NOVELTY - A gas diffusion electrode comprises gas permeable layer(s) providing a gas channel, and a primary conductive layer on primary side of the gas diffusion electrode.    USE - Gas diffusion electrode is used for electro-synthetic/electro-energy cell e.g. reversible fuel cell e.g. alkaline fuel cell e.g. alkaline water electrolyzer to produce chlorine, hydrogen peroxide, fuels from carbon dioxide, ozone, caustic, potassium permanganate, chlorate, perchlorate, fluorine, bromine and persulfate, acid fuel cell, and chloroalkali cell used in modular reactor used for on-site operation at location where reactor's products are required by user (all claimed).    ADVANTAGE - The gas diffusion electrode provides flexible and spiral-wound flat layer-arranged cell. The reactor or cell arrangement provides improved or maximum density of construction and enables economical deploying of gas diffusion electrodes in an electrochemical cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electro-synthetic or electro-energy cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen-oxygen or methane-oxygen fuel cell.    Central water reservoir (2300)    Water-free hydrogen entry chamber (2320)    Anode electrode (2340)    Catalyst (2350)    Electrical power output (2360)
NOVELTY - A feed composition or feed additive is used for reducing formation of ruminants and/or improving ruminant performance of methane emanating from digestive activities in which feed composition or additive contains p-nitroaniline derivative or its salt.    USE - Use of feed composition or feed additive for reducing formation of ruminants and/or improving ruminant performance of methane emanating from digestive activities (claimed).    ADVANTAGE - The feed composition or additive improves feed conversion ratio, reduces feed intake, improves weight gain, and/or improves carcass or milk yield, contributing to the improvement of ruminant performance.    DETAILED DESCRIPTION - A feed composition or feed additive is used for reducing formation of ruminants and/or improving ruminant performance of methane emanating from digestive activities in which feed composition or additive contains p-nitroaniline derivative of formula (I) or its salt.    R1,R2=H, Me, or -CH2R3;    R3=(cyclic) 1-8C hydrocarbon optionally substituted by 1-3 groups e.g. -OH, -NH2, or -COOH provided that 1 or 2 of the C atoms in the 1-8C hydrocarbon is optionally substituted by N or O, and greater than or equal to 1 organic molecule is substituted at any position with greater than or equal to 1 nitrooxy or its salt as defined by formula O2N-O-Y' (II);    Y'=organic molecule of formula CaHbOdNeSg;    a=1-25;    b=2-51;    d=0-8;    e=0-5; and    g=0-3.    INDEPENDENT CLAIMS are included for:    (1) feed composition or feed additive comprising p-nitroaniline derivative or its salt and greater than or equal to 1 organic molecule or its salt; and    (2) reduction of production of methane emanating from digestive activities of ruminants and/or improvement of ruminant animal performance which involves orally administering sufficient amount of feed composition or feed additive which comprises greater than or equal to 1 p-nitroaniline derivative or its salt to the animal.
NOVELTY - Method for producing fertilizer, involves (a) collecting lawn grass, separating sand and lawn grass, and washing the lawn grass, (b) grinding the separated sand and lawn grass, and fermenting the ground lawn grass, and (c) mixing with auxiliary materials.    USE - The method is useful for producing fertilizer (all claimed).    ADVANTAGE - The produced fertilizer is environmentally-friendly.
NOVELTY - The combustion wooden material has a depression portion (2) that is formed in the upper portion of the log (1) that crosses and runs through the depression portion. A cross-shaped communication channel (4) is provided more than the depth of the depression portion and less than the length of the log. The uneven-shaped groove pattern (3) is provided to the wall surface of the depression portion.    USE - Combustion wooden material used as heat source of illumination, cooking, and heating at camp and during disaster.    ADVANTAGE - The ignition from the convex portion of the uneven-shaped groove pattern of the depression portion wall surface to the log starts easily, when an ignition material is arranged in the depression portion,. The initial stage ignition to the log is ensured, and the ignition speed is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the combustion wooden material.    Log (1)    Depression portion (2)    Uneven-shaped groove pattern (3)    Cross-shaped communication channel (4)    Convex portion (31)
NOVELTY - Kitchen garbage processing involves sorting kitchen garbage, and then crushing them. The crushed garbage is mixed with fermenting additive material, and then fermented them for 12-16 days. The obtained material is filtered to obtain 8-90% organic matter and 1-20% residue. The obtained material is performed for dehydration process.    USE - Method for processing kitchen garbage (claimed).    ADVANTAGE - The method enables to process kitchen garbage in cost-effective and eco-friendly manner, ensures reduced production of harmful gases for safety purposes.
NOVELTY - Preparing pyraclostrobin (VII), comprises reacting (4-chlorophenyl)hydrazine (I) with ethyl acrylate to obtain 1-(4-chlorophenyl)pyrazolidin-3-one (II), epoxidizing (II) and then etherifying with 2-nitrobenzyl bromide to obtain 1-(4-chlorophenyl)-3-(2-nitrobenzyloxy)-1H-pyrazole (IV), reducing nitro group of ( IV) to obtain N-(2-((1-(4-chlorophenyl)-1H-pyrazol-3-yloxy)methyl)phenyl)hydroxylamine (V), performing N-acylation of (V) with methyl carbonochloridate to obtain methyl 2-(((1-(4-chlorophenyl)-1H-pyrazol-3-yl)oxy)methyl)phenyl(hydroxy)carbamate (VI), and then methylation of (VI).    USE - The method is useful for preparing (VII) (claimed).    ADVANTAGE - The method: has controllable reaction steps; improves product yield and preparation process stability; utilizes low cost medicament, less toxic agents and non-corrosive plastic pipelines; reduces production cost; and is environmentally friendly.    DETAILED DESCRIPTION - Preparing pyraclostrobin of formula (VII), comprises reacting (4-chlorophenyl)hydrazine of formula (I) with ethyl acrylate to obtain 1-(4-chlorophenyl)pyrazolidin-3-one of formula (II), epoxidizing pyrazole ring of (II) using oxidizing agent to obtain 1-(4-chlorophenyl)-1H-pyrazol-3-ol of formula (III), then etherifying (III) with 2-nitrobenzyl bromide to obtain 1-(4-chlorophenyl)-3-(2-nitrobenzyloxy)-1H-pyrazole of formula (IV), reducing nitro group of ( IV) using reducing agent to obtain N-(2-((1-(4-chlorophenyl)-1H-pyrazol-3-yloxy)methyl)phenyl)hydroxylamine of formula (V), performing N-acylation of (V) with methyl carbonochloridate to obtain methyl 2-(((1-(4-chlorophenyl)-1H-pyrazol-3-yl)oxy)methyl)phenyl(hydroxy)carbamate of formula (VI), and methylation of hydroxy group of (VI) under base condition.
NOVELTY - A recombinant nitrilase comprising fully defined 372 amino acids (SEQ ID NO. 1) given in the specification, is new.    USE - The recombinant nitrilase is useful for preparing 1-cyano-cyclohexyl-acetic acid (claimed).    ADVANTAGE - The recombinant nitrilase has good regioselectivity and catalytic activity in catalytic reactions. The method for preparing 1-cyano-cyclohexyl-acetic acid (production rate of 90%) is environment-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a gene encoding the recombinant nitrilase, comprising fully defined 1116 bp (SEQ ID NO. 2) given in the specification;    (2) a recombinant vector constructed by the gene or by the mutant gene;    (3) recombinant genetically engineered bacteria, converted by the recombinant vector;    (4) use of recombinant nitrilase for preparing 1-cyano-cyclohexyl-acetic acid comprising, after fermentation, centrifuging fermentative bacteria comprising nitrilase gene; using 1-cyano-cyclohexyl-acetonitrile as a substrate, to a pH of 3. 0-10.0 and 100 mM phosphate buffer solution as the reaction medium; performing conversion reaction at 25-70 degrees C; obtaining a mixture containing 1-cyano-cyclohexyl-acetic acid; and isolating and obtaining 1-cyano-cyclohexyl-acetic acid; and    (5) a recombinant nitrilase mutant, where the mutant is gene encoding recombinant nitrilase comprising Phe168Val and having a histidine tag in C-terminal protein.
NOVELTY - Preparation of crystalline form of linezolid involves adding an organic solvent (a) to linezolid residue at less than 50 degrees C, cooling, filtering, washing obtained slurry using an organic solvent (a) and drying.    USE - Preparation of crystalline form of linezolid used for treatment of infection caused by gram-positive bacteria e.g. Streptococcus and methicillin-resistant Staphylococcus aureus.    ADVANTAGE - The method efficiently provides crystalline form of linezolid with high yield and purity, by simple method without affecting the environment and without using anti-solvent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for crystalline form of linezolid, which has powder X-ray diffraction pattern.
NOVELTY - Concrete fermentation tank has support stand in which inner front end connection portion is connected along outer end direction of a fermentation tank which consists of concrete structure. The scraper unit which is equipped with lower portion of an agitating blade is installed in rotation shaft that is arranged at lower surface of fermentation tank. The rotation shaft and scraper unit are connected to the central axis pin. Both ends of support stand are connected to outer end direction of scraper unit and rotation shaft is connected to a connection axis pin.    USE - The concrete fermentation tank useful for processing human excrement or livestock manure.    DETAILED DESCRIPTION - Concrete fermentation tank has support stand in which inner front end connection portion is connected along outer end direction of a fermentation tank (10) which consists of concrete structure. The scraper unit (32) which is equipped with lower portion of an agitating blade is installed in rotation shaft (20) that is arranged at lower surface of fermentation tank. The rotation shaft and scraper unit are connected to the central axis pin (32a). Both ends of support stand are connected to outer end direction of scraper unit and rotation shaft is connected to a connection axis pin (34a).    DESCRIPTION OF DRAWING(S) - The drawing shows schematic representation of concrete fermentation tank. (Drawing includes non-English language text)    Fermentation tank (10)    Rotation shaft (20)    Scraper unit (32)    Central axis pin (32a)    Connection axis pin (34a)
NOVELTY - This new type utility claims one a closeness type fermentation device, comprising the fermentation jar, fermenting jar left side set with crusher, between the left side upper end set with feed wherein, and wherein set with feeding conveyor belt. Fermentation jar upper end set with upper cover, upper cover set with a maintenance window, upper cover left end set with a power tank, a tank driving a motor, motor fermentation jar right middle position. Driving a motor bearing, a fixed connecting rotating shaft, rotating shaft set with a number rows of agitator blade. Fermentation jar right above end set with an air outlet, a air outlet set with air cleaner. Fermentation jar right lower part set with a discharge end wherein the lower discharge wherein a fixing sieving machine right end set with sieving material wherein. Fermentation jar lower end set with heating plate, heating plate fixed in a bottom plate. Fermentation jar left lower end set with an air compressor, the air compressor and the fermentation jar through pipeline connection. This utility new type good fermentation effect, capable of continuously feeding and discharging, without pollution and increase the work efficiency and reduces the production cost.
NOVELTY - This utility new type relates to one a biological organic fertilizer production line, a category organic fertilizer manufacturing technology field. In turn comprising a stirrer, a crusher, a granulator, a disk granulator, the first dryer, the first dust-removing room, second dryer, second dust-removing room, a cooling machine, a vibration sieve, a colour machine, machine and packing machine. This utility new type is beneficial effect is: this production line design is reasonable, into ball, high pelletizing rate, realize automatic production, valid reduces the labour intensity of workers, increase the production efficiency, and is suitable for large scale production. Using the two secondary drying, drying temperature low, that is, maintain product nutrient is not lost, but also can maintain a uniform product, breaking bottom. Using underground dust exhausting system, reduce dust, smoke and dust pollution, and is beneficial to protect environment.
NOVELTY - This utility new type claims a new-type one chicken manure amino acid biological organic fertilizer production device, this device belonging to the biological organic fertilizer field, comprising: the first fermenting groove, second fermentation groove, a crusher, a mixing machine, a filter, a centrifugal separating machine, concentrating tank, a granulator, drying, wherein between the first fermenting groove and second fermentation groove set with the first conveyor, second fermentation groove and set with second crusher, between the crusher and mixing machine set with third conveyor between filter and centrifugal separating machine set with the first material slurry pump and pipeline, centrifugal separating machine and concentrating tank set with second material slurry pump and pipeline, concentrating tank and mixing machine set with the fourth conveyor between the mixing machine and machine set with fifth conveyer, a drying machine set with the sixth conveyor, a drying machine set with the finished product outlet.
NOVELTY - This utility new type claims a one a chicken manure biological organic fertilizer of machinery device, this device belonging to the biological organic fertilizer field, comprising the fermentation pool, the first fermenting groove, second fermentation groove, a crusher, a mixing machine, a granulator, a drying machine, wherein, a fermentation pool set with cake fertilizer, inlet, a fermentation pool and mill the set with the first conveyor, the first fermenting groove set with a chicken manure, fiber decomposing a, semi-decomposing a, decomposing a protein, organic phosphorus decomposing a inlet, the first fermenting groove and second fermentation groove set with second conveyor, a second fermentation groove set with aminating a, light and germ, microzyme, actinomycete, sterilizing deodorant inlet, second fermentation groove and set with third conveyor crusher, a crusher and mixing machine set with the fourth conveyor, a mixing machine and machine set with the fifth conveyer, a drying machine set with the sixth conveyor, a drying machine set with a finished product outlet.
NOVELTY - The system has a mass flow controller (400) that is connected to a pig ordure storage unit (100). A circulation aeration tank (200) is connected to the pig ordure storage unit. The mass flow controller is connected to the circulation aeration tank. A fermenter (300) which ferments the excrements cleaned up in the circulation aeration tank, and makes the liquefied fertilizer is connected to the circulation aeration tank. The mass flow controller which is connected to the fermenter controls the flow rate of the liquefied fertilizer.    USE - Environment-friendly pig ordure liquid state fertilizer system.    ADVANTAGE - The fermentation activity circulates the high liquefied fertilizer to the peggery so that high-quality liquefied fertilizer is produced efficiently without the separation of excrements.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the environment-friendly pig ordure liquid state fertilizer system.    Pig ordure storage unit (100)    Circulation aeration tank (200)    Aeration unit (210)    Fermenter (300)    Mass flow controller (400)
NOVELTY - Agent is prepared by mixing beans, corn, potatoes, leafy vegetables, straw and Penthorum chinense extract, soaking the mixture in warm water, crushing the soaked product, filtering the crushed product, adding weak acid buffer solution to the precipitate, fermenting the mixture using protease at 16-32 degrees C, subjecting the fermented broth to adsorption by adding cation adsorbent, adjusting pH to 5.3-7.5, eluting small molecules, concentrating eluate and spray-drying concentrate.    USE - The agent is useful for promoting growth (claimed) of plants.    ADVANTAGE - The agent is pure and organic in nature.
NOVELTY - Heteroaryl-containing transition metal complexes (A1) are new.    USE - (A1) are useful as catalysts for producing hydrogen from an aqueous solution (all claimed).    ADVANTAGE - (A1): are efficient electrocatalysts for producing hydrogen from aqueous solution; can be prepared in a convenient manner; and exhibit improved catalytic properties.    DETAILED DESCRIPTION - Heteroaryl-containing transition metal complexes (A1) of formulae (I) and (III), and their salts, solvates or hydrates are new.    M1, M2 = transition metal;    G1 = N,N-bis(2-pyridinylmethyl)-2,2'-bipyridine-6-methanamine, N,N-bis((isoquinolin-1-yl)methyl)(6-(pyridin-2-yl)pyridin-2-yl)methanamine, or their derivatives;    Y1 = halo or water moiety;    X1 = anion;    m = number of cations per metal complex;    n = number of anions per metal complex;    L1 = absent or neutral molecule;    a = number of neutral molecules per metal complex;    G2 = N,N-bis(2-pyridinylmethyl)-2,2'-bipyridine-6-methanamine, 6'-((bis(pyridin-2-ylmethyl)amino)methyl)-N,N-dimethyl-2,2'-bipyridin-6-amine, or N,N-bis((isoquinolin-1-yl)methyl)(6-(pyridin-2-yl)pyridin-2-yl)methanamine; and    Y2 = absent, halo or water moiety.    Provided that when G1 is N,N-bis(2-pyridinylmethyl)-2,2'-bipyridine-6-methanamine, M1 is not ruthenium. INDEPENDENT CLAIMS are also included for:    (1) a catalyst comprising (I);    (2) producing (P1) hydrogen from an aqueous solution, comprising adding the catalyst to the aqueous solution;    (3) N,N-bis((isoquinolin-1-yl)methyl)(6-(pyridin-2-yl) pyridin-2-yl)methanamine; and    (4) a metal complex (A2) comprising N,N-bis((isoquinolin-1-yl)methyl)(6-(pyridin-2-yl)pyridin-2-yl)methanamine or its derivative, and a transition metal, or its a salt, solvate or hydrate.
NOVELTY - This utility new type claims a one culture a environment-friendly septic tank, comprising filter area, manure culture area and a sludge from a left area, a septic culture area and sludge are separated with a partition wall from a left half area of the filter by the filter network of two compose sliding groove, a filter network a conical hopper-shaped, in culture a septic area a with active sludge, at the same time the inner mounted with an aeration tube, set with one inclined plate from the bottom left area of a sludge, inclined plate and the horizontal plane a 50 degrees to 60 degrees. This utility new type of a culture a environment-friendly septic tank, through filter area, manure culture area and a sludge from a left match process of area, a public toilet and rural cesspit malodor problem, at the same time a culture a septic tank structure is simple, the floor space is small and convenient operation, low investment and operation cost is low, and it is easy to maintain, and produce a residual active sludge for other can has a certain of sewage treatment effect, reduces the pressure of a subsequent municipal sewage treatment plant.
