Hence, the pollution to the environment with the smell of smoke is reduced. The raw material is reused after the reaction conserves the resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for controlling harmless processing device for processing of dead animal corpse.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the harmless processing device.    Heating system (1)    Reaction tube (2)    Bracket (4)    Slide rail (4-1)    Slide box cover (4-2)
NOVELTY - Zinc selenide calcium enriched foliar fertilizer comprises 60-70 pts. wt. biological fermentation amino acid, 30-40 pts. wt. humic acid, 20-30 pts. wt. boric acid, 15-25 pts. wt. potassium dihydrogen phosphate, 8-10 pts. wt. sodium bisulfite, 5-6 pts. wt. sodium selenite, 5-8 pts. wt. zinc sulfate, 6-8 pts. wt. calcium nitrate, 1-2 pts. wt. abscisic acid, 2-3 pts. wt. sodium nitrophenolate, 1-2 pts. wt. disodium EDTA, 2-3 pts. wt. microelement and 100 pts. wt. water.    USE - Used as zinc selenide calcium enriched foliar fertilizer.    ADVANTAGE - The fertilizer is rich in selenium, zinc or calcium element and boron, copper, iron, manganese, molybdenum trace elements, is capable of reducing pesticide dosage, contains boric acid that can extend the flowering period and enhance photosynthetic function, contains potassium dihydrogen phosphate that can supply necessary element for normal plant nutrition, and has reduced production cost.
NOVELTY - The utility model is new type relates to a plant organic fertilizer fermented inorganic material mixing system, comprising a fermentation site, converying vehicle, a second site, the first for a, a conveying belt, a cylinder, a conveying belt, a third site, the movable tripper, third transmission belt, hoisting machine, pulverizer, a, operating table, the fourth conveying belt, the fifth conveying belt, a cylinder, an inorganic material warehouse, sixth conveying belt, packer, seventh conveying belt, the finished product warehouse, inorganic material in a warehouse for a second, carrying on a second and a fifth conveying belt, the sixth conveying belt connected, each conveying belt is connected with power motor, each hopper is connected with adjustable speed for material transfer machine. A height the fermented organic fertilizer, fit and the inorganic material and organic fertilizer mixing process into formulated prescription fertilizer finished product, a fit and the inorganic material enter into packing form mixing fertilizer finished product, automatic degree high, material conveying and mixing fast, obvious increase production efficiency, reduce the labour intensity of the worker.
NOVELTY - Preparation of pure Form B of tapentadol hydrochloride (I) involves providing a solution of tapentadol base in solvent, cooling the resultant solution, adding carboxylic acid (excluding lower aliphatic carboxylic acid) to the cooled solution, optionally seeding with Form B of tapentadol hydrochloride, treating the reaction mixture with a source of hydrogen chloride, and isolating pure Form B of tapentadol hydrochloride.    USE - Preparation of pure Form B of tapentadol hydrochloride (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly preparation of Form B of tapentadol hydrochloride having high purity.    DETAILED DESCRIPTION - Preparation of pure Form B of tapentadol hydrochloride of formula (I) involves providing a solution of tapentadol base in solvent, cooling the resultant solution, adding carboxylic acid (excluding lower aliphatic carboxylic acid) to the cooled solution, optionally seeding with Form B of tapentadol hydrochloride, treating the reaction mixture with a source of hydrogen chloride, and isolating pure Form B of tapentadol hydrochloride.
NOVELTY - Recycling of organic waste involves crushing food waste, hydrolyzing, separating wastewater, transferring flushing water through drainage duct, mixing flushing water and hydrolyzed wastewater, concentrating, performing anaerobic digestion, obtaining biogas and digestive liquid, subjecting biogas to desulfurization purification, obtaining methane, centrifuging digestive liquid, mixing with biogas slurry, adding magnesium oxide and ferric chloride, obtaining organic sediment, mixing organic sediment with biogas, obtaining fertilizer, and adding sedimentation slurry to sewage pipe.    USE - Recycling of organic waste (claimed).    ADVANTAGE - The method enables recycling of organic waste by economical and environmentally-friendly process, within short period of time.    DETAILED DESCRIPTION - Recycling of organic waste involves crushing food waste collected using food waste breaker provided in kitchen drain, to product having particle size of 2-3 mm, hydrolyzing the pulverized product, separating wastewater, transferring flushing water through drainage duct, mixing flushing water and hydrolyzed wastewater in mixing tank, obtaining mixed sewage, concentrating, obtaining product containing 10-15% organic material, performing anaerobic digestion, obtaining biogas and digestive liquid, subjecting biogas to desulfurization purification, obtaining methane, centrifuging digestive liquid, mixing with biogas slurry and residue, adding magnesium oxide and ferric chloride, obtaining organic sediment, mixing organic sediment with biogas, obtaining fertilizer, and adding sedimentation slurry to municipal sewage pipe. An INDEPENDENT CLAIM is included for system for recycling of organic waste.
NOVELTY - The method involves injecting a fresh gas into a reactor (2). The volume of the reactor is 1/3-2/3. The organic object is subjected to the aerobic degradation reaction in the reactor. The soluble organic solution, soluble inorganic solution and fatty acids are poured into the reactor. A rotating device is provided to rotate a stirring device (8) in the reactor. The rotating device is connected with a conveying device. A bottom portion of the reactor is connected with a liquor discharging pipe (52). An activated sludge is added to the reactor.    USE - Method for processing and purifying organic and biological waste.    ADVANTAGE - The purifying effect of the organic and biological waste is reduced at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for processing and purifying organic and biological waste.    Reactor (2)    Stirring device (8)    Chamber (22)    Manifold (44)    Liquor discharging pipe (52)
NOVELTY - Aerobic fermentation of biological residue involves mixing dregs and complex agent in weight ratio of 1400:1-1800:1, adding biological residue, mixing, drying and subjecting resultant mixture to aerobic fermentation.    USE - Aerobic fermentation of biological residue (claimed).    ADVANTAGE - The method enables environmentally-friendly aerobic fermentation of biological residue within short period of time.
NOVELTY - A sheep cultivation and sheep farmyard manure is joint produced by setting sheep cultivation and sheep farmyard manure adjacent device comprising sheep barn and sheep farmyard manure pool with transparent ditch or underground dark tube connected by underground pipe, collecting sheep manure, and cultivating. The sheep manure is manufactured by water soaking corn or sunflower straw and wheat straw, adding manure, and stacking.    USE - Method for joint producing sheep cultivation and sheep farmyard manure (claimed).    ADVANTAGE - The method increases benefit.
NOVELTY - A double head poultry excrement target machine comprises roller (1), walking wheel (2), speed reducer (3), bottom plate (4), motor, flange, driving gear (7), shaft, transmission gear, electric appliance box, universal wheel, handle, rake teeth, target turn shaft, roller fixing plate, roller shaft and bar.    USE - Double head poultry excrement target machine.    ADVANTAGE - The machine greatly saves investment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of double head poultry excrement target machine.    Roller (1)    Walking wheel (2)    Speed reducer (3)    Bottom plate (4)    Driving gear (7)
NOVELTY - The equipment has burning kiln incineration lumen having kilns (1) inclined between 10-60 degrees . The burning cavity is provided with main motor to drive a drive spindle. The kilns have intake port, tobacco unit, feed unit (2), feed opening and closing doors (21). A feed cylinder is set with feeding auger that is connected to compression section. An auger shaft is provided with guillotine knife plate. An isolating network is connected with drive spindle.    USE - Ash fertilizer concentrate production equipment.    ADVANTAGE - The quality of the ash fertilizer is improved and environmental pollution is reduced. The waste heat is used for drying the raw materials and subsequent firing effect is enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ash fertilizer concentrate production equipment.    Kiln (1)    Feed unit (2)    Smoke tube (20)    Closing door (21)    Raw material drying apparatus (23)
NOVELTY - A mushroom cultivation matrix comprises 20-60 pts. wt. traditional Chinese medicine slag, 3-6 pts. wt. straw, 1-3 pts. wt. quicklime, 1-3 pts. wt. gypsum, 0.5-1 pt. wt. sucrose and 0.2-0.5 pt. wt. three-dimensional antheridiogen.    USE - Mushroom cultivation matrix.    ADVANTAGE - The matrix changes waste into treasure, saves planting cost and increases mushroom product quality, thus increasing economic benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mushroom cultivation matrix comprising taking traditional Chinese medicine slag, straw and quicklime, stirring, basking for 4-5 days, crushing, sieving to obtain main material, adding gypsum, sucrose and water, uniformly stirring to obtain mixed material, adding three-dimensional antheridiogen, diluting, spraying, wetting for 1-3 hours, stirring, packaging and sterilizing.
NOVELTY - A controlled-release fertilizer bag is prepared by grinding Eupatorium purple stems and non-purple stems as raw materials, pressing into transparent impermeable biodegradable film, forming into controlled-release films, adding biomass charcoal, fermented decomposition of peat by beneficial microorganisms, and inorganic nutrients, and mixing.    USE - Method for preparing controlled-release fertilizer bag (claimed).
NOVELTY - A tobacco plant composite fertilizer comprises ammonium dihydrogen phosphate, amino acid chelated manganese, zinc sulfate, amino acid chelated iron, amino acid chelated zinc, methionine, phytase, copper sulfate, amino acid chelated calcium, lysine, cobalt chloride hexahydrate, organic germanium, iodine yeast, ferrous ammonium citrate, boric acid, lentinan, and thiamethoxam.    USE - Tobacco plant composite fertilizer.    ADVANTAGE - The fertilizer has balance nutrient substance and insect pest preventive function.    DETAILED DESCRIPTION - A tobacco plant composite fertilizer comprises 10-20 pts. wt. ammonium dihydrogen phosphate, 0.8-1.2 pts. wt. amino acid chelated manganese, 0.4-0.6 pts. wt. zinc sulfate, 1.2-1.8 pts. wt. amino acid chelated iron, 1.2-1.6 pts. wt. amino acid chelated zinc, 0.5-0.8 pts. wt. methionine, 0.05-0.1 pt. wt. phytase, 0.3-0.6 pts. wt. copper sulfate, 0.002-0.004 pts. wt. amino acid chelated calcium, 0.4-0.5 pts. wt. lysine, 0.05-0.08 pts. wt. cobalt chloride hexahydrate, 0.05-0.1 pt. wt. organic germanium, 0.14-0.26 pts. wt. iodine yeast, 0.01-0.47 pts. wt. ferrous ammonium citrate, 0.1-0.3 pts. wt. boric acid, 0.4-0.6 pts. wt. lentinan, and 0.2-0.4 pts. wt. thiamethoxam.
NOVELTY - An organic fertilizer comprises 12-18 pts. wt. pre-fermented substance, 6-10 pts. wt. mineral, 0.5-0.8 pt. wt. Bacillus subtilis (ATCC 6633), 30-40 pts. wt. selenium-enriched rice bran, 5-10 pts. wt. Chinese medicine slag, and 15-20 pts. wt. humic acid. The pre-fermented material comprises 10-20 pts. wt. soybean meal, 1-3 pts. wt. humic acid, 3-5 pts. wt. molasses, 0.1-0.2 pt. wt. sodium selenite, and 0.1-0.2 pt. wt. Bacillus subtilis (ATCC 6633). The mineral substance comprises 40-60 pts. wt. phosphate ore, 40-60 pts. wt. medical stone, and 1-3 pts. wt. silicon powder.    USE - Organic fertilizer used for improving soil and preventing disease.    ADVANTAGE - The fertilizer contains large amount of organic selenium and is environment-friendly and convenient to prepare.    DETAILED DESCRIPTION - An organic fertilizer comprises 12-18 pts. wt. pre-fermented substance, 6-10 pts. wt. mineral, 0.5-0.8 pt. wt. Bacillus subtilis (ATCC 6633), 30-40 pts. wt. selenium-enriched rice bran, 5-10 pts. wt. Chinese medicine slag, and 15-20 pts. wt. humic acid. The pre-fermented material comprises 10-20 pts. wt. soybean meal, 1-3 pts. wt. humic acid, 3-5 pts. wt. molasses, 0.1-0.2 pt. wt. sodium selenite, and 0.1-0.2 pt. wt. Bacillus subtilis (ATCC 6633). The mineral substance comprises 40-60 pts. wt. phosphate ore, 40-60 pts. wt. medical stone, and 1-3 pts. wt. silicon powder. The fertilizer is prepared by weighing raw materials, taking pre-fermented material as raw material, mixing, naturally fermenting for 1-2 weeks, adding selenium-enriched rice bran in microorganism organic fertilizer, mixing, naturally fermenting, and turning once a week for 6 weeks.
NOVELTY - The methane gas generation system has a feedstock pipe (10) and a discharging pipe (20) which are detachably connected with a straight pipe (30). A discharging pipe blocking plate (34) is connected with the discharging pipe. A feedstock pipe blocking plate (32) is connected with the feedstock pipe. One-way valves are respectively provided in the feedstock pipe and discharging pipe, for controlling fermentation methane gas flowed in the feedstock pipe and discharging pipe.    USE - Methane gas generation system for use in agricultural field.    ADVANTAGE - The methane gas slurry circulation flow stirring performance is improved, and the uniform distribution of strain is promoted using the stirring methane gas slurry circulation flow. The gas production is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methane gas generation system.    Feedstock pipe (10)    Discharging pipe (20)    Straight pipe (30)    Feedstock pipe blocking plate (32)    Discharging pipe blocking plate (34)
NOVELTY - Hydrogen manufacturing device comprises direct current power supply with electrolyser connected to conductive electrode in form of circuit. The circuit is connected with the direct current power source and cell that is placed below electrolyser. The cell is connected with draft tube to solution tank.    USE - Hydrogen manufacturing device.    ADVANTAGE - The hydrogen manufacturing device prepares hydrogen in low cost.
NOVELTY - Producing hydrogen involves mixing chlorine and water with hydrochloric acid and hypochlorous acid. Free hydrogen ion from hydrochloric acid is utilized to generate hydrogen by electrolytic reaction.    USE - Method for producing hydrogen (claimed).    ADVANTAGE - The method enables to produce hydrogen in cost-effective manner.
NOVELTY - The utility model is new type provides one kind of rapid drying ability with the kitchen waste aerobic fermentation device with stirring function by the reaction cavity body, cooling water circulation and the condensation water collecting system, air heating and ventilating system with function of deodorization, water bath heating and heat preservation system with remote monitoring and intelligent control system is composed of. Inner cavity body is equipped with a temperature/humidity sensor and an oxygen concentration sensor, for monitoring the temperature, humidity and oxygen concentration in cavity, inner water bath cavity is provided with heater and temperature sensor, in a supply heat to a cavity body, outside water bath in a separate insulating interlayer, a cavity body is used for carrying out heat preservation, air heating and ventilating system may ensure that the oxygen concentration within a cavity, cool water circulation and the condensation water collecting system can be in time for the water steam of derive in a cavity, tail sum deodorizing system can prevent the gas for the second time pollute environment in a treatment process, a PLC intelligent control by a control operation. The utility model is new type equipment structure is simple, a low energy consumption, processing effect is good.
NOVELTY - The utility model is new type provide the a and c, cultivation waste fast producing fertilizer device, by mixer, a level a tank, second level fermentation tank, sum pump, ozone purification device, organic fertilizer granulator and composed of heater, the mixer A and a fermentation tank, second level fermentation tank are orderly connected, the first-stage fermentation jar and a seat bottom of a fermentation tank set with a driving stirring device, the internal bottom circle set with exhaust pipe, upper part of the mixer set with kitchen garbage throwing a and a, bottom set with a mixed material outlet of the first-stage fermentation tank and the top part is a fermentation tank equipped with a circular are with, the top part of tank body set with ozone outlet, the secondary fermentation tank and bottom part on side wall formed with organic fertilizer outlet; the organic fertilizer outlet to install with organic fertilizer granulator. The device with small floor space, without pollute, process is fast.
NOVELTY - Treatment of power plant desulfurization sewage comprises preparing biological agent comprising Thiobacillus denitrificans, Bacillus cereus, Acinetobacter baumannii, Rhodococcus rhodochrous, Pseudomonas fluorescens and carrier; and adjusting pH of sewage to 7-7.5, adding biological agent at 20 g/m3 sewage once a day for 3 days, standing for 1 week, filtering through plate and frame filter, and discharging.    USE - Method for treating power plant desulfurization sewage.    ADVANTAGE - The method effectively removes sulfur compounds and industrial chemical oxygen demand.    DETAILED DESCRIPTION - Treatment of power plant desulfurization sewage comprises: (A) respectively culturing T. denitrificans, B. cereus, A. baumannii, R. rhodochrous and P. fluorescens into concentration of 1x 108 cells//ml solution; mixing T. denitrificans, B. cereus, A. baumannii, R. rhodochrous and P. fluorescens at volume ratio of 3:2:2:1:1; mixing bacterial mixture with carrier at weight ratio of 1:2; uniformly stirring at 100 revolutions/minute for 3 minutes; and drying at 20-22 degrees C until water content is 6-8% to obtain biological agent; and (B) adjusting pH of sewage to 7-7.5, adding biological agent at 20 g/m3 sewage once a day for 3 days, standing for 1 week, filtering through plate and frame filter, and discharging.
NOVELTY - Soil improvement agent comprises 50-69 wt.% animal manure, 3-4.5 wt.% biological calcium nitrate, 10-15 wt.% potassium nitrate, 3-5 wt.% brown rice, 0.5-1.25 wt.% amino acid, 5-7 wt.% fine straw, 5-7 wt.% fine soybean, 0.5-5 wt.% biological rotten material, 2-5 wt.% diatomite and 0.5-2 wt.% cerium oxide.    USE - Soil improvement agent used for improving soil for greenhouse plantation (claimed).    ADVANTAGE - The soil improvement agent is environment friendly, and reduces soil hardening and increases water retention and nutrient storage of soil, and ensures reduced waste discharge and increased plant growth, plant yield and environmental protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil improvement agent, which involves;    (A) fermenting animal feces, biological calcium nitrate and diatomite in a sealing container for 7-14 days;    (B) continuing fermentation with brown rice, fine wheat straw and fine soybean for 3-5 days;    (C) filtering fermented materials;    (D) drying filtered residue; and    (E) mixing dry fermented materials with potassium nitrate, amino acid and cerium oxide in a mixer for 5-15 minutes to obtain product.
NOVELTY - Preparation of composite aqueous agent involves purifying the glyphosate mother liquor, adjusting pH value, performing adsorption process using activated carbon, obtaining purified glyphosate liquid, ammonifying the resultant mixture using aqueous ammonia, adding additives to the resultant mixture, concentrating, obtaining glyphosate, crystallizing, performing N-(phosphono-methyl-iminodiacetic acid) oxidation process, filtering and performing membrane separation process. Glyphosate mother liquor comprises glyphosate, formaldehyde and iron ion.    USE - Preparation of composite aqueous agent (claimed).    ADVANTAGE - The method provides composite aqueous agent having excellent stability, by environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of composite aqueous agent involves purifying the glyphosate mother liquor, adjusting pH value, performing adsorption process using activated carbon, obtaining purified glyphosate liquid, ammonifying the resultant mixture using aqueous ammonia, adding additives to the resultant mixture, concentrating, obtaining glyphosate, crystallizing, performing N-(phosphono-methyl-iminodiacetic acid) oxidation process, carrying out solid-liquid separation process, filtering and performing membrane separation process. The glyphosate mother liquor comprises 60-70 g/kg glyphosate, 20-30 g/kg formaldehyde and 0.05-0.1 g/kg iron ion.
NOVELTY - Removing molybdenum from industrial waste involves filtering sewage containing molybdenum ions to obtain filtrate. Obtained filtrate is passed through an ion exchange resin in a ratio of 6-10:1 at the rate of 1-2 bed volume per hour for adsorption to obtain concentrate of molybdenum ion in a weight ratio of 1:15-20 and elution flow rate of 0.5-1 bed volume per hour. Fermentation is carried out for 25-30 days at room temperature with stirring once in a day. Fermented product is dried and granulated to obtain molybdenum.    USE - Method for removing molybdenum from industrial waste (claimed).    ADVANTAGE - The method enables to remove molybdenum from industrial waste that prevents the water pollution, supports animals in water body. The method ensures good ecological and social benefit.
NOVELTY - A mustard fertilizer comprises solid organic fertilizer comprising 30-50 pts. wt. fresh chicken manure, 40-70 pts. wt. traditional Chinese medicine slag and 10-20 pts. wt. soybean, and liquid organic fertilizer comprising 20-40 pts. wt. fresh chicken manure, 50-80 pts. wt. traditional Chinese medicine slag, 10-30 pts. wt. wheat bran, 5-10 pts. wt. soybean and 1-10 pts. wt. fermentation strain.    USE - Mustard fertilizer.    ADVANTAGE - The method is simple and suitable for industrialization. The fertilizer is rich in nutrition. It reduces plant diseases and insect pests, increases immunity, and increases product yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mustard fertilizer comprising taking solid organic fertilizer traditional Chinese medicine slag, drying, adding soybean, crushing, adding fresh chicken manure, stacking, adding fermentation strain, adding 1-3 times water, ventilating for 8-15 days, adding liquid organic fertilizer, stirring 3-4 times for 15-25 minutes, and fermenting for 3-5 days.
NOVELTY - A controlled-release fertilizer comprises lignite wax resin, humic acid salt, resin solvent, lignite essence liquid, high polymer chitosan, and nutritional compound containing rice straw, animal dung, urea, calcium chloride, ferrous sulfate, manganese sulfate, soil conditioner, pesticides, borax, bentonite, shell, ammonium phosphate, release agent, phosphate rock, flour, disodium edetate, fulvic acid, and mixed bacteria powder.    USE - Controlled-release fertilizer used for peony (claimed).    DETAILED DESCRIPTION - A controlled-release fertilizer comprises 40-75 pts. wt. lignite wax resin, 5-8 pts. wt. humic acid salt, 5-10 pts. wt. resin solvent, 21-25 pts. wt. lignite essence liquid, 70-95 pts. wt. high polymer chitosan, and nutritional compound containing 600-820 pts. wt. rice straw, 300-400 pts. wt. animal dung, 10-12 pts. wt. urea, 10-12 pts. wt. calcium chloride, 3-4 pts. wt. ferrous sulfate, 2-3 pts. wt. manganese sulfate, 10-15 pts. wt. soil conditioner, 5-10 pts. wt. pesticides, 4-10 pts. wt. borax, 5-10 pts. wt. bentonite, 10-15 pts. wt. shell, 10-15 pts. wt. ammonium phosphate, 1-5 pts. wt. release agent, 20-30 pts. wt. phosphate rock, 20-30 pts. wt. flour, 1-6 pts. wt. disodium edetate, 30 pts. wt. fulvic acid, and 50 pts. wt. mixed bacteria powder. INDEPENDENT CLAIMS are included for:    (1) preparation of controlled-release fertilizer comprising mixing all raw materials, and stirring at 40-48 degrees C; and    (2) preparation of nutritional compound comprising burning rice straw to obtain ash, mixing ash, animal dung, and mixed bacteria powder at 80-90 degrees C, fermenting at 25-30 degrees C for 30-45 days, drying, milling, adding urea, calcium chloride, ferrous sulfate, manganese sulfate, soil conditioner, pesticides, borax, bentonite, shell, ammonium phosphate, release agent, phosphate rock, flour, disodium edetate, fulvic acid, and mixed bacteria powder, and mixing.
NOVELTY - A palladium/carbon catalyzed ortho iodinated functionalized aromatic ring is prepared by mixing substrate comprising functional group-containing aromatic ring, palladium/carbon catalyst, oxidizing agent, and iodination agent in solvent, and reacting at 50-120 degrees C for 3-12 hours, after finishing reaction, and post-processing reaction liquid to obtain ortho iodinated product.    USE - Method of preparing palladium/carbon catalyzed ortho iodinated functionalized aromatic ring (claimed).    ADVANTAGE - The method does not produce large amount of industrial waste, has less pollution to the environment, and high yield and selectivity, and is suitable for industrialization. The catalyst is recyclable and the iodination agent has low cost.    DETAILED DESCRIPTION - Preparation of palladium/carbon catalyzed ortho iodinated functionalized aromatic ring comprises mixing substrate comprising functional group-containing aromatic ring, palladium/carbon catalyst, oxidizing agent, and iodination agent in solvent, and reacting at 50-120 degrees C for 3-12 hours, after finishing reaction, and post-processing reaction liquid to obtain ortho iodinated product. The functional group-containing aromatic ring is specific functional group-substituted aromatic ring. The specific functional group is amide, cyano, carboxyl, carbonyl, or nitrogen-containing heterocyclic ring. The aromatic ring is substituted with specific functional group other than benzene, pyridine, furan, or thiophene, or is substituted with hydrogen, fluorine, chlorine, bromine, methyl, ethyl, phenyl, methoxyl, ethoxyl or trifluoromethyl. The oxidizing agent is oxygen, silver acetate, silver carbonate, iodobenzene diacetate, hydrogen peroxide, peracetic acid or t-butylhydroperoxide. The iodination agent is 1,3-diiodo-5,5-dimethylhydantoin, N-iodosuccinimide, elemental iodine, iodine chloride, hydroiodic acid, potassium iodide, sodium iodide, lithium iodide or cuprous iodide.
NOVELTY - A high purity phenazine is isolated from chemical products waste by preheating liquid containing phenazine raw material in heat exchanger, separating aniline and azobenzene, recycling aniline with purity of greater than 97%, allowing heavy stream to enter middle column, and taking 4-aminodiphenylamine as bottom heavy component.    USE - Method for isolating high purity phenazine from chemical products waste (claimed).    ADVANTAGE - The method has reduced energy consumption.