NOVELTY - The system has a shell (5) arranged on an anode room (6) and a cathode room (7), and an anode (2) and a cathode (3) arranged in the anode room and the cathode room. A positive ion exchange film (4) is arranged between the anode room and the cathode room. The anode room and the cathode room are arranged with a magnetic force stirrer, and the cathode produces the gas through a gas collecting tube (9). The shell is made of organic glass. A power supply (1) is connected with the anode room and the cathode room, which are equipped with waste water and sludge.    USE - Collecting waste water biological treatment and microorganism promoting electrolytic system.    ADVANTAGE - The system decomposes the organic matter and improves degradation efficiency of waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a collecting waste water biological treatment and microorganism promoting electrolytic method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a collecting waste water biological treatment and microorganism promoting electrolytic system.    Power supply (1)    Anode (2)    Cathode (3)    Positive ion exchange film (4)    Shell (5)    Anode room (6)    Cathode room (7)    Gas collecting tube (9)
NOVELTY - This utility new type claims a one leftover by fermenting a food, comprising sterilizing jar, fermenting jar, a storage jar, and the jar is up and down double-layer structure, the lower layer is heating room, the upper layer is sterilization room, heating room set at the bottom with heating device, sterilizing room set with residue entrance and a residue outlet, outlet of the sterilizing room a fermentation jar is feed wherein, discharge wherein a fermentation jar a storage jar. This utility new type and existing technology has following advantages: solid-liquid separating process, which not only solves the environment pollution problem, but also can reach the purpose of recycling. This utility new type is a with miniaturization, modularization is can be widely use in food.
NOVELTY - This new type utility claims the catering residue comprehensive processing system, including catering sewage treatment system and leftover by fermenting a food, catering sewage treatment system comprising a solid-liquid separating sieve, an anaerobic reactor, an anaerobic reactor by stainless steel shell body and is set with a filler of a stainless steel inner shell, the stainless steel shell body bottom set with a water inlet, the top part is set with water outlet and an air outlet, wherein a solid-liquid separating sieve a liquid wherein a water inlet of the anaerobic reactor, the filler by a porous ceramic, the leftover by fermenting a food by sterilizing jar, fermenting jar, a storage jar, and the jar is up and down double-layer structure, the lower layer is heating room, the upper layer is sterilization room, heating room set at the bottom with heating device, sterilizing room set with residue entrance and a residue outlet, outlet of the sterilizing room a fermentation jar is feed wherein, discharge wherein a fermentation jar a storage jar.
NOVELTY - This utility new type claims a one operation is simple, the floor space is small, special b process of ship sewage treatment device of sewage inner ship, including by glass steel of inner embedded steel framework is made of a tank, through support leg of the bottom fixed ship in a floor, a top end of tank opening, in a part of a tank set with one inclined a filter network, one along the filter screen is set with a inclined sliding plate is in the upper part of filter screen, in turn set with plant zeolite processing area, biological enzyme treatment area and settling zone in the lower part of filter screen, with bottom set with a spiral groove in the inner wall of a precipitation zone, a part of a zone set with the water tube, the bottom is set with mud settling zone. This utility new type processing process is simple, operation management maintenance is convenient.
NOVELTY - The utility model claims a new water quality treatment area, specifically relates to a kind of one microorganism by using sewage purification and water treatment device, wherein the water processing device comprises one frame body, with at least one belt of ball shell internal hole on the frame body, the frame body comprises upper hole and the inner through port is not large in diameter with hole ball shell and the outline size, the hole with ball shell with the microorganism carrier, the hole with ball shell surface has small hole, its aperture no less than the carrier of the microorganism load and maximum outline size. This new utility model is advantages as: 1, microorganism diversity in water and greatly increase. 2, breeding and growing environment of microorganism is greatly improving, counteracting of environment to microorganism activity of influence.
NOVELTY - The low dissolved oxygen magnetic biochemical treatment system has lean oxygen pool (2) which is connected to oxygen enrichment pool (3) and precipitating pool. The bottom portion of the oxygen enrichment pool is provided with aerator (6). The entrance end of drum separator (14) is connected to bottom portion of mud water separating area (9) through surplus sludge tube. A return pipe (16) is connected to oxygen enrichment pool through magnetic substance. The inner reflux pump (4) is connected to entrance end of oxygen-enriched pool and lean oxygen outlet pool.    USE - Low dissolved oxygen magnetic biochemical treatment system used in sewage processing factory.    ADVANTAGE - The nitrogen and phosphorus in the waste water is removed efficiently. The water quality of the waste water is increased. The size of the biochemical treatment system is reduced. The high load, high biological amount, and high processing efficiency of the system are ensured. The produce rate of sludge is reduced. The pollution free environment is provided.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a low dissolved oxygen magnetic biochemical treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the low dissolved oxygen magnetic biochemical treatment system.    Lean oxygen pool (2)    Oxygen enrichment pool (3)    Inner reflux pump (4)    Aerator (6)    Mud water separating area (9)    Drum separator (14)    Return pipe (16)
NOVELTY - Microbial fertilizer for rice, comprises: chicken manure (10-20 pts. wt.); straw leavening agent (1.5-4 pts. wt.); large granule urea (6-11 pts. wt.); Lactobacillus acidophilus (2-4 pts. wt.); Bacillus licheniformis (1.5-3.2 pts. wt.); soyabean cake (3.2-6 pts. wt.); potassium sulfate (5-10 pts. wt.); ammonium sulfate (2.3-4.9 pts. wt.); and bentonite (1.2-3.1 pts. wt.).    USE - As microbial fertilizer for rice (claimed).    ADVANTAGE - The fertilizer improves soil condition, thus increases yield and crop quality; and it reduces pollution.    DETAILED DESCRIPTION - Microbial fertilizer for rice, comprises: chicken manure (10-20, preferably 15 pts. wt.); straw leavening agent (1.5-4, preferably 2.9 pts. wt.); large granule urea (6-11, preferably 9 pts. wt.); Lactobacillus acidophilus (2-4, preferably 3 pts. wt.); Bacillus licheniformis (1.5-3.2, preferably 2.4 pts. wt.); soyabean cake (3.2-6, preferably 4.8 pts. wt.); potassium sulfate (5-10, preferably 7.5 pts. wt.); ammonium sulfate (2.3-4.9, preferably 3.6 pts. wt.); and bentonite (1.2-3.1, preferably 2.3 pts. wt.).
NOVELTY - Method for preparing loess-sulfur complex involves mixing 10-20 wt.% sodium hydroxide with 20-30 wt.% sulfur, adding 0.01-0.1 wt.% loess powder, 0.01-0.2 wt.% salt, 0.1-0.3 wt.% eggshell calcium, and 0.01-0.1 wt.% potash feldspar to mixture, adding 0.01-0.1 wt.% water to mixture, maintaining mixture at 100-150 degrees C, diluting obtained mixture using 0.025-0.05 wt.% water, adding 0.01-0.2 wt.% vinegar to diluted mixture and adjusting pH of the obtained mixture to 8-10.    USE - The method is useful for preparing loess-sulfur complex which is used for controlling plant disease chosen from powdery mildew, anthracnose, downy mildew, and sheath blight (claimed).    ADVANTAGE - The method enables to prepare product in an environmentally-friendly manner. The prepared product does not cause toxic effects.
NOVELTY - A persulfate organic wastewater treating method involves utilizing anaerobic reactor with compartment, and initiator organic sulfate anaerobic wastewater treatment systems, holding the hydraulic retention time for 24-30 hours. Operational control of organic sulfate anaerobic wastewater treatment system is performed by adjusting the anaerobic reactor pH value of the last three interior compartments liquid, controlling the third last countdown oxidation-reduction potential of the liquid compartment, adjusting the influent in the final penultimate compartment dosing metal ions.    USE - Method for treating persulfate organic wastewater.    DETAILED DESCRIPTION - A persulfate organic wastewater treating method involves utilizing anaerobic reactor with compartment, and initiator organic sulfate anaerobic wastewater treatment systems, holding the hydraulic retention time for 24-30 hours, a COD in water 1000 mg/L is gradually increased to 3000 mg/L, a range in water 60 mg/L is gradually increased to 200 mg/L, and a COD: SO42-value is (14 to 16): 1. Operational control of organic sulfate anaerobic wastewater treatment system is performed by adjusting the anaerobic reactor pH value of the last three interior compartments liquid to 6-8, 5.5-6.2, 6.5-8.2 respectively, controlling the third last countdown oxidation-reduction potential of the liquid compartment to -220 to -280mV, adjusting the influent COD: SO42- values by (14-16) startup, a lowering the final penultimate compartment dosing metal ions such as ferric ion, cobalt ion and nickel ion, respectively at 40 mg/L, 2 mg/L and 0.8 mg/L.
NOVELTY - The device has a double-screw rotating plate sludge dehydrating device, a heat exchanger and an incinerator that are connected with one another. A horizontal spiral discharging sedimentation centrifuge machine is fixed in a pedestal. Bottom part of an inner shell of the centrifuge machine is mounted with an inner water collecting groove. A middle drum is fixed with a horizontal spiral rotating shaft. A double-disk spiral sludge dewatering device and a smoke pneuma bag-type dust remover of a combustion furnace are connected together through a heat exchanger.    USE - Sedimentation centrifuge reduction based sludge treatment device.    ADVANTAGE - The device performs sludge reducing treatment by using low energy to maximize sludge reducing amount so as to ensure sludge treatment device performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a sludge drying method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a sedimentation centrifuge reduction based sludge treatment device.
NOVELTY - This utility new type relates to one a biological strengthening treatment of nitrobenzene waste water of device, device comprising reaction pool, the reaction pool mounted in the waste water with a longitudinal partition wall and the partition wall, a shell of reaction pool is provided with a water inlet and a rear water treatment of the waste water entering into a removing of outlet, outlet mounted with a ceramic film filter, ceramic film filter with from a suction pump, ceramic film filter mounted in inner part of reaction pool, from the pump mounting guiding hole in, a vertical insulating wall of reaction pool, inner guide hole mounted frequency conversion shaft flow pump. This utility new type and free microorganism phase compare, process speed is fast, effect is good, and the process for growing environment has good tolerance capacity. This utility new type reduces the yield of sludge, and a control shaft flow pump through a rotating speed, a solution circulation, water for a water quality regulating control to make the waste water for a better adaptability.
NOVELTY - The system collects domestic sewage flow through a buried pipe network. The domestic sewage is conveyed to three format sewage treatment pool treatment. The sewage orderly enters into three format sewage treatment pool sink eggs depositing room, an anaerobic sterilizing room and a clarification room. The insect eggs are killed and sinking pathogens by sewage anaerobic fermentation process. The three format sewage treatment pool of water that flows into an artificial ecological plant is absorbed. The standard-reaching exhaust and rear processing standard of water are discharged.    USE - New rural domestic sewage treatment system.    ADVANTAGE - The uniform domestic sewage treatment process is achieved. The power consumption is reduced. The production cost is low. The technology is simple, the operation cost is low, the operation process is simple and convenient to maintain the domestic sewage treatment pool.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the process of new rural domestic sewage treatment system. (Drawing includes non-English language text)
NOVELTY - Refinery oily sludge processing involves dissolving mixture containing oil sludge and water for regulating water content to 95% by using 100 meshes stainless steel filter screen. The pH value is regulated to neutral at 50-60 degrees C, and then the sludge is added in biological demulsifier. The demulsifier comprises a decline phase of Bacillus subtilis fermentation whole broth, which is stirred by using 40-60 Kilohertz ultrasonic wave to homogenize the sludge. The ultrasonic treatment changes sludge structure to release intracellular substance and to separate micro particles.    USE - Method for processing refinery oily sludge (claimed).    ADVANTAGE - The method processes refinery oily sludge in a simple, precise and eco-friendly manner.    DETAILED DESCRIPTION - Refinery oily sludge processing involves dissolving mixture containing oil sludge and water for regulating water content to 95% by using 100 meshes stainless steel filter screen. The pH value is regulated to neutral at 50-60 degrees C, and then the sludge is added in biological demulsifier. The demulsifier comprises a decline phase of Bacillus subtilis fermentation whole broth, which is stirred by using 40-60 Kilohertz ultrasonic wave to homogenize the sludge. The ultrasonic treatment changes sludge structure to release intracellular substance and to separate micro particles. The treated mixture is kept for 20 minutes for separating upper layer crude oil, in which 4-6 wt.% of conditioning agent is added. The conditioning agent includes humic acid (10-30%), incineration ash (30-40%), active carclazyte (20-30%), walnut shell activated carbon (5-10%), and aluminum sulfate (1-5%).
NOVELTY - Preparing drug ticagrelor (I) involves reacting the compound (VI) with a compound of (XI) in the presence alkali and catalyst to obtain compound (V). The compound (V) is treated with a reducing agent to obtain compound (IV) and (III). The compound (III) is reacted with an alkali metal nitrite for performing a cyclization reaction and to obtain compound (II). The compound (II) is reacted with compound (XII) to obtain the desired product.    USE - Method for preparing drug ticagrelor (Claimed).    ADVANTAGE - The method enables to prepare drug ticagrelor in simple, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing drug ticagrelor of formula (I) involves reacting the compound of formula (II) with a compound of formula (III) in the presence alkali and catalyst to obtain compound formula (IV). The compound formula (IV) is treated with a reducing agent to obtain compound of formula (V) and formula (VI). The compound of formula (VI) is reacted with an alkali metal nitrite for performing a cyclization reaction and to obtain compound of formula (VII). The compound of formula (VII) is reacted with compound of formula (VIII) to obtain the desired product.    R1=amino protecting group, trityl, benzyl, 4-methoxybenzyl, 4-methylbenzyl, 4-nitrobenzyl, 2,4-dimethoxybenzyl, benzyloxycarbonyl, 4-methoxy-benzyloxycarbonyl or 4-methyl-benzyloxycarbonyl group;    Y'=leaving group, halogen, R5C(O)O acyloxy group or R6S(O2) sulfonyl group;    R5=1-6C alkyl group, trifluoromethyl or aryl group; and    R6=1-6C alkyl group, 1-6C fluoroalkyl or aromatic group.    .
NOVELTY - Cyclohexanetriol derivative (I) is new.    USE - Cyclohexanetriol derivative (I) used for preparing valiolamine hydrate and voglibose (claimed).    ADVANTAGE - The method is simple, and has fewer steps compared to conventional method, recyclable catalyst, less pollution and stable yield.    DETAILED DESCRIPTION - Cyclohexanetriol of formula (I) is new.    Cbz=carboxybenzyl.    INDEPENDENT CLAIMS are included for:    (1) preparation of compound (I); and    (2) preparation of valiolamine hydrate (VI) comprising hydrolyzing and deprotecting compound (I) by adding hydrogen bromide (HBr)/acetic acid (HOAc) mixed solution, where the molar ratio of HBr and HOAc is 1:1-5, preferably 1:3.
NOVELTY - The method involves loading specified amount of raw coal into furnace hole of heated oven carbonization chamber. Raw coal is heated in the final carbonization process. The waste gas generated in combustion chamber is burned using direct heating at 750 to 800 degrees centigrade. The blue carbon coke quenching device is made to fall through bottom of scraper conveyor. The coal is cooled to 75 to 80 degrees centigrade. A rectifying tower is provided for rectifying ammonia water so as to produce anhydrous ammonia.    USE - Coal carbonization method.    ADVANTAGE - The waste of pneuma, residue and water is avoided, so that the better environmental protection is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the coal carbonization process. (Drawing includes non-English language text)    Blower (1)    Bag type pulse dust remover (2)    Quenching device (6)    Direct cooling tower (7)    Transverse cooler (8)
NOVELTY - A tetrahydrofuran-2,5-dicarbaldehyde (I) is new.    USE - New tetrahydrofuran-2,5-dicarbaldehyde is used for preparing furanic derivatives (claimed). Uses include but are not limited to solvent, resin, plasticizer, surfactant, pharmaceutical, dispersant, organic acid, plant protection agent, polyurethane and polybutylene terephthalate.    ADVANTAGE - The tetrahydrofuran-2,5-dicarbaldehyde is manufactured with yield of more than 60%. The furanic derivative is prepared by economical and environmentally-friendly process in short period of time using tetrahydrofuran-2,5-dicarbaldehyde.    DETAILED DESCRIPTION - A tetrahydrofuran-2,5-dicarbaldehyde of formula (I) is new. INDEPENDENT CLAIMS are included for the following:    (1) preparation of tetrahydrofuran-2,5-dicarbaldehyde (I), which involves reacting reaction mixture containing tetrahydrofuran diols and inert organic solvent with oxidizing agent at 10-50?oC in non-inert atmosphere;    (2) preparation of furanic derivative, which involves preparing tetrahydrofuran-2,5-dicarbaldehyde (I) and transforming resultant product to furanic derivative compound; and    (3) furanic derivative compound.
NOVELTY - Preparing lapatinib intermediate compounds (I), comprises reacting 2-chloro-4-(quinazolin-4-ylamino)phenol compounds (II) with 1-bromomethyl-3-fluoro-benzene under action of organic or inorganic bases.    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method: is simple, safe, and environmentally friendly; produces product with good yield; and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing lapatinib intermediate compounds of formula (I), comprises reacting 2-chloro-4-(quinazolin-4-ylamino)phenol compounds of formula (II) with 1-bromomethyl-3-fluoro-benzene compound of formula (III) under action of organic or inorganic bases.    R=Cl, Br, I, 5-((N-tert-butoxycarbonyl-(2-(methylsulfonyl)ethyl)aminomethyl))furan-2-yl or 5-formyl-furan -2-yl.    INDEPENDENT CLAIMS are also included for:    (1) 4-((6-bromoquinazolin-4-yl)amino)-2-chlorophenol (VII) and 5-(4-((3-chloro-4-hydroxyphenyl)amino)quinazolin-6-yl)-2-furaldehyde (IX); and    (2) preparation of (VII) and (IX), comprising (a) reacting 6-bromo-4-chloroquinazoline (VI) with 4-amino-2-chlorophenol (V) or its salts to obtain (VII), and (b) reacting (VII) with 5-formylfuran-2-ylboronic acid (VIII) in presence of organic or inorganic bases under action of catalyst to obtain (IX).