NOVELTY - Pretreatment of organic waste involves providing an organic waste, treating the organic waste with specified amount of alkaline and/or peroxide composition by ultrasonic processing, and adding specified amount of alkaline and/or peroxide composition for preset time, while ultrasonic processing the organic waste. The treatment of organic waste with alkaline composition is carried out simultaneously or concomitantly.    USE - Pretreatment of organic waste e.g. waste activated sludge, primary sludge, food waste, oily waste and solid waste (claimed) used for producing methane.    ADVANTAGE - The method provides pretreated organic waste having high organic content with reduced energy consumption, and reduced amount of sodium hydroxide and lime. The organic waste provides methane with high productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste treatment plant.
NOVELTY - The utility model is new type relates to a plant for family organic garbage treatment for organic fertilizer of device, belongs to a device of energy-saving and emission reduction technology can field. The device can separate use, or a toilet bowl connected can use. The device through a conveying pipe connected to storage drying bucket, storage drying bucket provided with sealing top cover, a storage drying bucket internal upper part provided with microwave wave high warm a storage drying bucket internal up and down orderly set with smashing cutter and a water processing device, smashing cutter and a motor, the additive container through pipeline connecting storage drying bucket, storage bucket bottom provided with drying pipe, drying storage bucket one side set with material discharging pipe, a material discharging pipe provided with an exhaust fan. The device can directly organic garbage in local processing, using or reducing waste of water resource, reducing waste to the environment, in particular also for the a. c. processing is a very useful organic fertilizer, saving can realize reduction of goal.
NOVELTY - The utility model is new type belongs to compost. technology field, especially relates to a single layer structure a translation of a plate turn fertilizer machine. Comprises a lengthways drive mechanism, a transverse driving mechanism, mechanism main body, rotating device, wherein lengthways driving mechanism used for driving the whole turn fertilizer machine a groove along the lengthways direction, transverse drive mechanism used for driving main body the transverse translation mechanism, thus make alignment of the collective distribution of compost material. Main body mechanism can change the horizontal included angle a floor under the effect of a rotating device. A specific lath mounting has a multi-piece cutting, b mounted adjacent 2 strip of cutting chip of a mutually staggered a turning process and thus the compost material a cutting block. Rear side of transverse driving mechanism a transverse through out of t 1 by motor drive can rotate the crushing stick, process for preparing compost material in the crushing and turning process.
NOVELTY - The new type utility claims one plant gear transmission turning, the turning and, by engine power output to the power distributor, power distributor for power distribution to the gear in gear box, gear box in sequence for transfer power mesh, a bottom gear shaft for power input to the turning roller. The manure by using gear transmission, increase the power output efficiency and prolongs the using life of transmission mechanism, reducing the failure rate.
NOVELTY - The utility model is new type provide a small plant organic fertilizer for aerobic fermentation groove, a bottom side, a left side face, a right side face, front side face and rear side, also located on the left side and a sliding groove on a right side face, a front side face mounted in a sliding groove, a sliding groove along a lower moving, the bottom side face has a stirring device and an aeration groove, the aeration groove through pipeline and high pressure air pump connection, the bottom side surface and the rear side surface connecting installation has a supporting device, the supporting device by a pedestal, b pedestal is set with a lifting upright post is one. The device using suitable, operation is simple, a small batch fermentation meet the farmer or scientific research unit a need of organic fertilizer, at the same time with reduce the labour intensity, increase production organic fertilizer efficiency of the function, which is good for our country environment of comprehensive treatment.
NOVELTY - An anti-Ebola virus drug BCX4430.2Hcl is prepared by cyclization reacting raw materials to obtain (1S,3R,4S,5R,6S)-1-phenyl-3-(1-benzotriazolyl)-4,5-diacetoxy-1H,6H-naphtho(1,2-e)pyrrolo(2,1-b)(1,3)oxazine, substitution reacting with N-acetyl-7-bromo-4-amine-5H-pyrrolo(3,2-d)pyrimidine under presence of metal magnesium to obtain (1S,3R,4S,5R,6S)-1-phenyl-3-(N-acetyl-5H-pyrrolo(3,2-d)pyrimidin-4-amine-7-yl)-4,5-diacetoxy-1H,6H-naphtho(1,2-e)pyrrolo(2,1-b)(1,3)oxazine, addition reacting with tert.-butyloxy methyl chloride, benzyl removal reacting, and hydrolytic deprotecting.    USE - Preparation of anti-Ebola virus drug.    ADVANTAGE - The preparation has easily available raw material, is environment-friendly and economic, and promotes raw material medicine production and its economic development.    DETAILED DESCRIPTION - An anti-Ebola virus drug BCX4430 of formula (I) is prepared by cyclization reacting 2,5-dimethoxy-3S,4R-dimethoxy tetrahydrofuran, (S)-1-( alpha -aminobenzyl)-2-naphthol, and benzotriazole to generate (1S,3R,4S,5R,6S)-1-phenyl-3-(1-benzotriazolyl)-4,5-diacetoxy-1H,6H-naphtho(1,2-e)pyrrolo(2,1-b)(1,3)oxazine, substitution reacting obtained compound with N-acetyl-7-bromo-4-amine-5H-pyrrolo(3,2-d)pyrimidine under presence of metal magnesium to obtain (1S,3R,4S,5R,6S)-1-phenyl-3-(N-acetyl-5H-pyrrolo(3,2-d)pyrimidin-4-amine-7-yl)-4,5-diacetoxy-1H,6H-naphtho(1,2-e)pyrrolo(2,1-b)(1,3)oxazine, addition reacting obtained compound with tert.-butyloxy methyl chloride to obtain (1S,2R,3S,4R,5R)-1-( alpha -(((2-N-acetyl-5H-pyrrolo(3,2-d)pyrimidin-4-amine-7-yl)-3,4-acetoxy-5-methyl-tert.-butyryloxy)pyrrolidinyl)benzyl)-2-naphthol, benzyl removal reacting compound to obtain (2R,3S,4R,5R)-2-((N-acetyl-5H-pyrrolo(3,2-d)pyrimidin-4-amine-7-yl)-3,4-diacetoxy-5-methyl-tert.-butyryloxy)pyrrolidine, and hydrolytic deprotecting.
NOVELTY - Preparing (S)-6-(2,5-difluorophenyl)-7a-phenyl-5,7a-dihydro-1H,3H-pyrrolo(1,2-c)oxazol-3-one (I), comprises e.g. (i) reacting 4-phenyl-4-vinyl-1,3-dioxolan-2-one with 2-methoxy-phenyl isocyanate under action of palladium complex catalyst to obtain (S)-3-(2-methoxyphenyl)-4-phenyl-4-vinyl-oxazolidin-2-one (IV), (ii) reacting (IV) with silver nitrate and ammonium persulfate to obtain (S)-4-phenyl-4-vinyl-oxazolidin-2-one (V), (iii) reacting (V) with sodium hydride and 2-((3-bromopropen-2-yl))-1,4-difluorobenzene, and (iv) reacting obtained compound in presence of ruthenium compound catalyst.    USE - The method is useful for preparing (S)-6-(2,5-difluorophenyl)-7a-phenyl-5,7a-dihydro-1H,3H-pyrrolo(1,2-c)oxazol-3-one.    ADVANTAGE - The method: has short reaction step, mild reaction conditions, high product yield, and excellent enantioselectivity; and produces (I), which is an important intermediate for the preparation of anticancer drug MK-0731.    DETAILED DESCRIPTION - Preparing (S)-6-(2,5-difluorophenyl)-7a-phenyl-5,7a-dihydro-1H,3H-pyrrolo(1,2-c)oxazol-3-one of formula (I), comprises (i) reacting 4-phenyl-4-vinyl-1,3-dioxolan-2-one of formula (II) with 2-methoxy-phenyl isocyanate of formula (III) in an organic solvent at 0-100 degrees C for 3-48 hours under action of palladium complex catalyst (obtained by reacting palladium source with chiral ligand) to obtain (S)-3-(2-methoxyphenyl)-4-phenyl-4-vinyl-oxazolidin-2-one of formula (IV), (ii) reacting (IV) with silver nitrate and ammonium persulfate in a mixed solvent of acetonitrile and water to obtain (S)-4-phenyl-4-vinyl-oxazolidin-2-one of formula (V), then (iii) reacting (V) with sodium hydride and 2-((3-bromopropen-2-yl))-1,4-difluorobenzene of formula (VI) in tetrahydrofuran to obtain (S)-3-(2-(2,5-difluorophenyl)allyl)-4-phenyl-4-vinyl-oxazolidin-2-one of formula (VII), and (iv) reacting (VII) in presence of ruthenium compound catalyst in an organic solvent to obtain final product.
NOVELTY - Catalytic synthesis of sulfur-containing carboxylic acid amide compound (I) and sulfur compound (II) involves disulfide-containing compound and aliphatic amide compound (III) with acid or phosphorus ligand as ligand, inorganic salt as base and polar solvent as solvent in presence of nickel catalyst under the action of cerium ammonium nitrate or lithium hydroxide at 100-180 degrees C for 5-48 hours.    USE - Catalytic synthesis of sulfur-containing carboxylic acid amide compound and sulfur compound (claimed).    ADVANTAGE - The method enables environmentally-friendly catalytic synthesis of sulfur-containing carboxylic acid amide compound and sulfur compound.    DETAILED DESCRIPTION - Catalytic synthesis of sulfur-containing carboxylic acid amide compound of formula (I) and sulfur compound of formula (II) involves disulfide-containing compound and aliphatic amide compound of formula (III) with acid or phosphorus ligand as ligand, inorganic salt as base and polar solvent as solvent in presence of nickel catalyst under the action of cerium ammonium nitrate or lithium hydroxide at 100-180 degrees C for 5-48 hours.
NOVELTY - A watermelon-seedling-culturing substrate comprises an organic mixture, peat, perlite, vermiculite, plant ash, and a small amount of inorganic fertilizer.    USE - Substrate is used for culturing watermelon seedling.    ADVANTAGE - The substrate enables soil-less cultivation, is economical and full of nutrients, and has a light texture.
NOVELTY - Preparation of rice fertilizer additive involves dissolving antimicrobial active substance in water, stirring for 8-10 hours, obtaining solution of antimicrobial active substance, adding powder material and stirring uniformly. The powder material is obtained by fermenting 10-15 pts. wt. organic material for 25-30 days, adding 8-10 pts. wt. trace elements, 3-5 pts. wt. humic acid and water, stirring , heating, adding 4-7 pts. wt. release agent and 2-3 pts. wt. antiviral agent, heating at 100-110 degrees C, drying the resultant material and pulverizing in a pulverizer into powder.    USE - Preparation of additive used for rice fertilizer.    ADVANTAGE - The additive improves soil conditions.    DETAILED DESCRIPTION - Preparation of rice fertilizer additive involves dissolving antimicrobial active substance in 4-6 volumes of water, stirring at room temperature for 8-10 hours, obtaining solution of antimicrobial active substance, adding powder material and stirring uniformly. The powder material is obtained by fermenting 10-15 pts. wt. organic material for 25-30 days, adding 8-10 pts. wt. trace elements, 3-5 pts. wt. humic acid and water, stirring uniformly, heating at 90-100 degrees C for 30 minutes, adding 4-7 pts. wt. sustained-release agent and 2-3 pts. wt. antiviral agent, heating at 100-110 degrees C for one hour, drying the resultant material and pulverizing in a pulverizer into powder.
NOVELTY - A planting fertilizer comprises 100-120 pts. wt. cow manure, 30-50 pts. wt. Bupleurum, 20-40 pts. wt. woody, 40-60 pts. wt. diatomaceous earth, 15-17 pts. wt. Sophora flavescens, 30-50 pts. wt. pine needle, 18-20 pts. wt. Isatidis, 8-10 pts. wt. pepper powder, 12-14 pts. wt. peanut cake, 14-16 pts. wt. monoammonium phosphate, 10-12 pts. wt. calcium powder and 150-170 pts. wt. water.    USE - Planting fertilizer is used for soil.    ADVANTAGE - The environmentally-friendly planting fertilizer is rich in nutrients, and effectively improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of planting fertilizer which comprises mixing all the crushed components with water, fermenting for 3-5 days while sealed, standing for 15 hours and granulating the product.
NOVELTY - Soil conditioning agent comprises Bacillus subtilis, Bacillus licheniformis and Trichoderma in ratio of 0.5-2:0.2-1.8:0.3-1.5.    USE - Soil conditioning agent used for treating pseudoginseng disease while continuous cropping (claimed).    ADVANTAGE - The soil conditioning agent increases survival rate of pseudoginseng, increases microorganism that promotes decomposition of organic matter in soil, and reduces generation of harmful pathogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil conditioning agent, which involves:    (A) mixing Bacillus subtilis, Bacillus licheniformis and Trichoderma to carry out fermentation to obtain broth 1-10 ml; and    (B) mixing carrier 100-5000g with broth and heating at 15-70 degrees C for 48 hours, and then adding active component to obtain final product.
NOVELTY - Preparation of high-purity epigallocatechin gallate involves dissolving tea polyphenol crude extract with epigallocatechin gallate content of 20-60% in 10% aqueous ethanol, filtering undissolved substance, eluting by using gradient aqueous ethanol, adjusting pH of eluent to 4-5 using glacial acetic acid, concentrating, diluting resultant eluent concentrate as raw material with water, loading sample, collecting the solutions with epigallocatechin gallate content of 95-98 wt.% and more than 98 wt.%, concentrating resultant product, and drying.    USE - Preparation of high-purity epigallocatechin gallate (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of high-purity epigallocatechin gallate with high yield.    DETAILED DESCRIPTION - Preparation of high-purity epigallocatechin gallate involves dissolving tea polyphenol crude extract with epigallocatechin gallate content of 20-60% in 10% aqueous ethanol in an amount of 5-8 times of weight of the crude extract, filtering undissolved substance, eluting by using gradient aqueous ethanol when the sample loading amount is 5-8:1, adjusting pH of eluent to 4-5 using glacial acetic acid, collecting resultant product, concentrating, diluting resultant eluent concentrate as raw material with water in an amount of 2-3 times of volume of eluent concentrate, loading sample in a column volume of 20-30:1 in which eluent is 8% aqueous ethanol (adjusting pH value to 4-5 using glacial acetic acid), collecting the solutions with epigallocatechin gallate content of 95-98 wt.% and more than 98 wt.%, concentrating resultant product, and drying. The eluent includes 2-3 BV water, 4-5 BV 30% ethanol and 5-8 BV 40% ethanol.
NOVELTY - The resistance-net anaerobic fluidized bed has an annular resistive network that is composed of a three-dimensional multi-layer barrier region (1). Several multi-faceted layers of foam hollow ball (2) are provided. A double polyethylene plastic material (3) is provided inside and outside the ball.    USE - Resistance-net anaerobic fluidized bed.    ADVANTAGE - Efficient anaerobic digester biogas production capacity is obtained. The rural domestic fuel gas requirement is satisfied. The large industrial production is achieved. The resistance-net anaerobic fluidized bed is obtained at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the annular resistive network of the resistance-net anaerobic fluidized bed.    Three-dimensional multi-layer barrier region (1)    Foam hollow ball (2)    Double polyethylene plastic material (3)
NOVELTY - Extraction of lipid fraction from trap grease involves mixing a volume of waste cooking oil with a volume of trap grease to form a mixture comprising aqueous fraction, solid fraction and lipid fraction, heating the mixture to 55-85 degrees C for 45-210 minutes to extract at least 80% of lipids from the trap grease, and separating a portion of the lipid fraction from the solid fraction by a process chosen from filtration process and heating process. The heating process involves heating the mixture for preset time for evaporating at least majority portion of the aqueous fraction.    USE - Extraction of lipid fraction from trap grease used for forming biodiesel (claimed).    DETAILED DESCRIPTION - Extraction of lipid fraction from trap grease involves mixing a volume of waste cooking oil with a volume of trap grease to form a mixture comprising an aqueous fraction, a solid fraction, and a lipid fraction, heating the mixture to 55-85 degrees C, and maintaining for 45-210 minutes to extract at least 80% of lipids from the trap grease, and separating a portion of the lipid fraction from the solid fraction by a process chosen from filtration process and heating process. The heating process involves heating the mixture for preset time for evaporating at least majority portion of the aqueous fraction. The volumes of waste cooking oil and trap grease are mixed in the ratio 1.5:1-4.5:1 (ml:mg). An INDEPENDENT CLAIM is included for formation of biodiesel from tap grease.
NOVELTY - The apparatus has an evaporator (86) that is provided in a fuel gas supply flow path (20). A mixing chamber is provided in fuel gas supply flow path and to which water vapor and raw fuel gas are mixed. The mixing chamber and evaporator are arranged from upper direction at the fuel gas supply path. The mixed gas uniform supply portions (112,113) are provided to equalize the supply of mixed gas with respect to modification catalyst (96) in a modification portion (94) and provided rather than the inlet port of modification portion, in the upstream of fuel gas supply path.    USE - Solid oxide fuel cell apparatus.    ADVANTAGE - The mixed gas is uniformly supplied with respect to the modification portion. The variation in supply amount of the mixed gas with respect to the modification catalyst is suppressed. Equalization of supply of the mixed gas with respect to the modification portion is realizable by simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the fuel cell container incorporated in the solid oxide fuel cell apparatus.    Fuel gas supply flow path (20)    Evaporator (86)    Modification portion (94)    Modification catalyst (96)    Mixed gas uniform supply portions (112,113)
NOVELTY - The system has a bioreactor (10) located in an upper part of a separation zone. A pipe line is equipped with a waste valve (13) and a digested matter tank (14). An upper wall of the bioreactor is connected with a gas pipeline (17) that is attached with a valve (18) for discharging biogas to a high pressure gas tank (9). A pipe (15) is provided with a gas valve (16) of a biogas low pressure gas tank (6). A bottom part of the bioreactor is arranged in an outlet pipe that is attached with a valve (19) for discharging the sedimenting fractions in the digested matter tank.    USE - System for producing biogas during anaerobic digestion process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for producing biogas during anaerobic digestion process.    Biogas low pressure gas tank (6)    High pressure gas tank (9)    Bioreactor (10)    Waste valve (13)    Digested matter tank (14)    Pipe (15)    Gas valve (16)    Gas pipeline (17)    Valve (18)    Valve (19)
NOVELTY - The system has a first section located in tank substrate (1) and a dosing pump substrate (2). An expansion vessel (4) provides a reciprocating motion in the tank substrate. An upper part of a bioreactor (3) is located in a separation zone and extended from a reservoir (17), where transmitted digestive waste is separated from biogas. Discharged gas pipelines are equipped with a gas valve (9). A bottom part of the bioreactor is situated in an outlet pipe for discharging the sedimenting fractions to the bioreactor that is arranged in a fermentation unit.    USE - System for processing an organic material to obtain biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for processing an organic material.    Tank substrate (1)    Dosing pump substrate (2)    Bioreactor (3)    Expansion vessel (4)    Gas valve (9)    Reservoir (17)
NOVELTY - The furnace has a furnace body comprising an outside cylinder and an inner cylinder. An upper end of the inner cylinder is provided with a feeding port. A furnace cover seals a feeding port. A lower end of the inner cylinder is provided with an igniter that is connected with an air outlet structure. A week wall ring is connected with an air outlet. An inner wall of the outside cylinder is provided with a vertical separating plate. The separating plate is divided into two compartments.    USE - Low tar yield biomass gasification furnace.    ADVANTAGE - The furnace increases combustion gas conversion rate and reduces tar pollution to environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a low tar yield biomass gasification furnace.
NOVELTY - The utility model is new type is one fine particle A or biomass gasification process system of solid fossil fuel, the combustion system using fine particle biomass or circulation fluidization bed combustion technology and efficient cyclone separating technology, fine particle circulation fluidization combustion technology of solid fossil fuel use have flat orientation, realize coal granule and refining; fine particle or solid fossil fuel and biomass fluidization bed gasification reactor system using fine particle sum by technology, fine particle sum by using technology have flat orientation, that have the current coal gas technique system of gas, gas heat value and low problem of waste heat use system for gasification process sum and carry heat conversion to steam and supplied to fine particle or solid fossil fuel and biomass fluidization bed gasification reactor system, using its own energy source, reduce cost, also comprising ash processing system and gasification process sum purification system, which solves waste heat problem ash carry the gasification process sum and carry the sulphide and dust processing net is not problem.
NOVELTY - The utility model is new type one plant biomass gasification fuel gas applied for kiln furnace sintering system, belonging to biomass gasification heat using technology field, wherein feeding port for gasification furnace is mounted on side wall of gasification air blower through air pipe and gasification furnace gasification, after gasification furnace part in turn mounted first-stage cyclone separator, second level cyclone separator and fuel gas pipe, the fuel gas pipe through water sealing and emptying pipe, the fuel gas pipe through the burner and furnace, the burner mounted at two edge kiln furnace and side wall above the air blower through air pipe and burner connected with phase, adopt the utility new type design of biomass gasification fuel gas applied for kiln furnace sintering system, with high efficiency, stable running, no pollute equal, it solves existing biomass heat using technology is difficult to apply for technology problem the kiln furnace sintering system.
NOVELTY - Method for preparing compost, involves obtaining substrate, where the substrate comprises oil palm harvested material including at least palm kernel cake (PKC) and empty fruit bunches (EFB), inoculating aqueous mixture of molasses, mesocarp fibers and EFB compost, inoculating raw PKC, adding rock phosphate, EFB fibers and EFB ash, adjusting moisture content, maintaining mixture at temperature of 70 degrees C or less, turning the substrate and adding alkaline material to adjust pH to obtain the product.    USE - The method is useful for preparing compost (claimed).    ADVANTAGE - The method enables to prepare compost which is nontoxic.    DETAILED DESCRIPTION - Method for preparing compost, involves obtaining substrate, where the substrate comprises oil palm harvested material including at least palm kernel cake (PKC) and empty fruit bunches (EFB), inoculating aqueous mixture of molasses, mesocarp fibers and EFB compost, inoculating raw PKC to substrate containing PKC, adding rock phosphate, EFB fibers and EFB ash, adjusting moisture content to 50%, maintaining mixture at temperature of 70 degrees C or less, turning the substrate regularly to maintain the oxygen level of more than 12%, and adding alkaline material to adjust pH to obtain the product, where the compost comprises high levels of humic and fulvic acids which can be extracted to prepare liquid fertilizers.
NOVELTY - Invention describes a method of producing biodiesel fuel from plant material, which includes physical treatment of a mixture of vegetable oil, alcohol and an alkali, wherein treatment is carried out with a stream of microwave energy, and the alcohol used is isopropanol, wherein the mixture is placed in a resonator which operates as a reaction vessel; a magnetron is placed over the resonator; a waveguide is placed between the resonator and the magnetron such that the waveguide can move in the vertical plane and when producing biodiesel fuel, the treated mixture is pumped through a closed loop.    USE - Chemistry.    ADVANTAGE - Speeding up the process while simultaneously improving consumer properties of the end product - biodiesel fuel, and excluding methanol from the process.5 cl, 1 dwg
NOVELTY - The utility model claims Livestock manure deodorizing device using decomposing inoculant , comprising a liquid storage tank, an infusion pipe, pressure pump, spray pipe, an atomizing shower nozzle, comprising a liquid storage tank bottom connected with transfusion tube, a transfusion tube through pressure pump and spray pipe connected with, wherein spray pipe set up with atomizing shower nozzle, the utility model is new type with convenient operation, deodorizing ability is strong.
NOVELTY - The new type utility claims have one kind medicine clean tube, comprising needle head, an infusion tube, a liquid injection pipe, head pipe and liquid storage room, wherein the needle head mounted on one end of infusion tube, another end of infusion hose mounted at one end liquid injection pipe is, another end tube is set with liquid feedstock wherein near one end wherein the feedstock in liquid injection pipe mounted with glue head tube close to one end wherein the feedstock injection tube mounted on the first connected with pipe, at the first connected pipe connected with liquid storage room, room and one end connected with the second connected tube, one end connected pipe is connected on the second injection pipe above, the first connected pipe, room and the second connected pipe form one of connected loop. The medicine clean pipe can realize further clean recovery and to drug use, which avoids have pollute and waste of medicine.
NOVELTY - The new type utility claims have one kind novel heat tube type biomass gasification device, comprising a biomass gasification furnace, upper end of the biomass gasification furnace set with biomass inlet, lower end set with ash outlet, the body wall of the biomass gasification furnace of inner shell and composed of shell, between the inner shell and the shell form a gap interlayer cavity, lower end of the interlayer cavity through pipeline and steam generator connected, through out of the inner shell set with high temperature heat pipe, the high temperature heat pipe and outside end is located in the interlayer cavity, said inner shell and upper end through fuel gas tube and a cyclone separator connected, the cyclone separator and the upper end in turn connected and purifier and filter, and the filter upper end set with purification gas outlet. The utility model is new type using hot water steam replaced by air as gasifying agent, can can avoid the nitrogen dilution gas in air, make increase thermal value, heat value is for direct air supply heat gasification of 2 to 3 times.
NOVELTY - The manufacturing method involves stacking the members including gas separators (15,16) through engagement of gas separators with the fuel cell manufacturing apparatus by engaging the first engagement component (28) with a first guide member, and engaging second engagement component with a second guide member. The stacked members satisfy a configuration that a first support location and second support location of first and second engagement components supported by first and second guide members are arranged at positions away from each other.    USE - Manufacturing method for fuel cell, e.g. solid oxide fuel cells.    ADVANTAGE - Facilitates the positioning and stacking of respective gas separators with high accuracy since the gas separators are kept parallel to the direction of gravity. Facilitates the operation of compensating for the layer misalignment of the previously stacked gas separators since the stacking of gas separators in the suspended state does not cause the gravitational force to act in the stacking direction. Improves the operability during assembly for stacking the unit cells since the visual recognition with regard to the orientation of unit cells can be enhanced. Suppresses the layer misalignment during stacking since the configuration of modification facilitates the operation of positioning and stacking unit cells with high accuracy. Enhances the accuracy of positioning of the unit cell in the horizontal direction while suppressing the complexity of the configuration of the manufacturing apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gas separator for fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a unit cell.    Unit cell (10)    Power generation assembly (12)    Resin frames (13,14)    Gas separators (15,16)    Engagement component (28)
NOVELTY - An alpha -carboxyl- omega -hydroxyl fatty acid oxidized from a substantially pure Candida host cell, is new. The substantially pure Candida host cell is characterized by: a first genetic modification class that comprises one or more genetic modifications that collectively or individually disrupt an alcohol dehydrogenase (ADH) gene, and a second genetic modification class, where the second genetic modification class comprises an insertion of a first gene into the Candida host cell genome.    USE - The alpha -carboxyl- omega -hydroxyl fatty acid is useful for producing biofuels.    ADVANTAGE - Methods are provided for the genetic modification of Candida species to produce strains improved for the production of biofuels. Biological conversion methods for compounds use readily renewable resources such as fatty acids as starting materials rather than non-renewable petrochemicals. For example, omega -hydroxy fatty acids and alpha , omega -dicarboxylic acids can be produced from inexpensive long-chain fatty acids, which are readily available from renewable agricultural and forest products such as soybean oil, corn oil and tallow. Moreover, a wide range of alpha -carboxyl- omega -hydroxyl fatty acids with different carbon length can be prepared because the biocatalyst accepts a wide range of fatty acid substrates.
NOVELTY - An anaerobic digestion device comprises a digester body (110) with an opening through which organic waste is received; a removable digester drum inserted into the digester body for receiving the organic waste; and ports (150) spaced along the digester body and arranged to vent biogas from the organic waste contained in the digester drum.    USE - The device is used for anaerobic digestion of organic waste (claimed).    ADVANTAGE - The device is used for anaerobic digestion of organic waste (claimed).    DETAILED DESCRIPTION - An anaerobic digestion device comprises a digester body (110) with an opening through which organic waste is received; a removable digester drum inserted into the digester body for receiving the organic waste; and ports (150) spaced along the digester body and arranged to vent biogas from the organic waste contained in the digester drum.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an anaerobic digestion system.    Digester body (110)    Ports (150)    Hydrogen sulfide scrubber (160)    Storage vessel (170)    Tubing/piping (180)
NOVELTY - Conversion of solid biomass to hydrocarbons involves feeding at least a portion (311,313) of a regenerated catalyst (340,342) to biomass conversion unit in 2 or more stages, treating biomass in biomass conversion unit in 2 or more stages, and feeding 1 or more components regenerated in each stage. The regenerated catalyst comprises acidic component, basic component and metallic component.    USE - Conversion of solid biomass to hydrocarbon used for renewable fuel e.g. biofuels.    ADVANTAGE - The method provides hydrocarbon with high yield by economical process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the conversion of solid biomass to hydrocarbon.    Catalyst portions (311,313)    Regeneration unit (318)    Solid separator (324)    Spent catalyst (330)    Regenerated catalyst (340,342)
NOVELTY - An electrochemical cell comprises an anode, a cathode and a water-in-salt electrolyte.    USE - Electrochemical cell is used for plug-in hybrid electrical vehicles and electric vehicles.    ADVANTAGE - The hybrid high-voltage electrochemical cell has high conductivity and low viscosity, and is economical, safe and environmentally-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining electrochemical reaction of magnesium/hydrogen battery in water-in-salt electrolyte.
NOVELTY - Production of aromatics and other chemicals, involves providing methane feedstock to reactor (R1) to produce a product stream (S1) comprising aromatics and hydrogen, in which the methane feedstock is contacted with a catalyst, recovering aromatics from the product stream (S1) to create an aromatics depleted resulting stream, mixing the aromatics depleted resulting stream with a feed stream to create a combined product stream, and providing the combined product stream to a reactor (R2) to produce a product stream (S2) comprising water and unconverted methane.    USE - Production of aromatics used for producing methane-rich gas (claimed) used in chemical industries.    ADVANTAGE - The method enables efficient and economical production of aromatics with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of methane-rich gas, which involves receiving a resulting stream from one or more dehydroaromatization reactions, extracting aromatics from the resulting stream, which is converted to an aromatic depleted resulting stream, mixing the aromatics depleted resulting stream with a carbon dioxide feed or steam feed stream to create a combined stream, mixing the combined stream with one or more methanation catalysts in a methanation reactor to produce another resulting stream, and extracting water from the another resulting stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of integrated system for producing aromatics.    Integrated process (101)    Feed line (102)    Dehydromatization reactor (103)    Transfer line (107)    Methanation reactor (109)
NOVELTY - Bioplateau with an air aqueous vegetation for cleaning of sewage, comprises walls made from screen box containers, with outer faces formed by a rock material of the ejected and/or metamorphic rock, where bioplateau made with the possibility of arrangement of microflora and microorganisms, which contains strains of the bacteria Pseudomonas, yeast Candida and other microorganisms, destructors of petroleum hydrocarbons, where the containers are covered with elastic plain India-rubber and filled with rubber crumb with size of 0.5-1.2 microns.    USE - Bioplateau with an air aqueous vegetation for cleaning of sewage (claimed).
NOVELTY - The method involves providing water for planting non-polluted organic plant or vegetable on the edible fungus site. The product is soaked and planted to be processed on the edible fungus site. The water content of the edible fungus site is set in the range of 8-13 %. The inoculating rod relative humidity is set in the range of 50-65 %. The temperature of the edible fungus site is in the range of 5-40 degrees C.    USE - Method for planting non-polluted organic plant or vegetable e.g. mushroom, lucid ganoderma, oyster mushroom, radish, cucumber, tomato, cowpea, bitter gourd, Chinese cabbage, potato, sweet potato and pepper (all claimed).    ADVANTAGE - The non-polluted organic plant or vegetable can be planted effectively and easily. The environment can be protected safely from the pollution.
NOVELTY - Photovoltaic hydrogen production system comprises photovoltaic hydrogen production device (11), wireless communication aggregation node (13), photovoltaic modules, direct current converter, electrolytic cell, wireless sensor module and state controller.    USE - Photovoltaic hydrogen production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of photovoltaic hydrogen production system.    Photovoltaic hydrogen production device (11)    Wireless communication aggregation node (13)
NOVELTY - Device comprises a biogas fermenter, an anode, a cathode and an exoenzyme-farm. The anode is attached to the inside of the biogas fermenter. In the operation of the biogas fermenter the biomass present in the biogas fermenter is at least partially available in contact with colonized exoelectrogenic bacteria. The cathode is attached to the outside of the biogas fermenter and is electrically connected to the anode. The cathode is separated from the anode by an ion-permeable separator. The exoenzyme-farm is arranged outside the biogas fermentor.    USE - The device is useful for production of biogas and electrical energy (claimed).    ADVANTAGE - The device increases biogas Producing rate, accelerates polymer degradation, and does not utilize external electric power.    DETAILED DESCRIPTION - Device comprises a biogas fermenter, an anode, a cathode and an exoenzyme-farm. The anode is attached to the inside of the biogas fermenter. In the operation of the biogas fermenter the biomass present in the biogas fermenter is at least partially available in contact with colonized exoelectrogenic bacteria. The cathode is attached to the outside of the biogas fermenter and is electrically connected to the anode. The cathode is separated from the anode by an ion-permeable separator. The exoenzyme-farm is arranged outside the biogas fermentor and can be loaded with biomass. The exoenzyme-farm is loaded with biomass colonized aerobic microorganisms and enzymes produced by aerobic microorganisms in the exoenzyme-farm are fed into the biogas fermenter via a conduit.
NOVELTY - Purifying contaminated organophosphorus product containing at least one organophosphorus compound and at least one chlorine compound as impurity, comprises (a) providing the contaminated organophosphorus product, (b) completely dissolving the contaminated organophosphorus product in a solvent to obtain a contaminated solution, (c) separating the contaminated solution by a filter and/or a membrane separation unit to obtain a purified solution, and (d) removing the solvent from the purified solution to obtain a purified organophosphorus product.    USE - The method is useful for purifying contaminated organophosphorus product to prepare a catalyst system for hydroformylation, hydrocyanation and hydrogenation of unsaturated compounds (all claimed).    ADVANTAGE - The method purifies contaminated organophosphorus product in environmentally friendly.    DETAILED DESCRIPTION - Purifying contaminated organophosphorus product containing at least one organophosphorus compound and at least one chlorine compound as impurity, comprises (a) providing the contaminated organophosphorus product, (b) completely dissolving the contaminated organophosphorus product in a solvent to obtain a contaminated solution, (c) separating the contaminated solution by a filter and/or a membrane separation unit to obtain a purified solution, (d) removing the solvent from the purified solution to obtain a purified organophosphorus product. The organophosphorus product comprises at least one organophosphorus compound and at least one chlorine compound as impurity. An INDEPENDENT CLAIM is also included for producing a catalyst system containing a metal and at least one organophosphorus compound as a ligand, comprising utilizing the above purified organophosphorus product.
NOVELTY - The invention claims a mobile marsh gas pool, with convenient material discharge and capable of using solar energy. It is composed of a fermentation in size, a fertilizer, a moving hood, a striker plate, a track, a feeding port, an overflow fertilizer, a solar heat collector in a certain volume. Moving the collected sum can be cover makes slag is suitable, there is no incrustation phenomenon, it can fast make the biological garbage local decomposing into gas and fertilizer.
NOVELTY - The utility model claims a fermentation tank, in particular to a laboratory marsh gas fermentation tank. The laboratory marsh gas fermentation tank disclosed in the utility model comprises a tank body, the tank body internal mounting can rotate with the stirring shaft, the stirring shaft fixedly mounted with upper stirring blade, tank body mounted on the upper bracket, the tank body upper part set with waste input mouth, strain input mouth and gas outlet, and the waste input mouth set with may open on the end cover, the outside face of the jar body set with constant temperature device, the strain input mouth on installation with valve. It comprises supplementary strain space-time sum would not from strain input wherein it entering into the marsh gas fermentation tank, can increase raw material and proportion determine strain and marsh gas yield measure of accuracy.
NOVELTY - The utility model relates to a fermentation tank, in particular to a laboratory marsh gas fermentation tank capable of stirring materials fully. The laboratory marsh gas fermentation tank capable of stirring materials fully of the utility model comprises a tank body, wherein inside the tank body internal is mounted with a rotatable stirring shaft; the stirring shaft fixedly mounted with upper stirring blade, tank body mounted on the upper bracket, the tank body upper part set with waste input mouth, strain input mouth and gas outlet, and the above strain input mouth and the input mouth set with excrement can open the end cover, outside face of the jar body set with constant temperature device, end part of said stirring blade is fixedly connected with spring, and length of the spring is larger than distance between end part and the tank body inner surface of the stirring blade. The material in it can full stirring marsh gas fermentation tank, increase raw material and proportion determine strain and marsh gas yield measure of accuracy.
NOVELTY - The new type utility claims have one kind urine sample, it comprises transparent material made of kettle body is marked scale on kettle body at side wall, provided with handle on the kettle body one side, provided with moving cover on the kettle opening of the kettle body at the top part, provided with a dropper on the upper cover, the dropper cap in the kettle cover upper part, a dropper and a dropper top end seal through the kettle cover in the kettle body. Wherein the advantages: special for container can not related substance to avoid influence of light plastic bottle can be directly read total amount urea, rotatable bottle cover not only can ensure not spraying urine leakage, but also prevents odor pollute air; in the dropper bottle for preservative can be pre-stored in inner tube, releasing out after preservative, but also can do stir rod uniformly mixing urine, also can through the head top end left and finally getting the sample, taking the sample process and carrying out in in sealed container, not pollute environment and personnel, patient himself can repeat use, low cost (one-off can), simple and practical, with very high clinical popularization and application value.
NOVELTY - The utility model claims a fermenter for culturing microorganisms solid waste, wherein the fermentation tank is the left side in the cylindrical tube, the tube is sleeved in fixed circular sleeve is transversely set in the cylinder body and the right side respectively set with one of solid material storage groove, and the solid material storage slot of filtration screen one, connected with the solid material storage groove and tube to set with feedstock mouth and sealing cover, the side of fixing sleeve is set with two and three solid material storage groove in operation and wherein the same one vertical section, the utility model is new type that have the agitator blade in stirring when solid material and the loss problem, suitable full contact between the solid material and microorganism, and change solid material suitable, saves time and labour force when, no need to extra culture is finished after the separating operation, basic no affect by continuous production of enterprise, and greatly increase have working efficiency of enterprise culture microorganism.
NOVELTY - An urban and rural homes solitary building sewage treatment facility comprises biogas pool (1), sewage filter composite cyclone water separator (2), biogas discharge pipe (3), biogas pool liquid level controller (4), biogas output pipe (5), truncated cone internal and external rotation water filter cartridge, sewage inlet pipe, rotary device, inner and outer annular cylinder reservoir, discharge pipe, lifting water pump and flushing pipe.    USE - Urban and rural homes solitary building sewage treatment facility.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of urban and rural homes solitary building sewage treatment facility. (Drawing includes non-English language text)    Biogas pool (1)    Sewage filter composite cyclone water separator (2)    Biogas discharge pipe (3)    Biogas pool liquid level controller (4)    Biogas output pipe (5)
NOVELTY - Sewage treatment tank comprises reverse flushing water inlet (6), partition plate, tank body, partition plate support grooves, discharge outlets, embedded strips, sewage inlet pipe (91), treated water outlet pipe (92), processing sections, enzyme solution feeder (601), enzyme solution feed valve, valve switch (603), partition plate recesses, flange stoppers, partition plate receiving groove, sewage treatment devices and guiding inclined plane.    USE - Sewage treatment tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cleaning sewage treatment tank comprising closing sewage inlet pipe and treated water outlet pipe, pulling out embedded strips, opening reverse flushing water inlet and cleaning processing sections and sewage treatment devices.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of sewage treatment tank.    Reverse flushing water inlet (6)    Sewage inlet pipe (91)    Treated water outlet pipe (92)    Enzyme solution feeder (601)    Valve switch (603)
NOVELTY - The method involves preparing biomass gasification and biomass raw material after smashing the biomass gasification reaction furnace and hot chemistry reaction device. Oxygen is introduced to enter into oxidation layer by oxidation reaction. Oxidation product gas is entered into a reducing layer to perform reduction reaction. Carbon dioxide is reduced for containing carbon monoxide. Reducing reaction device is rich in carbon element. Reverse reaction is performed using carbon and water under high temperature status. The reducing device is set to generate high heat value fuel gas.    USE - Method for gasifying biomass raw material.    ADVANTAGE - The reducing reaction is re-participated in furnace. The hydrogen rich, or methane gas is generated. The yield of thermal value is increased.
NOVELTY - The system has a gasification reactor (1) which is set with a fuel gas outlet pipe. A gas-heat source medium heat exchanger (4) is connected with gas outlet pipe and gas burning application device (5). A fume inlet pipe is connected with heat exchanger. A gas-heat source medium inlet is set with heat exchanger low temperature heat source medium pipe. A liquid working substance evaporator heat source medium side inlet pipe (9) is connected with a heat source medium outlet pipe. The gas-heat source medium heat exchanger is connected with a fume-heat source medium heat exchanger (6).    USE - Chemical working substance circulating solid fuel gasification system.    ADVANTAGE - Fuel gasification quadratic energy can be increased. Production of fuel gas can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for chemical working substance circulating solid fuel gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the chemical working substance circulating solid fuel gasification system. (Drawing includes non-English language text)    Gasification reactor (1)    Gas-heat source medium heat exchanger (4)    Gas burning application device (5)    Fume-heat source medium heat exchanger (6)    Liquid working substance evaporator heat source medium side inlet pipe (9)
NOVELTY - Molybdenum disulfide and silver modified silicon nanowire array photochemical hydrogen evolution electrode comprises conductive substrate, composite silicon nanowires and molybdenum disulfide nanoparticles.    USE - Molybdenum disulfide and silver modified silicon nanowire array photochemical hydrogen evolution electrode used for producing hydrogen (claimed).
NOVELTY - Foamed transition metal solid/gas state phosphate self-supporting hydrogen evolution electrode comprises three-dimensional porous electrode, metal foam and transition metal phosphide.    USE - Foamed transition metal solid/gas state phosphate self-supporting hydrogen evolution electrode.    ADVANTAGE - The preparation method is simple, inexpensive and easy to control. The raw materials are easy to obtain.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of foamed transition metal solid/gas state phosphate self-supporting hydrogen evolution electrode comprising removing foamed metal oxide surface layer, sprinkling red phosphorus, adding argon, nitrogen and hydrogen gas, performing phosphating process at 400-700 degrees C for 1-10 hours, cooling to 250 degrees C for 1-10 hours and cooling to room temperature.
NOVELTY - The utility model is new type relates to one kind of reuse water use is applied to scenery marsh system of underground garage, comprising garage is set on top surface of the planting area, wherein the plant cell comprises from outside to inside incline downward and gradient, between the end connected with scenery marsh pool, planting area and scenery marsh pool set with overflow water wall, planting area from upper to lower comprising planting layer and water resistance of layer, the scenery marsh pool in form floating water plant cell, plant cell and aquatic water biology cell, inner bottom of scenery marsh pool in turn form filtering layer and impounding reservoir, water pool set with water pump and out water tube. The utility model is new type landscape with rain and sewage collecting, processing and using, small area realize green use from supplied water and from the balance, ecological and environment-friendly.
NOVELTY - The new type utility claims have one kind Anaerobic reactor, comprising container main body, is equipped with container main body bottom is water inlet water distribution system and equipped with three phase separator container at the top part of the container main body water inlet water distribution system and are between three phase separator is also set with can for containing sewage sludge by the sludge treatment bed section, a sludge bed section bottom to top along the direction of bypass is equipped with container main body internal to form cloth water gallery channel, bottom sludge containing sewage by the water inlet water distribution system entering into container main body, and down return flow sludge bed section forming the cloth corridor, at last through three phase separator separate. By said embodiment, it can realize uniform cloth water, sewage processing optimizing condition so as to increase sewage treatment efficiency, and can make three phase separator with good operation stability.
NOVELTY - A plant automatic shaping machine, wherein, comprising pillar, beam, carrying on cloth roller, cloth out roller, the shaping system, the automatic shaping machine using design of carding, carding and prior to comb hair by cutter for finishing fabric start, for removing impurities and finish fabric part, which is good for increase of follow-up effect, increase working efficiency, the automatic shaping machine using design of gluing device, through extrusion roller for fabric surface by extrusion, which is good for increase spraying effect, through the fabric surface by spraying shower nozzle, which is good for uniform distribution of medicament increase, increase working efficiency, the automatic shaping machine using design and steaming device, through steam shaping roller and the fabric is, the device is not only energy saving and environment-friendly, and shaping effect, which is good for increase work efficiency and saves cost.
NOVELTY - Method for purifying river water contaminated with sewage-treatment water, involves adding fermentation culture liquid to sewage-treatment water, performing fermentation, adding enzyme, acid and bioactive substance, continuing fermentation, collecting treated water, mixing the treated water with natural river water, preventing mixture from oxidation and putrefaction, contacting the mixture with air and airborne bacteria, and purifying mixture.    USE - The method is useful for purifying river water contaminated with sewage-treatment water (claimed).    ADVANTAGE - The method improves water quality, and controls offensive odor.    DETAILED DESCRIPTION - Method for purifying river water contaminated with sewage-treatment water, involves adding specific quantity of fermentation culture liquid to sewage-treatment water, performing fermentation in which antagonism of natural microbe is suppressed and symbiosis effect of cultured microorganisms is increased, adding enzyme, acid and bioactive substance, continuing fermentation, collecting treated water, mixing the treated water with natural river water, allowing mixture to flows through a certain distance, preventing mixture from oxidation and putrefaction by providing waterfall of fixed height, contacting the mixture with air and airborne bacteria to remove contaminants, and purifying mixture by providing several waterfalls of fixed height installed several places.
NOVELTY - An emulsifying mixture comprises mono- or diglycerides of long chain fatty acids (A) in admixture with glycol esters or glycerides of long chain fatty acids, and salt of long chain fatty acid with amine compound (B). The weight ratio of components (A) and (B) is 65:35-80:20.    USE - Emulsifying mixture is used for preparing fuel emulsion (all claimed) used for internal combustion device such as electrical motor generator.    ADVANTAGE - The emulsifying mixture provides stable fuel emulsion. The generator using the fuel emulsion release reduced amount of particulates and greenhouse gases.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of emulsifying mixture, which involves preparing component (A) by partial transesterification of vegetable oil with glycol or glycerin, preparing component (B) by salification reaction of long chain fatty acid with amine compound, and mixing components (A) and (B);    (2) fuel emulsion, which comprises the emulsifying mixture; and    (3) preparation of fuel emulsion, which involves fast stirring emulsion mixture at 2000-6000 rpm in container.
NOVELTY - Manufacture of bicyclic compound (I) involves reacting cis-2,5-bis(hydroxymethyl)tetrahydrofuran with at least one amine (II) in a liquid reaction medium and in presence of catalytic system. The catalytic system is chosen from homogeneous catalyst which is complex comprising iridium and/or ruthenium, and at least one donor ligand (H1) and heterogeneous catalyst (H2) comprising at least one group 8-11 transition metal element and one poor metal element.    USE - Manufacture of bicyclic compound used in drugs and clinical applications.    ADVANTAGE - The method enables economical, efficient and environmentally-friendly manufacture of bicyclic compound with high yield.    DETAILED DESCRIPTION - Manufacture of bicyclic compound of formula (I) involves reacting cis-2,5-bis(hydroxymethyl)tetrahydrofuran with at least one amine of formula: NH2R' (II), in a liquid reaction medium and in presence of catalytic system. The catalytic system is chosen from homogeneous catalyst which is complex comprising iridium and/or ruthenium, and at least one donor ligand (H1) and heterogeneous catalyst (H2) comprising at least one group 8-11 transition metal element and one poor metal element.    R,R'=H or 1-36C hydrocarbyl.
NOVELTY - Reducing or preventing damage to a wood containing substrate, comprises: applying to a surface of the substrate a first solution comprising a water soluble quinone compound to form a wetted substrate, such that the water soluble quinone compound penetrates beneath the surface of the substrate; and converting the water-soluble quinone compound to a water insoluble quinone compound or its derivative.    USE - The method is useful: for reducing or preventing damage to a wood containing substrate, where the damage is caused by birds, termites or fungi and the wood containing substrate is a power pole, telephone pole, dimensional lumber, pressure treated lumber, piling, shingles, siding or other building materials; and for protecting building materials by repelling birds (all claimed). Test details are described but no results given.    ADVANTAGE - The method: utilizes the water-soluble quinone compound, which penetrates at least 0.5 mm beneath the surface of the substrate (claimed); provides more environmentally friendly treatment of wood containing and some non wood containing materials by using quinone compounds for reducing or preventing damage.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a cellulosic based substrate comprising a water insoluble quinone compound, where the water insoluble quinone compound is at least 1 mm beneath the surface of the substrate; and    (2) a building material comprising 0.1-10 wt.% of a bird repellent compound.
NOVELTY - The utility model is new type and new type immobilized microorganism reactor and sewage treatment system, including one for buried reaction pool and a control room equipment, equipment control room is inside set with underground drainage pump, a variable frequency air pressure tank and variable-frequency control cabinet, a vertical provided with one clapboard reaction pool in, and clapboard is divide into the first space and the second space, the reaction pool top part set with air outlet provided with the cover plate, the first lower space part side edge provided with water inlet pipe and gas distribution pipe, and the first space part provided with porous soft filler, under the second space part outside set with water out pipe, between out water pipe and baffle plate set with non-polar porous microorganism filter, the water inlet pipe and drain pipe connected with underground, water out pipe water drainage pump and one end connected with the drainage pump another terminal and frequency conversion air tank and water using terminal connected with the variable-frequency control cabinet respectively and drainage pump and variable-frequency air pressure tank connected with power. Porous soft filler and inorganic porous microorganism using sludge by biological filter material layer, the absorbing microorganism degradation effect, make the water outlet water quality active increase.
NOVELTY - The new type utility claims have one kind household garbage comprehensive processing system, comprising in turn connected with the marsh gas generating pool, biological aeration pool, sediment pool, marsh gas generating pool divided solid area and liquid cell, solid area between liquid area and equipped with filter screen, a marsh gas generating pool the top set with biogas sum collected pipe sum, sum sum collected pipe and marsh gas power generation unit connected with the liquid area by pipe and biological aeration pool connected with, respectively equipped with biological filter material in the biological aeration pool divided Anaerobic area and aerobic area, Anaerobic area and aerobic area, area liquid is waste water from above downward by Anaerobic cell enter into biological aeration pool, then the following from bottom upwards enter into sediment pool, biological aeration pool by aerobic area after part set with aeration pipe. The utility model is new type especially aiming at domestic cell design, can effective and resource use of domestic garbage and biomass, and waste water to carry out processing. Square meter small floor space, low investment, operation cost is low, technology stable reliability, operation and management relative simple technology.
NOVELTY - The utility model claims a fermentation tank, comprising a tank body, a transmission device and stirring device set in the tank body and inside, the stirring device of stirrer and stirring shaft make up, the stirring shaft use double end surface machine seal, shaft end of the transmission device and the stirring shaft between set has three division type shaft joint, on the stirring shaft fixedly set with placing ring below the placing ring set with bearing base, the bearing base fixed on the tank body, the stirring shaft set up with three pull rod hanging shaft, the three pull rod hanging shaft and three pulling pole fixed on one upper sealing head of the fermentation tank to. The utility model adopts double end surface machine seal and three division type shaft coupling, sealing effect is good, not easy to wear, suitable have service, at the same time using three pull rod hanging shaft, reducing have pollute, increase have product quality.