NOVELTY - The system gas a conveyance roller (21) for conveying an electrode sheet (200). A laser apparatus (24) irradiates a laser to the electrode sheet. A dust collection unit removes suction force (P1) of foreign material discharged by a groove (40). The conveyance roller is in contact with a roll part (41) bordering on the groove in which an electrode of the electrode sheet is coated. A suction opening (44) sucks an uncoated part (202) provided in a surface of another roll part (42) with another suction force (P2) such that the latter suction force is made larger than the former suction force.    USE - System for inspecting an electrode sheet utilized for manufacture of a lithium ion battery and a fuel cell.    ADVANTAGE - The uncoated part is sucked to the roll part with strong suction force, so that need to flutter depressing in the uncoated part can be suppressed during conveyance of the electrode sheet or groove, thus matching focus of laser irradiation in a correct manner and giving a marking by the laser irradiation with respect to the electrode sheet in a stable manner.    DETAILED DESCRIPTION - The dust collection unit is a lower dust collection cover (26).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a conveyance roller.    Suction forces (P1, P2)    Conveyance roller (21)    Laser apparatus (24)    Lower dust collection cover (26)    Groove (40)    Roll parts (41, 42)    Suction opening (44)    Electrode sheet (200)    Uncoated part (202)
NOVELTY - This utility new type relates to a one fertilizer production device, specifically is a histidine compound fertilizer production with one efficient energy-saving tube-type reactor. Comprising tube body, is set with a nozzle pipe body one end and connected of the ammonia pipe in the other end tube body, wherein the acid inlet, the middle section of tube body in venturi tube and spiral fin pipe, in the inner cavity of the spiral fin tube set with middle shaft, shaft and inner wall in spiral fin tube is set with spiral fins; the heating cavity, the heating cavity is sleeved outside the annular spiral fin pipe is a pipe with a water inlet and the water pipe is hollow shell-shaped. This pipe type reactor use Venturi tube and speed and direction of spiral fin multi-time change material flow, which is good for material is fully mixed reaction, spiral fin and heating cavity matching, which is good for a reaction temperature, save energy and increase product quality.
NOVELTY - This utility new type claims a liquid fertilizer is a one unit, belonging to the field of agricultural fertilizer processing technology field, comprising orderly set with a source liquid storage pool, Anaerobic fermentation pool, an aerobic fermenting pool, stir pool and the finished product storage pool. This utility new type low cost, high efficiency, convenient operation, Anaerobic and aerobic fermentation production of the liquid fertilizer quality, the liquid fertilizer effect, is no longer a simple material mix.
NOVELTY - This utility model provides a biomass gasification combustion system, including a flame outlet, an exhauster, smoke outlet, a steam cooker, a one-way sealing cover, pedestal, discharging device, a slag discharging port, fermentor pressure pole, pressure. This utility new type fermentor using a process gas, the steam stove through a. produce a pneuma smoke exhauster through filtering after discharging, environment protection, for connection with a pressure pole, pressure pole set up with a voltage divider, this utility new type is more safe and reliable.
NOVELTY - Invention relates to agriculture. The device for environmentally safe recycling of organic substrates into biogas and fertilisers, consisting of the first device of mechanical separation hydraulically connected with the line of feeding the initial substrate, the anaerobic bioreactor with immobilised microflora equipped with outlet of biogas and effluent, the anaerobic bioreactor with suspended microflora and the second device of mechanical separation, and the outputs of the liquid fraction of the first and second mechanical separation devices are connected to the input of the anaerobic bioreactor with immobilised microflora, and the output of the solid fraction of the first mechanical separation device is connected to the input of the anaerobic bioreactor with the suspended microflora provided with heating means, and an aerobic bioreactor is additionally provided, an anaerobic bioreactor with immobilised microflora, the first device of mechanical separation are located inside the housing of the aerobic bioreactor, anaerobic bioreactor with the suspended microflora and the second device of mechanical separation are combined in one housing.    USE - Agriculture.    ADVANTAGE - Invention enables to apply the stage of aerobic thermophilic hydrolysis of the initial substrate in conjunction with the integration of all the main processes of processing the substrate in one housing.2 dwg
NOVELTY - Group of inventions relates to agriculture. Method of recycling organic substrates into gas, liquid and solid fertilisers and technical water, in accordance with which initial substrate is successively subjected to homogenisation, anaerobic processing, mechanical condensation with obtaining solid and liquid fractions, with further application of solid fraction for manufacturing solid fertilisers, deammoniation of liquid fraction by stripping with chemisorption of vapour-gas mixture by acidic or alkaline reagents with obtaining liquid fertilisers and after-purification of deammoniated liquid fraction; liquid fraction of aerobically processed substrate is subjected to anaerobic processing, after-purification of deammoniated liquid fraction is carried out in aerobic mode, gases after after-purification of deammoniated liquid fraction are successively used for preliminary deammonification of initial substrate, with part of vapour-gas mixture being used for ammoniation of solid phase in production of solid fertilisers. Device for realisation of method of processing organic substrates into biogas, liquid and solid fertilisers and technical water.    USE - Chemistry.    ADVANTAGE - Group of inventions makes it possible to effectively use heat energy, reduce degree of environment pollution, as well as to increase profitability.2 cl, 2 dwg
NOVELTY - The present invention discloses a bio-diesel improving apparatus and method thereof, at least including a storage/feeding tank, a reactant solution storage tank, a reaction tank, a purification tank and at least one absorbing device. The storage/feeding tank stores waste oil or bio-fuel. The reactant solution tank stores reactant solution. The reactant solution tank and the storage/feeding tank are connected to the reaction tank to allow waste oil or bio-fuel and the reactant solution to enter the reaction tank and perform a transesterification reaction so as to produce bio-diesel. Moreover, the reaction tank is connected to the purification tank to allow the bio-diesel to enter the purification tank and distill moisture from the bio-diesel by a distillation process. The absorbing device has an absorbing substance for absorbing impurities and moisture, and is disposed to at least one of the following locations: before the storage/feeding tank or between the storage/feeding tank and the reaction tank, before the purification tank or following the purification tank.
NOVELTY - Aquaculture water quality is improved by mixing 5-20 pts. wt. Effective Microorganisms original fluid, 1-5 pts. wt. red sugar, 1-3 pts. wt. honey, and 50-80 pts. wt. yellow soil; uniformly kneading the mixed materials to form ball-shaped slow-release agent having weight of 0.5-0.75 kg; and treating the water with the slow-release agent every month.    USE - Method for improving aquaculture water quality (claimed).    ADVANTAGE - The method can restrain growth of harmful microorganisms while purifying water to improve water quality.
NOVELTY - A dehydrated sludge aerobic fermentation device comprises mixer (1) and fermentation portion in which fermentation portion (4) comprises 2 rows of fermentation tank (10), middle of fermentation tanks has 2 conveyors (2,9) and is set with automatic fabric machine (3) and automatic reclaimer (8).    USE - A dehydrated sludge aerobic fermentation device (claimed).    ADVANTAGE - Dehydrated sludge aerobic fermentation device accelerates fermentation rate and shorten fermentation time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dehydrated sludge aerobic fermentation which involves adding dehydrated sludge and fermentation return material into mixer, mixing, transporting to automatic fabric machine through conveyor, distributing in each 1st fermentation tank, covering surface of each 1st fermentation tank with tarpaulin, compacting seam with ballast, aerating, fermenting, measuring aeration rate of oxygen content in fermentation process, reducing moisture content of fermentation material to less than or equal to 45%, opening tarpaulin, taking portion of fermentation material into automatic reclaimer, returning to mixer through conveyor, mixing with dehydrated sludge to be processed, feeding remaining portion of fermentation material into each 2nd fermentation tank through automatic reclaimer until moisture content is less than or equal to 35%, and transporting into landfill or landscaping sector as nutritive soil or saline-alkali soil or abandoned mine for soil improvement.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a dehydrated sludge aerobic fermentation device. (Drawing includes non-English language text).    Mixer (1)    Conveyor (2)    Automatic fabric machine (3)    Fermentation portion (4)    Automatic reclaimer (8)    Conveyor (9)    Fermentation tank (10)
NOVELTY - The device comprises a transmission chain drive, a conveyor chain, a feeding port, a fermentation chamber, and a knife. The fermentation chamber is provided with a stirring shaft. Two sides of the stirring shaft and fermenting chamber are connected with a steering wheel. The stirring shaft is connected with an agitator blade and a spiral discharging machine. The feeding port is provided with a deodorization chamber that is provided with a deodorant filler comprising active carbon, molecule sieve, compost product and mixture of sawdust and straw.    USE - The device is useful for recycling kitchen waste (claimed).    ADVANTAGE - The device is capable of rapidly recycling the kitchen waste.    DETAILED DESCRIPTION - The device comprises a transmission chain drive, a conveyor chain, a feeding port, a fermentation chamber, and a knife. The fermentation chamber is provided with a stirring shaft. Two sides of the stirring shaft and fermenting chamber are connected with a steering wheel. The stirring shaft is connected with an agitator blade and a spiral discharging machine. The feeding port is provided with a deodorization chamber that is provided with a deodorant filler comprising active carbon, molecule sieve, compost product and mixture of sawdust and straw according to volume ratio of 3-4:1-2:1-2. A bottom part of the deodorization chamber is provided with an air inlet. A top part of the deodorization chamber is provided with an air outlet and a monitor. Side wall of the fermenting chamber is provided with a heating plate. The deodorizing chamber is connected with a spraying device and a draught fan.
NOVELTY - A silkworm excrement organic fertilizer comprises 30-45 pts. wt. bran, 30-45 pts. wt. silkworm compost ferment, 5-10 pts. wt. phosphate fertilizer, and 5-10 pts. wt. potash fertilizer.    USE - Silkworm excrement organic fertilizer.    ADVANTAGE - The fertilizer shortens culture time, reduces cultivation cost, and it has high organic matter and nutrition element contents, and long efficiency effect for fast growth of fruit and vegetable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising:    (A) placing silkworm excrement into ground at thickness of 18-20 cm; mixing 20 wt.% oligosaccharide and dry yeast at ratio of 300:1, stirring, spraying on silkworm excrement until all wet, covering with plastic film, fermenting for 20 days, opening cover, turning ferment, covering, and continuously fermenting for 15 days to obtain silkworm excrement compost ferment;    (B) crushing 60 pts. wt. sugarcane leaves and 20 pts. wt. filter mud, adding into fermentation tank with 0.5 pts. wt. calcium superphosphate, 1 pt. wt. rice bran and 1 pt. wt. gypsum, mixing, adding 0.5 pts. wt. dry yeast, fermenting for 20 days, turning ferment, fermenting, adjusting temperature to 58-60 degrees C to carry out disinfection and sterilization, cooling to 42-52 degrees C, and incubating for 10 days; and cooling to 30 degrees C or less, adding into mushroom room to carry out edible fungi cultivation, harvesting mushroom when matured, and collecting waste bran materials; and    (C) mixing with silkworm excrement compost ferment, stacking, naturally fermenting for 5 days, adding phosphate fertilizer and potash fertilizer, mixing, granulating, and drying.
NOVELTY - A sodium glutamic acid waste is used in production of fertilizer by preparing sodium glutamic acid fermentation liquid, filtering, decoloring, concentrating, and crystallizing.    USE - Method for using sodium glutamic acid waste in production of fertilizer (claimed).    ADVANTAGE - The method has simple technique, and reduced cost.
NOVELTY - Microbial organic fertilizer comprises 1-5 wt.% Bacillus cereus solution, 35-40 wt.% tobacco residue, 35-45 wt.% peat, 8-10 wt.% oil cake and 9-12 wt.% flower residue.    USE - Microbial organic fertilizer used for suppressing tobacco black shank (claimed).    ADVANTAGE - The microbial organic fertilizer ensures reduced environmental pollution because of using less amount of chemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial organic fertilizer, which involves mixing Bacillus cereus solution, tobacco residue, peat, oil cake and flower residue with water to obtain a mixture that is fermented for 40 days to obtain product.
NOVELTY - Bio-organic fertilizer comprises 1-5 % Bacillus pumilus solution, 35-40 % tobacco residue, 35-45 % peat, 8-10 % oil cake and 7-12 % flowers residue.    USE - Bio-organic fertilizer used for inhibiting root-knot nematode (claimed) in tobacco.    ADVANTAGE - The bio-organic fertilizer ensures reduced environmental pollution because of using low amount of chemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) mixing raw materials to obtain a mixture;    (B) stirring obtained mixture with Bacillus pumilus liquid and water;    (C) fermenting obtained mixture for 40 days; and    (D) observing fermented material until removal of peculiar smell to obtain product.
NOVELTY - 4,4'-dinitro-2,2'-bis(trifluoromethyl)diphenyl ether is prepared by adding 2-chloro-5-nitrobenzotrifluoride as raw material in aprotic solvent, heating, and reacting with presence of weak alkaline under normal pressure conditions in which aprotic solvent is N-methyl pyrrolidone or dimethyl sulfoxide, and weak alkaline is anhydrous sodium phosphate or aqueous dodecyl sodium phosphate.    USE - Preparation of 4,4'-dinitro-2,2'-bis(trifluoromethyl)diphenyl ether (claimed).    ADVANTAGE - The preparation has simple operation, low cost, less pollution, easy to purchase reaction device, uses recyclable solvent, and obtains product which has good color and quality.
NOVELTY - Preparation of erlotinib base monohydrate crystal form I comprises mixing erlotinib hydrochloride, alkali and organic solvent by stirring, after the reaction is finished, stirring until clear, dropwise adding in water, under stirring, cooling to 0-5 degrees C, filtering, vacuum drying and obtaining the product.    USE - Preparation of erlotinib base monohydrate crystal form I (claimed).    ADVANTAGE - The method uses inexpensive organic solvent, which is green and environment-friendly, is safe, environment-friendly, stable and suitable for industrial production, has simple operation, low cost, good repeatability, and very high economic value and provides erlotinib base monohydrate crystal form I with high purity.
NOVELTY - Preparation of imatinib (I) comprises performing coupling reaction with N-(3-amino-4-methylphenyl)-4-((4-methylpiperazin-1-yl)methyl)benzamide (II) and 2-hydroxy-4-(3-pyridyl)pyrimidine derivative (V) in the presence of organic alkali.    USE - Method for preparing imatinib (I) (claimed).    ADVANTAGE - The method has high yield, short process, and no harmful or toxic effect to the environment, produces imatinib with ideal purity, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of imatinib (I) comprises performing coupling reaction with N-(3-amino-4-methylphenyl)-4-((4-methylpiperazin-1-yl)methyl)benzamide (II) and 2-hydroxy-4-(3-pyridyl)pyrimidine derivative of formula (V) in the presence of organic alkali.    R=1-8C straight chain or branch chain alkane, or benzyl, preferably methyl or ethyl.
NOVELTY - Plant for treating organic waste comprises: an area for storing organic waste (4); means (22) for introducing and extracting air to and from the storage area (2); means (19) for filtering the air extracted from the storage area; many removable containers (3) for accumulating the organic waste, where the containers are manoeuvrable individually for being filled with organic waste and inserted in succession inside the storage area, and comprise means for turning the organic waste contained inside the removable container.    USE - The plant is useful for treating organic waste for the production of compost (claimed).    ADVANTAGE - The plant is simple and requires minimum intervention, even by a single operator.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing compost inside the plant, comprising: preparing an area for storing organic waste; preparing many removable containers for accumulating organic waste; filling in succession each container and inserting it inside the area; and introducing air inside the container present in the area.    DESCRIPTION OF DRAWING(S) - The figure shows a section view of the plant.    Storage area (2)    Removable containers (3)    Organic waste (4)    Means for filtering the air (19)    Means for introducing and extracting air (22)
NOVELTY - The metal doped zeolite membrane comprises a porous substrate, and a zeolite layer with metal doping and with MFI framework structure into which heteroatoms are incorporated. The zeolite membrane framework has channels of zeolite pores and sites in the channels.    USE - The metal doped zeolite membrane is useful for separating hydrogen, oxygen, methane or olefin from syngas or another gas mixture containing carbon dioxide, nitrogen, methane, carbon monoxide and/or hydrogen oxide, and in a molecular sieve (all claimed) and a membrane reactor system for reactions involving high temperatures and high pressures.    ADVANTAGE - The metal doped zeolite membrane has excellent thermal stability and improved chemical and structural stability, and enables efficient separation of hydrogen, oxygen, methane or olefin from syngas with high selectivity and quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for making a composite zeolite membrane;    (2) a method for forming a seeded layer on a porous substrate; and    (3) an improved method of separating hydrogen from syngas or another gas mixture containing carbon dioxide, nitrogen, methane, carbon monoxide and/or hydrogen oxide using a catalyst.