NOVELTY - The method involves sending nitrifying sludge and denitrifying sludge to a bioreactor (1) with a film separating component. The nitration reaction of nitrifying sludge in interior region of membrane separation module is carried out. The denitrification of denitrification sludge in outer region of membrane separation module is carried out. The ammonia wastewater is passed into interior region of membrane separation module, and an aeration system is used to perform back-mixing. A membrane is used for separating outer area of component, and the external outflow is passed via an outlet.    USE - Method for performing synchronous nitrification and denitrification treatment of ammonia containing waste water.    ADVANTAGE - The interference of nitration sludge and denitrifying sludge is prevented, and increased synchronous nitration and de-nitrification efficiency is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the device for performing synchronous nitrification and denitrification treatment of ammonia containing waste water.    Bioreactor (1)    Film separating module (2)    Nitrification area (3)    Aeration system (5)    Water inlet (7)
NOVELTY - Preparation of sofosbuvir (I), comprises: (a) reacting phenyloxy-phosphodichloridate (VII) with substituted N-containing heterocyclic compound (VI) to obtain substituted N-containing heterocyclic phenyl-1-ylphosphonochloridate (V); (b) reacting (V) with (S)-2-amino-propionic acid isopropyl ester (IV) to produce phenyl phosphordiamidates (III); and (c) reacting (III) with 1-((2R,3R,4R,5R)-3-fluoro-4-hydroxy-5-hydroxymethyl-3-methyl-tetrahydro-furan-2-yl)-1H-pyrimidine-2,4-dione (II) to obtain (I).    USE - The method is useful for preparing sofosbuvir (claimed), which is useful for treating hepatitis C. No biological data given.    ADVANTAGE - The method is simple, cost-effective, eco-friendly and commercially viable.    DETAILED DESCRIPTION - Preparation of sofosbuvir of formula (I), comprises: (a) reacting phenyloxy-phosphodichloridate of formula (VII) with nitrogen containing heterocyclic compound of formula (VI) to obtain nitrogen containing heterocyclic phenyl-1-ylphosphonochloridate of formula (V); (b) reacting (V) with (S)-2-amino-propionic acid isopropyl ester (IV) to produce phenyl phosphordiamidates of formula (III); and (c) reacting (III) with 1-((2R,3R,4R,5R)-3-fluoro-4-hydroxy-5-hydroxymethyl-3-methyl-tetrahydro-furan-2-yl)-1H-pyrimidine-2,4-dione of formula (II) to obtain (I).    X = S or O; and    R, R1 = aryl (optionally substituted) H, or 1-6C alkyl.
NOVELTY - Catalyst comprises aluminum modified mesoporous molecular sieve and is selected from oxides of cerium, cobalt, iron and manganese. The aluminum modified oxide source is trivalent aluminum or aluminate. The aluminum modified mesoporous molecule sieve carrier is dipped in metal nitrate in ethanol solution and stirred for 12 hours. The solution is distilled by a rotary evaporator to dryness and calcined under an air atmosphere at 550 degrees C for 6 hours. The metal loading amount is 5 wt.% and the metal is selected from cerium, cobalt, iron or manganese.    USE - Catalyst used for dechlorinating methane chloride.    ADVANTAGE - The catalyst has high carbon dioxide activity and selectivity, efficiency of 56-100%, good selectivity in a temperature range of the experiment and purifies nitrogen oxide at 400-550 degrees C.
NOVELTY - Organic liquid fertilizer comprises 10-20 wt.% oil meal, 8-10 wt.% amino acid, 3-5 wt.% microorganism, 6-8 wt.% trace element, 5-7 wt.% activator and 25-45 wt.% water.    USE - Organic liquid fertilizer.    ADVANTAGE - The green fertilizer is pollution-free, enhances crop nutrition, increases stress resistance, increases crop quality, increases crop yield, reduces 10-30 wt.% nitrate content, and prolongs storage period.
NOVELTY - An efficient eco-packing biological carrier water purification method comprises setting carrier, carrying out fractional or microorganism culture, propagating microorganism via high active biological film, placing carrier in biochemical pool, forming fluidization bed biological film, and putting specific sensor to obtain fluidized bed biofilm sensor.    USE - Efficient eco-packing biological carrier water purification method (claimed).    ADVANTAGE - The method inhibits toxic refractory material and substances, enhances system to load, inhibits pH and temperature tolerance, reduces excess sludge production, and has simultaneous nitrification and denitrification processes.
NOVELTY - The device has extractive distillation column (3) whose top portion is provided with first outlet, and bottom portion is provided with a second outlet. The upper portion of the flash column (15) is provided with a flash column import material. The top portion of flash column is provided with first outlet, and bottom portion is provided with a second outlet. The second outlet of extractive distillation column is connected to flash column import material of flash column. The flash column extraction agent of flash column is connected to the second out let of extractive distillation column.    USE - Device for separating propylene and propane.    ADVANTAGE - The device structure is simplified, so that the cost of the device is reduced. The excellent separation effect and the high product purity are achieved. The energy consumption in the manufacturing process is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for separating of propylene and propane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for separating propylene and propane.    Extractive distillation column (3)    Extractive distillation column overhead reflux line (7)    Propane product discharge line (8)    Flash column (15)    Extracting agent mixer (21)
NOVELTY - Performing anaerobic sludge fermentation involves mixing sludge with ferric salt, and then adding sodium sulfide in closed reactor.    USE - Method for performing anaerobic sludge fermentation used for improving release rate of phosphorus (all claimed).    ADVANTAGE - The method is easy, and has good operability and controllability.
NOVELTY - Food packaging film comprises 80-90 pts. wt. concentrated whey protein powder, 50-60 pts. wt. sodium carboxymethyl cellulose, 30-35 pts. wt. hydroxypropyl methylcellulose, 20-25 pts. wt. rhizoma coptidis, 15-20 pts. wt. rosemary, 15-18 pts. wt. rapeseed oil, 12-15 pts. wt. wheat gluten, 12-15 pts. wt. low methoxyl pectin, 10-12 pts. wt. konjak glucomannan, 8-10 pts. wt. calcium citrate, 8-10 pts. wt. sucrose ester, 6-9 pts. wt. edible gelatin, 5-8 pts. wt. butylhydroxyanisole, 5-8 pts. wt. stearic acid, 3-5 pts. wt. beeswax, 3-5 pts. wt. genipin and 1500-1800 pts. wt. water.    USE - Food packaging film.    ADVANTAGE - The food packaging film is environment-friendly, and has strong physical and mechanical performance, and antibiosis and antioxidant properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing food packaging film, which involves:    (A) dissolving whey protein powder in water at 60-80 degrees C for 25-35 minutes;    (B) cooling the dissolved material to 40-50 degrees c and then adding the cooled material with proper amount of enzyme to obtain enzymolysis liquid;    (C) adding the obtained liquid with rhizoma coptidis and rosemary and 5 times water into a extraction tank and then heating the obtained material for 35 minutes after soaking for 30-35 minutes;    (D) extracting, cooling and filtering to obtain rhizoma coptidis and rosemary extract liquid and then mixing the extracted material with sodium carboxymethyl cellulose, hydroxypropylmethyl cellulose, enzymolysis liquid of whey protein, rapeseed oil and wheat gluten at 50-60 degrees C for 20-25 minutes;    (E) adding the mixed material with rest components and then stirring the obtained material at a rotating speed of 3500-4000 revolutions per minute for 10-15 minutes; and    (F) drying the stirred material for 12-15 hours to obtain the desired product.
NOVELTY - The method involves performing crushing materials through a crushing mechanism comprising blade group (3). The material is crushed and extruded to a baffle plate (8). The material is extruded through variable pitch screw rod. The material volume is compressed and expanded. The material is separated using cyclone separating device. The material is decomposed, and hemicelluloses and lignin are separated. The lignin is separated using action of biological enzyme, and is passed into a solid collecting device. The cellulose solution and water are discharged into liquid collecting device.    USE - Method for using agriculture and forestry waste to produce energy materials.    ADVANTAGE - The pollution caused by agriculture and forestry waste is reduced, and the operation safety is ensured.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the material decomposing and separating device.    L-shaped cylinder (1)    Blade group (3)    Hopper (4)    Hammering device (5)    Baffle plate (8)
NOVELTY - Seasonal cultivation of wild edible fungus comprises pre-wet stacking, mixing, packaging, sterilizing, cooling, inoculating, culturing, cooking, adding to soil, fruiting, and harvesting.    USE - Method for seasonal cultivation of wild edible fungus (claimed).    ADVANTAGE - The method reduces pollution rate.
NOVELTY - A manganese-containing soil-less culture medium comprises 100-200 pts. wt. animal urine, 250-400 pts. wt. crop straw, 100-500 pts. wt. agricultural and industrial by-products, 0.05-0.1 pt. wt. inorganic manganese, and 400-1000 pts. wt. sand.    USE - Manganese-containing soil-less culture medium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of manganese-containing soil-less culture medium comprising crushing crop straw, adding animal urine, agricultural and industrial by-products and inorganic manganese, mixing, fermenting to 28-35 degrees C, turning once every 12 hours, continuously fermenting for 14-21 days to obtain decomposed organic matter, and mixing with sand.
NOVELTY - Cultivation substrate comprises 100-200 pts. wt. animal urine, 250-400 pts. wt. crop straw, 100-500 pts. wt. industrial and agricultural by-products, 0.05-0.1 pts. wt. inorganic magnesium and 400-1000 pts. wt. machine-made sand.    USE - Used as cultivation substrate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing comprising cultivation substrate, comprising (i) crushing crop straw to a length of 0.5-2 cm, and uniformly mixing animal urine, industrial and agricultural by-product, inorganic magnesium, to obtain base material, fermenting the base material at 28-35 degrees C, stirring once in every 12 hours, and terminating the fermentation process after 14-21 days, to obtain decomposed organic matter; and (ii) uniformly mixing the decomposed organic matter with water, to obtain the final product.
NOVELTY - An iron-containing soil-less culture medium comprises 100-200 pts. wt. animal urine, 250-400 pts. wt. crop straw, 100-500 pts. wt. agricultural and industrial by-products, 0.05-0.1 pt. wt. inorganic iron, and 400-1000 pts. wt. sand.    USE - Iron-containing soil-less culture medium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of iron-containing soil-less culture medium comprising crushing crop straw, adding animal urine, agricultural and industrial by-products and inorganic iron, mixing, fermenting to 28-35 degrees C, turning once every 12 hours, continuously fermenting for 14-21 days to obtain decomposed organic matter, and mixing with sand.
NOVELTY - Cultivation of water flea involves placing water fleas in culture medium, feeding with treated sewage sludge nutrient solution, and placing beneficial microorganism in culture tank.    USE - Method for cultivating water flea used for ecological restoration.    ADVANTAGE - The method is environmental-friendly.
NOVELTY - Preparation method of radix fici hirtae extract involves adding 10-40 times ethanol (60-100%) to radix fici hirtae, extracting mixture by ultrasonic assisted extraction at 40-60 degrees C and ultrasonic frequency of 30-40 KHz for 30-150 minutes, filtering extract and recovering ethanol, and concentrating recovered product.    USE - The method is useful for preparing radix fici hirtae extract, which is useful for preventing and controlling pathogens preferably Penicillium italicum, P.digitatum, Geotrichum candidum and Alternaria citri in orange, and preparing medicinal composition, and as preservative agent for orange (claimed).    ADVANTAGE - The method prepares radix fici hirtae extract which leaves no residue, is environmentally-friendly, and delays drug resistance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) radix fici hirtae extract;    (2) medicinal composition comprising radix fici hirtae extract; and    (3) preservative agent for orange.
NOVELTY - The system has a fixing device for fixing a to-be- administered object. An administration device is utilized for administering drip medicine in a breathing tube. An anesthesia device is provided with a remote controlled trolley that is provided with a carrier. The remote controlled trolley is utilized for carrying the to-be- administered object. A remote controller is utilized for controlling the remote controlled trolley. A cabin is connected with a vacuum device. A worktable is vertically fixed with a table-board. The fixing device is provided with a clamp holder.    USE - Respiratory tract quick suction pipe drip administration system.    ADVANTAGE - The system is non-invasive, inexpensive, convenient to operate and environment-friendly. The system has high working efficiency. The system establishes various diseases models.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a respiratory tract quick suction pipe drip administration method.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a quick suction pipe drip administration system.
NOVELTY - The preparation method of high protein content of cerebroprotein hydrolyzate involves taking tissue homogenate and then liquefying, adding protein to the liquefied tissue homogenate, uniformly mixing, concentrating the mixture, adding pepsin to the mixture and then enzymolyzing, adding trypsin to the mixture and then enzymolyzing, ultrafiltering the mixture, and concentrating using temperature-sensitive polyacrylamide gel.    USE - The method is useful for preparation of high protein content of cerebroprotein hydrolyzate (claimed).    ADVANTAGE - The method enables preparation of cerebroprotein hydrolyzate with high protein content of more than 88 in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for high protein content of cerebroprotein hydrolyzate prepared by the method.
NOVELTY - Fertilizer comprises 30-40 pts. wt. rice straw stick, 30-40 pts. wt. rice corn, 40-50 pts. wt. grass, 20-30 pts. wt. starch, 15-20 pts. wt. sugar, 1-5 pts. wt. humic acid, 5-15 pts. wt. quicklime, 2-3 pts. wt. sodium chloride, 3-5 pts. wt. manganese chloride, 5-7 pts. wt. zinc sulfate, 2-4 pts. wt. potassium iodide and 5-10 pts. wt. ethephon.    USE - Fertilizer used for maturing apple (claimed).    ADVANTAGE - The fertilizer is prepared in a simple, cost-effective and eco-friendly manner, and accelerates flowering and fruit growth of apple.
NOVELTY - Biological fertilizer comprises 40-60 wt.% charcoal powder, 5-10 wt.% montmorillonite powder, 5-20 wt.% humic acid, 20-25 wt.% organic matter and 5-10 wt.% microorganism strain.    USE - Biological fertilizer used for preventing and treating soil compaction (claimed).    ADVANTAGE - The biological fertilizer improves physical and chemical properties of soil, increases cation exchange quantity and soil organic matter, and reduces carbon dioxide release amount.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological fertilizer, which involves:    (A) chopping corn straw or waste wood into parts and performing carbonization;    (B) sprinkling montmorillonite on surface on moist part of montmorillonite and cooling to room temperature; and    (C) adding remaining components with the product, and then pulverizing it, and activating and vaporizing into furnace to obtain final product.
NOVELTY - Soilless cultivation matrix comprises 100-200 pts. wt. animal urine, 250-400 pts. wt., crop straw, 100-500 pts. wt. industrial and agricultural by-products, 0.1-0.5 pts. wt. silicon dioxide and 400-1000 pts. wt. sand.    USE - Soilless cultivation matrix used for plant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soilless cultivation matrix, which involves:    (A) crushing crop straw to obtain particle with size of 0.5-2 cm, and then mixing uniformly animal urine, industrial and agricultural by-products and silicon dioxide; and    (B) performing fermentation of the mixture at 28-35 degrees C for 14-21 days to obtain rotten organic, and then mixing 400-1000 parts decomposed organic product.
NOVELTY - Eco-friendly bio-organic fertilizer comprises 45-65 pts. wt. animal manure, 20-40 pts. wt. edible fungus residue, 8-15 pts. wt. humic acid, 5-15 pts. wt. lard residue, 0.05-0.1 pts. wt. leavening agent strain, 0.5-1.5 pts. wt. zinc sulfate, 0.2-0.6 pts. wt. boric acid and 1.0-2.0 pts. wt. ferrous sulfate.    USE - Eco-friendly fertilizer.    ADVANTAGE - The eco-friendly fertilizer is recycled and harmless.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing eco-friendly fertilizer, which involves:    (A) mixing raw materials and processing to obtain nutrient solution    (B) adding water with the nutrient solution in a reactor to maintain carbon nitrogen and oxygen level in ratio of 25:1-30:1, and pH value at 6.5-8.5;    (C) fermenting the nutrient solution by adding leavening agent strain at 50-60 degrees C for 2-7 days and drying; and    (D) granulating the dried product, cooling it, drying, sieving, transporting through machine, and then packaging and storing.
NOVELTY - Bio-organic fertilizer comprises 25-35 wt.% grain, 15-25 wt.% traditional Chinese medicinal residue, 35-45 wt.% chicken manure, 4-6 wt.% mineral powder, 0.01-0.03 wt.% microorganism microbial inoculum I type, 10-20 wt.% conditioning agent and 0.1-5 wt.% microorganism microbial inoculum II type.    USE - Bio-organic fertilizer used for planting tea (claimed).    ADVANTAGE - The bio-organic fertilizer is eco-friendly and cost-effective, improve yield and quality of tea, and soil structure, and provides comprehensive nutrition to tea.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) mixing grain with chicken manure in ratio of 10:1;    (B) covering layer grain in material surface and piling for 2-3 days for harmless treatment of material;    (C) adding 5-20% sodium bicarbonate, humic acid and mineral powder in the mixture and stirring for 12- 24 hours and mixing microorganism microbial inoculum I type to carry out fermentation to maintain pH value at 6.5-7.5;    (D) adding remaining components with microorganism microbial inoculum II type to carry out fermentation; and    (E) mixing both products uniformly, and then packaging.
NOVELTY - Organic foliar fertilizer comprises wood vinegar powder, water mixed clove and rhizoma acori graminei, sunflower cake, egg shell powder, phosphorus pentoxide, wheat bran, deionized water and polyglutamic acid powder.    USE - Organic foliar fertilizer.    ADVANTAGE - The organic foliar fertilizer ensures purification of indoor air.
NOVELTY - Organic soilless cultivation matrix comprises 100-200 animal urine, 250-400 crop straw, 100-500 industrial and agricultural by-products, 0.05-0.1 acid salt and 400-1000 sand.    USE - Organic soilless cultivation matrix.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic soilless cultivation matrix, which involves:    (A) crushing crop straw to obtain particle with size of 0.5-2 cm, and then mixing uniformly animal urine, industrial and agricultural by-products and acid salt; and    (B) performing fermentation of the mixture at 28-35 degrees C for 14-21 days, and then mixing 400-1000 parts organic molybdenum.
NOVELTY - Soilless cultivation matrix comprises 100-200 pts. wt. animal urine, 250-400 pts. wt. crop straw, 100-500 pts. wt. industrial and agricultural by-products, 0.05-0.1 pts. wt. inorganic zinc and 400-1000 pts. wt. sand.    USE - Soilless cultivation matrix used for plant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soilless cultivation matrix, which involves:    (A) crushing crop straw to obtain particle with size of 0.5-2 cm, and then mixing uniformly animal urine, industrial and agricultural by-products and acid salt; and    (B) performing fermentation of the mixture at 28-35 degrees C for 14-21 days to obtain rotten organic, and then mixing 400-1000 parts decomposed organic product.
NOVELTY - Soilless cultivation matrix comprises 100-200 pts. wt. animal urine, 250-400 pts. wt., crop straw, 100-500 pts. wt. industrial and agricultural by-products, 0.05 pts. wt. inorganic boron and 400-1000 pts. wt. sand.    USE - Soilless cultivation matrix used for plant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soilless cultivation matrix, which involves:    (A) crushing crop straw to obtain particle with size of 0.5-2 cm, and then mixing uniformly animal urine, industrial and agricultural by-products and inorganic boron; and    (B) performing fermentation of the mixture at 28-35 degrees C for 14-21 days to obtain rotten organic, and then mixing 400-1000 parts decomposed organic product.
NOVELTY - Preparing organic fertilizer involves utilizing molasses waste liquid, lime, fly ash, filter mud and bagasse pulp. The raw materials are mixed and spraying molasses alcohol waste liquid. The mixture is granulated through a granulating machine, and then dried at 600-800 degrees C by using a drier. The dried product is packaged.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer in a simple, eco-friendly and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for preparing organic fertilizer, which involves hopper, a transmission belt, granulator, drier and sieving machine.
NOVELTY - Eco-friendly fertilizer comprises 30-40 pts. wt. pine bark, 25-40 pts. wt. potassium sulfate, 5-10 pts. wt. urea, 5-10 pts. wt. humic acid, 5-10 pts. wt. mineral clay, 5-10 pts. wt. sulfate balancing agent, 3-5 pts. wt. fermentation auxiliary agent obtained from tree bark and 1-5 pts. wt. accelerant. Sulfate balancing agent is a mixture of maifanite stone and limestone in ratio of 2-4:1. Accelerator is selected from citric acid, malic acid, acetic acid or polylactic acid.    USE - Eco-friendly fertilizer used for plant (claimed).    ADVANTAGE - The Eco-friendly fertilizer ensures quick effect, avoids loss of large amount of fertilizer in soil, increases crop stress resistance capacity of plant, enhances microorganism activity and organic content in the soil, and is safe and non-toxic for human and livestock.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing co-friendly fertilizer, which involves:    (A) crushing pine bark with a pulverizer to obtain powder having particle diameter 1-5 cm, and then adding urea, bark fermentation auxiliary agent and humic acid;    (B) adding pH regulator in the mixture to regulate pH value at 5-5.5, and fermenting at 45-50 degrees C for 2-3 days;    (C) adding remaining components with the fermented product and fermenting for 5-8 days; and    (D) drying the fermentation product, and then mixing uniformly sulfate balancing agent.
NOVELTY - The system has a feedstock tube (10) and a discharge tube (20,22,42) which are inserted into end sides of U-type fermentation pipe (30). A blocking plate is arranged in side wall of feeding/discharging pipe. A one end side of water pipe is connected with water pressure valve and another end side is connected with cloth bacteria pipeline. The discharging water pipe is provided with water pressure control valve for discharging biogas liquid into feedstock tube. The cloth bacteria device (50) is connected in a position higher than discharge pipe at lowest point.    USE - Anaerobic fermentation system.    ADVANTAGE - The uniform strain distribution is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of anaerobic fermentation system.    Feedstock tube (10)    Discharge tube (20,22,42)    U-type fermentation pipe (30)    Hydraulic portion (40)    Cloth bacteria device (50)
NOVELTY - The method involves pouring fermentation raw material into U-type fermentation pipe (30) via feedstock tube (10) to produce marsh gas. The marsh gas is collected in the space between sidewalls of feedstock pipe and discharging pipe (20). The marsh gas occupied inside the space is flowed into the water pressure chamber (40) through feedstock pipe and discharge pipe. The pressure of marsh gas in fermentation pipe is reduced, so that slurry stored in chamber flows back into fermentation pipe through feedstock and discharge pipes. The slurry is circulated using drain pipe.    USE - Method of generating marsh gas using U-shaped super efficient anaerobic fermentation device.    ADVANTAGE - The marsh gas fermentation efficiency is improved. The fermentation route is short. The biogas convection effect is enhanced. The uneven distribution of strain inside the fermentation device is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic fermentation device.    Feedstock tube (10)    Discharging pipe (20)    U-type fermentation pipe (30)    Air guide pipe (32)    Water pressure chamber (40)
NOVELTY - The fermentation method of biogas using attapulgite, crop straw and manure involves taking crop straw and manure and then crushing, adding sodium hydroxide to the crushed particles, pretreating the mixture to obtain crop straw residues, adding attapulgite to the crop straw residues and then stirring to obtain a mixed material, placing the mixed material in a digestion device and then stirring, inoculating fermented materials and then adjusting pH value to 6.5-7.5, sealing the digestion device and then reacting at 25-35 degrees C for 1-2 days, and fermenting for 30-40 days.    USE - The method is useful for fermentation of biogas using attapulgite, crop straw and manure (claimed).    ADVANTAGE - The method enables fermentation of biogas with excellent methane fermentation efficiency.    DETAILED DESCRIPTION - The fermentation method of biogas using attapulgite, crop straw and manure involves taking crop straw and manure and then crushing, adding 4-6 %mass sodium hydroxide to the crushed particles, uniformly mixing, pretreating the mixture to obtain crop straw residues, adding attapulgite to the crop straw residues and then stirring under carbon and nitrogen atmosphere in ratio of 20-30:1 to obtain a mixed material, placing the mixed material in a digestion device and then uniformly stirring, inoculating 10-20 wt.% fermented materials and then adjusting pH value to 6.5-7.5, sealing the digestion device and then reacting at 25-35 degrees C for 1-2 days, and fermenting for 30-40 days.
NOVELTY - The improved alkali method for pre-processing lignocellulosic biomass involves adding lignocellulosic biomass to traditional Chinese medicine liquid mixture, uniformly mixing, stirring the mixture at 60-170 degrees C under a pressure of 0-0.8 MPa and then pre-processing, separating black liquid, and sulfonating. The traditional Chinese medicine liquid mixture contains 0.5-8 %mass lignosulfonates, 2-15 %mass alkaline reagents and/or and 0.01-0.5 %mass oxidizing agent.    USE - The improved alkali method is useful for pre-processing lignocellulosic biomass (claimed).    ADVANTAGE - The improved alkali method is capable of pre-processing lignocellulosic biomass with high quality, and excellent conversion and utilization rate in a simple and an economical manner.
NOVELTY - The preparation method of peptone using enzymatically decomposed earthworm powder involves adding earthworm powder to Soxhlet extraction system and then extracting, adding petroleum ether to the system, uniformly mixing, extracting the mixture and then washing, degreasing the mixture and then ventilating, drying the mixture, adding citric acid and sodium citrate buffer to the mixture and then stirring, heating the mixture, adding trypsin solution to the mixture and then enzymolyzing, centrifuging the mixture, and drying under reduced pressure.    USE - The method is useful for preparation of peptone, which is useful as microbial culture (claimed) for culturing Escherichia coli and lactic acid bacteria.    ADVANTAGE - The method enables simple preparation of peptone with high efficiency in an environmentally-friendly manner.    DETAILED DESCRIPTION - The preparation method of peptone using enzymatically decomposed earthworm powder involves adding earthworm powder to Soxhlet extraction system and then extracting at 45-55 degrees C, adding petroleum ether to the extraction system, uniformly mixing, extracting the mixture for 25-30 minutes and then washing using petroleum ether for 25-30 minutes, degreasing the mixture and then ventilating, drying the mixture to obtain a skimmed earthworm powder, adding citric acid and sodium citrate buffer to the skimmed earthworm powder and then adjusting pH value to 4-8, stirring the mixture and then heating at 40-80 degrees C, adding 2-5 wt.% trypsin solution to the mixture and then enzymolyzing at 90-100 degrees C for 1-4 hours, centrifuging the mixture for 15-20 minutes to obtain a supernatant and then adjusting pH value to 5.5-7.5, and drying under reduced pressure. The earthworm powder, citric acid and sodium citrate buffer are used in a ratio of 5-25 g/100 ml. An INDEPENDENT CLAIM is included for use of peptone for microbial culture.