NOVELTY - Invention relates to method of ecologically pure obtaining urea (CO(NH2)2) from wastes of any composition. Method includes the following stages: a) obtaining synthesis-gas, which contains CO, CO2 and H2, by high-temperature processing of wastes in reactor in presence of oxygen O2, obtained by the process of cryogenic air separation; b) conversion of CO, contained in synthesis-gas, with application of H2O, into CO2+H2 (shift reaction) and separation of CO2 from H2; c) conversion of H2, obtained at stage (b) with application of N2, obtained from the process of cryogenic air separation at stage (a), with obtaining ammonia (NH3), and d) conversion of NH3 from stage (c), with application of CO2 from stage (b) with obtaining urea (CO(NH2)2).    USE - Chemistry.    ADVANTAGE - Invention makes it possible to obtain urea by economical way without air-polluting gaseous emissions.1 dwg
NOVELTY - The system has an absorptive tower (1) to absorb acidic gas using absorbent, and a regenerator (2) to separate process gas from absorbent. A heat exchanger (10) and an absorbent supply line (100) are provided facing the regenerator. The process gas emitted in regenerator is supplied to condenser (70) through process gas exhaust line, so that the water is condensed in condenser. The condensed water from reboiler (80) is recirculated to absorptive tower through condensed water supply line, such that the absorbent of low temperature is heated and supplied as absorbent of high temperature.    USE - System for separating and collecting acidic gas.    ADVANTAGE - The absorbent supplied to regenerator is preheated to re-cycling condensed water heat-exchanging with high temperature steam of regenerator upper end. The reboiler demand calorie is lowered by the absorbent supplied to water of high temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for separating and collecting acidic gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for separating and collecting acidic gas.    Absorptive tower (1)    Regenerator (2)    Heat exchanger (10)    Condenser (70)    Reboiler (80)
NOVELTY - The electrolysis system comprises: an electrolyzer (4) for producing hydrogen and oxygen; a waste heat conduit (6) for discharging a waste heat stream generated in the electrolysis process from the electrolyzer; a cooling circuit (7) with at least one rear cooler (8, 9) for regulating the temperature level of the electrolyzer; and an absorption refrigerator (10) for generating a refrigeration stream from the waste heat stream to the waste heat conduit. The refrigeration stream generated in the absorption refrigerator is fluidically coupled via a refrigerant line with the electrolyzer.    USE - Electrolysis system.    ADVANTAGE - The cost-effective electrolysis system including the rear coolers exhibits improved cooling efficiency.    DETAILED DESCRIPTION - The electrolysis system comprises: an electrolyzer (4) for producing hydrogen and oxygen; a waste heat conduit (6) for discharging a waste heat stream generated in the electrolysis process from the electrolyzer; a cooling circuit (7) with at least one rear cooler (8, 9) for regulating the temperature level of the electrolyzer; and an absorption refrigerator (10) for generating a refrigeration stream from the waste heat stream to the waste heat conduit. The refrigeration stream generated in the absorption refrigerator is fluidically coupled via a refrigerant line with the electrolyzer. The refrigeration stream is fluidically connected to the cooling circuit of the electrolyzer. The cooling circuit includes another rear cooler. The waste heat stream is formed by process water from the electrolyzer, and has a temperature of 60-80 degrees C. The refrigeration stream has a temperature of 5-15 degrees C. An INDEPENDENT CLAIM is included for a method for operating an electrolysis system.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an electrolysis system.    Electrolyzer (4)    Waste heat conduit (6)    Cooling circuit (7)    Rear cooler (8,9)    Absorption refrigerator. (10)
NOVELTY - One plasma de-water a hydrogen preparing efficient energy saving strong fire stove, wherein a furnace core in mounting with a casting aluminum heater and oil water evaporator, a cast aluminum inner heater mounted with an electric heater, mounted with heating pipeline and a steam outlet tube inner oil in water evaporator, the pipe mounted in a furnace core, upper nozzle and lower nozzle, a nozzle mounting a base, an air outlet pipe of oil water evaporator connecting with lower steam storage room, lower storage room a steam air inlet pipe with a plasma catalyst, steam outlet pipe of catalyst a plasma with a gas storage room, the spray pipe base mounted in front of a gas storage room, an intelligent controller and high frequency high voltage power supply is integrated, and a connection with an ignition needle, a flame sense pin, a fuel pump, a plasma catalyst electrode, temperature sensor and electric heater. In the embodiment a valid decomposition water molecule a hydrogen making, a save fuel, 20-60 % of a methyl alcohol furnace with a ideal update of replacing a new technology product, the market prospect is very wide.
NOVELTY - Production of high-efficiency haloxyfop-P-methyl microemulsion comprises adding toluene into first stirring tank, stirring, successively adding ethanol and haloxyfop-P-methyl, and stirring; adding water into first high-speed stirring tank, stirring, adding alkyl sulfonate, and stirring until completely dissolved; and adjusting stirring speed, slowly adding first stirring tank mixture, and stirring.    USE - Method for production of high-efficiency haloxyfop-P-methyl microemulsion (claimed) used for herbicide.    ADVANTAGE - The method uses universal device, achieves good product quality, and it has simple technique, mild reaction condition, and no waste pollution. The microemulsion is water dispersible, and it has low organic solvent content, high activity and usage rate, strong penetrability on target weeds, and good adhesive force and stability.    DETAILED DESCRIPTION - Production of high-efficiency haloxyfop-P-methyl microemulsion comprises adding 10-12 wt.% toluene into first stirring tank, stirring to room temperature at 30-35 revolutions/minute, successively adding 14-16 wt.% ethanol and 12-14 wt.% haloxyfop-P-methyl, and stirring for 1-1.2 hours; adding water into first high-speed stirring tank, stirring to room temperature at 50-60 revolutions/minute, adding 6-8 wt.% alkyl sulfonate, and stirring until completely dissolved; and adjusting stirring speed to 210-220 revolutions/minute, slowly adding first stirring tank mixture, and stirring for 1.2-1.4 hours.
NOVELTY - The machine has a cylindrical medicine bottle body whose bottom part is sleeved with a medicine bottle cover and a top cover. An outer circumference of the medicine bottle cover is formed with a medicine outlet. A core rotating shaft is connected with a tablet core turntable. An infrared counter is connected with a stepping motor that is connected with a chassis. A center part of a medicine fork wheel is connected with the core rotating shaft. A MSP430-type multi-single board computer is connected with a driver that is connected with the infrared counter in the medicine bottle body.    USE - Traditional Chinese medicine dispensing machine for a patient.    ADVANTAGE - The machine is simple to use, and has less volume, and can effectively taking dispensing medicine caused by human error, and reduces power consumption to depend on power supply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a traditional Chinese medicine dispensing machine utilization method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a traditional Chinese medicine dispensing machine.
NOVELTY - Composite fertilizer comprises 60-70 pts. wt. organic fertilizer, 20-25 pts. wt. inorganic fertilizer, 1-5 pts. wt. microelement, 0.1-5 pts. wt. composite fermentation, 1-2 pts. wt. ferment fungus, 2-5 pts. wt. humic acid, 1-5 pts. wt. chitosan oligosaccharide and 1-5 pts. wt. biological bacteria, which is a mixture of Pseudomonas HN103 and Bacillus pumilus Y11.    USE - Composite fertilizer.    ADVANTAGE - The composite fertilizer is environment-friendly, provides crop nutrient (content of nitrogen, phosphorus and potassium is more than 5%, organic matter is not less than 50%, and viable count is not less than 1 hundred million per gram), and solves problem of heavy metal and organic matter in agricultural production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing composite fertilizer, which involves:    (A) taking organic fertilizer, inorganic fertilizer, microelement, composite fermentation, ferment fungus, humic acid, chitosan oligosaccharide and biological bacteria;    (B) mixing composite fermentation and water in the weight ratio of 1:(5-50) uniformly to obtain liquid;    (C) adding obtained liquid in organic fertilizer;    (D) mixing the obtained mixture uniform;    (E) stacking the obtained mixture;    (F) fermenting the obtained mixture for 10-15 days obtain fermented product;    (G) adding ferment fungus to the fermented material;    (H) fermenting the obtained mixture;    (I) drying the fermented material at low temperature;    (J) crushing the dried material to obtain fermented product;    (K) adding inorganic fertilizer, microelement, humic acid, chitosan oligosaccharide and biological bacteria to the fermented material;    (L) mixing the obtained mixture uniformly; and    (M) granulating the obtained mixture into ball to obtain the desired product.
NOVELTY - Biological organic fertilizer comprises 80-90 pts. wt. organic fertilizer, 5-8 pts. wt. inorganic fertilizer, 1-3 pts. wt. trace element, 0.1-3 pts. wt. composite fermentation, 1-2 pts. wt. ferment fungus, 1-3 pts. wt. humic acid and 0.1-1 pts. wt. biological bacteria, which is a mixture of Pseudomonas HN103 and Bacillus pumilus Y11.    USE - Biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer is cost-effective, and provides crop nutrient and solves problem of heavy metal and organic matter in agricultural production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological organic fertilizer, which involves:    (A) taking organic fertilizer, inorganic fertilizer, trace element, Bacillus subtilis, ferment fungus, humic acid and biological bacteria;    (B) mixing composite fermentation and water in the weight ratio 1:5-50 uniformly to obtain liquid;    (C) adding organic fertilizer in the obtained liquid;    (D) mixing the obtained mixture uniformly;    (E) stacking the obtained mixture;    (F) fermenting the obtained mixture for 10-15 days;    (G) adding ferment fungus to the fermented material;    (H) fermenting the obtained mixture;    (I) drying the obtained mixture at low temperature;    (J) crushing the dried material to obtain fermented product;    (K) adding inorganic fertilizer, trace element, humic acid and biological bacteria to the fermented product;    (L) mixing the obtained mixture uniformly; and    (M) granulating the obtained mixture into ball to obtain biological organic fertilizer.
NOVELTY - Fermentation production of 16 alpha -hydroxy-hydrocortisone comprises carrying out fermentation process by adding seed culture into culture medium in a jacketed fermenter, sterilizing, cooling, inoculating 5-8% Streptomyces roseochromogenes and carrying out fermentation by performing cell growth phase after 20-24 hours of inoculation, adjusting the pH to 6-6.5, adding substrate hydrocortisone, passing clean air; and conducting microbial transformation stage.    USE - The method is useful for fermentation production of 16 alpha -hydroxy-hydrocortisone (claimed).    ADVANTAGE - The method is environmentally-friendly, and has high yield.    DETAILED DESCRIPTION - Fermentation production of 16 alpha -hydroxy-hydrocortisone comprises taking fermentation medium including 10-14 g/l glucose, 5-7 g /l yeast extract, 30-40 g/l malt extract, 4.5 g/l potassium dihydrogen phosphate, 20 g/l dipotassium hydrogen phosphate, and pH of 7; and carrying out fermentation process by adding seed culture into culture medium in a jacketed fermenter, sterilizing at charge coefficient of 0.7-0.8, cooling to 30-35 degrees C, inoculating 5-8% Streptomyces roseochromogenes and carrying out fermentation by (i) carrying out cell growth phase after 20-24 hours of inoculation, adjusting the pH to 6-6.5, adding substrate hydrocortisone, so that the fermentation broth concentration is 0.5-0.9 g/l, passing clean air, so that oxygen saturation is 20-30%, and adjusting the temperature to 30-35 degrees C; and (ii) conducting microbial transformation stage until the end of fermentation, where the fermentation time is 120-140 hours; then adjusting the pH to 7-7.5, adding substrate hydrocortisone, so that the fermentation broth concentration is 1.5-2 g/l, passing clean air, so that oxygen saturation is 50-60%, then adjusting the temperature to 35-40 degrees C, and stopping the flow of hydrocortisone 40-50 hours prior to stopping the fermentation.
NOVELTY - Preparing tigecycline (I) comprises (a) reacting N-tert-butyl-glycine (V) with 4-(4,6-dimethoxy-1,3,5-triazin-2-yl)morpholin-4-ium chloride (IV) to obtain 4,6-dimethoxy-1,3,5-triazin-2-yl tert-butylcarbamate (III), and (b) reacting (III) with 9-amino minocycline hydrochloride (II) to obtain (I).    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method: utilizes mild reaction conditions; produces product with good quality; does not produce pollution; and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing tigecycline of formula (I) comprises (a) reacting N-tert-butyl-glycine of formula (V) with 4-(4,6-dimethoxy-1,3,5-triazin-2-yl)morpholin-4-ium chloride of formula (IV) to obtain 4,6-dimethoxy-1,3,5-triazin-2-yl tert-butylcarbamate of formula (III), and (b) reacting (III) with 9-amino minocycline hydrochloride of formula (II) to obtain (I).
NOVELTY - Salt-resistant kitchen waste treatment complex microbial inoculum comprises complex bacterial cells and a carrier, where the complex bacterial cells include basic treatment bacterial cells, composed of Bacillus subtilis, Bacillus coagulans and Saccharomyces cerevisiae, where the Bacillus subtilis total viable count is 30-65%, Bacillus coagulans total viable count is 20-65%, and Saccharomyces cerevisiae total viable count is 5-50%.    USE - Used as salt-resistant kitchen waste treatment complex microbial inoculum.    ADVANTAGE - The complex microbial inoculum is suitable for heat preservation, ventilation and stir functional kitchen waste processor, contains microorganism capable of forming stable microecology, ans can tolerate high salinity, thus the kitchen waste residue after treatment can be used as microbial inoculum to continue next kitchen waste treatment, and achieves long-term use of bacteria.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing salt-resistant kitchen waste treatment complex microbial inoculum comprising (i) culturing complex microbial inoculum of various strains of bacteria, collecting bacterial cells by centrifugation, mixing to obtain wet powder complex bacterial cell, (ii) mixing carrier material each component to obtain mixed carrier, and (iii) taking step (i) obtained wet powdery complex bacterial cell and step (ii) obtained mixed carrier, preparing microbial inoculum, where the weight ratio of wet powdery complex bacterial cell and carrier is (0.8-1.3):1, preferably 1:1, drying so that the complex microbial inoculum water content is 15%, then vacuum packaging; and    (2) use of complex microbial inoculum in kitchen waste processing.
NOVELTY - This utility new type provide a one rubbish classification collecting combine marsh gas system, comprising garbage collecting wherein one of cylindrical, a garbage collection wherein, garbage collection wherein, and a corresponding set of waste discharge valve below one end in a 3 a, a garbage discharge valve, waste discharge valve; the one of waste discharge valve, a garbage discharge valve, waste discharge valve common one garbage conveying pipeline, the other end garbage conveying pipeline is connected one a garbage discharge valve, a garbage discharge valve, waste exhaust valve, one exhaust valve garbage is futher connected one garbage collecting station, a garbage discharge valve is futher connected a garbage collecting station, garbage discharge valve is futher connected three garbage collecting station, the utility model is new type is further set with a marsh gas pool, a marsh gas conveying pipeline and a gas terminal, this utility new type through rubbish classification collecting, storage, processing, and a marsh gas system, a maximum use.
NOVELTY - A capsule comprises 80-90 pts. wt. Cervus elaphus powder, 20-35 pts. wt. rhizoma drynariae extract supplement, 20-35 pts. wt. epimedium herb extract, 95-120 pts. wt. red yeast, 50-65 pts. wt. pregelatinized starch, and 50-65 pts. wt. silica.    USE - Capsule for increasing bone density (claimed).    ADVANTAGE - The capsule is safe and has no toxic and side effect. Its preparation is simple, environment-friendly, economic, efficient, and non-toxic.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the capsule comprising passing cleaned raw materials into 80 items sieve, mixing for 15-25 minutes to obtain mixed powder, and placing in capsule fill machine.
NOVELTY - The gaseous-phase contact reaction of a vicinal diol compound, formaldehyde, ammonia and a primary amine compound or primary alcohol compound is carried out in presence of a catalyst containing copper and chromium, to obtain 1-alkylimidazole compound.    USE - Manufacture of 1-alkylimidazole compound used for pharmaceutical, agrochemical, functional material, and for manufacturing ionic liquid used as recyclable solvent.    ADVANTAGE - The method enables manufacture of 1-alkylimidazole compound, with high yield.
NOVELTY - Producing bio-alcohol from jackfruit waste material comprises collecting jackfruit waste, i.e. core (rind) and fibrous part (flesh with rag); cutting and grinding to form a slurry by adding water; treating slurry of jackfruit core (rind) and fibrous part (flesh with rag) with diastase enzyme; treating the obtained slurry with Aspergillus oryzae after sterilization; centrifuging the medium and the supernatant; and inoculating the sterilized medium with Saccharomyces cerevisiae and incubating.    USE - The method is used for producing bio-alcohol from jackfruit waste material (claimed).    ADVANTAGE - A low cost and efficient method for the production of bio-alcohol from jackfruit waste material is provided. The method provides high yield content of bio-alcohol from jackfruit waste.    DETAILED DESCRIPTION - Producing bio-alcohol from jackfruit waste material involves saccharification and fermentation reactions to convert jackfruit waste into bio-alcohol utilizing mold and yeast comprises (a) collecting jackfruit waste, i.e. core (rind) and fibrous part (flesh with rag); (b) cutting and grinding to form a slurry by adding water in the ratio of 1:3; (c) treating slurry of jackfruit core (rind) and fibrous part (flesh with rag) with diastase enzyme after sterilization and incubated overnight at 30 degrees C; (d) treating the obtained slurry with A. oryzae after sterilization and incubating for 5 days at 30 degrees C at stationary conditions; (e) centrifuging the medium and the supernatant thus collected is sterilized and pH of the medium is adjusted to 4.5 before sterilization; (f) inoculating the sterilized medium with S. cerevisiae and incubating for 2 days at 30 degrees C; (g) filtering the resulting medium and distilling out the filtrate; and (h) producing alcohol which is further determined by A.O.A.C. method using specific gravity bottle.
NOVELTY - The apparatus has a cathode which comprises a macroscopic electric conducting material coated in part by nanoscopic conduction material. The photo anode and cathode are conductively interconnected for electron flow and is separated by a proton exchange membrane or a membrane electrode assembly (MEA) comprising the proton exchange membrane for the proton flow to the cathode. A self-hydrating or water capturing material is provided from the group consisting of water capturing micro-porous material and self-hydrating monolithic.    USE - Apparatus for hydrogen production from ambient air humidity and light and for transformation of generated hydrogen into electricity.    ADVANTAGE - The water oxidation is performed without back reaction and without deteriorated photo efficiency by the hydrogen generating device having semiconductor photo anode. The need to feed by liquid water supply is eliminated. The need for liquid water supply that paves the way to water-neutral sustainable energy systems is eliminated. The hydrogen production device is composed of lightweight materials and need for other input is avoided, thus energy device is compact and easier for users to employ in practice. The dehydration of the membrane electrode assembly is reduced to control or heating up of the semiconductor photo anode is reduced. The ineffective wavelengths are filtered out from the light source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for operating the apparatus for hydrogen production from ambient air humidity and light and for transformation of generated hydrogen into electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating the hydrogen production measured by mass spectrometry and estimated from the integrated photocurrent assuming 100% Faradaic efficiency.
NOVELTY - The system (10) has a moisture removal device (12) and a compressor (22) for generating a low moisture compressed natural gas stream. A multi-phase turbo expander (30) expands the cooled compressed discharge stream (32) and generates an expanded exhaust stream (34). A separator (38) separates the expanded exhaust stream and generates a vapor stream (40) comprised of methane and a LNG/ice/solid carbon dioxide slurry stream (42). One additional separator separates LNG/ice/solid carbon dioxide slurry stream, and generates a LNG output stream (52) comprised of ice/solid carbon dioxide.    USE - System for producing liquid natural gas (LNG) from natural gas stream.    ADVANTAGE - The LNG producing method integrates natural gas cleanup and refrigeration to produce the LNG by utilizing a multi-phase turbo expander. The multi-phase turbo expander allows for separation of a methane vapor stream and a LNG/ice/solid carbon dioxide slurry stream from the gas stream within the multi-phase turbo expander, and thus the need for an additional separator e.g. cyclone or gravity separator, can be eliminated. Thus, the LNG producing method provides lower equipment cost, smaller footprint, increased LNG production and lower overall cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing LNG from a natural gas stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a LNG production system.    LNG production system (10)    Moisture removal device (12)    Compressor (22)    Multi-phase turbo expander (30)    Cooled compressed discharge stream (32)    Expanded exhaust stream (34)    Separator (38)    Vapor stream (40)    LNG/ice/solid carbon dioxide slurry stream (42)    LNG output stream (52)
NOVELTY - Thermochemical process, comprises either (a) reducing an oxygenated hydrocarbon to form an alkane, and (b) using the alkane in a reforming reaction as a reducing agent for water and/or a reducing agent for carbon dioxide, or reducing a metal oxide to form a reduced metal oxide, reducing an oxygenated-hydrocarbon with the reduced metal oxide to form an alkane, and the step (b) as above per se.    USE - The thermochemical process is useful for producing fuel such as hydrogen, carbon monoxide, syngas, methanol, ethanol, butanol and propanol (all claimed).    ADVANTAGE - The thermochemical processes efficiently and economically converts solar or nuclear energy into fuels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system, comprising a reformer configured to perform the above thermochemical process.
NOVELTY - Heat generating system comprises a heat source (1) that provides sufficient heat to a fatty accelerator element to react with water, where a heat source sensor (C) is provided, which allows to adjust the temperature of the heat source. A vessel is provided with a fatty throttle element (2), which aims to maintain the fatty element throttle. A separating filter (3) is provided with multiple metal gratings. A combustion unit (4) is provided with a heat exchanger circuit. A vent (6) is formed in the heat exchanger circuit.    USE - Heat generating system.    ADVANTAGE - The heat generating system is portable and cost-effective.    DETAILED DESCRIPTION - Heat generating system comprises a heat source (1) that provides sufficient heat to a fatty accelerator element to react with water, where a heat source sensor (C) is provided, which allows to adjust the temperature of the heat source. A vessel is provided with a fatty throttle element (2), which aims to maintain the fatty element throttle. A separating filter (3) is provided with multiple metal gratings. A combustion unit (4) is provided with a heat exchanger circuit. A vent (6) is formed in the heat exchanger circuit. A water regulating unit (5) provides a water flow that maximizes heat production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a heat generating system.    Heat source (1)    Fatty throttle element (2)    Separating filter (3)    Combustion unit (4)    Water regulating unit (5)    Vent (6)    Heat source sensor (C)
NOVELTY - The cell has a membrane electrode assembly located between a pair of two-piece bipolar plates (800) and comprising an anode compartment, a cathode compartment and a proton exchange membrane. A sealing surface is formed in the bipolar plates. A gasket is located between the sealing surface and the proton exchange membrane. The gasket plastically deforms to create a seal (871) about one of the cathode compartment and the anode compartment. The gasket defines yield strength greater than yield strength of proton exchange membrane material. The sealing surface includes protrusions.    USE - Electrochemical cell for use as a fuel cell or electrolysis cell in a hydrogen purifier, a hydrogen expander and a hydrogen compressor for generating current from chemical reactions and converting chemical energy of fuel i.e. hydrogen, and an oxidant e.g. air or oxygen, into electricity and waste products of heat and water. Can also be used for natural gas, methanol and petroleum.    ADVANTAGE - The gasket can accommodate variations in pocket depth and flow fields as the gasket can deform over relatively large range of thickness, while maintaining relatively uniform compression pressure. The cell allows a cladding to provide metal benefits in which the bipolar plate is fabricated from stainless steel-clad aluminum, thus protecting an aluminum core from corrosion during cell operation, while providing high strength-to-weight ratio, high thermal and electrical conductivity of the aluminum. The cell eliminates a problem of amount of energy usage, wear and tear on moving parts, excessive noise, bulky equipment and hydrogen embrittlement.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded top perspective view of a two-piece bipolar plate.    Two-piece bipolar plates (800)    Flow structure (805)    Seals (871, 881, 891)    Pressure zone (890)    Low pressure volume (893)    Low pressure port (894)
NOVELTY - A synthesis gas comprising carbon monoxide, carbon dioxide and hydrogen is produced by treatment of municipal solid waste in reactor with oxygen produced by cryogenic air separation process. Carbon monoxide in synthesis gas is converted into mixture of carbon dioxide and hydrogen using water by water shift reaction. Carbon dioxide is separated from produced mixture and hydrogen produced is converted into ammonia using nitrogen . Ammonia is converted to urea using carbon dioxide.    USE - Manufacture of urea used as nitrogen-rich synthetic fertilizer.    ADVANTAGE - The method enables manufacture of urea, without carbon dioxide emissions. During manufacture, the elementary nitrogen which arises as by-product in the air separation is used together with hydrogen contained in the shifted synthesis gas.    DETAILED DESCRIPTION - A synthesis gas comprising carbon monoxide, carbon dioxide and hydrogen is produced by high-temperature treatment of municipal solid waste in reactor at 1000-2000 degrees C with oxygen produced by cryogenic air separation process. The indwell time of synthesis gas in the reactor is 1-5 seconds. Carbon monoxide contained in synthesis gas is converted into mixture of carbon dioxide and hydrogen using water by water shift reaction. Carbon dioxide is separated from mixture produced and hydrogen produced is converted to ammonia using nitrogen derived from cryogenic air separation. Ammonia is converted to urea using carbon dioxide, to obtain urea.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of manufacture of urea.
NOVELTY - Conversion of biomass to alkanes involves heating a biomass and a catalyst mixture to form alkane(s), at a single temperature and pressure. The catalyst mixture comprises a noble metal, and transition metal and/or transition metal compound.    USE - Conversion of biomass to alkane e.g. methane, ethane, propane, butane, pentane, hexane, alkyl cyclohexane, 1-hexanol and cyclohexyl alcohol (all claimed).    ADVANTAGE - The method enables conversion of biomass to alkane with high yield, by a single-step process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) catalyst mixture, which comprises noble metal, transition metal and/or transition metal compound, and solid acid; and    (2) reactor system, which has a reactor vessel configured to receive a biomass and a catalyst mixture, and a heater configured to heat the biomass and the catalyst mixture in the reactor vessel to produce alkane(s).
NOVELTY - Device equipped with sludge intake exhaust facility comprises sludge groove, slope portion, sludge intake exhaust pump which is installed on top of device to discharge sludge intake, sludge suction hose for sucking sludge, where end of the hose is located in the groove, hose end, 2-4 lines for pulling the hose, 2-4 line driving apparatus to move the hose, sludge reservoir for storing sludge, reflux pump which refluxes supernatant of the sludge reservoir to the fermenter and control unit for controlling the reflux pump.    USE - The device is useful for fermenting liquefied fertilizer (claimed).    DETAILED DESCRIPTION - Device equipped with sludge intake exhaust facility comprises, sludge groove (115), slope portion (117), sludge intake exhaust pump (126) which is installed on top of device to discharge sludge intake, sludge suction hose (125) for sucking sludge, where end of the hose is located in the groove, hose end (110), 2-4 lines (105) for pulling the hose, 2-4 line driving apparatus (130) to move the hose, sludge reservoir (200) for storing sludge, reflux pump (178) which refluxes supernatant of the sludge reservoir to the fermenter and control unit (300) for controlling the reflux pump.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of the liquefied fertilizer fermenting device. (Drawing includes non-English language text)    Lines (105)    Hose end (110)    Sludge groove (115)    Sludge portion (117)    Sludge suction hose (125)    Sludge intake exhaust pump (126)    Substructure (128)    Line driving apparatus (130)    Reflux pump (178)    Sludge reservoir (200)    Control unit (300)
NOVELTY - A composition used as a petroleum substitute comprises an organic solvent extract of Euphorbia tirucalli plant material.    USE - The composition is used as a petroleum substitute (claimed).    ADVANTAGE - The composition can be produced from renewable plant-based sources in a simple and economical manner.
NOVELTY - The apparatus has a first auger tube i.e. horizontal auger tube (2), provided with an inlet for a heat carrier and a second inlet for biomass, and a first outlet for pyrolysis gas and a second outlet for the heat carrier and transformed biomass. A second inclined auger tube i.e. inclined auger tube (3), is provided with an inlet at the second outlet of the first auger tube to receive the heat carrier and transformed biomass from the second outlet of the first auger tube and an outlet communicating with the first inlet of the first auger tube to deliver heat carrier to the first auger tube.    USE - Apparatus for pyrolysis of organic material biomass into solid, liquid and gas pyrolysis products.    ADVANTAGE - The apparatus prevents carryover of sand into a char recovery system to ensure balancing of sand size and airflow. The sand in the fluid bed is in a low density medium and contact between sand particles. The apparatus is provided with a steel shot that has a higher thermal conductivity than sand, so that the high energy can be transferred at a lower operating temperature from the shot to the biomass in an equivalent period of time as compared to sand reactors. The use of steel shot over sand significantly reduces auger wear and heat carrier attrition when compared to sand filled reactors.    DETAILED DESCRIPTION - The outlet of the auger tube is connected to the first inlet of the first auger tube via a classifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for pyrolysis of organic material biomass into solid, liquid and gas pyrolysis products.    Horizontal auger tube (2)    Inclined auger tube (3)    Condensation unit (4)    Charcoal recovery system (5)    Small radial fan blower (7)
NOVELTY - Preparation of methionine involves reacting 3-chloropropionaldehyde, hydrocyanic acid and ammonium bicarbonate, obtaining 5-( beta -chloroethyl)hydantoin, reacting the obtained 5-( beta -chloroethyl)hydantoin with thiourea and dimethyl sulfate, obtaining 5-( beta -methylthioethyl)hydantoin, carrying out alkali hydrolysis of 5-( beta -methylthioethyl)hydantoin, crystallizing, concentrating, desalting and recrystallizing.    USE - Preparation of methionine (claimed).    ADVANTAGE - The method provides odorless methionine by an environmentally-friendly process without producing methyl mercaptan and hydrogen sulfide.
NOVELTY - Preparation of 5-methyl-3,4-diphenyl-1,2-oxazole (III) involves subjecting (1-methyl-2-phenylcyclopropyl)(phenyl)methanone (I) to rearrangement reaction under action of catalyst (a1), obtaining 1,2-diphenylbutane-1,3-dione (II), and reacting obtained product with hydroxylamine hydrochloride under action of catalyst (a2).    USE - Preparation of 5-methyl-3,4-diphenyl-1,2-oxazole used as intermediate of parecoxib sodium.    ADVANTAGE - The method enables simple, economical and environmentally-friendly preparation of 5-methyl-3,4-diphenyl-1,2-oxazole under mild reaction conditions.    DETAILED DESCRIPTION - Preparation of 5-methyl-3,4-diphenyl-1,2-oxazole of formula (III) involves subjecting (1-methyl-2-phenylcyclopropyl)(phenyl)methanone of formula (I) to rearrangement reaction under action of catalyst (a1), obtaining 1,2-diphenylbutane-1,3-dione of formula (II), and reacting obtained product with hydroxylamine hydrochloride under action of catalyst (a2).
NOVELTY - Synthetic fireplace log comprises: wood derivative materials; and non-petroleum based binder for binding the wood derivative materials.    USE - The synthetic fireplace logs are useful in natural wood burning fireplaces.    ADVANTAGE - The synthetic fireplace logs cab be easily made from relatively inexpensive components, thus economical, and do not result in unpleasant off-gassing.
NOVELTY - Manufacture of nano-scaled graphene platelets involves performing electrochemical reaction by imposing current upon layered graphite as anode material and metal or graphite as cathode material using carboxylic acid as electrolyte source and intercalate source, respectively, obtaining carboxylic acid-intercalated graphite compound, exposing resultant material to thermal shock, obtaining exfoliated graphite and subjecting resultant exfoliated graphite to mechanical shearing treatment. The thickness of nano-scaled graphene platelets is less than 30 nm.    USE - Manufacture of nano-scaled graphene platelets used for field-emission device, hydrogen fuel storage and rechargeable battery electrode.    ADVANTAGE - The method enables manufacture of nano-scaled graphene platelets having excellent electrical property, thermal property, mechanical property and uniformity with high yield by economical and environmentally-friendly process.
NOVELTY - Preparing an alkyl compound or a mixture of alkyl compounds, involves: preparing a ketene compound (I); reacting the compound (I) to form a self-addition product; and hydrogenating the self-addition product in the presence of a metal catalyst to form the alkyl compound or mixtures of alkyl compounds. The alkyl compounds are selected from 1-butanol and 2-butanol.    USE - For preparing an alkyl compound or a mixture of alkyl compounds such as 1-butanol and 2-butanol (claimed) useful as fuel, industrial chemical, and as solvent.    ADVANTAGE - The method selectively synthesize higher alcohols useful as fuels and industrial chemicals from syngas and biomass.    DETAILED DESCRIPTION - Preparing an alkyl compound or a mixture of alkyl compounds, involves: preparing a ketene compound of formula (I); reacting the compound (I) to form a self-addition product; and hydrogenating the self-addition product in the presence of a metal catalyst to form the alkyl compound or mixtures of alkyl compounds. The alkyl compounds are selected from 1-butanol and 2-butanol.    R1 and R2=H or 1-6C alkyl.
NOVELTY - Reducing selenium levels in cell biomass from fermentation of a carbon monoxide-containing gaseous substrate, comprises fermenting the carbon monoxide-containing gaseous substrate in a fermentation medium.    USE - The processes are useful for reducing selenium levels in cell biomass from fermentation of a carbon monoxide-containing gaseous substrate.    ADVANTAGE - The processes: are effective for providing a cell density of at least 1 g/l, a carbon monoxide conversion of at least 5-99%, a specific space time yield of at least 1 g of ethanol/(l.day.g cells), and a selenium content in cell biomass exiting the fermentation, of less than or equal to 1 ppm, preferably less than 1 ppm (all claimed); and are cost effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) fermenting a carbon monoxide-containing gaseous substrate, comprising fermenting the carbon monoxide-containing gaseous substrate in a fermentation medium; and    (2) the fermentation medium.
NOVELTY - Production of biogas from non-pumpable biomass with gas- and liquid-tightly sealable fermenters (1) for the biomass, a biogas removal opening (2) in each fermenter, a purge gas supply opening (3) in each fermenter, and a biogas consumer, involves rinsing a fermenter using the exhaust gases from a particular additional combustion device, where the fuel is operated with a defined composition.    USE - The method is useful for the production of biogas from non-pumpable biomass (claimed).    ADVANTAGE - The method is capable of energy-efficiently producing biogas from non-pumpable biomass using fermenters in an inexpensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biogas plant for the production of biogas from non-pumpable biomass, comprising gas- and liquid-tightly sealable fermenters for the biomass, a biogas removal opening in each fermenter, a purge gas supply opening in each fermenter, a biogas consumer, and a particular additional combustion device, which can burn both the biogas and other fuels with a particular defined composition, and is connected with its exhaust pipe with the individual fermenters.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a method for the production of biogas from non-pumpable biomass.    Fermenter (1)    Biogas removal opening (2)    Purge gas supply opening (3)    Purge gas removal opening (4)    Heating pipe. (5)
NOVELTY - Biogas plant for production and utilization of biogas from non-pumpable biomass (7), comprises many gas- and liquid tight sealable fermenters (1) for biomass, a biogas removal opening (2), a weak gas-removal opening and a flushing air-removal opening in each fermenter, a flushing gas supply opening (3) in each fermenter, a weak gas collecting line (4), which is connected with the fermenter, a biogas load, and a metering controller for metering weak gas in the biogas for providing the biogas for the biogas load.    USE - The biogas plant is useful for production and utilization of biogas from non-pumpable biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing and utilizing biogas from non-pumpable biomass, comprising adding weak gas to the biogas in a small amount for the usage of the mixture of weak gas and biogas for the connected biogas-load.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Fermenter (1)    Biogas removal opening (2)    Flushing gas supply opening (3)    Weak gas collecting line (4)    Biomass (7)
NOVELTY - Special fertilizer comprises urea, monoammonium phosphate, potassium chloride, manganese sulfate, zinc sulfate, fermented chicken manure, peat, attapulgite and decomposed stone powder.    USE - The special fertilizer is useful for wheat (claimed).    ADVANTAGE - The fertilizer improves crop yield, exhibits effect for a long period of time, has improved utilization rate, and is environmentally-friendly, convenient to use, and prepared simply.