NOVELTY - The new type utility claims have a a sewage processing device, a sewage collecting tank and sewage treatment pool, a sewage collecting tank provided with a water inlet pipe, a sewage processing pool in a partition wall forming the purification pool and , a drain pipe between sewage collecting tank and a purification pool, a drain pipe installation height of the water inlet pipe is lower than the mounting height, cover soil layer on the upper layer a internal purification pool, a pipe connected between a purification pool and . The utility model is new type using soil layer and a upper part as a purification and planting wetland plant, sewage and lower part for carrying out biochemical degradation process, with obvious and sewage purification effect, saves the land a square meter, green square meter advantageously increase environment protection, sewage by a product of the water available for farmland irrigation or spray, and can save water resource, and it is widely suitable for rural area.
NOVELTY - A recombinant vector comprising inducible promoter induced under condition in which ammonium is not present or nitrate is present, and glyceraldehyde-3-phosphate dehydrogenase (GAPDH) protein coding gene under the promoter, is new.    USE - The recombinant vector is useful for producing transgenic algae which is useful for producing lipid, and preparing biodiesel (all claimed).    ADVANTAGE - The recombinant vector improves biomass and lipogenesis of the microalgae as compared to the existing wild-type algae.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of producing transgenic algae;    (2) transgenic algae obtained by the above-mentioned method;    (3) composition for increasing biomass of the microalgae;    (4) method for producing lipid; and    (5) method for preparing biodiesel.
NOVELTY - Conversion of kitchen waste into liquid organic fertilizer comprises passing kitchen waste by stainless steel sieve plate, separating solid and liquid to get solid components and liquid components; passing liquid components by oil water separator; adjusting pH to 2-4 using concentrated acid to kill pathogenic fungus; adding acid-microorganism fermentation microbial inoculum and auxiliary organic nutrient substance, aerobic fermenting to get organic liquid fertilizer concentrate; and diluting organic liquid fertilizer, cultivating green vegetables and fruits, and curing garden soil.    USE - Method for converting kitchen waste into liquid organic fertilizer (claimed).
NOVELTY - Chinese chestnut growth prompting basal fertilizer comprises 60-80 pts. cattle manure, 20-30 pts. sheep manure, 20-30 pts. pig manure, 0.05-0.1 pts. sulfur-based complex fertilizer, 0.05-0.1 pts. diammonium phosphate, 0.05-0.1 pts. urea, 1-2 pts. calcium superphosphate and 0.001-0.002 pts. borax.    USE - Used as Chinese chestnut growth prompting basal fertilizer.    ADVANTAGE - The fertilizer provides sufficient nutrients to chestnut trees and lays a solid foundation for next year harvest.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing basal fertilizer, comprising: (i) carrying out compact stacking fermentation of cattle manure, sheep manure and pig manure for 70-80 days; (ii) blending sulfur-based complex fertilizer, diammonium phosphate, urea, calcium superphosphate and borax; and (iii) mixing the product of step (i) and (ii), then packing into bags.
NOVELTY - Organic fertilizer comprises 1-5 %mass peanut cake, 1-3 %mass peanut shell, 5-9 %mass river sand, 2-6 %mass bagasse, 1-4 %mass sheep bone, 3-8 %mass pig manure, 0.6-1 %mass egg shell, 0.2-0.5 %mass rhizoma coptidis, 1-3 %mass plant ash, 3-6 %mass pine needle, 1-5 %mass balloon flower, 1-2 %mass snail, 0.002-0.008 %mass onion peel, 1-2 %mass bean residues, 0.5-1 %mass garlic peel, 2-5 %mass waste cabbage leaves, 2-10 %mass distilled water and glucose solution (remainder).    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is highly nutritious, has rapid absorption rate and increases utilization rate by 40-50%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the organic fertilizer, which involves obtaining the above raw materials, crushing the materials, placing the powder in 25 degrees C distilled water for 18-24 hours, then centrifuging the mixture for 10-15 minutes, adding glucose solution, boiling the mixture for 25-35 minutes and then drying to obtain the product.
NOVELTY - Organic fertilizer comprises 3-6 wt.% waste vegetable leaves, 2-5 wt.% animal bone, 0.4-0.8 wt.% egg, 2-4 wt.% watermelon peel, 0.2-0.5 wt.% common Cnidium fruit, 0.1-0.5 wt.% radix sophorae flavescentis, 1-5 wt.% balloon flower, 1-3 wt.% plant ash, 3-8 wt.% animal manure, 3-6 wt.% peanut cake product, 2-4 wt.% snail, 0.005-0.008 wt.% onion outer layer, 10-20 wt.% river silt, 1-5 wt.% walnut, 1-2 wt.% sea tangle, 1-2 wt.% alcohol solution and rice water.    USE - Organic fertilizer used for improving soil (claimed).    ADVANTAGE - The organic fertilizer is absorbed by soil quickly, and provides nutrient to crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) crushing fructus cnidii after fruit and soaking with 90-95% of alcohol solution for 22-24 hours;    (B) centrifuging the soaked product for 10-15 minutes to obtain extraction liquid in a glass bottle;    (C) heating radix sophorae flavescentis root at 60-70 degrees C for 10-15 minutes and cooling;    (D) crushing the remaining components and boiling at atmospheric pressure of 0.2-0.4 megapascals for 30-35 minutes;    (E) fermenting the product in a container at 25-30 degrees C for 7-10 days; and    (F) mixing the fermented product with extraction liquids and boiling for 10-15 minutes, and then drying.
NOVELTY - Preparing edible fungus cultivation substrate using potato residue comprises e.g. removing the rotten potato pulp, spreading potato pulp and airing, dehydrating and increasing ventilating force, evaporating water of potato pulp, drying and smashing potato pulp, and sieving, mixing potato residue, sawdust, bean cake, straw powder, gypsum and mixing uniformly, adding water so that water content is 60-62% after stirring uniformly, stirring uniformly each raw material, packaging, high pressure sterilizing to prepare edible fungus cultivation substrate.    USE - The method is useful for preparing edible fungus cultivation substrate using potato residue (claimed).    ADVANTAGE - The method uses leftovers of agricultural and forest for producing edible fungus planting needed culture material, reduces cultivation cost, increases biological conversion rate, solves the environmental pollution in potato processing, and generates good ecological benefit.    DETAILED DESCRIPTION - Preparing edible fungus cultivation substrate using potato residue comprises (i) pre-processing potato pulp waste: removing the rotten potato pulp, spreading potato pulp and airing, dehydrating and increasing ventilating force, evaporating water of potato pulp, drying and smashing potato pulp, and sieving, (ii) mixing raw material: taking 15-20 pts. wt. potato residue, 10-15 pts. wt. sawdust, 4-5 pts. wt. bean cake, 62-66 pts. wt. straw powder, 1-2 pts. wt. gypsum and mixing uniformly, adding water so that water content is 60-62% after stirring uniformly, and (iii) sterilization packaging: stirring uniformly each raw material, packaging, high pressure sterilizing for 45-60 minutes to prepare edible fungus cultivation substrate.
NOVELTY - Preparing organic fertilizer involves composting chicken manure in a fermentation tank, and then adding, humus soil nutrient, microorganism, super absorbent polymer water retention agent, nitrogen fertilizer, phosphate fertilizer, potash fertilizer and trace element fertilizer. The mixture is stirred and dried in a drying box. The dried mixture is ground into powder, and then packaged.    USE - Method for preparing organic fertilizer (claimed) used for planting fruit and vegetable seedling.    ADVANTAGE - The method is simple and cost-effective, enables to prepare organic fertilizer that increases plant seedling survival rate.
NOVELTY - Preparing multifunctional plant foliar nutrient liquid involves utilizing 68-72% biogas slurry, 8-10% tobacco pole, 8-10% neem tree root or bark, 10% pumpkin vine and 1-2% composite mold. Composite mold comprises thermophilic fungus and Streptomyces, which is proliferated in a test tube. Thermophilic fungus mother culture medium is grown into culture medium in ratio of 1:100 at 26 degrees C for 84 hours having pH 7.3. Culture medium comprises 4-15g beef extract, 15-20g peptone, 3g soluble starch, 6-8g edible salt, 18-20g agar and water.    USE - Method for preparing multifunctional plant foliar nutrient liquid (claimed).    DETAILED DESCRIPTION - Preparing multifunctional plant foliar nutrient liquid involves utilizing 68-72% biogas slurry, 8-10% tobacco pole, 8-10% neem tree root or bark, 10% pumpkin vine and 1-2% composite mold. Composite mold comprises thermophilic fungus and Streptomyces, which is proliferated in a test tube. Thermophilic fungus mother culture medium is grown into culture medium in ratio of 1:100 at 26 degrees C for 84 hours having pH 7.3. Culture medium comprises 4-15g beef extract, 15-20g peptone, 3g soluble starch, 6-8g edible salt, 18-20g agar and water. Culture medium is prepared by performing anaerobic fermentation at 18-30 degrees C for 200 hours. Streptomyces culture medium comprises 15-25g soluble starch, 0.5-1.5g potassium nitrate, 0.4-0.8g salt, 0.4-0.8g potassium hydrogenphosphate trihydrate, 0.4-0.8g magnesium sulfate heptahydrate, 0.005-0.02g iron(II)sulfate heptahydrate, 15-25g agar and water, and its pH value is 7.2-7.4. Streptomyces is mixed with culture medium in ratio of 1:100 at 26 degrees C for 84 hours. Streptomyces product, thermophilic fungus product and crushed product of remaining components are mixed in ratio of 1:1:1 at 15-30 degrees C for 240-300 hours in a culture tank.
NOVELTY - An organic fertilizer comprises 40-60 pts. wt. activated humic acid and 40-60 pts. wt. strengthening material.    USE - Organic fertilizer used for improving orchard soil (claimed).    ADVANTAGE - The fertilizer rapidly raises soil pH value and has double effect on improving soil and organic matter level.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising taking natural humic acid as raw material and activating; mixing with strengthening material and substrate and carrying out fluidization complex process; and pelletizing and carrying out surface treatment.
NOVELTY - Treating fractional factorial designs sludge by: filtering sludge concentrated residue, pumping, concentrating, separating supernatant, filtering material layer through filter, and entering sewage treatment system; mixing filter material and strain, aerobic fermenting or anaerobic fermenting, setting into deodorizing device, deodorizing, collecting, drying to water content of 60%, separating, and drying.    USE - Method for treating fractional factorial designs sludge (claimed) used as organic fertilizer raw material.    ADVANTAGE - The method has low cost and small emitting odor, implements effective use of sludge, is environment-friendly, and realizes reduction of sludge treatment and reuse.
NOVELTY - Biological organic fertilizer comprises 10-20 pts. wt. soybean residue, 10-20 pts. wt. corn flour, 5-10 pts. wt. egg shell powder, 1-3 pts. wt. brown sugar and 30-50 pts. wt. rice water.    USE - Biological organic fertilizer.    ADVANTAGE - The product is low-cost and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic fertilizer comprising mixing soybean residue, corn flour, egg shell powder, brown sugar and rice water, standing at 10-30 degrees C and stacking for 5-10 days.
NOVELTY - Preparation of dairy manure comprises taking cow dung, carrying out solid-liquid separation, drying to moisture content of 55-70%, stacking while maintaining moisture content at 55-70%, fermenting at 55 degrees C, turning, maintaining temperature at 70 degrees C for more than 7 days and adjusting moisture content to 20-35% when temperature is below 50 degrees C.    USE - Method for preparing dairy manure (claimed).    ADVANTAGE - The method is environment-friendly.
NOVELTY - Kitchen waste and sludge high temperature anaerobic digestion comprises collecting kitchen waste, transporting to the mixing chamber, transporting dewatered sludge into the mixing chamber, pouring water, stirring to obtain mixed slurry material, delivering to hydrolysis acidification pool, carrying out hydrolysis acidification, pumping into the fermentation tank, fermenting, performing oxidation treatment, pumping into thermophilic anaerobic digestion tank for further fermentation, fermenting, dehydrating and transported to the storage tank.    USE - Method for carrying out high temperature anaerobic digestion of kitchen waste and sludge (claimed).    ADVANTAGE - The method has high yield.    DETAILED DESCRIPTION - Kitchen waste and sludge high temperature anaerobic digestion comprises collecting kitchen waste, transporting to the mixing chamber, transporting dewatered sludge with moisture content of 80-90% into the mixing chamber where volume of kitchen waste is 0.5-2 times the volume of mixing chamber, pouring water, stirring to obtain mixed slurry material with moisture content of 90-95%, delivering to hydrolysis acidification pool, carrying out hydrolysis acidification for 1-3 days, pumping into the fermentation tank, fermenting at 32-38 degrees C for 10-15 days, performing oxidation treatment for 60-100 minutes where amount of ozone is 0.05-0.2 g/g, pumping into thermophilic anaerobic digestion tank for further fermentation, fermenting at 52-58 degrees C for 5-10 days, dehydrating, transported to the storage tank and using dehydrated cake as organic fertilizer.
NOVELTY - Liquid fertilizer and its preparation method are claimed. The liquid fertilizer is prepared by (a) obtaining fish waste, microbial fermentation composition, molasses, ammonium sulfate, calcium superphosphate and enzyme powder, (b) adding purified water to the above-mentioned components, uniformly stirring obtained mixture, fermenting the mixture, and filtering fermented product, and (c) adding potassium sulfate, magnesium sulfate and urea to obtained filtrate, stirring obtained mixture, processing and filtering the mixture, and packaging obtained product.    USE - The liquid fertilizer is useful for plants.    ADVANTAGE - The liquid fertilizer is rich in nutritional components, and harmless, and improves quality of plants.    DETAILED DESCRIPTION - Liquid fertilizer and its preparation method are claimed. The liquid fertilizer is prepared by (a) obtaining 20-40 wt.% fish waste, 10-20 wt.% microbial fermentation composition, 7-8 wt.% molasses, 1-3 wt.% ammonium sulfate, 1-3 wt.% calcium superphosphate and 0.02-0.04 wt.% enzyme powder, (b) adding 40-50 wt.% purified water to the above-mentioned components, uniformly stirring obtained mixture, fermenting the mixture for 50 days, and filtering fermented product, and (c) adding 20 kg potassium sulfate, 20 kg magnesium sulfate and 20 kg urea to filtrate obtained in step (b), uniformly stirring obtained mixture, performing sedimentation for 30 minutes, filtering the mixture for removing impurities, and stirring and packaging obtained product.
NOVELTY - A high-fertilizer complex organic fertilizer is prepared by taking 32-35 pts. wt. wheat straw stick slag, 20-23 pts. wt. seaweed residue, 13-16 pts. wt. chicken manure, 15-18 pts. wt. chelated molasses alcohol fermentation liquid, 0.2-0.5 pt. wt. urea, 0.4-7 pts. wt. diammonium phosphate, 1.1-1.3 pts. wt. potassium chloride and 0.02-0.05 pt. wt. decomposing inoculant, mixing, stacking for 5-8 days, fermenting for 2.5-4 days at 35-40 degrees C, drying, crushing, sieving, and granulating.    USE - Method for preparing high-fertilizer complex organic fertilizer (claimed).    ADVANTAGE - The fertilizer is low-cost, and has high organic content and adequate amount of trace elements.
NOVELTY - Production of bioorganic fertilizer comprises mixing cassava dregs and rock phosphate powder at dry weight ratio of 100:15-30, adding composite fermentation agent and molasses, and fermenting twice. The fermentation agent comprises Bacillus megaterium, B. licheniformis and Aspergillus niger strains at ratio of 10-50:10-50:1.    USE - Method for producing bioorganic fertilizer (claimed).    ADVANTAGE - The method realizes resource utilization of cassava dregs, improves conversion efficiency of total phosphorus to phosphorus, and improves bioactivity of fertilizer.
NOVELTY - A low-cost fertilizer comprises animal bone soup ferment, calcium superphosphate, vegetable dry powder, modified glucose, potassium sulfate and ammonia mixture, potassium permanganate solution, and sodium nitrate.    USE - Low-cost fertilizer used for flowers.    ADVANTAGE - The fertilizer is full of nutrients, contains chlorine, phosphorus pentoxide, potash and necessary trace elements, can improve soil activity, enhances flower's disease resistance, promotes full absorption of nutrients, and it has adequate sources of raw materials, simple process, low cost, high efficiency, and no environmental pollution and any side effects.
NOVELTY - High-efficiency fertilizer comprises animal bone soup fermentation product, animal bone powder, vegetable dry powder, modified glucose, mixture of methylene succinate and ammonium hydroxide, phosphorus pentoxide solution, and hydrogen peroxide.    USE - High-efficiency fertilizer for flowers (claimed).    ADVANTAGE - The fertilizer is simple to prepare, safe and reliable, and rich in nutrients, chlorine, phosphorus pentoxide, potassium oxide and trace elements; can fertilize up to 6 months; improves vitality of soil and enhances stress resistance of flowers; promotes full absorption of nutrients; and has wide raw material source, low cost, no environment pollution and no side effects.
NOVELTY - Preparation of multivariate ecological organic/inorganic fertilizer comprises taking 1-95 pts. wt. Canna edulis starch residue, 0-90 pts. wt. cassava starch, 1-90 pts. wt. fly ash, 1-5 pts. wt. aqueous ammonia and 1-90 pts. wt. other starches, mechanically or manually mixing and bagging.    USE - Method for preparing multivariate ecological organic/inorganic fertilizer (claimed) used in modern ecological agriculture for reducing usage of chemical fertilizers, promoting food safety and ecological agriculture modernization and improving soil.
NOVELTY - Production of mushroom cultivation material includes drying mushroom foot, crushing, soaking in water, mixing with wood chips and cottonseed hull, piling into heap, covering with grass, and naturally fermenting; turning while adding lime, gypsum and bran, and stopping fermentation; and cooling, loading into polyethylene bags, adding bacterial strain, inoculating until mycelium appears, and performing fruiting management.    USE - Method for production of mushroom cultivation material (claimed).    ADVANTAGE - The method promotes microbial growth, improves microbial flora in the material, accelerates catalytic decomposition of cultivated material, saves manpower and other resources, and reduces environmental pollution. The mushroom cultivation material has natural nutrient solution and variety of bioactive substances contents, and high activity of bacteria and its active metabolite.    DETAILED DESCRIPTION - Production of mushroom cultivation material comprises:    (A) drying 4-5 wt.% mushroom foot, crushing into granules, adding 20-30 times water, soaking at room temperature for 18-24 hours, mixing with 54-60 wt.% wood chips and 14-18 wt.% cottonseed hull, piling into heap, controlling dry weight to 300-500 kg, making 10-15 cm diameter vertical holes, covering with grass, and naturally fermenting;    (B) turning once a day for 5-6 days when material temperature reaches 60 degrees C for 24 hours, adding 2.5 wt.% lime, turning, adding 1 wt.% gypsum, turning, adding 18-20 wt.% bran, and stopping fermentation when moisture content is 63-65%; and    (C) cooling, loading into polyethylene bags, adding bacterial strain, inoculating for 40-42 days through dark room while controlling temperature to 20-22 degrees C and humidity to 60-75% until mycelium appears, and performing fruiting management.    The wood chips are broadleaf hardwood. The mushroom foot is shiitake mushroom waste.
NOVELTY - A selenium-enriched microbial organic fertilizer comprises 12-18 pts. wt. fermentation material, 6-10 pts. wt. mineral substance, 0.5-0.8 pts. wt Bacillus subtilis 10147, 30-40 pts. wt. edible fungus, 5-10 pts. wt. Chinese medicine slag, and 15-20 pts. wt. aqueous biogas.    USE - Selenium-enriched microbial organic fertilizer.    ADVANTAGE - The microbial organic fertilizer is environment-friendly and suitable for large agricultural production, contains a lot of organic selenium, improves the soil, and it has disease prevention effect.    DETAILED DESCRIPTION - A selenium-enriched microbial organic fertilizer comprises 12-18 pts. wt. fermentation material, 6-10 pts. wt. mineral substance, 0.5-0.8 pts. wt Bacillus subtilis 10147, 30-40 pts. wt. edible fungus, 5-10 pts. wt. Chinese medicine slag, and 15-20 pts. wt. aqueous biogas. The fermentation material comprises 10-20 pts. wt. maggot powder, 1-3 pts. wt. aqueous biogas, 3-5 pts. wt. molasses, 0.1-0.2 pts. wt. sodium selenite, and 0.1-0.2 pts. wt. Bacillus subtilis 10147. The mineral substance comprises 40-60 pts. wt. phosphate, 40-60 pts. wt. coal gangue, and 1-3 pts. wt. silicon powder. The fermentation material is prepared by mixing ingredients into fermentation tank, and naturally fermenting for 1-2 weeks. The selenium-enriched microbial organic fertilizer is prepared by adding raw materials into fermentation tank, mixing, naturally fermenting for 6 weeks, and turning once a week.
NOVELTY - A compound fertilizer comprises 20-80 pts. wt. inorganic fertilizer, 10-40 pts. wt. organic matter, 2-20 pts. wt. soil modifier, 0.01-2 pt. wt. microelement, and 0.1-4 pts. wt. microorganism strain. The inorganic fertilizer comprises ammonium dihydrogen phosphate, diammonium phosphate, potassium sulfate, and/or potassium chloride. The organic fertilizer is urea, humic acid and weathered coal. The soil modifier is bentonite and medical stone. The microelement comprises iron, boron, zinc, and/or manganese.    USE - Compound fertilizer used for improving soil structure.    ADVANTAGE - The fertilizer increases crop needed beneficial flora, has slow decomposing soil nutrient effect, prolongs soil fertilizer effect, increases crop yield and fertilizer use rate, and relieves compaction of soil and detoxification of heavy metals.    DETAILED DESCRIPTION - A compound fertilizer comprises 20-80 pts. wt. inorganic fertilizer, 10-40 pts. wt. organic matter, 2-20 pts. wt. soil modifier, 0.01-2 pt. wt. microelement, and 0.1-4 pts. wt. microorganism strain. The inorganic fertilizer comprises ammonium dihydrogen phosphate, diammonium phosphate, potassium sulfate, and/or potassium chloride. The organic fertilizer is urea, humic acid and weathered coal. The soil modifier is bentonite and medical stone. The microelement is iron, boron, zinc, and/or manganese. The microorganism strain is Azotobacter, phosphorus-decomposing bacteria, potassium bacteria, and/or Bacillus subtilis. An INDEPENDENT CLAIM is included for preparation of fertilizer comprising measuring major elements, trace elements, and organic matter in soil; separating microbial strain, screening, identifying, and culturing; adding flour as microorganism carrier and nutrient substance, stirring, and drying; mixing major elements, trace elements, and organic matter and stirring; and adding inorganic fertilizer, soil modifier, and water, mixing, drying, and packing.
NOVELTY - 1 Pt. wt. deionized water, 0.1 pt. wt. metallic zinc, 18 pts. wt. p-aminophenol and 34 pts. wt. acetic acid are added to a reactor, temperature of the reactor is raised to 45 degrees C, and the raw materials are stirred uniformly, to obtain a reaction liquid. The reaction liquid is dehydrated using dehydration membrane machine for 8 hours by maintaining back side pressure to -0.1 MPa. The reaction liquid is cooled to 15 degrees C, crystallized for 8 hours, vacuum-dried at 60 degrees C for 20 hours and vacuum degree of -0.1 MPa to obtain paracetamol.    USE - Preparation of paracetamol (claimed).    ADVANTAGE - The method enables preparation of paracetamol with improved quality by preventing generation of waste acid and by consuming reduced amount of energy.
NOVELTY - The preparation method of 2-bromomethyl-benzene compound (I) involves reacting methyl-benzene compound (II) with bromate salt in an organic solvent, in the presence of catalyst and bisulfite salt.    USE - Method is useful for preparation of 2-bromomethyl-benzene compound (I) (claimed).    ADVANTAGE - The method enables simple, economical and environmentally-friendly preparation of 2-bromomethyl-benzene compound with high yield, product selectivity and utilization of bromine, under mild condition in non-corrosive environment.    DETAILED DESCRIPTION - The preparation method of 2-bromomethyl-benzene compound of formula (I) involves reacting methyl-benzene compound of formula (II) with bromate salt in an organic solvent, in the presence of catalyst and bisulfite salt.    R1,R2=1-4C alkyl;    X=N or O;and    Z=CH or N.
NOVELTY - Preparation of bispyribac intermediate i.e. 4,6-dimethoxy-2-methanesulfonyl-pyrimidine comprises using 4,6-dimethoxy-2-methylthiopyrimidine as raw material, acetic acid as solvent, heteropoly acid as catalyst, aluminum-doped mesoporous silicon dioxide SBA-15 as carrier, and hydrogen peroxide as oxidizing agent, and oxidation reacting.    USE - Preparation of bispyribac intermediate i.e. 4,6-dimethoxy-2-methanesulfonyl-pyrimidine (claimed).    ADVANTAGE - The method has increased oxidation selectivity, uses reusable heteropoly acid catalyst supported on mesoporous carrier, and reduces waste discharge and production cost.