NOVELTY - Producing organic fertilizer, by (a) crushing kaolin, river silt and eggplant, heating the crushed product, and cooling to room temperature, (b) mixing dried horse manure, shrimp, sea clam shell powder, humus, hay powder and stone powder, and fermenting the mixture for 15-18 days, and (c) mixing the products obtained in steps (a) and (b), adding Angelica powder and indole-3-acetic acid to the mixture, adding water, turning the mixture, controlling moisture content to 52-55%, formulating the mixture into pellets having size of 5 mm, and drying the pellets.    USE - The method is useful for producing organic fertilizer (claimed) which is useful for promoting root growth of seedling.    ADVANTAGE - The prepared fertilizer increases survival rate of seedling and is suitable during transplanting time.    DETAILED DESCRIPTION - Method for producing organic fertilizer, involves (a) mixing kaolin and river silt in mass ratio of 5:1, mixing dried horse manure, shrimp and sea clam shell powder in ratio of 1:6, and weighing humus, hay powder, stone powder, Angelica powder, eggplant and indole-3-acetic acid, (b) crushing kaolin, river silt and eggplant to 80-120 meshes, heating the crushed product at 150-200 degrees C, maintaining for 4 hours, and cooling to room temperature, (c) mixing dried horse manure, shrimp, sea clam shell powder, humus, hay powder and stone powder, and fermenting the mixture for 15-18 days, and (d) mixing the products obtained in steps (b) and (c), adding Angelica powder and indole-3-acetic acid to the mixture, adding water, turning the mixture, controlling moisture content at 52-55%, formulating the mixture into pellets having size of 5 mm, and drying the pellets.
NOVELTY - Treating plant raw material pellets comprises exposing plant raw material pellets to a high-frequency electromagnetic field, where the exposure to a high-frequency electromagnetic field is carried out until the temperature of surface of the pellets achieves 410-450 degrees K.    USE - The method is useful for treating plant raw material pellets (claimed) for obtaining fuel.    ADVANTAGE - The method enhances the heating value of the fuel and decreases energy costs.
NOVELTY - The method involves wounding blade on conveyor shaft along backward direction, so that conveyor is charged with biomass by charge portion, while conveyor shaft is rotated. The biomass is transported through retort reaction zone where biomass is mixed continuously dried and partially gasified at retort section. The gas products of reaction are carried out with retort through outlet hole at retort section. The solid product or torrefaction is carried out through retort outlet (5) and insulated manhole (6) to oxygen-free chamber (B).    USE - Method for converting biomasses into renewable fuel.    ADVANTAGE - The waste decomposition effect is improved by reducing gas content in solids, such that the material for conversion is introduced through charging hole to chamber. The size of machine is reduced.    DETAILED DESCRIPTION - The biomass is kept in oxygen-free atmosphere for 2 to 5 minutes in temperature below 300 degrees C. The fuel which is obtained is carried out of oxygen-free chamber through the renewable fuel chute. An INDEPENDENT CLAIM is included for machine for biomass conversion into renewable fuel, has blade whose stroke is increased arithmetically from 0.04 L to 0.08 L. The retort of power generator is from length 5 to 6 m, so that stroke of blade is increased in retort reaction zone from between 0.03 and 0.05 to between 0.07 and 0.09 L along retort section.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the machine for biomass conversion into renewable fuel.    Retort (1)    Conveyor (2)    Blade (3)    Charge unit (4)    Retort outlet (5)
NOVELTY - Method for inhibiting occurrence of thermal decomposition deposit in thermal decomposition gasification system involves gasifying biomass (S2) through pyrolysis in a thermal decomposition gasifier (5) to form pyrolysis gas (G1) and carbide (C) which are continuously generated, subjecting pyrolysis gas (G1) and carbide (C) to separation in solid-gas separation unit (7), providing oxygen-containing gas (G3) to separated pyrolysis gas (G1), and introducing pyrolysis gas (G1) with oxygen-containing gas (G3) to combustion furnace (6) through a pipe (9) of pyrolysis gas line (8).    USE - Method for inhibiting occurrence of thermal decomposition deposit in thermal decomposition gasification system used for manufacturing carbide as carbonized fuel for electric power generation.    ADVANTAGE - The method inhibits occurrence of thermal decomposition deposit in thermal decomposition gasification system by efficient process. Generation of increase of fan output with deterioration of balance of an impeller, obstruction of piping and increase in vibration in inhibition of occurrence of thermal decomposition deposit in thermal decomposition gasification system are suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for thermal decomposition gasification system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the thermal decomposition gasification system. (Drawing includes non-English language text)    Thermal decomposition gasifier (5)    Combustion furnace (6)    Solid-gas separation unit (7)    Pyrolysis gas line (8)    Pipe (9)    Carbide (C)    Pyrolysis gas (G1)    Oxygen-containing gas (G3)    Biomass (S2)
NOVELTY - An isolated strain expressing lipase (CGMCC 7507), is new.    USE - The isolated strain expressing lipase is useful for producing lipase and biodiesel (all claimed).    ADVANTAGE - The isolated strain is produced cost-effectively, and has high substrate specificity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) lipase comprising (a) an amino acid sequence of SEQ ID NO: 1, or (b) conservative variants having the amino acid sequence of SEQ ID NO: 1; (2) isolated nucleic acid molecule encoding the lipase, comprising 1-1842 base pair sequences of SEQ ID NO: 2, where the nucleic acid molecule comprises base pair sequence of SEQ ID NO: 2; (3) recombinant cell comprising the nucleic acid molecule, where the recombinant cell is Escherichia coli and yeast, preferably Escherichia F6 (CGMCC 7507); (4) recombinant vector comprising the nucleic acid molecule, where the recombinant vector is plasmid chosen from pUC19 containing nucleic acid molecule of pWB201, PRK415 containing nucleic acid molecule of pWB204, and pCold-TF containing nucleic acid molecule of pWB210; (5) method for producing lipase, involves culturing above-mentioned strain and/or recombinant cell in a culture medium, adding lipase inducing agent to the culture medium, and obtaining lipase, where the strain and/or recombinant cell have ability to produce lipase, the lipase inducing agent is triglycerides, and the triglyceride is olive oil, palm oil, coconut oil, soybean oil or palm kernel oil; and (6) method for producing biodiesel, involves using the a strain, lipase, or recombinant cell, where the solution comprising lipase acts as catalyst. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published pct sequences/publication.
NOVELTY - Photoelectrically active parent functional branched macromolecules are prepared, and dissolved in N,N-dimethylformamide, to obtain polymer solution. To the obtained solution, carbon nanotubes are added, deionized water is dripped and self-assembled, to obtain polymer/carbon nanotube composite. Product is dripped in surface of electrode (e1), UV light is irradiated and dried. The electrode (e1), reference electrode (e2) and counter electrode (e3) are placed in lithium perchlorate/acetonitrile, and electrically-aggregated, to obtain carbon nanotube composite electrochemical sensor.    USE - Preparation of carbon nanotube composite electrochemical sensor used in simultaneous detection of dopamine and paracetamol.    ADVANTAGE - The method enables energy saving and environmentally-friendly preparation of carbon nanotube composite electrochemical sensor having excellent stability and durability, and high sensitivity.    DETAILED DESCRIPTION - Photoelectrically active parent functional branched macromolecules are prepared by chain transfer radical polymerization method. The resultant product is dissolved in N,N-dimethylformamide, to obtain polymer solution. To the obtained solution, carbon nanotubes are added and ultrasonically dispersed in a water bath, to obtain polymer/nanotube mixture. Deionized water is slowly dripped in the polymer/nanotube mixture under magnetic stirring action, and self-assembled, to obtain polymer/carbon nanotube composite. The resultant product is placed in a dialysis bag. The resultant product is dripped in surface of electrode (e1), UV light is irradiated and naturally dried. Then, three-electrode system of obtained electrode (e1), a reference electrode (e2) and counter electrode (e3) are placed in lithium perchlorate/acetonitrile, and electrically-aggregated in electrochemical workstation, to obtain carbon nanotube composite electrochemical sensor.
NOVELTY - An environmentally-friendly fuel comprises 36-56.8 %mass refined biodiesel, 42.6-63.2 %mass refined coking diesel, 0.5-0.7 %mass mutual solvent and 0.008-0.1 %mass antioxidant. The refined biodiesel is obtained by carrying out crude methanol synthesis using waste cooking oil and methyl ester as raw material, carrying out oxidation bleaching process, and deacidifying the resultant product. The refined coking diesel is obtained by processing coking diesel as raw material using ionic liquid.    USE - Environmentally-friendly fuel is used for vehicle.    ADVANTAGE - The environmentally-friendly fuel having high quality is manufactured by economical and safe process.    DETAILED DESCRIPTION - An environmentally-friendly fuel comprises 36-56.8 %mass refined biodiesel, 42.6-63.2 %mass refined coking diesel, 0.5-0.7 %mass mutual solvent and 0.008-0.1 %mass antioxidant. The refined biodiesel is obtained by carrying out crude methanol synthesis using waste cooking oil and methyl ester as raw material, carrying out oxidation bleaching process, and deacidifying the resultant product. The refined coking diesel is obtained by processing coking diesel as raw material using ionic liquid, degumming the resultant product, carrying out saponification and washing the resultant product using alkali compound to remove odor and nitrogen oxide.
NOVELTY - Platenomycin A1 separation and purification involves stirring inorganic acid or organic acid solution of 2-6 pH value, and then centrifuging or filtering to prepare acidic solution. An alkaline solution of 7.0-8.0 pH value is added in the prepared acidic solution for fermenting to get filtered liquid fermentation liquid. The obtained fermentation liquid is mixed with alkaline solution of 9.0-11.0 pH value to get primary alkali precipitation.    USE - Method for separating and purifying Platenomycin A1 (claimed).    ADVANTAGE - The method provides Platenomycin A1 in a simple, cost-effective and eco-friendly manner on industrial scale.    DETAILED DESCRIPTION - Platenomycin A1 separation and purification involves stirring inorganic acid or organic acid solution of 2-6 pH value, and then centrifuging or filtering to prepare acidic solution. An alkaline solution of 7.0-8.0 pH value is added in the prepared acidic solution for fermenting to get filtered liquid fermentation liquid. The obtained fermentation liquid is mixed with alkaline solution of 9.0-11.0 pH value to get primary alkali precipitation. The formed primary alkali precipitate is dissolved in acidic solution of 2.0-6.0 pH value to form penicillin salt solution, which is added in alkaline solution having pH value of 9.0-11. The resulting mixture is fermented to get primary alkali precipitate, which is refined and dried to obtain pure carbonaceous solid as the finished product.
NOVELTY - Methanol denaturant comprises 5-20 pts. vol. methyl tertiary butyl ether, 1-4 pts. vol. methyl oleate, 1-6 pts. vol. dimethoxymethane, 1-4 pts. vol. acetone, 0.5-2 pts. vol. ethanolamine, 0.05-0.2 pts. vol. methylbenzotriazole, 0.05-0.2 pts. vol. mercaptobenzothiazole, 0.2-1 pts. vol. isopropyl palmitate, and 0.1-0.5 pts. vol. methylcyclopentadienyl manganese tricarbonyl.    USE - The methanol denaturant is useful for preparing gasoline from methanol (claimed).    ADVANTAGE - The methanol denaturant produces No. 93 gasoline, reduces cost by more than 20% and reduces emissions by 20-80%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the methanol denaturant, comprising (i) stirring and dissolving methylbenzotriazole and mercaptobenzothiazole in dimethoxymethane at room temperature to obtain solution A, (ii) stirring and dissolving methylcyclopentadienyl manganese tricarbonyl in acetone to obtain solution B, and (iii) pumping methyl tertiary butyl ether into a reaction kettle, stirring under speed of 30-50 revolutions/minute, adding methyl oleate, solution A, solution B, isopropyl palmitate, ethanolamine, and stirring for 15-30 minutes; and    (2) use method of the methanol denaturant in preparing gasoline from methanol, comprising stirring and pumping methanol, methanol synthesis gas, alcohol ether fuel poly-methoxy that formaldehyde (sic) and methanol denaturant into a reaction kettle and stirring under speed of 20-40 revolutions/minute at 20-30 degrees C for 10-20 minutes.
NOVELTY - Treating an organic waste material, comprises (a) subjecting waste to anaerobic fermentation in a biogas digester, (b) mechanically separating effluent from the biogas digester into a concentrated fraction and a liquid fraction, (c) heating the liquid fraction to a high temperature below the boiling point of the liquid, (d) introducing the heated liquid to a flash column to partially remove volatile carbon dioxide and to elevate pH of the liquid, and (e) removing ammonia from the liquid.    USE - The method is useful for treating an organic waste material (claimed) including manure from intensive livestock production, e.g. intensive production of pigs and dairy cattle, wastes from households, industries and agricultures, sewage from institutions such as hospitals, and effluents from biofuel production. The organic waste material is useful for producing biogas, phosphate rich fertilizers, producing ammonium sulfate rich fertilizers and/or producing potassium rich fertilizers for crop production. The biogas is useful as fuel for gas motors and power generation.    ADVANTAGE - The method economically treats the organic waste material with little maintenance to increase production of biogas in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plant for treatment of an organic waste material, comprising a biogas digester, a unit for mechanically separating effluent from the biogas digester into a concentrated fraction and a liquid fraction, a unit for heating the liquid fraction, a flash column to partially remove volatile carbon dioxide and to elevate pH of the liquid, and a unit for removing ammonia from the liquid.
NOVELTY - A fluoropyruvic acid derivative (I) or hydrate of fluoropyruvic acid derivative (II) is reduced asymmetrically using ( alpha )-keto acid dehydrogenase or ( alpha )-keto acid reductase, to obtain optically-active fluorolactic acid derivative (III).    USE - Manufacture of optically-active fluorolactic acid derivative. Uses include but are not limited to intermediate of pharmaceutical and agrochemical, liquid crystal, surfactant, and functional film.    ADVANTAGE - The method enables efficient manufacture of optically-active fluorolactic acid derivative with high optical purity and productivity, by economical and environmentally-friendly process.    DETAILED DESCRIPTION - A fluoropyruvic acid derivative of formula (I) or hydrate of fluoropyruvic acid derivative of formula (II) is reduced asymmetrically using ( alpha )-keto acid dehydrogenase or ( alpha )-keto acid reductase, to obtain optically-active fluorolactic acid derivative of formula (III).    n=1-3;and    R=H or 1-10C linear or branched alkyl.
NOVELTY - Anaerobic digestion involves producing a gas including condensable vapors and non-condensable gasses from pyrolysis of a feedstock (A), and adding the gas to an anaerobic digester (1), in which the condensable vapors are added in vapor or liquid form.    USE - Anaerobic digestion (claimed).    ADVANTAGE - The method enables efficient anaerobic digestion with reduced usage amount of bio-solids.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of anaerobic digestion and pyrolysis system.    Anaerobic digester (1)    Pyrolysis reactor (5)    Gas heat exchanger (6)    Feedstock (A)    Digestate (B)
NOVELTY - Producing (P1) carbon nano fibers and/or tubes, involves pyrolyzing a particulate cellulosic and/or carbohydrate substrate that has been impregnated with a metal compound or combination of metal compounds, which are capable of forming carbides, in oxygen free, volatile silicon compound containing atmosphere, optionally in the presence of a carbon compound.    USE - For producing carbon nano fibers and/or tubes (claimed) which are useful for catalytic applications.    ADVANTAGE - The method produces carbon nano fibers and/or tubes from relatively abundantly occurring natural materials, in some circumstances even without the need for external supply of carbon compounds (often from non-renewable sources).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a catalyst (D1) comprising a support material and at least one catalytically active material or a precursor of it, where the support material is carbon nanotubes and/or nanofibers prepared by the process (P1); and    (2) performing at least one chemical reaction in the presence of a supported catalyst, where the supported catalyst comprises the catalyst (D1).
NOVELTY - System (100) comprises processor (102) for reducing the water content in carbonaceous material; and tank connected to the processor, for storing fluids, and for transmitting fluids to and from the processor.    USE - As system useful for upgrading carbonaceous materials such as biomass, where sources of biomass feedstock include plant matter, animal matter, sea matter, organic waste, and other materials of biological origin; petroleum coke such as coal, coker unit operations, or cracker unit operations; and carbonaceous waste products e.g. carbon-containing material susceptible to upgrading and representing waste from industrial, natural, or municipal sources.    ADVANTAGE - The system provides carbonaceous materials that not only have decreased moisture and impurity contents, but also have stability to atmospheric moisture, decreased dustiness, and reduced likelihood of spontaneous combustion.    DESCRIPTION OF DRAWING(S) - The figure shows depicts of system for upgrading carbonaceous material.    System (100)    Processor (102)    Input/output mechanism (104)    Input (106, 108, 110)
NOVELTY - A purified saccharification mixture comprising sugars including glucose and xylose is concentrated to provide saccharified biomass.    USE - Method for saccharifying biomass used for producing energy, fuel e.g. gasoline for powering cars, trucks, tractors, ships, trains, planes having jet engines and helicopters. Can also be used for producing foodstuffs, hydrogen, n-propanol, n-butanol, sugars, biodiesel, acetic acid and/or lactic acid, hydrocarbons, cellulolytic proteins, carboxylic acids, etc.    ADVANTAGE - The method provides fuel which can be transported economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for purified saccharification mixture.
NOVELTY - Genetically enhanced ethanologenic Cyanobacterium sp. ABICyanol host cell comprising Cyanobacterium sp. ABICyanol deposited in ATCC accession number - not defined comprising a genetically enhanced plasmid derived from a plasmid that is endogenous to Cyanobacterium sp. ABICyanol, is new, where the plasmid comprises a heterologous adh gene and a heterologous pdc gene. The adh gene is operably linked to a constitutive promoter, and the pdc gene is operably linked to an inducible promoter.    USE - The genetically enhanced ethanologenic Cyanobacterium sp. ABICyanol host cell is useful for producing chemical compounds including biofuels, industrial chemicals, pharmaceuticals, nutrients, carotenoids and food supplements.    ADVANTAGE - The genetically enhanced ethanologenic Cyanobacterium sp. ABICyanol host cell can tolerate salinities of 35 practical salinity units, and/or can tolerate temperatures of up to 55 degrees C, can tolerate dissolved oxygen concentrations of up to 1000 mu mol/l, and/or can tolerate ethanol concentrations of up to 1% for 16 weeks, and produces 0.017-0.031 vol./vol. ethanol per OD(750) per day (claimed).
NOVELTY - Use of amide or ester derivatives (I) as a deodorizing agent, is claimed.    USE - (I) are useful as a deodorizing agent in a cosmetic composition for treating body odor, preferably underarm odor (all claimed).    ADVANTAGE - (I) can effectively reduce or eliminate the unpleasant underarm odors, and can be simply prepared with high quality.    DETAILED DESCRIPTION - Use of amide or ester derivatives of formula (I) or their optical isomers as a deodorizing agent, is claimed.    X- = organic or inorganic anion;    Y1 = O or NR1;    R = linear or branched, optionally saturated 2-22C-alkyl, aralkyl (in which alkyl is linear or branched, optionally saturated 1-22C-alkyl and the aryl is phenyl optionally substituted by linear or branched 1-4C-alkyl) or aryl, preferably phenyl (optionally substituted by linear or branched 1-4C-alkyl); and    R1 = H or R.    INDEPENDENT CLAIMS are included for:    (1) amide or ester derivatives of formula (A) or (B) or their optical isomers;    (2) a cosmetic composition comprising, in a medium, (I) optionally in combination with at least one active antiperspirant and/or at least one another active deodorant, where the composition is accompanied by a packaging or user information with visual information concerning the treatment of odor and/or perspiration of a human, and/or information about the presence of the active antiperspirant and/or active deodorant, optionally other visual information; and    (3) an aerosol device comprising at least one container comprising the composition, at least one propellant, and at least one unit for distributing the composition in aerosol form.    Z- = organic or inorganic anion preferably bromide, sulfate, methanesulfonate, citrate, lactate or acetate, Z excludes chloride.
NOVELTY - One of rural household garbage and sewage treatment system, comprising sewage collecting pool and domestic garbage bin, on sewage collecting pool provided with grizzly screen well, sewage collecting pool and regulating pool, Anaerobic slot, anoxic groove, oxidation pool, sediment pool and shallow underground water filtering system and sterilizing pool orderly connected, domestic garbage storage bin and marsh gas pool connected with marsh gas output end of marsh gas pool, slag input end and output end separately marsh liquid and marsh gas tank, a sludge dry in room and regulating connection pool, marsh gas storage tank connected with the marsh gas power generation system, a sludge dry in room and waste gas output end and shallow underground water filtering system connected, Anaerobic groove, groove and anoxic oxidation pool are set with sludge relux port, relux port sludge by sludge pool and marsh gas pool connected with. The utility model is new sewage processing station via AAO technology process and shallow underground water filtering system purification water quality, and domestic garbage processing system and connected, can be comprehensively processing rural household garbage, sewage and sewage treatment station sludge equal problem, the suitable high efficient, low investment cost low, small land occupation, high benefit.
NOVELTY - Production of carbon disulfide using biological waste comprises waste material processing to biological charcoal, mixing combustible gas, reacting and heating.    USE - Method for producing carbon disulfide using biological waste (claimed).    ADVANTAGE - The method is simple, convenient, economical, environment-friendly and has short reaction time.
NOVELTY - This utility new type claims a hydropower station one sterile water surface garbage processing system, comprising transmission belt in turn through connecting a garbage stacking chamber, sterilizing room, a cutting system, mix stirrer, a compressor, a drying room, a granulator, and a finished product bin, further comprising mix and a stirrer of a combustion improver storage bin and adhesive. This utility new type garbage becomes the new fuel, not only the requirement of sanitary production, purification and subsequent environment of garbage treatment, fine fuel form a unified specification, a changing waste into valuable, solves the problem that the waste caused by the accumulation of a secondary pollution, which is good for protection of the environment, but also obtain the a duration of fuel resource, has wide social value and economic value.
NOVELTY - Synthesizing dehydropregnenolone acetate oxime (I) with molar yield of 99% and product content of 98% or more.    USE - The method is useful for synthesizing dehydropregnenolone acetate (I) (claimed).    ADVANTAGE - The method is simple, clean and suitable for large-scale production of dehydropregnenolone acetate (I), has high sensitivity, produces high quality dehydropregnenolone acetate at yield of not less than 99%, and reduces generation of waste.    DETAILED DESCRIPTION - Synthesizing dehydropregnenolone acetate oxime of formula (I) with molar yield of 99% and product content of 98% or more.
NOVELTY - Production of biomass methane involves performing solid-liquid separation of biogas slurry using mesh filter, adding filtered slurry to settling tank, adding slurry to upper water washing column using pump, compressing biogas using compressor, adding compressed biogas to bottom of water washing column, contacting compressed biogas and slurry, absorbing carbon dioxide and hydrogen sulfide, discharging absorbing liquid from bottom of washing tower, and discharging overhead biogas to molecular sieve dryer.    USE - Production of biomass methane (claimed).    ADVANTAGE - The method enables preparation of biomass methane having methane concentration of more than 88%, carbon dioxide concentration of less than 10% and high purity, with reduced water consumption. The discharge produced during the method does not cause eutrophication of lakes and rivers, and contaminate soil and groundwater. The raw material biogas slurry is easily bio-decomposed.
NOVELTY - An environmentally-friendly clean alternative methanol diesel fuel oil is obtained by providing methanol, diesel, biodiesel and high-boiling solvent oil as main raw materials, and adding multifunctional composite additives. The raw material comprises 10-40 wt.% methanol, 10-40 wt.% diesel, 5-50 wt.% biodiesel, 5-30 wt.% high-boiling solvent oil and 8-30 wt.% multifunctional composite additive.    USE - Environmentally-friendly clean alternative methanol diesel fuel oil is used in diesel engine and industrial boilers.    ADVANTAGE - The clear, bright, odorless and environmentally-friendly clean alternative methanol diesel fuel oil has excellent viscosity, stability and dynamic characteristics, and high calorific value. The environmentally-friendly clean alternative methanol diesel fuel oil does not change color and separate into layers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environmentally-friendly clean alternative methanol diesel fuel oil, which involves adding complexing agent (A) to methanol with stirring, adding biodiesel and diesel for 10 minutes, adding high-boiling point solvent oil for 15 minutes, adding complexing agent (B) and complexing agent (C) with stirring for 10 minutes, filtering and obtaining yellowish transparent complex methanol-diesel fuel oil.
NOVELTY - A composite microbial inoculum comprises liquid inoculant made by the fermentation of bacteria, total number of viable cells of not less than 2\108, Candida utilis, Aspergillus sojae, Lactobacillus bulgaricus, Lactobacillus lactis, Rhodopseudomonas palustris, capsular red sphere Pseudomonas aeruginosa per ml of the inoculum.    USE - Composite microbial inoculum for use in sludge anaerobic digestion treatment.    ADVANTAGE - The inoculum increases degradation rate of organic matter, accelerates sludge hydrolysis process, shortens anaerobic digestion time, and improves bio gas production effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing a composite microbial inoculum.
NOVELTY - The system has three-inlet ports connected to raw material pump (5), auxiliary material pump (6) and additive pump (7). The material output end of reverse emulsifying device (2) is connected with bottom of feeding deice by valve and pipeline. The forward emulsifying device (3) is set with multi-way liquid flow pipeline. The reverse emulsifying device is used to provide reverse impact force so as to fully emulsify methanol and gasoline. Filter device (4) is set with a filter screen. Lower portion of filter device is fixed with a discharging port for discharging the hydrocarbon oil.    USE - MCH-40 hydrocarbon oil production system for producing hydrocarbon oil used for powered vehicles.    ADVANTAGE - Continuous and uninterrupted production of hydrocarbon oil is ensured. The productivity and production efficiency of the system is improved. The emulsifying process is performed continuously and easily without the need of a stirrer. The system uses molecular collision theory to perform the production process, such that the production process is simple. The energy consumption of the system is reduced. The oil production cost is reduced. The production quality is improved. High quality hydrocarbon oil is produced. The production system is effectively used in factories.    DETAILED DESCRIPTION - The discharge port is connected with the top portion of reverse emulsifying device through valve and pipeline. The inside of reverse emulsifying device is set with an efficient atomizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrocarbon oil production system.    Reverse emulsifying device (2)    Forward emulsifying device (3)    Filter device (4)    Raw material pump (5)    Auxiliary material pump (6)    Additive pump (7)
NOVELTY - This utility new type relates to a one large medium marsh gas concentration automatic monitoring system of gas supplying engineering, comprising monitoring computer, in a set with a temperature sense device of fermentation reaction furnace and a fermentation pool, liquid level sensor and the pH a sense device, pressure sense device set in a fermentation pool of a, set with a gas component detection in a dehydrating device and storage cabinet in pneuma, set with a physicochemical property sensor in pre-processing pool and mounted in a biogas pneuma metering in a user, this utility new type the embedded system is introduced to biogas fermentation engineering in, the monitoring device can greatly reduce the cost for a temperature, pH value, such as liquid level in the marsh gas pool. change time real-time detecting, monitoring personnel know the change of marsh gas fermentation pool, and the monitoring system in a meter reading charging function, the existing methane gas monitoring device function more complete.
NOVELTY - The system has a feeder (200) whose two ends are connected to the storage hopper (100). The sawdust granulating machine (300) is connected with the storage hopper for granulating the wood chips. The system comprises a fan (400) and dust removing device (500). The dust removing device is connected with the discharge port of the sawdust granulating machine. The fan is connected with the dust removing device. The waste gas in the sawdust granulating machine is removed by dust-removing device, using gas-solid separating process.    USE - Sawdust granulation system for reducing environmental pollution.    ADVANTAGE - The system can process waste gas with low environmental pollution so that the working quality in the workshop is improved, and the dust collected with the dust removing is returned to the storage hopper for recycling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sawdust granulation method for reducing environmental pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the Sawdust granulation system for reducing environmental pollution.    Storage hopper (100)    Feeder (200)    Sawdust granulating machine (300)    Fan (400)    Dust removing device (500)
NOVELTY - This utility new type claims a biomass granule fuel one molding machine, the technology solution feeding cover 4 is set with a cutting device, cutting device comprise cutting knife, a telescopic column, guide pipe, pressing plate, a feeding cover 4 outside the circumferential side wall and set with a same of telescopic telescopic cylinder through hole, the telescopic column is set in guide tube, the telescopic cylinder and guide pipe matched with the guide tube one end fixed up in a feeding cover 4 outside the circumference side wall, guide tube and telescopic through hole, the telescopic cylinder through the through hole extends into the flexible feeding cover 4 inner cutting knife fixed in a telescopic cylinder relative feeding cover 4 one end, the other end set with telescopic cylinder sliding wheel, a guide tube outside the side set with limiting device, pressing plate comprise active plate, transmission plate, a driving plate and transmission plate are set with the guide pipe set with a device side, a driving plate and a sliding connecting device, transmission plate and the driving plate is 45 degrees, the transmission plate is propped against in a sliding wheel, a telescopic cylinder set with reset device.
NOVELTY - The furnace has a feeding port (12) through a feeding pipe (11) is connected to the bottom of the furnace housing (1). An air outlet is provided in the upper surface of the furnace housing. A lower pushing feeding device comprises a feeding pushing plate and the left and right sliding plates. The left and right sliding plates are connected with the feeding port. The feeding pushing plate is connected with a material feeding port (16). The size of the outward inner wall of the feeding port is made smaller than a size of the inner feeding tube.    USE - Straw gasification furnace.    ADVANTAGE - The combustion and removal of the gasification furnace are made efficient, the structure is simple, the operation is convenient, time saving is achieved, and the ash-discharge property and combustion gasification are attained.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the straw gasification furnace.    Furnace housing (1)    Feeding pipe (11)    Feeding port (12)    Lug boss (13)    Material feeding port (16)
NOVELTY - This new utility model claims of one resource again using a kind of system, this system comprises sorting plant, plant gas, RDF plant and landfill plant, sludge of the system can domestic garbage and municipal, harmless and recycling high degree of resource consume low, this new utility model that uses the energy substance are from domestic garbage and municipal sludge, and is set with the separation plant, air plant, power plant and landfill plant can finish using resource of each other, energy supply from the can and for natural gas pipe network and state power grid supply biology natural gas and electric energy.
NOVELTY - The furnace has a hopper-shaped ash outlet (2) and a hopper-shaped dust collecting pool (3) at an outer furnace (1). The pool is externally connected with an ash outlet pump (4). A pair of pressing roller support is lifted on the inner and outer tracks up along the inner and outer rails around an axis rotating state. A lifting bearing base is connected with a lifting press spring. A press roller is connected on the lifting bearing base in a rotating state. The lower portion of the outer furnace is externally connected with a speed reducer and an inner shaft (8).    USE - Gasification furnace of primary-secondary garbage straw.    ADVANTAGE - The gasification furnace satisfies different raw material gasification, in large scale production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the primary-secondary garbage straw gasification furnace.    Outer furnace (1)    Ash outlet (2)    Dust collecting pool (3)    Ash outlet pump (4)    Inner shaft (8)
NOVELTY - The furnace has a lower push feeding device connected with a bottom part of a furnace body through a feeding pipe and a feeding port. An upper part of the furnace body is fixed with an air outlet. A lower pushing feeding device is provided with a feeding oil jar, a feeding push plate, the feeding pipe, a feeding sealing plate and a feeding oil jar. An anti-dropping baffle plate is fixed vertical to the feeding port along axial direction. The anti-drop baffle plate is connected with an anti-dropping oil jar that is separated from the feeding port and the feeding oil jar.    USE - Lower material pushing pole pneuma straw gasification furnace.    ADVANTAGE - The furnace has high combustion gasification efficiency and discharge property, and is convenient to operate. The furnace reduces labor time and labor intensity.    DETAILED DESCRIPTION - The furnace body is provided with an ash-scraping shaft i.e. gap.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a lower material pushing pole pneuma straw gasification furnace.
NOVELTY - The biomass-feeding device is comprised of a horizontal feeding pipe (1), a vertical feeding pipe (2), a spiral feeder (3), a gas turbine (4) and an air supply pipe (5). One end of the horizontal feeding pipe is connected with the vertical feeding pipe. The feeding pipes are connected with the gas turbine. The spiral feeder is equipped at an inner portion of the horizontal feeding pipe which is arranged in parallel with respect to the air supply pipe.    USE - Biomass-feeding device for pyrolysis.    ADVANTAGE - The biomass-feeding device is featured with high reliability, compact structure, high heating speed, fast and reliable feeding, convenient temperature regulating function, good adaptability, high heat utilization rate, and wide market prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic structural view of the biomass-feeding device.    Horizontal feeding pipe (1)    Vertical feeding pipe (2)    Spiral feeder (3)    Gas turbine (4)    Air supply pipe (5)
NOVELTY - A cellodextrin transport (CDT-2) protein in yeast for transporting oligosaccharides is new.    USE - The CDT-2 protein is useful for transporting oligosaccharides (claimed) for improved biofuel production.    ADVANTAGE - The CDT-2 protein is used for low cost and improved biofuel production.
NOVELTY - This utility new type claims a one energy-saving environment-friendly alkali catalytic ester exchange method production device of biological diesel oil. Device comprising raw material mix tank, reactor, the first buffering tank, a methanol rectifying tower, second buffering tank, a first liquid tank, a second liquid tank, an evaporator, a first condenser, a glycerol glycerine condenser second and third glycerine condenser. This utility new type technology to be solved is the problem existing with homogeneous alkali catalysis ester exchange reaction method a biological diesel oil technique flow is long, the unit yield energy consumption, waste liquid discharge amount of large, obviously shortened, at least the step of water washing and drying. This utility new type in which greatly improves utilization rate of the raw material, methanol all a, alkali catalyst also can be crystallized from a use in the back evaporation, so utilization rate of the raw material is high.