NOVELTY - Method for processing Panicum virgatum silage involves fermenting P.virgatum with complex microbial inoculum and cellulase under anaerobic condition, where the cellulase is chosen from cellulase of Basidiomycetes sp. D9515 strain, cellulases derived from Aspergillus sp. V2010 strain, cellulases derived from Trichoderma longibrachiatum C9748 strain, Aspergillus oryzae strain and their combinations.    USE - The method is useful for processing P.virgatum silage (claimed).    ADVANTAGE - The method is environmentally-friendly, simple, cost-effective and improves fermentation level of P.virgatum and fermented products. The P.virgatum silage has high crude protein content and nutrition value and low pH and fiber, cellulose, hemicellulose and lignin content.    DETAILED DESCRIPTION - Method for processing Panicum virgatum silage involves fermenting P.virgatum with complex microbial inoculum and cellulase under anaerobic condition. The complex microbial inoculum is prepared by fermenting Lactobacillus plantarum, Bacillus subtilis and Lactococcus separately and mixing the resulting fermentation broth. The cellulase is chosen from cellulase of Basidiomycetes sp. D9515 strain, cellulases derived from Aspergillus sp. V2010 strain, cellulases derived from Trichoderma longibrachiatum C9748 strain, Aspergillus oryzae strain and their combinations.
NOVELTY - An environment-friendly highly effective pengze crucian carp feed comprises fishmeal, soybean meal, peanut meal, cotton, vegetable, flour, distiller's dried grains with solubles alcohol protein, rice bran, rapeseed oil, choline chloride, salt, chelated microelement, fish multivitamins, vitamin E, vitamin C phosphate, taurine, calcium biphosphate and methionine.    USE - Environment-friendly highly effective pengze crucian carp feed.    ADVANTAGE - The feed is rich in nutrition and prevents nitrogen ratio imbalance. It increases absorption rate and immunity.    DETAILED DESCRIPTION - An environment-friendly highly effective pengze crucian carp feed comprises 11-14 pts. wt. fishmeal, 23-26 pts. wt. soybean meal, 7-9 pts. wt. peanut meal, 7-9 pts. wt. cotton, 10-13 pts. wt. vegetables, 13-16 pts. wt. flour, 6-8 pts. wt. distiller's dried grains with solubles alcohol protein, 9-12 pts. wt. rice bran, 5-6 pts. wt. rapeseed oil, 0.3-0.4 pt. wt. choline chloride, 0.2-0.3 pt. wt. salt, 0.3-0.5 pt. wt. chelated microelement, 0.1 pt. wt. fish multivitamins, 0.03 pt. wt. vitamin E, 0.2 pt. wt. vitamin C phosphate, 0.1 pt. wt. taurine, 2 pts. wt. calcium biphosphate and 0.2 pt. wt. methionine. An INDEPENDENT CLAIM is included for preparation of environment-friendly highly effective pengze crucian carp feed comprising taking raw materials except rapeseed oil, mixing, adding 60-65 wt.% rapeseed oil, mixing at 90 degrees C for 5 minutes, extruding at 98 degrees C, drying at 58 degrees C, adding remaining rapeseed oil, heating at 60-80 degrees C, and cooling.
NOVELTY - The new type utility claims a sewage treatment plant and a device, a drain outlet, a screen, machine, lathe dog, pressure table, a discharge valve, a sensor, a pressure material rod, sewage and waste material adding device, a filtering device and water for floating ball switch, a drain equipped with a hair is l. the screen is equipped with a hair l internal periphery, a pressing material plate, and a wall in hair l tightly contact, the hoop and detachable clamping connection mechanism, a pressure table and pressure material rod top end connected with, the automatic exhaust valve is set with pressure table above and a pressure material rod a, the sewage treatment and a device, a domestic sewage or domestic garbage collective to carry out fermentation, then can be again to obtain the use on the ground fertilizer, the waste as treasure, environmental protection energy saving, with centrifuge motor waste in a whole device in full mixing, a rate increase.
NOVELTY - The new type utility claims a kitchen waste integrated treatment device A using a groove and a discharging device. A slot the automatic discharging device, comprising a groove body provided with a discharge at a slot in body, to discharge a set with a discharging of a door, the discharging a door arrangement with a discharge door opening and closing mechanism, a drive shaft internal in a groove body, provided with multiple stirring blade group on a drive shaft, and also provided with a group to a discharge position at a drive shaft of row material shovel, discharge a formed at the upper position and a slot body. The utility model is new type row material by a stirring shovel coaxial to increase in a groove wherein the discharge, a common function of the following row material and stirring , which can take a complete fertilizer all automatic fast discharging. In addition, the utility model is new type material in a design in a high position, suitable fast feeding.
NOVELTY - The new type utility claims a self-control one enzyme cleaning agent and environment-friendly device, comprising container main body, the container main body is round, semi-diameter of a container larger than semi-diameter of bottom container, provided with a filtering network in the container main body and internal lower part, the filter network is semi-diameter of round filter screen container larger than the inner diameter of a container wherein a smaller semi-diameter, provided with a one-way exhaust valve on a bottle cover. The filter network is 80 meshes to 120 meshes. The utility model is novel manufacture process is more suitable, fast.
NOVELTY - Enhancing decomposition of solid waste involves introducing culture media for growth of inoculants, performing anaerobic fermentation and aerobic fermentation using polyethylene, injecting inoculants derived from indigenous local materials such as, hay, banana trunks, rice, pulp of soybean and other locally found materials into fermented material to produce inoculants, and processing the inoculants to hasten microbial growth an optimum level by enhancing harvest of methane gas and organic fertilizer that serve as an organic pesticide.    USE - The method is useful for enhancing decomposition of solid waste which is useful for producing organic fertilizer that promotes production of crops.    ADVANTAGE - The method provides low cost organic fertilizer compared to inorganic fertilizer and biogas.
NOVELTY - Producing livestock manure, comprises (a) providing medium producing rice straw and livestock manure, crushing the rice straw, and removing liquid wastes and solid waste from livestock manure, (b) impregnating the pulverized rice straw into the livestock manure of liquid waste, and softening the rice straw, and (c) mixing the softened rice straw with solid waste and wood chips, and fermenting.    USE - The method is useful for producing livestock manure (claimed).    ADVANTAGE - The method improves productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing livestock manure using mushroom compost medium, comprising (i) impregnating livestock manure into liquid wastes to perform softening, mixing the softened rice straw with solid waste and wood chips, and fermenting, (ii) inoculating with mushroom spawn and granular culture medium with bacteria and fungus, rooting the fungus, and forming mushroom fruiting body, and (iii) harvesting the mushroom fruiting body.
NOVELTY - A plant soil comprises 50-70 wt.% shale particles, 20-40 wt.% excrement, and 10-30 wt.% river sand. The excrement is fermented livestock manure and poultry manure, preferably sheep and/or cow manure mixture.    USE - Plant soil.    ADVANTAGE - The plant soil has better soil permeability which ensures smooth progress of plant roots aerobic respiration and normal growth, high soil fertility, better plant roots anchoring effect, and simple and low cost production process that is suitable for large-scale industrial production.
NOVELTY - Organic fertilizer comprises 20-100 pts. wt. swill water, 1-2 pts. wt. corn flour, 0.5-1 pts. wt. micro-organism leavening agent, 200-1000 pts. wt. human and animal feces soil rich in zinc, 0-200 pts. wt. poultry excrement, 0-200 pts. wt. fishponds sapropel, 0-200 pts. wt. lees, 0-200 pts. wt. biogas sludge, 0-200 pts. wt. bacteria bag waste and 20-100 pts. wt. green manure.    USE - Organic fertilizer used for planting tea.    ADVANTAGE - The organic fertilizer ensures no public hazard and ecological protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves;    (A) mixing and crushing human and animal feces soil rich in zinc, poultry excrement, fishponds sapropel, lees, biogas sludge, bacteria bag waste and green manure to obtain mixture;    (B) fermenting obtained mixture, cornmeal, micro-organism leavening agent, swill water and clean water for 5-10 days; and    (C) drying fermented material to obtain product.
NOVELTY - Manufacturing fertilizer involves crushing and mixing uniformly crop straw and livestock manure and molasses residue. Water is added in the mixture, and then effective microorganisms strain is mixed and stirred for 15 days in a pool. The mixture is mixed with water (0.3-0.5 times) and then fermented for 1-3 days. The fermented product is mixed with Camellia and then fermented for 3-5 days to obtain fertilizer.    USE - Method for manufacturing fertilizer used for plant (claimed).    ADVANTAGE - The method enables to manufacture fertilizer has multifunctional enzyme. The fertilizer provides nutrition to crop adequate, improves soil fertility, increases economic benefit, and eliminates insect pests.
NOVELTY - Organic fertilizer is prepared by mixing monosodium glutamate waste liquid, rice bran and chicken manure ash in ratio of (3-7):(2-4):(1-2), and then fermented to obtain fermentation product. The fermentation product is crushed, sieved, and then packaged.    USE - Organic fertilizer used for planting economic crops (claimed).    ADVANTAGE - The organic fertilizer is prepared in a cost-effective manner, and regulates nitrogen, phosphorous and potassium in plant.
NOVELTY - Fertilizer comprises 10-12% cassia twig residue, 12-15% fructus momordicae medicinal slag, 15-18% Astragalus medicinal slag, 20-22% grass, 2-4% soil, 30-32% rabbit manure and 2-3% microbial inoculum.    USE - Fertilizer used for planting balloon flower (claimed).    ADVANTAGE - The fertilizer promotes plant absorption, adjusts water content of soil, improves soil and increases utilization rate of fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves;    (A) mixing cassia twig residue, fructus momordicae medicinal slag and Astragalus medicinal with water slag for 2 days at 35 degrees C;    (B) grinding and pulping obtained mixture;    (C) fermenting obtained pulp with microbial inoculum for 20 days; and    (D) drying fermented materials to obtain product.
NOVELTY - Bio-organic fertilizer comprises main material and auxiliary material. The main material comprises 15-40 wt.% straw, 5-20 wt.% cassava residue, 3-15 wt.% fungus residue, 10-18 wt.% leaves, 8-25 wt.% soybean meal, 5-20 wt.% cotton powder, 2-18 wt.% bran and 12-28 wt.% sheep manure. Auxiliary material comprises 10-45 wt.% cattle liver, 0-20 wt.% arbuscular mycorrhizal fungus, 0-20 wt.% Aspergillus niger, 0-20 wt.% effective microorganism, 5-20 wt.% urine and 30-80 wt.% calcium superphosphate, the main material. The main material and auxiliary material are present in ratio of 50-100:1.    USE - Bio-organic fertilizer.    ADVANTAGE - The bio-organic fertilizer is cost-effective and biodegradable, and improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) crushing main materials, such as straw, cassava residue, fungus residue, leaves, soybean meal, cotton powder, bran and sheep manure through a crusher to obtain powder;    (B) crushing and mixing auxiliary materials and fermenting;    (C) mixing main materials uniformly with auxiliary materials, and then performing natural fermentation at 50-60 degrees C for 10-15 days in a container;    (D) granulating the fermented product, and then pelleting; and    (E) drying the pellets at 40-45 degrees C, and then packaging and sealing.
NOVELTY - The utility model is new type provide the a one for a biological organic fertilizer is a double layer bacteria adding device of technology scheme, the scheme comprises a powder feeding device, liquid bacteria adding device and a material mixing device, powder through bacteria adding device for pulling in bacillus subtilis powder bacteria adding pipeline, a can of a bacillus subtilis is added with weight, in liquid through bacteria adding device beneficial for a spraying roller, a bacillus subtilis, a and organic fertilizer in a material mixing in a fully uniform mixing, a. the biological organic fertilizer is a quality is good, the production efficiency high.
NOVELTY - The utility model is new type relates to a plant straw sludge comprehensively using system, specifically comprising: pre-processing system 1, mixing a. 2 and finished product sieving and packing system 3 of a sub-system, a is a number sub-system connected in turn. C, pre-processing system 1 comprises sludge dewatering and drying straw smashing two strip processing line, mixing a. 2 comprises in turn connecting the mixer and a groove, the groove is provided with a ventilation aeration device, finished product sieving and packing system 3 comprises in turn a sieving machine and the bagging machine. The b a b for municipal sludge and solves two planting crop straw and solid waste caused by improper located to cause the serious environmental problem pollute, sludge and straw two plant waste by the a mixed fermentation, two second interaction, wherein at last a conversion for a high-quality organic fertilizer, the harmlessness, reduction and reclamation of two plant waste.
NOVELTY - Organic chromium in wastewater is degraded by adding aerobic activated sludge from wastewater treatment plant to nutrient solution with ratio carbon (C):nitrogen (N):phosphorus (P) of 100:5:1 to form 110 ml suspension, adding to solutions with different organic chromium concentrations, domesticating, adding 1 g granular activated carbon, adsorbing and fixing microorganisms to form fixed microorganisms, adding to wastewater containing organic chromium, adjusting pH to 2-3, and standing for 100-120 minutes.    USE - Degradation of organic chromium in wastewater.    ADVANTAGE - Degradation of organic chromium in wastewater is simple and fast.    DETAILED DESCRIPTION - Organic chromium in wastewater is degraded by adding aerobic activated sludge from wastewater treatment plant to nutrient solution with ratio carbon (C):nitrogen (N):phosphorus (P) of 100:5:1 to form 110 ml suspension, adding to solutions with different organic chromium concentrations, domesticating, adding 1 g granular activated carbon, adsorbing and fixing microorganisms to form fixed microorganisms, adding to wastewater containing organic chromium, adjusting pH to 2-3, and standing for 100-120 minutes in which each 200 ml wastewater solution with chromium concentration of 50 mg/L is added with 1 g activated carbon containing 110 ml activated sludge suspension.
NOVELTY - A biological aerated filter comprises filter body, water inlet pipe, water outlet pipe, aeration pipe, backwash fan, backwash pump, return pump, and filter medium in which filter medium is prepared by mixing 1-2 cm barley straw pieces:activated sludge with volume ratio of 2:1, and filter contains porous grid with pore size of less than or equal to 1 cm.    USE - A biological aerated filter for treating algae containing polluted water (claimed).    ADVANTAGE - Biological aerated filter is safe and low-cost, inhibits growth of harmful algae, and promotes biological nitrogen removal and water purification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment of algae containing polluted water which involves filling biological aerated filter with filter medium to packing line, continuously aerating with aeration pipe, pumping algae containing polluted water with flowrate of 2.5-5 m/hour for 20-40 minutes every 25-45 minutes, examining activated sludge in filter every 24 hours using microscope until Virticella, Epistylis, Zoothamnium, flagellates, amoebae, suctoria, Oxytricha, Euplotes, rotifers, and/or roundworms appear, exposing polluted water to air from aeration tube with gas:water ratio of 1:1-1.5 and water flowrate of 8-10 m/hour, hydraulic load of 0.35-1.05 m3/m2.hour, and pH of 6-8 until thickness of biofilm in filter medium reaches 270-420 less than or equal to mm, starting backwash cycle, closing water inlet pipe and aeration pipe valve, starting backwash fan, opening backwash inlet valve, air washing at 8-18 L/m2.s for 3-7 minutes, starting backwash pump, backwashing with air and water with water strength of 4-7 L/m2.s for 4-8 minutes, closing backwash fan and backwash inlet valve, washing with water to remove biofilm and suspended solids for 3-7 minutes, and repeating filtering and backwashing steps.
NOVELTY - A sewage treatment biological enzyme modified charcoal filler is prepared by sieving and grinding natural charcoal, spraying modifying agent, adding mixed enzyme agent, fully stirring and standing, vacuumizing by vacuum pump, and air drying until water content is 8-10% in which weight ratio of natural charcoal and modifying agent is 3:1, modifying agent consists of liquid (A) and liquid (B), liquid (A) consists of 1-5 wt.% glucosamine, 1-5 wt.% glucosamine hydrochloride, 0.5-4 wt.% glucosamine sulfate % hydrochloric acid, and balance water, and liquid (B) consists of 5-20 wt.% corn pulp.    USE - Preparation of sewage treatment biological enzyme modified charcoal filler.    ADVANTAGE - Product has long service life.    DETAILED DESCRIPTION - A sewage treatment biological enzyme modified charcoal filler is prepared by sieving and grinding natural charcoal, spraying modifying agent, adding mixed enzyme agent, fully stirring and standing, vacuumizing by vacuum pump, and air drying until water content is 8-10% in which weight ratio of natural charcoal and modifying agent is 3:1, modifying agent consists of liquid (A) and liquid (B), liquid (A) consists of 1-5 wt.% glucosamine, 1-5 wt.% glucosamine hydrochloride, 0.5-4 wt.% glucosamine sulfate % hydrochloric acid, and balance water, sum of components of liquid (A) is 100%, liquid (B) consists of 5-20 wt.% corn pulp, 4-20 wt.% peptone, 0.5-3 wt.% ammonium sulfate, 0.1-2 wt.% ferric sulfate, 0.1-2 wt.% potassium dihydrogen phosphate, 0.1-2 wt.% magnesium sulfate, 1-5 wt.% yeast, and balance water, sum of components of liquid (B) is 100%, mass ratio of natural charcoal and mixed enzyme agent is 1:1000-2000, mixed enzyme agent consists of 2-20% pectinase, 5-20% protease, 5-20% lipase, 5-25% cellulase, 5-20% catalase, 5-20% amylase, and balance water, and sum of components of mixed enzyme is 100%.
NOVELTY - A water ecological filtering device comprises suspended sleeve (1), filter cloth area (2), and strip (4) in which filter cloth area contains loose filter cloth area (21) and tight filter cloth area (22) made of nanofiber nonwoven fabric.    USE - A water ecological filtering device for domestic wastewater, lake, and river.    ADVANTAGE - Water ecological filtering device has high purification efficiency and specific surface area, simple operation, strong adsorption force, and good filtering ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of water ecological filtering device which involves dissolving hydrophilic polymer in organic solvent to form spinning solution, forming into nanofiber membrane using electrostatic spinning machine, lacing to form loose filter cloth and tight filter cloth, stitching to form filter cloth area, stitching to suspended sleeve, and cutting to form strip.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of water ecological filtering device.    Suspended sleeve (1)    Filter cloth area (2)    Strip (4)    Loose filter cloth area (21)    Tight filter cloth area (22)
NOVELTY - A microorganism microbial inoculum comprises pyridine-degrading bacteria Arthrobacter sp. TJKYBD-02 with preservation number CGMCC No. 10176, quinoline-degrading bacteria Pseudomonas chlororaphis, phenol-degrading bacteria Acinetobacter calcoaceticus, o-cresol-degrading bacteria Pseudomonas sp. TJKYLJF-01 with preservation number 10177, naphthalene-degrading bacteria Bacillus subtilis, and n-hexadecane-degrading bacteria Pseudomonas aeruginosa.    USE - A microorganism microbial inoculum for strengthening coking wastewater treatment (claimed).    ADVANTAGE - Microorganism microbial inoculum reduces operation cost, enhances refractory organics removal, and strengthens COD, ammonia, and total nitrogen removal.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) strengthening of coking wastewater treatment which involves performing hydrolysis acidification on coking wastewater to improve biodegradability, adding microorganism microbial inoculum, performing aerobic strengthening treatment to remove organic matter and refractory organics, and performing anoxic denitrification and aerobic nitrification to remove ammonia and total nitrogen; and    (2) coking wastewater treatment device.
NOVELTY - A biofilm system comprises 30-55 pts. wt. 1st film-forming matrix e.g. agar, 5-10 pts. wt. 2nd film-forming matrix e.g. sodium carboxymethyl cellulose, 1-5 pts. wt. 3rd film-forming matrix e.g. gelatin, 3-5 pts. wt. toughening agent, 25-50 pts. wt. biofilm skeleton e.g. glass fiber, 25-50 pts. wt. adsorbent, 100-300 pts. wt. deionized water, and 10-20 pts. wt. bioactive component in which toughening agent comprises 3-9 pts. wt. starch, 0.2-0.8 pt. wt. disodium EDTA, 0.5-1.5 pts. wt. copper sulfate pentahydrate, and 0.1-0.8 pt. wt. ammonium bicarbonate.    USE - A biofilm system for sewage treatment.    ADVANTAGE - Biofilm system has improved degradation efficiency.    DETAILED DESCRIPTION - A biofilm system comprises 30-55 pts. wt. 1st film-forming matrix e.g. agar, 5-10 pts. wt. 2nd film-forming matrix e.g. sodium carboxymethyl cellulose, 1-5 pts. wt. 3rd film-forming matrix e.g. gelatin, 3-5 pts. wt. toughening agent, 25-50 pts. wt. biofilm skeleton e.g. glass fiber, 25-50 pts. wt. adsorbent, 100-300 pts. wt. deionized water, and 10-20 pts. wt. bioactive component in which toughening agent comprises 3-9 pts. wt. starch, 0.2-0.8 pt. wt. disodium EDTA, 0.5-1.5 pts. wt. copper sulfate pentahydrate, and 0.1-0.8 pt. wt. ammonium bicarbonate, and adsorbent comprises 10-15 pts. wt. charcoal powder and 1-3 pts. wt. ferrous oxide. An INDEPENDENT CLAIM is included for preparation of biofilm system which involves adding toughening agent to deionized water, heating to 95-100 degrees C, maintaining temperature for 10 minutes, cooling to 10 degrees C within 5 minutes, adding 1st film-forming agent, 2nd film-forming agent, 3rd film-forming agent, biofilm skeleton, and adsorbent, stirring and heating to 90-95 degrees C, maintaining temperature for 15-20 minutes to obtain molten mass, cooling to 40-45 degrees C, adding bioactive component, shocking, adhering to substrate surface, cooling, and solidifying.
NOVELTY - An organic waste aerobic fermentation cylinder gas supply system comprises aerobic fermentation roller (101), gas distribution device (102), branch pipe adjusting valve (103), main pipe adjusting valve (104), gas supply pipeline (105), fan, monitoring device, controller, air supply pipe, roller and sensor.    USE - Organic waste aerobic fermentation cylinder gas supply system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic waste aerobic fermentation cylinder gas supply system.    Aerobic fermentation roller (101)    Gas distribution device (102)    Branch pipe adjusting valve (103)    Main pipe adjusting valve (104)    Gas supply pipeline (105)
NOVELTY - Preparation of livestock manure organic fertilizer comprises crushing cow dung, sending into fermentation tank, adding silkworm waste, lees, straw and effective microorganisms strain, fermenting for 4-6 weeks, adding urea, potassium sulfate and diammonium phosphate, continuously fermenting for 2-3 weeks, adding potassium bicarbonate, adjusting pH to 7-8, drying to water content of 13%, mixing, cooling, crushing to 60-80 mesh, adding adhesive, granulating, cooling and packaging.    USE - Method for preparing livestock manure organic fertilizer used for strawberry (claimed).
NOVELTY - Preparation of livestock manure organic fertilizer comprises crushing mixture of dairy manure and chicken manure, adding into plastic greenhouse fermentation facility, adding rice, persulfate and clay, fermenting, adding potassium bicarbonate, adjusting pH to 7-8, drying to water content of 13%, mixing, cooling, crushing to 60-80 mesh, adding water-retention agent, completely mixing, adding adhesive, granulating, cooling and packaging.    USE - Method for preparing livestock manure organic fertilizer (claimed).    ADVANTAGE - The fertilizer prevents loss of water for crops, thus reducing watering applications and reducing labor intensity.
NOVELTY - Synthesis of haloxyfop intermediate comprises reacting first haloxyfop intermediate and second haloxyfop intermediate.    USE - Method for synthesizing haloxyfop intermediate (claimed).    ADVANTAGE - The method produces high optical purity target product, has low cost, is easy to control, and reduces industrial pollution.    DETAILED DESCRIPTION - Synthesis of haloxyfop intermediate comprises reacting first haloxyfop intermediate and second haloxyfop intermediate, where first haloxyfop intermediate is prepared by taking L-lactate and p-toluenesulfonyl chloride as starting materials and reacting with methylene chloride as solvent and triethylamine as acid binding agent to obtain S-p-toluenesulfonyl lactate and second haloxyfop intermediate is prepared by reacting 3-chloro-2-fluoro-5-trifluoromethyl pyridine and benzene diester as starting raw materials in the presence of potassium carbonate to obtain 3-chloro-2-(4-thiophenoxy)-5-trichloromethylpyridine. The first haloxyfop intermediate is synthesized by taking p-toluenesulfonyl chloride (I) and L-lactate (II) and as starting materials and reacting with methylene chloride as solvent and triethylamine as acid binding agent at - 5-5 degrees C for 4-15 hours to obtain S-p-toluenesulfonyl lactate (III), where ratio of L-lactate, p-toluenesulfonyl chloride, and triethylamine is 1:1.1-1.5:1-2. The second haloxyfop intermediate is synthesized by taking 2-fluoro-3-chloro-5-trifluoromethylpyridine (IV) and hydroquinone (V) as starting materials and reacting in the presence of potassium carbonate at 105-125 degrees C for 3-8 hours to obtain 3-chloro-2-(4-thiophenoxy)-5-trichloromethylpyridine (VI), where ratio of 2-fluoro-3-chloro-5-trifluoromethylpyridine, hydroquinone and potassium ratio is 1:1.2-2.5:1.2-2.
NOVELTY - An erbium co-doped zinc sulfide quantum dot aqueous phase is prepared by dissolving cerium nitrate hexahydrate, erbium nitrate pentahydrate, and zinc acetate dihydrate in deionized water to prepare 1st solution, uniformly stirring under magnetic force, dissolving glutathione, sodium hydroxide, and sodium sulfide nonahydrate in deionized water, dropping glutathione solution under nitrogen protection to 1st solution, uniformly stirring, heating water bath, cooling, adding anhydrous ethyl alcohol, separating white precipitate, performing centrifugal separation, washing, and vacuum drying.    USE - Microwave preparation of erbium co-doped zinc sulfide quantum dot aqueous phase for probe, drug screening, and heavy metal ion.    ADVANTAGE - Preparation process is environment-friendly and has good electrochemical performance and stability.    DETAILED DESCRIPTION - An erbium co-doped zinc sulfide (ZnS) quantum dot aqueous phase is prepared by dissolving cerium nitrate hexahydrate (Ce(NO3)3.6H2O), erbium nitrate pentahydrate (Er(NO3)3.5H2O), and zinc acetate dihydrate (Zn(CH3COO)2.2H2O) in deionized water to prepare 1st solution, uniformly stirring under magnetic force, dissolving glutathione (GSH), sodium hydroxide (NaOH), and sodium sulfide nonahydrate (Na2S.9H2O) in deionized water to prepare GSH solution, NaOH solution, and Na2S.9H2O solution, dropping GSH solution under nitrogen protection to 1st solution, uniformly stirring, controlling pH by using NaOH solution, uniformly stirring, slowly adding Na2S.9H2O solution, uniformly stirring, heating water bath by microwave to obtain cerium, erbium-doped ZnS quantum dot aqueous solution, cooling, adding anhydrous ethyl alcohol, separating white precipitate, performing centrifugal separation, washing precipitate with anhydrous alcohol, and vacuum drying.    DESCRIPTION OF DRAWING(S) - The drawing shows an image of erbium co-doped zinc sulfide quantum dot fluorescence emission spectrum.
NOVELTY - The sandy mineral soil conditioner comprises 30-50 wt.% limestone, 10-30 wt.% humic acid, 10-20 wt.% of zeolite, 10-20 wt.% silica, 1-3 wt.% yeast, 1-5 wt.% nitrogen-fixing bacteria, 1-3 wt.% radix curcumae (turmeric), 5-10 wt.% turmeric, and 1-5 wt.% chinaberry fruit.    USE - Sandy mineral soil conditioner.    ADVANTAGE - The sandy mineral soil conditioner balances criteria and soil property, activates a mutual reaction under a certain condition, and generates soil structure change.
NOVELTY - To-be-fermented raw materials are fermented in a fermenting system, such that biogas is generated. When the pressure of the biogas in the fermentation area is increased, the biogas fluid in a fermenting pipeline flows into a hydraulic unit by virtue of the discharging tube drainage pipe. When the pressure of the biogas in the fermentation area is decreased, most of the biogas fluid in the hydraulic unit is provided into the fermenting pipeline. Thus, the circular flow of the biogas fluid is completed.    USE - Method for generating methane from multi-region hydraulic circular flow bacterium distribution fermenting system.    DETAILED DESCRIPTION - To-be-fermented raw materials are fermented in a fermenting system, such that biogas is generated. The generated biogas is collected in a fermentation area formed by spaces between the sidewall of a feeding/discharging tube and adjacent gas baffle plates or in a fermentation area formed by a space between the adjacent gas baffle plates. When the pressure of the biogas in the fermentation area is increased, the biogas fluid in a fermenting pipeline reaches the lowest points of the feeding tube drainage pipe and the bacterium distribution device, then reaches the lowest point of the discharging tube drainage pipe, and finally flows into a hydraulic unit by virtue of the discharging tube drainage pipe. When the pressure of the biogas in the fermentation area is decreased, most of the biogas fluid in the hydraulic unit is provided into the fermenting pipeline in one direction through the feeding tube drainage pipe and the bacterium distribution device, and some biogas fluid in the hydraulic unit is provided into the discharging tube through the discharging tube drainage pipe. Thus, the circular flow of the biogas fluid is completed.
NOVELTY - Producing marsh gas involves feeding raw material into feeding pipe (40) to produce marsh gas in fermentation system. The marsh gas is collected in fermentation zone, which is formed between adjacent block plates (34). When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (20) and drain pipe (44) to the lowest position.    USE - Method for producing marsh gas (claimed).    DETAILED DESCRIPTION - Producing marsh gas involves feeding raw material into feeding pipe (40) to produce marsh gas in fermentation system. The marsh gas is collected in fermentation zone, which is formed between adjacent block plates (34). When gas pressure is increased in fermentation system liquid is flowed in feeding pipe and discharge pipe. The liquid pressure is increased in feeding tube and then liquid is flowed into discharge pipe (20) and drain pipe (44) to the lowest position. When liquid pressure is reduced in fermentation system, liquid is flowed into feeding pipe, discharging pipe, drain pipe and reflux pipe to pipe (30) inside fermentation system. The liquid is collected into other fermentation system to obtain marsh gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of marsh gas production method.    Discharge pipe (20)    Pipe (30)    Block plates (34)    Feeding pipe (40)    Drain pipe (44)
NOVELTY - The new type utility claims a hydraulic crawler walking FORMULA a stacking machine frame, by two side plate and the connection plate make up of a door-shaped frame, the installation has a crawler bracket in two side upper door frame plate of the install crawler drive wheel has a front end crawler bracket, a speed reducer and a motor, a crawler driving wheel and a speed reducer connected, a speed reducer and a motor connected, installation has a crawler tensioning wheel in crawler bracket after the mounting has crawler supporting wheel in crawler bracket middle part, install crawler has a crawler driving wheel and a crawler tension wheel, a hydraulic motor through a pipeline and a control valve connected, a control valve and a pump connected, hydraulic pump and engine connected. The machine frame using a method a driving action of the two crawler, which not only is a no easy happen fault, and two strip crawler can independently carry out forward and backward, and no interference, the turning semi-diameter is small.
NOVELTY - The utility model is new type relates to organic fertilizer production equipment field, especially a plant organic fertilizer fermentation device, comprising a full-closed of a room, close the fermentation room is long strip type structure, a double end room is equipped with a delivery door has, in a double side lower end face of a room has set with supporting wall, the supporting wall through the whole fermentation room, is set on a supporting wall and the two side, and a free movement on a supporting wall, set has object carrier trolley on the bottom face between a supporting wall, a multi-carrier object trolley along a length direction side by side room of the fermentation room; at a top end is set with room has multiple air outlet pipe. The organic fertilizer fermentation device, wherein a matrix of a different order after entering into a room, and at last sequentially in a fermentation room a package using, for a process of matrix is more flexible and use performance is more excellent.
NOVELTY - Diagnostic kit comprises multiple compartments which can be separate and sealed, respectively, and drug in concentration of 0.25-0.4 mu g/cm2 bifenthrin, 0.4-0.5 mu g/cm2 bifenazate, 0.012-0.016 mu g/cm2 chlofenapyr, 0.15-0.0.25 mu g/cm2 cyenopyrafen, 2-3 mu g/cm2 endosulfan, 2.2-3.4 mu g/cm2 fenothiocarb, and 0.16-0.25 mu g/cm2 omethoate, stored in the each compartments.    USE - The kit is useful for determining drug susceptibility on Tetranychus urticae to control growth of Tetranychus urticae (all claimed).    ADVANTAGE - The kit determines drug susceptibility within 8 hours (claimed), and is environmentally friendly and economical.
NOVELTY - Producing enzyme composition, comprises (a) preparing first aged product by aging first mixture, (b) preparing second aged product by aging second mixture, (c) obtaining first aging solution and second aging solution by filtering the obtained first aged product and the second aged product, (d) producing mixed solution by mixing the obtained first aging solution and second aging solution, (e) aging the obtained mixed solution, and (f) culturing the aged mixed solution.    USE - The composition is useful in organic fertilizer (claimed).    ADVANTAGE - The composition produces organic fertilizer of high quality. The method ages for long period of time, and shortens fermentation period of the organic fertilizer.    DETAILED DESCRIPTION - Producing enzyme composition, comprises (a) preparing first aged product by aging first mixture containing Plantago asiatica, milk vetch root, ginseng, Korean Lespedeza, Amaranthus retroflexus, Solanum nigrum, bark of Ulmus davidiana, native mulberry, Setaria viridis, orostachys herba, Japanese hop and terra alba mixed in a weight ratio 1:1:1:1:1:1:1:1:1:1:1:1, (b) preparing second aged product by aging second mixture containing Schisandra, Actinidia arguta, persimmon, pear, prune and terra alba mixed in a weight ratio 1:1:1:1:1:1, (c) obtaining first aging solution and second aging solution by filtering the obtained first aged product and the second aged product, (d) producing mixed solution by mixing the obtained first aging solution and second aging solution, (e) aging the obtained mixed solution, and (f) culturing the aged mixed solution. An INDEPENDENT CLAIM is also included for enzyme composition prepared by the above method.
NOVELTY - Recovery of valsartan crude mother liquor comprises recycling solvent from valsartan crude mother liquor to obtain an oil; adding ester solvent and water, cooling, using alkali to adjust pH value to 10, transferring back to the acid pH value of 1-4, washing organic phase with water, drying and cooling to 20-30 degrees C, adding valine and continue cooling at 0-5 degrees C to crystallize, separating the solid, and drying to obtain valsartan crude product.    USE - Method for recovering valsartan crude mother liquor (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has low cost, good product quality, purity of not less than 99%, and yield of not less than 35%.
NOVELTY - Organic fertilizer comprises a mixture comprising manure (40-60 pts. wt.), crushed crop straw (40-60 pts. wt.), rapeseed cake (20-40 pts. wt.) and water (60-80 pts. wt.), organic manure fermentation broth, liquid discharge line agents, ascorbic acid, synergistic fertilizer, and soil water retention agent.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer ensures enhanced immunity of crop and is effective against fusarium wilt, verticillium wilt, blight, root rot, blight, anthracnose, vine column gray mold, and root diseases. The organic fertilizer reduces frequency of fertilizer application.    DETAILED DESCRIPTION - Organic fertilizer comprises a mixture comprising manure (40-60 pts. wt.), crushed crop straw (40-60 pts. wt.), rapeseed cake (20-40 pts. wt.) and water (60-80 pts. wt.), organic manure fermentation broth, liquid discharge line agents, ascorbic acid, synergistic fertilizer, and soil water retention agent. Ratio of mixture with organic manure fermentation broth, liquid discharge line agents, ascorbic acid, synergistic fertilizer, and soil water retention agent is (1:200-1:400 pts. wt.), (1:80-1:150 pts. wt.), (1:100-1:300 pts. wt.), (1:400-1:600 pts. wt.), and (1:80-1:150 pts. wt.) respectively. An INDEPENDENT CLAIM is included for a method for preparation of inorganic fertilizer, which involves:    (A) weighing animal manure, crop straw, and rapeseed cake;    (B) adding water to weighed ingredients;    (C) adding effective microbes to liquid mixture to carry out fermentation;    (D) adding Actinomycetes to the fermented product to carry out secondary fermentation;    (E) adding ascorbic acid to the fermented product to obtain a mixture;    (F) adding sodium nitrophenolate synergistic fertilizer to the obtained mixture;    (G) adding perlite to the obtained mixture; and    (H) drying the obtained product and palletizing to obtain organic fertilizer.
NOVELTY - A bio-organic fertilizer comprises 400-600 parts mass livestock manure, 200-400 parts mass poultry faeces, 100-200 parts mass mushroom residue, 50-100 parts mass coconut husk, 0.75-1.3 parts mass number 1 microbial inoculum (A) and 1.5-2.6 parts mass number 2 microbial inoculum (B).    USE - Bio-organic fertilizer (claimed).    ADVANTAGE - The bio-organic fertilizer does not contain pathogens and weed seeds, and is prepared with less pesticide residues. The fertilizer is easy to use and store. After administration, the fertilizer improves soil structure, soil fertility, growth of vegetables, and fruit quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of bio-organic fertilizer which comprises:    (1) forming layers of livestock manure, poultry faeces, mushroom residue and coconut husk with a width 1-3 m and height of 1-1.5 m;    (2) adding microbial inoculum number 1 to mushroom residue in a molar ratio of 1:5, mixing and spraying on the stack surface in a ratio of 1:1000;    (3) fermenting the stack with stirring, turning after the temperature is more than 60 degrees C every 4-6 days, maintaining at more than 60 degrees C to ferment for 15-20 days, reducing the temperature to 35-45 degrees C to complete aerobic fermentation,    (4) adding number 2 microbial inoculum in a ratio of 1:500 for anaerobic fermentation, stirring and fermenting for 6-8 days, the product of this invention is a    biological organic fertilizer.
NOVELTY - A bioorganic fertilizer comprises 30-40 pts. wt. pig manure, 20-35 pts. wt. plant rotten rice straw, 10-15 pts. wt. wheat bran, 5-10 pts. wt. clay, 5-10 pts. wt. humic acid, 2-5 pts. wt. urea, 5-10 pts. wt. composite microbial inoculum and 5-10 pts. wt. functional microbial agent.    USE - Bioorganic fertilizer (claimed).    ADVANTAGE - The bioorganic fertilizer is rich in nutritional value, and effectively improves physical and chemical properties of soil, and crop yield, and prevents physiological diseases of plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bioorganic fertilizer which comprises forming a stack of pig manure, rotten straw straw, wheat bran, clay and humic acid which is 2 m long, 1 m wide and 2 m high, spraying the microbial inoculum on the stack surface and adjusting the initial water content to 70% and the urea C/N ratio to 30:1, stirring to initiate fermentation, turning the stack every 4 days when the temperature is above 60 degrees C, fermenting for 15 days, cooling to naturally to 40 degrees C, adding functional microbial agent to ferment for 7 days to obtain the fertilizer, crushing, sieving, granulating, drying, cooling and packaging.
NOVELTY - A Trichoderma aculeatus T-1 strain (CGMCC 9722), is new.    USE - The T.aculeatus T-1 strain is useful for reducing and recycling organic waste or garbage, preferably for composting municipal, town and household garbage, dining or kitchen waste, vegetable and urban green waste and straw crop rich in cellulose and protein organic wastes, preparing organic fertilizer and producing high-yields of composite cellulose for degrading enzymes (all claimed). The strain is a biocontrol agent applied to crops to prevent diseases.    ADVANTAGE - The T.aculeatus T-1 is fast growing stain, has strong sporulation ability, tolerance to pH, converts variety of cellulose materials to substrate and improves the efficiency of waste degradation of cellulose-based material and quality of waste compost product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the strain.
NOVELTY - Preparation of biological growth-promoting agent involves collecting solids separated from kitchenware swill, removing oil from the surface of collected solid, centrifugal dewatering, dehydrating, precipitating, crushing, mixing with 5-8 wt.% corn flour and 42-50 wt.% water, placing the mixture inside a pressure cooker, maintaining at 111-122 degrees C and 0.048-0.11 MPa for 1-1.2 hour, adding 3-3.5 wt.% pancreatic digestive enzyme solution to obtained biological growth-promoting agent solution, stirring, reacting, concentrating, and measuring by physical and chemical indicators.    USE - Preparation of biological growth-promoting agent used in wastewater treatment.    DETAILED DESCRIPTION - Preparation of biological growth-promoting agent involves collecting solids separated from kitchenware swill, removing oil from the surface of collected solid, centrifugal dewatering, dehydrating, precipitating, crushing, mixing with 5-8 wt.% corn flour and 42-50 wt.% water, placing the mixture inside a pressure cooker, maintaining at 111-122 degrees C and 0.048-0.11 MPa for 1-1.2 hour, adding 3-3.5 wt.% pancreatic digestive enzyme solution to obtained biological growth-promoting agent solution, maintaining at 45-50 degrees C, stirring, reacting for 2-2.5 hours, adjusting pH of prepared stock solution at 5-5.5, concentrating, and measuring biological growth-promoting agent having ammonia nitrogen content of 5.75% or more, urea nitrogen content of 12.5% or more, nitrate content of 5.75 or more, chelated iron content of 0.1 or more, chelated manganese content of 0.05% or more and chelated zinc content of 0.05% or more by physical and chemical indicators. The pancreatic digestive enzyme solution contains 5-8 wt.% pancreatic digestive enzyme and 92-95 wt.% water. The pancreatic digestive enzyme has trypsin content of 1800 mu m/g or more, pancreatic amylase content of 21000 mu m/g or more and pancrelipase content of 12000 mu m/g or more.
NOVELTY - Organic fertilizer comprises 35-50 wt.% chicken manure, 8-15 wt.% calcium silicate powder, 8-15 wt.% fused calcium magnesium phosphate, 8-12 wt.% cow manure, 8-15 wt.% Chinese medicine residue, 4-6 wt.% humic acid, and 1-3 wt.% biological bacteria.    USE - The organic fertilizer is useful for rice growth (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising mixing chicken manure, cow manure, calcium silicate powder, fused calcium magnesium phosphate, Chinese medicine residue and humic acid, stirring, adding biological bacteria, maintaining moisture to 40-45%, fermenting for 15 days, turning, and fermenting for 10 days; carrying out aerobic fermentation by mixing fermented chicken manure, cow manure, calcium silicon powder, calcium magnesium phosphate, Chinese medicine residue and humic acid, maintaining water content to 20%, until there is no odor, discharging from the fermentation tower; crushing, screening, inspecting, and finally granulating into powder.
NOVELTY - Bio-fermented organic fertilizer comprises 105-120 pts. wt. deer manure, 38-44 pts. wt. goose dung, 22-26 pts. wt. peanut, 8-9 pts. wt. potassium alginate, 30-35 pts. wt potato starch, 25-30 pts. wt. castor, 33-38 pts. wt. medical stone powder, 12-15 pts. wt. ammonium hydrogen carbonate, 1-1.5 pts. wt. Geobacillus stearothermophilus, 0.8-1.2 pts. wt. plant Lactobacillus, 1.5-2 pts. wt. Bacillus pumilus and 1.2-1.4 pts. wt. Trichoderma viride and 1.2-1.4 pts. wt. antibacterial agent.    USE - As fertilizer for sugarcane.    ADVANTAGE - The fertilizer is easily absorbed by the plants, promotes the growth of sugarcane stem, increases sucrose content in sugarcane and improves the quality of cane juice.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the organic fertilizer, which involves weighing the above raw materials, adding 40 kg water to the materials, stirring uniformly, heating the mixture to 85-95 degrees C for 3-4 hours, then reacting the mixture for 25-30 days, inoculating the strain and processing the mixture at 29-38 degrees C for 3-5 days.
NOVELTY - Method of preparing Chinese herbal okra pest control solution involves mixing fructus toosendan, radix sophorae flavescentis, wood hellebore and Artemisia capillaries, crushing the raw materials, cleaning, drying, crushing and mixing stevia, pine, pine needles and seaweed in a weight ratio of 5:2:2:1, preparing plant straw powder, mixing all the components in a weigt ratio of 5:3:2 with 70% water, transferring the mixture to a container, then adding 3% molasses or sweetening material, stirring uniformly and fermenting the mixture for 8-10 days to obtain the product.    USE - Used for controlling okra insect pests.    ADVANTAGE - The method is simple, cost-effective and environmentally-friendly, and enables to obtain product with high-quality.
NOVELTY - A composite microbial fertilizer comprises 20-31 wt.% microbial agent, 5-15 wt.% biochar, 15-25 wt.% urea, 5-9 wt.% diammonium phosphate, 4-8 wt.% potassium dihydrogen phosphate, 5-10 wt.% potassium sulfate, 1-5 wt.% boric acid, 1-6 wt.% magnesium sulfate, 1-5 wt.% trace elements, 3-5 wt.% titanium dioxide, 5-10 wt.% Chinese medicine composition and 2-4 wt.% vinegar. The biochar is obtained by drying corn stalks at 70 degrees C, crushing, heating at 550 degrees C for 1.5 hours, cooling to room temperature, and sieving through 100 mesh.    USE - Composite microbial fertilizer is used for growing grapes.    ADVANTAGE - The composite microbial fertilizer has excellent physicochemical property, enables growth of grapes with high yield and quality, and is economical.    DETAILED DESCRIPTION - The microbial agent is obtained by fermenting Bacillus subtilis, Bacillus cereus, Bacillus pumilus and Bacillus megaterium with ratio of 1:1:0.5:0.8, mixing, and grinding. The biochar is obtained by drying corn stalks at 70 degrees C, crushing, heating at 550 degrees C for 1.5 hours, cooling to room temperature, and sieving through 100 mesh. The trace element contains amino acid chelated zinc, amino acid chelated iron, amino acid chelated manganese and/or amino acid chelated boron with weight ratio of 1:1-1.2:0.9-1.2:1.5. The traditional Chinese medicine composition contains ginger leaves, pyrethrum and neem with weight ratio of 1:1-2:1-1.5. The composite microbial fertilizer is obtained by mixing raw material, heating at 120-130 degrees C, cooling at room temperature, precipitating, filtering, distilling with vinegar, milling, sieving through 100 mesh, evenly mixing, granulating, drying, screening, and packing.
NOVELTY - The system has a pipeline which is equipped with a lever and is connected with gas-guide tube and second level fermentation unit. A feedstock tube and discharging tube are inserted in second level pipe (24). A blocking plate is arranged in second level pipe. A discharging pipe (52,54) is provided with one-way valve for discharging biogas into feedstock pipe. The water level of feedstock pipe (42) is higher than that of discharge pipe. A level hydraulic pipe is connected with a third guide water pipe (32) set with one-way valve for discharging biogas slurry into first level pipe (22).    USE - Secondary synchronization methane fermentation system.    ADVANTAGE - The efficiency of fermentation system is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of secondary synchronization methane fermentation system.    Primary system (10)    First level pipe (22)    Second level pipe (24)    Third guide water pipe (32)    Feedstock pipe (42)    Discharging pipe (52,54)
NOVELTY - Diatom fixed carbon dioxide processing of oil field sewage comprises taking air as gas source, performing flotation, degreasing oxygenizing, biological contact oxidizing, adding nitrogen and phosphorus nutrients, aerobic biological processing to total carbon content of less than 60 mg/L and chemical oxygen demand content of less than 150 mg/L, directly flowing into track-type micro-algae culture system with 3-15% carbon dioxide flue gas, diatom growing, purifying, filtering by diatomite, collecting diatom, pressing and deoxidizing.    USE - Method for diatom fixed carbon dioxide processing of oil field sewage (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of diatom fixed carbon dioxide processing of oil field sewage (Drawing includes non-English language text).
NOVELTY - Selective hydrogenation of lightweight eicosapentaenoic fraction comprises performing selective hydrogenation of lightweight eicosapentaenoic fraction in presence of hydrogen and partially vulcanized nickel/aluminum oxide as catalyst in a hydrogenation catalyst fixed bed, where in the reaction process, the partial hydrogenated reaction product is recycled as solvent, mixed with hydrogenated lightweight eicosapentaenoic fraction and added to the hydrogenation catalyst fixed bed, the volume liquid hourly space velocity is 1-20/hour and the system pressure is 1-3 MPa.    USE - The method is useful for selective hydrogenation of lightweight eicosapentaenoic fraction (claimed).    ADVANTAGE - The method reduces energy consumption, is economical, and has economic benefits.    DETAILED DESCRIPTION - Selective hydrogenation of lightweight eicosapentaenoic fraction comprises performing selective hydrogenation of lightweight eicosapentaenoic fraction in presence of hydrogen and partially vulcanized nickel/aluminum oxide as catalyst in a hydrogenation catalyst fixed bed, where in the reaction process, the partial hydrogenated reaction product is recycled as solvent, mixed with hydrogenated lightweight eicosapentaenoic fraction and added to the hydrogenation catalyst fixed bed, the volume liquid hourly space velocity is 1-20/hour, the system pressure is 1-3 MPa, the feeding temperature is 20-100 degrees C and the molar ratio of total amount of alkyne and hydrogen and lightweight eicosapentaenoic fraction to hydrogenated in diene is (1-1.8):1.
NOVELTY - The anti-freezing hydrogen oxygen generating machine has a housing unit (1) that is provided with a working liquid chamber to which an electrolytic groove (12) is provided. A baffle plate is provided in a cover structure (13). An electrode plate (21) is connected in series with an electric joint (23) to which a cover chamber (131) is provided.    USE - Anti-freezing hydrogen oxygen generating machine.    ADVANTAGE - The freezing of the hydrogen oxygen generating machine to produce hydrogen by electrolysis of ambient temperature is avoided. The practicability of the anti-freezing hydrogen oxygen generating machine is increased greatly. The anti-freezing hydrogen oxygen generating machine is easy to operate at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of anti-freezing hydrogen oxygen generating machine.    Housing unit (1)    Electrolytic groove (12)    Cover structure (13)    Electrode plate (21)    Electric joint (23)    Cover chamber (131)
NOVELTY - The method involves taking a raw material feedstock into a feedstock tube (42). The marsh gas production and accumulation in a cell is performed of the side wall of inlet and outlet. The marsh gas is accumulated in a cell discharge pipe side wall. The marsh gas is passed within a time of the biogas slurry in the level discharging tube through a guiding pipe. The methane is generated using marsh gas.    USE - Tower-type multi-level interactions promote feedstock ultra-efficient fermentation system methane producing method.    ADVANTAGE - The generation of the methane is enhanced efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the ultra-efficient fermentation system.    Ultra-efficient fermentation system (10)    Raw material (12)    Feedstock tube (42)    Discharge pipe (44)    Baffle plate (45)
NOVELTY - The reduction method involves bonding carbon dioxide with an activator so as to form an intermediate. An electrical potential is applied to the intermediate under conditions that cause reduction of the carbon dioxide bound in the intermediate. The reduction of carbon dioxide in the intermediate generates a liquid organic fuel, gaseous organic fuel and methane. Carbon dioxide is linear before bonding with the activator but has a bent configuration in the intermediate.    USE - Reduction method of carbon dioxide for solar fuels generation.    ADVANTAGE - Protects the underlying electrode from competing reactions such as oxygen reduction and/or protects the electrode from highly acidic environments. Enables to exchange ions sufficiently to maintain a desired power of hydrogen (pH) gradient and separate the reaction products sufficiently to prevent from re-combining. Allows efficient conversion of carbon dioxide to a particular one of the fuels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reduction device of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic diagram of an electrolysis system.    Cathodes (10)    Anodes (14)    Vessel (16)    Electrolyte (18)    Voltage source (20)
NOVELTY - The electrolyzed water generating apparatus has an electrolytic cell that forms an electrolysis chamber, when two case elements (50,60) are adhered. Several protrusions (53,63) are arranged in matrix form in vertical direction (V) and horizontal direction (H) to the inner surface of the case elements and are contacted to anode electric power feeding portion and cathode electric power feeding portion. The protrusions are positioned adjacent to each other at the distance nearest to the vertical direction and are adjoined to each other at the distance nearest to the horizontal direction.    USE - Electrolyzed water generating apparatus for electrolyzing water and producing electrolytic hydrogen water for household cooking and hemodialysis applications.    ADVANTAGE - The electrolyzed water generating apparatus that increases the dissolved hydrogen concentration easily is provided.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective views of the cast elements.    Case elements (50,60)    Mating faces (51,61)    Protrusions (53,63)    Horizontal direction (H)    Vertical direction (V)
NOVELTY - The method involves utilizing a biomass fuel feeding biomass gasification furnace for perform gasification furnace pyrolysis gasification process. Hot fuel gas cleaning operation is performed. The cleaned hot fuel gas is entered into a biomass burner. Hot fuel gas combustion operation is performed. The biomass fuel gas and combustion-supporting hot air are mixed in the biomass burner. The combustion-supporting air is introduced into a biomass dedicated burner that is fixed with an air heat exchanger to realize heat exchanging operation with temperature of about 150-200 degrees centigrade.    USE - Clean wind hot biomass fuel gas combustion product manufacturing method.    ADVANTAGE - The method enables realizing clean wind hot biomass fuel gas product combustion operation so as to obtain uniform a clean wind hot biomass fuel gas combustion product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a clean wind hot biomass fuel gas combustion product. '(Drawing includes non-English language text)'
NOVELTY - Insulation board that is developed with the use of green plant leaves after drying them and pulverizing them, comprises polyester resin with help of cobalt and catalyst or biodegradable materials as binders.    USE - The insulation board is useful as insulating material for saving energy or for preventing heat transfer.    ADVANTAGE - The insulation boards from banana leaf pulverized powder present a good opportunity for use as insulating material for energy saving while also being environment-friendly. Additionally, the insulation boards can be used to produce furniture with an advantage to get rid of weeds. The material can be used to prevent heat transfer, and thus increase operating efficiency, from pipes, ducts, or other parts of a power system to its surroundings. The material also can be used to prevent or reduce damage to equipment from exposure to fire or corrosive atmospheres.
NOVELTY - Catalyst represents mesoporous silica gel (Ssp.=100-300 m2/g) with applied on its surface silver in a quantity of 1-8% of the catalyst weight, which is in a highly disperse (nanosize) condition with the average size of particles of 2.8 nm. The claimed catalyst contains one or several oxides from CeO2, MnOx, ZrO2, FeOx with their summary content of 0.5-8% of the catalyst weight. The claimed invention also relates to methods of obtaining acetaldehyde and acetaldehyde together with hydrogen.    USE - Chemistry.    ADVANTAGE - Catalyst has high activity in the transformation of ethanol into acetaldehyde.3 cl, 3 dwg, 3 tbl, 7 ex
NOVELTY - This utility new type claims a domestic garbage into fuel A a device, comprising machine frame, a motor, a speed reducer, a driving gear, a driven gear, a driving shaft, a driven shaft, a driving roller and a driven roller, a driving roller and a driven roller respectively fixed set at the driving shaft and the driven shaft a, the driving shaft and driven shaft are set with a machine frame a, the driving gear and driven gear respectively set in a driving shaft and a driven shaft of the driving gear and the driven gear is mesh, a driving roller and a driven roller which contact the driving uniform is provided with semi-spherical concave upper roller, a driven roller and a driving roller provided with a corresponding and equal size of semi-spherical; the driving shaft speed reducer, the speed reducer connect a electric machine. After using a technology plan, this utility new type A a domestic garbage into fuel a device, structure is simple, the cost is low, use is convenient, production efficiency is high, is a use of waste, the waste is valuable provide a powerful technology support.
NOVELTY - Treating a fermentation stream to remove dissolved gases, comprises: (a) obtaining a fermentation stream comprising water, at least one fermentation product and dissolved gases; (b) continuously or semi-continuously sonicating the fermentation stream to generate, in the fermentation stream, acoustically cavitated gases comprising at least a portion of the dissolved gases; and (c) releasing at least a portion of the acoustically cavitated gases from the fermentation stream, thus forming a treated fermentation stream.    USE - The method is useful for treating a fermentation stream to remove dissolved gases (claimed).    ADVANTAGE - The method: is capable of releasing at least 75%, preferably at least 85% of the dissolved gases from the fermentation stream (claimed); positively impacts downstream operations and product quality by removing dissolved gases; is economical; preserves the yield of the fermentation product; allows production of ethanol (or other product) at a higher pH (such as greater than or equal to 6), due to reduced formation potential for carbonic acid or other acids derived from other gases; and improves operations of the distillation or stripping column such as increased capacity, reduced maintenance requirements or other benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for removing dissolved gases from a fermentation stream, comprising: a sonication unit for continuously or semi-continuously sonicating a fermentation stream comprising water and dissolved gases, to generate acoustically cavitated gases comprising at least a portion of the dissolved gases; and a separation unit, in operable communication with the sonication unit, configured for releasing at least a portion of the acoustically cavitated gases from the fermentation stream.
NOVELTY - An isolated ionic liquid-tolerant beta -glucosidase having at least 70% or at least 90% identity to an amino acid sequence of one of fully defined 425-933 amino acids (SEQ ID NOS: 1-15) given in the specification, is new.    USE - The isolated ionic liquid-tolerant beta -glucosidase or isolated ionic liquid-tolerant endoglucanase is useful for increasing yield of soluble sugar from biomass (claimed).    ADVANTAGE - Provided are ionic liquid-tolerant and thermo-tolerant cellulase enzymes, including enzymes whose activities are stimulated in the presence of ionic liquids which can be used in saccharification reactions to obtain sugars from lignocellulosic biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a composition comprising a beta -glucosidase or endoglucanase and an ionic liquid;    (2) an isolated ionic liquid-tolerant endoglucanase having at least 70% identity or at least 90% identity to an amino acid sequence of one of fully defined 260-614 amino acids (SEQ ID NOS: 16-26) given in the specification;    (3) a recombinant host cell comprising a heterologous nucleic acid sequence encoding the ionic liquid-tolerant beta -glucosidase or the ionic liquid-tolerant endoglucanase;    (4) a method of producing an ionic liquid-tolerant beta -glucosidase;    (5) a method of producing an ionic liquid-tolerant endoglucanase comprising culturing the recombinant host cell under conditions in which endoglucanase is expressed; and    (6) a method of increasing yield of soluble sugar from a biomass comprising incubating biomass with the ionic liquid-tolerant beta -glucosidase or with the ionic liquid-tolerant endoglucanase in an enzymatic hydrolysis reaction.
NOVELTY - The process involves condensing a vapor phase product (6) to provide a liquid phase product comprising fully deoxygenated hydrocarbon liquid and aqueous material and separating the liquid phase product from a gas phase product. The aqueous material is removed from the fully deoxygenated hydrocarbon liquid. A portion of the fully deoxygenated hydrocarbon liquid is hydroprocessed in a hydroprocessing reactor vessel in the presence of hydrogen (27) and hydroprocessing catalysts comprising a reduced metal on a solid support to provide an upgraded liquid hydrocarbon stream.    USE - Process for producing liquid hydrocarbon products from solid biomass and residual waste feedstocks e.g. feedstocks containing waste plastics and biomass feedstocks containing lignocellulose such as woody biomass, agricultural residues, forestry residues, residues from wood products and pulp and paper industries and sorted municipal solid waste.    ADVANTAGE - The process enables providing conversion of lignocelluloses-containing biomass into the liquid hydrocarbon products in which the liquid hydrocarbon products meet petrol and diesel specifications in locations worldwide. The process enables producing the liquid hydrocarbon products from the solid biomass and residual waste feedstocks in an effective manner.    DETAILED DESCRIPTION - The gas phase product comprises hydrogen, carbon monoxide, carbon dioxide and C1-C3 gases.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a structure illustrating a process for producing liquid hydrocarbon products from solid biomass and residual waste feedstocks.    Vapor phase product (6)    Hydroconversion reactor (7)    Pump (24)    Fixed-bed hydrogenation reactor (26)    Hydrogen (27)    Hydrogen stream (29)
NOVELTY - Organic fuel from household waste comprises mixture comprising two ingredients containing equivalent elements of carbon, nitrogen, oxygen and hydrogen obtained by mechanical mixing quantitatively.    USE - Used as organic fuel.    ADVANTAGE - The organic fuel achieves more energy from the waste through its drying, crushing and mechanical mixing with high-carbon natural turf, to the level of alternative fuels (claimed).
NOVELTY - Controlling biogas plant comprises setting a preset value for gas flow rate, with which the gas is to be fed into a gas utilization device, determining a substrate parameter of the substrate, supplying the substrate into a fermenter by a supply device, determining an expected value of gas flow rate by an optical measuring instrument, which can be produced with the substrate based on pre-determined substrate parameters, comparing the set value with the expected value, and controlling the supply of the substrate based on the result of comparison.    USE - The method is useful for controlling a biogas plant (claimed).    ADVANTAGE - The device: has high efficiency, ensures rapid pre-heating to increase the efficiency of the subsequent method in the reactor; and consumes less energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for controlling biogas plant comprising an optical measuring device, a data processing device connected with the optical measuring device for processing data, and a designed data processing device to determine an expected gas flow rate value based on the determined substrate parameter, to compare the expected and desired gas flow rate values and to supply the substrate in response to the comparison result. The optical measuring device is designed to determine the substrate parameters to be fed into a fermenter of the biogas plant.    DESCRIPTION OF DRAWING(S) - The figure shoes a schematic representation of the device for controlling biogas plant (Drawing includes non-English language text).
NOVELTY - The digester (100) has digester main portion (1) that is made of steel plate. A heating apparatus (2) is provided to heat the sludge injected into digester main portion. A heat insulating structure (5) is provided in bottom portion of digester main portion. A support material (6) is provided to support the load of sludge. The heat insulating material such as polystyrene foam is filled between support materials.    USE - Steel plate made digester used for performing anaerobic fermentation process of organic waste such as sewage sludge and foodstuff waste material.    ADVANTAGE - The intensity of steel plate made digester is improved by providing heat insulating structure in bottom portion of digester main portion. The steel plate made digester is maintained effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the steel plate made digester.    Digester main portion (1)    Heating apparatus (2)    Heat insulating structure (5)    Support material (6)    Steel plate made digester (100)
NOVELTY - Biomass gasification-combustion unite circulation system. The biomass gasification furnace is main device of gasification reaction. Using rate of fuel gasification combustion system using at present is low, heat can not full use and easy to pollute atomphere. The utility model is new type is composed of comprising: bin (1), a fuel bin and fuel conveyor (2) connected with the fuel conveyor and fuel feeding device (3) is connected with the fuel feeding device mounted in gasification furnace (4), the gasification furnace and sedimentation separator (5) is connected with the sedimentation separator and humidifier (9) is connected with the humidifier respectively and gasification blower (10), a plate tube type heat exchanger (11) is connected with the gasification furnace through fume pipeline and fuel gas boiler (15) is connected with the fuel gas boiler and coal economizer (16) is connected with the coal economizer and bag-type dust remover (17) connected with, a bag-type dust collector and exhaust fan (18) is connected, mounted in boiler chimney (20) above. The utility model is new type used for biomass gasification and combustion.
NOVELTY - The reactor has a biomass dosing device (1) arranged above a heating body (12), which is arranged within a gasification chamber (8), where a lower portion of the gasification chamber is opened into a collecting basket (11) of a carbon component. The heating body comprises a thermal graphite area (3) with an electric current supply (2). A graphite sheet (4) is provided with a graphite insulation part (5) and arranged on a back part of the graphite area. A back part of the graphite insulation part is attached to a reactor wall (6). The gasification chamber is provided with a gas outlet (9).    USE - Reactor for quick thermal decomposition of biomass with absence of oxygen.    ADVANTAGE - The reactor ensures the quick thermal decomposition of biomass with absence of oxygen in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reactor for quick thermal decomposition of biomass with absence of oxygen.    Biomass dosing device (1)    Electric current supply (2)    Thermal graphite area (3)    Graphite sheet (4)    Graphite insulation part (5)    Reactor wall (6)    Gasification chamber (8)    Gas outlet (9)    Collecting basket (11)    Heating body (12)
NOVELTY - Polyolefin ketone having sulfonated side chain (I), is new.    USE - (I) is useful to produce water treatment membrane for water treatment module, and polymer electrolyte membrane for producing fuel cell (all claimed).    ADVANTAGE - (I) provides excellent heat-resistant, proton conductivity, electrochemical stability at high temperature and mechanical strength to water treatment membrane, and is economical.    DETAILED DESCRIPTION - Polyolefin ketone having sulfonated side chain of formula (I), is new.    n = 4000-13000; and    m = 400-6500.    INDEPENDENT CLAIMS are also included for:    (1) preparation of (I);    (2) water treatment membrane comprising a support, and a polymer membrane containing (I), and formed on one or both surfaces of the support; and    (3) producing polymer electrolyte membrane, comprising (a) dissolving (I) into solvent to obtain a mixed solution, (b) casting the mixed solution on substrate to obtain an electrolyte membrane, and (c) washing and drying the electrolyte membrane.
NOVELTY - Making devices for repulsion and/or elimination of harmful pests including insects and mites, comprises: preparing a bath comprising a mixture of essential oils to effect repulsion and/or elimination in relation the harmful insects; impregnating wooden parts with the mixture by immersion in the bath for 1-3 weeks; removing the wooden parts out of the bath and draining; surface drying the wooden parts for 6-8 hours; and hermetic packaging the mixture impregnated and surface dried wooden parts.    USE - The method is useful for making devices for repulsion and/or elimination of pests including insects and mites from wood, which is natural wood of cedar, fir or pine (all claimed).    ADVANTAGE - The method provides the devices by utilizing natural essential oils and non-chemical treatment methods, hence safe and environmentally friendly.
NOVELTY - A catalyst comprises active metals (a) comprising metal (a1) chosen from palladium and/or platinum, and metal (a2) chosen from copper, iron, nickel, zinc, silver, chromium and/or tin, and a modified support (b). The modified support comprises a support material (b1) chosen from silica, silica/alumina, pyrogenic silica, high purity silica, and/or carbon, and support modifiers (b2) comprising 0.2-10 wt.% modifier (b21) chosen from oxides of cobalt, and 0.2-25 wt.% modifier (b22) chosen from alkaline-earth metal oxides or metasilicates of alkaline earth metals.    USE - Catalyst is used in manufacture of ethanol (claimed). Uses include but are not limited to fuel, pharmaceutical products, cleansers, sanitizers, hydrogenation transport or consumption, source material for manufacture of ethyl acetate, aldehydes, butanol.    ADVANTAGE - The catalyst has excellent stability and economically provides ethanol.    DETAILED DESCRIPTION - A catalyst comprises active metals (a) comprising metal (a1) chosen from palladium and/or platinum, and metal (a2) chosen from copper, iron, nickel, zinc, silver, chromium and/or tin, and a modified support (b), where the active metals are provided on the modified support. The modified support comprises a support material (b1) chosen from silica, silica/alumina, pyrogenic silica, high purity silica, and/or carbon, and support modifiers (b2) comprising 0.2-10 wt.% modifier (b21) chosen from oxides of cobalt, and 0.2-25 wt.% modifier (b22) chosen from alkaline-earth metal oxides or metasilicates of alkaline earth metals. The content of metal (a1) is less than 1 wt.%, and the total content of metals (a1) and (a2) is 0.1-10 wt.% with respect to total weight of the catalyst. An INDEPENDENT CLAIM is included for manufacture of ethanol, which involves contacting feed stream comprising acetic acid and/or ethyl acetate, and hydrogen in reactor in presence of a catalyst.
NOVELTY - The new type utility claims one kind to have water vapour as gasification medium of waste plasma gasification furnace, comprising upper part of garbage gasification room and lower part of high temperature water steam generating room, a garbage gasification room and high temperature water steam generating room set with gap arranged between the water cold furnace arch, a water cold furnace arch for garbage gasification room and high temperature water steam generating room; the high temperature water steam generating wall in the circumferential direction arranged two room of plasma torch, using low temperature water steam as working gas and plasma torch, the utility new type using plasma gasification, steam for gasification reaction supply have one of high temperature, environment, material heating speed is fast, reaction speed is fast, it is set with the high processing efficiency, also can happen some can not happen in normal gasification under the reaction condition.
NOVELTY - Magnetizable hydrothermal carbonization biocoal, comprises an organic phase comprising elemental carbon, and an inorganic magnetizable phase comprising at least one inorganic magnetizable component. The organic phase surrounds the inorganic phase.    USE - The magnetizable hydrothermal carbonization biocoal is useful for immobilizing enzymes, microbial cells and/or microorganisms, as process aid for concentrating and purifying liquids and gases, as process aid during fermentation of nitrogen-containing biomass, as process aid in producing biogas in biogas reactors, as process aid for purifying biogas and/or as a support for biofilms (claimed).    ADVANTAGE - The magnetizable hydrothermal carbonization biocoal can be produced in simple and cost-efficient manner, and adsorbs contaminants e.g. ammonia from fermentation liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the magnetizable hydrothermal carbonization biocoal, comprising providing a pressure container, filling the pressure container with water and biomass, adding inorganic magnetizable phase, heating the container at a pressure of 1-8 MPa to 160-280 degrees C, and separating the obtained hydrothermal carbonization biocoal from the production liquid.
NOVELTY - The reactor has an assistant reaction room (2) partitioned into a separating room (5) and a pre-heating room (6), where a bottom part of the pre-heating room is provided with a funnel. The funnel is connected with a fan (8). A middle part of the separating room is mounted with a discharge cylinder (9). A bottom end of the discharge cylinder is connected with a middle part of a middle partition wall (4). The discharge cylinder is connected with an inclined plate (10). A lower part of the inclined plate is connected with the discharge cylinder that is provided with an exhaust port (11).    USE - Biomass-coal section fluidization bed type reactor.    ADVANTAGE - The reactor is stable.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass-coal section fluidization bed type reactor.    Assistant reaction room (2)    Middle partition wall (4)    Separating room (5)    Pre-heating room (6)    Fan (8)    Discharge cylinder (9)    Inclined plate (10)    Exhaust port (11)
NOVELTY - Chemical sewage treatment comprises disposing wastewater into bioreactor, and adsorbing Klebsiella pneumoniae on bacterial carrier, and treating for 0.5-72 hours.    USE - Chemical sewage treatment used for removing Klebsiella pneumoniae (claimed).
NOVELTY - The method involves taking mattress prepared material, where mattress prepared material comprises sawdust and rice hull at volume ratio of 4:6. The mattress prepared material is added with water and enzyme to obtain mixture. A mixture fermentation process is performed at temperature of 30-70 degrees Celsius to obtain a fermentation bed product, where thickness of the fermentation bed product is 20-45 cm and thickness of a rice shell layer is 1-2cm.    USE - Method for manufacturing a fermentation bed for livestock and poultry.    ADVANTAGE - The method enables providing controlling function of discharge of ammonium and hydrogen sulfide equal harmful gas so as to reduce harmful gas dangerous to the livestock. The method enables avoiding need of livestock and poultry excrement cleaning process in a cultivation shed, thus saving labor force and cultivation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a fermentation bed manufacturing method. '(Drawing includes non-English language text)'
NOVELTY - Wastewater microbial deodorizing device comprises large pool (1), pool (2), and small pool (3). Front end of large pool is provided with inlet (4), and small pool is provided with outlet (5). Large pool, pool, and upper part of small pool are provided with through holes. Inlet is provided with filters. Large pool is provided with pump and microbial deodorant feed tank near the top of the inlet.    USE - Wastewater microbial deodorizing device used for processing sweet potato waste water (claimed).    ADVANTAGE - The wastewater microbial deodorizing device is simple and cost-effective.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of wastewater microbial deodorizing device.    Large pool (1)    Pool (2)    Small pool (3)    Inlet (4)    Outlet (5)
NOVELTY - The method involves separating carbon dioxide from biogas by washing with a washing solution, and regenerating the washing solution in a regeneration column (6) by desorption of carbon dioxide. The regenerated washing solution is re-used for washing the biogas. The regenerated washing solution or the desorbed carbon dioxide of the washing solution saturated with water is cooled by heat exchange with a flow, where the flow is selected in such a way that recovered heat is used in another device e.g. biogas producing digester.    USE - Method for treatment of biogas obtained from fermentation of organic wastes of plant or animal origin and from landfills, sewage treatment plants or agricultural sources.    ADVANTAGE - The method enables washing and regenerating the washing solution with amines in an efficient manner by consuming less energy without increasing cost of the washing solution or facility. The method enables eliminating carbon dioxide from biogas, which provides thermal energy to a process requiring heat input such as biogas production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for production and treatment of a biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for production and treatment of a biogas.    Ducts (1, 3-5)    Regeneration column (6)    Heat exchangers (8, 10)    Filtration unit (11)    Condenser (12)
NOVELTY - A small and medium sized boiler exhaust gas denitration method involves mixing nitrogen oxide-containing exhaust gas with reducing gas, and putting the mixed gas into an electrode region or electrode plasma reactor apparatus. The reducing gas molecules are activated, and redox reaction is performed on the reaction product containing harmful gases such as carbon dioxide.    USE - Method for denitration of small and medium sized boiler exhaust gas that is utilized in the treatment of industrial furnaces or marine engine exhaust applications (claimed).    ADVANTAGE - The method enables realizing denitration of small and medium sized boiler exhaust gas in a simple and economical manner with high denitration efficiency and wide application range, and without requiring additional heating system.
NOVELTY - Biodiesel preparation involves removing dirt and solid substances and then heating at 70-80 degrees C to obtain oil preprocessing liquid. The oil preprocessing liquid is heated with 0.5-0.8% sulfuric acid with stirring uniformly at 65-75 degrees C for 8-12 hours, and then kept for layering to obtain preprocessing cleaning liquid. The oil pre-processing cleaning liquid is transferred in a reaction kettle with 30-40% methyl alcohol with uniform mixing at 100-110 degrees C, and then mixed with 0.1-0.2% phosphate and 1-2% sodium hydroxide for 2-4 hours.    USE - Method for preparing biodiesel by using cooking oil as raw material (claimed).    ADVANTAGE - The method prepares biodiesel in a simple and cost-effective manner with high yield.    DETAILED DESCRIPTION - Biodiesel preparation involves removing dirt and solid substances and then heating at 70-80 degrees C to obtain oil preprocessing liquid. The oil preprocessing liquid is heated with 0.5-0.8% sulfuric acid with stirring uniformly at 65-75 degrees C for 8-12 hours, and then kept for layering to obtain preprocessing cleaning liquid. The oil pre-processing cleaning liquid is transferred in a reaction kettle with 30-40% methyl alcohol with uniform mixing at 100-110 degrees C, and then mixed with 0.1-0.2% phosphate and 1-2% sodium hydroxide for 2-4 hours. The resulting reaction mixture is treated 2-3% aluminum chloride and 0.05-0.1% polyacrylamide at 95-100 degrees C for 10-15 minutes to form biodiesel.
NOVELTY - Biodiesel separation involves performing esterification and alkylation simultaneous for upgrading oil by distillation to collect low boiling point solvent and esters. The resulting mixture is treated through vacuum distillation at 50-110 degrees C for 0.5 hour for removing water phase, where vacuum distillation extraction is carried out for isolating biodiesel.    USE - Method for separating biodiesel (claimed).    ADVANTAGE - The method separates biodiesel in a simple manner with improved effectiveness.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the biodiesel separation method. (Drawing includes non-English language text).
NOVELTY - Biodiesel production involves using waste oil obtained after pretreatment of vinegar slurry and cation resin in steam column during esterification reactions conducted with methanol gas and free fatty acids. The free fatty acids and fatty acid methyl ester give a crude biodiesel. The formed crude biodiesel undergoes enzyme catalyzed esterification reaction with methanol gas to give another crude biodiesel. The formed crude biodiesel is separated through sedimentation to obtain a crude refined biodiesel and glycerol.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces biodiesel in a simple and cost-effective manner by using high activity catalyst and without changing the catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the biodiesel production method. (Drawing includes non-English language text).
NOVELTY - Biodiesel production involves taking as catalyst, and readily available vegetable oils (containing a large amount of fatty acids) as starting materials. The reaction is carried out in an alcohol solvent at 100 degrees C to get an esterified product (II).    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces biodiesel in a simple, cost-effective and eco-friendly manner with high yield under mild reaction condition.    DETAILED DESCRIPTION - Biodiesel production involves taking Cp2Zr(H2O)3(OSO2C8F17)2asteriskTHF of formula (I) as catalyst, and readily available vegetable oils (containing a large amount of fatty acids) as starting materials. The reaction is carried out in an alcohol solvent at 100 degrees C to get an esterified product of formula R2COOR1 (II).    R1 and R2=alkyl or aryl group.
NOVELTY - A malt cooking waste heat utilization system comprises boiler (1), steam condenser (2), energy storage tank (3), juice pre-cooler (4), condensed water cooler (5), hot water circulation pump, condensed water tank, water circulation pump, plate-type heat exchanger, and washing unit.    USE - Malt cooking waste heat utilization system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of malt cooking waste heat utilization system.    Boiler (1)    Steam condenser (2)    Energy storage tank (3)    Juice pre-cooler (4)    Condensed water cooler (5)