NOVELTY - Method for comprehensive application of seeds of Celastrus orbiculatus and/or Amaranthus retroflexus, involves (a) drying seeds of C.orbiculatus and/or A.retroflexus, and extracting the seeds to separate oil and to obtain extract (A), (b) adding water to residues of C.orbiculatus and/or A.retroflexus obtained in step (a), extracting obtained mixture to separate oil and to obtain extract (B), and subjecting extract (B) to alcohol precipitation, and (c) fermenting residues obtained in step (b) to obtain organic fertilizer.    USE - The method is useful for comprehensive application of seeds of C.orbiculatus and/or A.retroflexus and for producing feedstock which is used for biodiesel production, and preparing oral liquid which is used for nourishing stomach, and organic fertilizer which is used for plants including C.orbiculatus and/or A.retroflexus and improving growth of plants (claimed).    ADVANTAGE - The method is environmentally-friendly, and avoids waste disposal problems.    DETAILED DESCRIPTION - Comprehensive application method of seeds of Celastrus orbiculatus and/or Amaranthus retroflexus, involves (a) drying seeds of C.orbiculatus and/or A.retroflexus, and extracting seeds of C.orbiculatus and/or A.retroflexus to separate oil and to obtain extract (A) which is used as feedstock for biodiesel production, (b) adding water to residues of C.orbiculatus and/or A.retroflexus obtained in step (a), extracting obtained mixture to separate oil and to obtain extract (B), and subjecting extract (B) to alcohol precipitation, where extract (B) is used as oral liquid for nourishing stomach, and (c) fermenting residues obtained in step (b) to obtain organic fertilizer which is used for plants including C.orbiculatus and/or A.retroflexus and improving growth of plants. An INDEPENDENT CLAIM is included for use of extract (A) in preparation of feedstock for biodiesel production.
NOVELTY - This utility new type relates to a one conversion into biological diesel oil of oil recovery using system, comprising a waste oil collecting tank, the tank through pipeline and the first filter, the rear filter of waste oil through one pump conveying to the first molecule distiller, rear distillation of the product conveying to a neutral oil collecting tank and fatty acid collecting tank through pipeline, and the methanol conveying tank catalyst tank through pipeline and a neutral oil collecting tank and a fatty acid collecting tank, a through ester exchange reactor and esterification reactor rear, and a methanol recovery tank and a rear reaction product conveying to crude fatty acid methyl ester settling tank, and a second molecule distiller through pipeline, by a rear product distilled through the mix for the a separate separator, separate rear through a conveying pipeline to biological diesel oil collecting tank and plant asphalt collecting tank. This utility new type fully of the conversion into biological diesel oil, reduce environmental pollution, avoids the waste of resource, increase the valid utilization rate of resource.
NOVELTY - This new type utility claims one of a low temperature CO2-rich methanol washing to reduce a loss rate of device, wherein comprising tower and medium-pressure flash tower. The traditional low temperature methanol washing the two medium-pressure flash tank a is replaced by a medium-pressure flash tower one, using the rear and a crude synthetic pneuma pneuma lift as the medium-pressure flash tower, the CH4, H2 and so on valid gas extracting pneuma; pneuma carrying out with a gas entering into a circulation pneuma to a pressurizing entering into absorption tower increase in a rate of a, reduces a from the tail pneuma, and reduces the environmental burden.
NOVELTY - The reaction kettle has small gear (5) that drives circumferential gear (9) to rotate, and rotates horizontal cylindrical casing (10) fixed with heat insulation layer (3). Other end of horizontal column-shaped casing is connected with a fixed storage hopper (18). The first discharge device structure is set with discharging pipe (8). The feeding port of horizontal spiral discharging machine is arranged on storage hopper connected to top side of gas phase product outlet (13). The casing of feeding cabin (15) or storage hopper is set with thermometer and pressure table.    USE - Horizontal rotating type domestic garbage pyrolysis reaction kettle.    ADVANTAGE - The heat utilization efficiency is improved. The heat transfer effect is improved. The domestic garbage continuous production of horizontal rotating pyrolysis slag in reaction kettle is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the domestic garbage pyrolysis reaction kettle. (Drawing includes non-English language text)    Heat insulation layer (3)    Small gear (5)    Discharging pipe (8)    Circumferential gear (9)    Horizontal cylindrical casing (10)    Gas phase product outlet (13)    Feeding cabin (15)    Storage hopper (18)
NOVELTY - Composition comprises a fermented product of an organic acid extract of Oenanthe javanica as an active ingredient.    USE - The composition is useful as a food composition for preventing or treating inflammation diseases (all claimed). No biological data given.
NOVELTY - A power generation system by fermented straw. A traditional combustion generating electricity by straw of method exist operation efficiency is low, the operation cost is high, seasonal limit, product market limit, environment pollution and resource waste and so on. This utility new type is include the marsh gas tank (5), the marsh gas tank and a filter press (1), marsh gas purifier (6), a waste heat boiler (12), a heat exchanger (4) connect, the filter and the storage tank (2) connecting, the liquid storage tank and the condenser (7) connect, the condenser and a tower (3), the heat exchanger, the waste heat boiler, a steam turbine (11) connecting, the a and a waste heat boiler of a steam turbine, a gas engine (9) connect, the biogas engine with the pneuma cabinet (8) connect, the gas storage cabinet is connected with the marsh gas purifier connect. This utility new type used for generating electricity by straw fermentation.
NOVELTY - Preparing a lubricant product comprises: (a) combining at least one olefin and at least one coordination-insertion catalyst under conditions such that at least one oligomer product is formed; (b) fractionating the oligomer product to produce a fractionated oligomer product such that an average carbon number of the fractionated oligomer product is greater than or equal to 20; and (c) hydrogenating the fractionated oligomer product to form the lubricant product. The coordination-insertion catalyst is: a metal-ligand complex, where the metal is zirconium, hafnium or titanium.    USE - The process is useful for preparing a lubricant product such as a saturated hydrocarbon (all claimed).    ADVANTAGE - The process is capable of economically preparing the lubricant product with high stability, low pour points and improved cold temperature performance and viscosity index.    DETAILED DESCRIPTION - Preparing a lubricant product comprises: (a) combining at least one olefin and at least one coordination-insertion catalyst under conditions such that at least one oligomer product is formed; (b) fractionating the oligomer product to produce a fractionated oligomer product such that an average carbon number of the fractionated oligomer product is greater than or equal to 20; and (c) hydrogenating the fractionated oligomer product to form the lubricant product. The coordination-insertion catalyst is: a metal-ligand complex; and has an ethylene/octene reactivity ratio of up to 20, at an operating reactor temperature, and a kinetic chain length of up to 20 monomer units. The metal is zirconium, hafnium or titanium. An INDEPENDENT CLAIM is included for the lubricant product prepared by the process.
NOVELTY - This new type utility claims a fast biological filter water processing reactor, include the are located on the same one inner container from lower to upper is arranged, a filter material layer and radiating layer water, further can comprise a connected water tube in the container, said inner supporting mounting with a gas distribution system and a water tube, a filter material layer is embedded with an exhaust system, a heat water layer inside is embedded with cloth water system 6. Through the exhaust system from the gas distribution system in entering into a air smoothly transporting layer in rear apron to heat air in a convenient aeration, to prevent a gap between the filter material in filter layer is too small to cause aeration can not successfully process and sewage process load high, small floor area, from about 1.5 to about 3 square per ton, reduces the floor area, reduces construction cost and operation maintenance is simple, it does not need aritificial management.
NOVELTY - Timber is made into dry wood, fed into continuous furnace, air is introduced, combustion of wood is carried out in combustion zone, heat is provided to produce gasoline and diesel, steam distillation is performed in distillation zone, carbonized steam is separated, separated steam is collected in collection chamber, and cooled in cooling unit. Wood is sent to slagging machine, produced carbon dioxide is fed into air to provide reaction gas, gas is drawn in gas collection chamber, concentrated, ash is removed, and gasoline and diesel are separated by regeneration method.    USE - Regeneration method for producing gasoline and diesel used for vehicle.    DETAILED DESCRIPTION - Timber are made into dry wood, fed into continuous furnace through wooden feeder, the roof of wooden feeder is sealed, air is introduced from the bottom of sealed furnace, combustion of wood is carried out in combustion zone, heat is provided to produce gasoline and diesel, steam distillation is performed in distillation zone, carbonized steam is separated by air pump, separated steam is collected in a collection chamber, and cooled in cooling unit. Wood is sent to slagging machine placed above the combustion zone, produced carbon dioxide is fed into air to provide reaction gas, gas is drawn in the gas collection chamber by suction from the furnace, concentrated, ash is removed from the furnace, and gasoline and diesel are separated by regeneration method.
NOVELTY - This utility new type provide the one aeration fan of a wind supply device, wherein, comprise total new wind pipeline, total new air pipeline connecting a multi-branch pipeline, the branch pipeline connecting fan, wherein the total new air in pipeline set with heat exchanger in branch pipeline set with branch pipeline valve. This utility new type for the original system does not need a large improvement to a finish for a multi-fan for new air of a pre-heating, it can provide to the biochemical technology with compare stable temperature of ambient air, the air suction temperature of aeration fan in full year compare stable, increase sludge fermentation process production efficiency, and a branch pipeline valve of it does not need power, aeration fan of the opening and closing of opening and closing for a branch pipeline control, low investment, simple mounting of.
NOVELTY - The present invention is directed to the use of microwave combined with activated carbon for the transesterification reaction, and recycling of frying oil as a raw material for the manufacture of bio-diesel refining biodiesel. Study found the microwave at a low power (200W), add the powdered activated carbon reaction in just two minutes, biodiesel conversion rate reached to 97.80%, activated carbon than not add more than 18% higher. Without the addition of activated carbon conversion rate is not very different in microwave high power (600W). In addition, the water bath was heated with stirring at a reaction time of 30 minutes or more in order to achieve the conversion rate of 98.74%. The method can be effective in reducing the reaction time and reducing the manufacturing cost. Studied optimal reaction conditions for the alcohol (methanol) to oil ratio of 7: 1, adding 1 wt% of activated carbon, catalyst (NaOH) is added to 1 wt%, the microwave power 200W, 65 DEG C for reaction for 2 minutes. This process gives a yield reach to 97.8% biodiesel which the biodiesel are within the limits prescribed by the standard CNS 15072 the yield of methyl ester at 96.5%.
NOVELTY - The method involves contacting sour gas with an absorbent solvent at predetermined temperature of less than 0 degree Celsius to remove acid gas and form a treated gas stream (80). The treated stream is heated to predetermined temperature of greater than 0 degree Celsius to form a partially heated treated gas stream (82). The partially heated stream is made to contact with water to remove an entrained absorbent solvent and form a solvent-depleted treated gas stream (90), where cooled sour gas stream (32) and partially loaded absorbent solvent stream (42) contact each other in an absorber (20).    USE - Method for removing acid gas e.g. hydrogen sulfide (claimed) and carbon dioxide, from sour gas e.g. synthesis gas and natural gas, in a gas processing industry. Can also be used for removing carbonyl sulfide and hydrogen cyanide.    ADVANTAGE - The method enables removing acid gas from the sour gas using the absorbent solvent with improved-acid gas absorption and recovering the entrained absorbent solvent with water to be feasible without freezing water and disturbing operation of a water wash zone when the partially heated treated gas stream is formed at temperature that is greater than a freezing point-of water i.e. 0 degree Celsius.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for removing acid gas from sour gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for removing acid gas from sour gas.    Absorber (20)    Cooled sour gas stream (32)    Partially loaded absorbent solvent stream (42)    Treated gas stream (80)    Partially heated treated gas stream (82)    Solvent-depleted treated gas stream (90)
NOVELTY - A hydrocarbon conversion process involves disproportionating hydrocarbon feed comprising normal or branched 4C alkane by contacting the hydrocarbon feed with a liquid catalyst in a reaction zone under disproportionation conditions to form a product mixture comprising at least 0.2 wt.% less than or equal to 3C alkanes and greater than or equal to 5C alkanes in 1 hour based on the 4C alkanes in the hydrocarbon feed. The liquid catalyst comprises an unsupported ionic liquid and a carbocation promoter. A mass ratio of liquid catalyst to hydrocarbon feed is less than 0.75:1.    USE - As hydrocarbon conversion process, preferably for disproportionation of butane (claimed).    ADVANTAGE - The method provides disproportionating and isomerizing a hydrocarbon feed using less ionic liquid, which is expensive, and obtaining better results at a faster rate. The reaction will proceed simply by contacting the feed and liquid catalyst, the reaction rate is generally too slow to be commercially viable. The reaction rate is substantially increased by increasing stirring speed of the reaction. This indicates that under some conditions rate of reaction is mass transfer limited and is not reflective of the true elementary steps of the reaction. In addition to simply stirring the reaction mixture, a baffle can be included in the reactor to aid in obtaining good mixing. The baffle helps to prevent a vortex from forming in the reactor. The formation of a vortex would reduce the amount of mixing even in the presence of stirring.
NOVELTY - Organic fertilizer comprises cow dung manure, maggot and hydrolyzed amino acid according to a mass ratio of 62-65:19-20:15-19.    USE - The organic fertilizer is useful for promoting growth of melon.    ADVANTAGE - The organic fertilizer has rich nutrition, good promoting effect and high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic fertilizer comprising inoculating 40-60 l/ton of plant growth-promoting rhizobacteria T-E5 into a fermentation medium, then first fermenting for 1 day, and second fermenting at 50 degrees C for 7 days to obtain a fermentation liquid, where the growth-promoting rhizobacteria T-E5 has a dry weight organic fertility of greater than or equal to 108 CFU/g, mixing cow dung manure, maggot and hydrolyzed amino acid to with the fermentation liquid.
NOVELTY - Rapid fermentation of organic fertilizer comprises putting silkworm excrement on cocoon cluster for 4 hours, uniformly scattering composite microorganism microbial inoculum on silkworm excrement surface, spraying, and processing for 4 hours; stacking at more than 100 cm high, maintaining silkworm excrement, and ventilating; and fermenting for 10-20 hours, heating to 60-70 degrees C, mixing, fermenting for 10-14 hours, removing smell of silkworm excrement, and maturing; spreading 50 cm flat silkworm excrement, naturally cooling to room temperature, and storing.    USE - Method for rapid fermentation of organic fertilizer (claimed).    ADVANTAGE - The method is easy and simple, and has short fermentation time and high production efficiency. The organic fertilizer has high granular fertilizer quality.
NOVELTY - The device comprises a first walking mechanism, a second walking mechanism and a discharging device. The first walking mechanism comprises a girder vehicle and a car slide rail part. The second walking mechanism comprises mobile tower frame paver and a mobile tower frame slide rail part. The mobile tower frame paver is set with a fermentation groove. The discharging device comprises a conveying belt and a discharging vehicle. The discharging vehicle is set with a conveyor belt. The device further comprises a programmable logic controller and an ultrasonic level meter.    USE - The device is useful for fermenting compost (claimed).    ADVANTAGE - The device ferments the compost with less energy consumption in an economical manner.    DETAILED DESCRIPTION - The device comprises a first walking mechanism, a second walking mechanism and a discharging device. The first walking mechanism comprises a girder vehicle and a car slide rail part. The second walking mechanism comprises a mobile tower frame paver and a mobile tower frame slide rail part. The mobile tower frame paver is set with a fermentation groove. The discharging device comprises a conveying belt and a discharging vehicle. The discharging vehicle is set with a conveyor belt. The mobile tower frame paver includes a paver main body, a grab bucket and a transverse bracket. The transverse bracket is set with the paver main body. The grab bucket is set with a first electric machine and a lifting screw rod. The screw rod is set with the transverse bracket. The discharging vehicle is set with a spiral discharger. The spiral discharger comprises a screw rod and a second electric machine, and is set with a speed reducer. The speed reducer is located at the second electric machine. The device further comprises a programmable logic controller and an ultrasonic level meter. The PLC controller is connected with the car slide rail part, mobile tower frame paver, conveying belt, and screw discharger.
NOVELTY - An organic fertilizer fermenting device comprises insulating layer cylinder, stir device, support frame, heat guide device, outlet pipe, heat conducting oil pipe, high temperature oil furnace, oil pump, oil pipe, and heating plate.    USE - Organic fertilizer fermenting device.    ADVANTAGE - The device is environment-friendly and convenient to maintain, reduces energy consumption, stir resistance and heat loss, and increases product quality.
NOVELTY - Biological complex fertilizer comprises e.g. 30-55 pts. wt. chicken manure, 25-35 pts. wt. rice bran, 34-46 pts. wt. wheat bran, 10-24 pts. wt. potato, 5-9 pts. wt. sucrose, 9-15 pts. wt. agar, 3-8 pts. wt. phosphate rock, 4-7 pts. wt. monocalcium phosphate, 1-6 pts. wt. calcium nitrate, 2-6 pts. wt. magnesium sulfate, 2-6 pts. wt. sodium chloride, 1-4 pts. wt. ammonium dihydrogen phosphate, 1-3 pts. wt. sodium pyrophosphate, 0.1-0.3 pts. wt. nitrogen-fixing bacteria powder, 0.1-0.3 pts. wt. phosphobacteria powder, and 0.1-0.3 pts. wt. Rhizopus stolonifer fungal powder.    USE - The fertilizer is used for preventing and treating underground pests, and treating blight, fusarium wilt, rust blight disease, Verticillium wilt, and root rot.    ADVANTAGE - The fertilizer reduces pests breeding rate, and repels underground pest.    DETAILED DESCRIPTION - Biological complex fertilizer comprises 30-55 pts. wt. chicken manure, 25-35 pts. wt. rice bran, 34-46 pts. wt. wheat bran, 10-24 pts. wt. potato, 5-9 pts. wt. sucrose, 9-15 pts. wt. agar, 3-8 pts. wt. phosphate rock, 4-7 pts. wt. monocalcium phosphate, 1-6 pts. wt. calcium nitrate, 2-6 pts. wt. magnesium sulfate, 2-6 pts. wt. sodium chloride, 1-4 pts. wt. ammonium dihydrogen phosphate, 1-3 pts. wt. sodium pyrophosphate, 0.1-0.3 pts. wt. nitrogen-fixing bacteria powder, 0.1-0.3 pts. wt. phosphobacteria powder, 0.1-0.3 pts. wt. Rhizopus stolonifer fungal powder, 15-35 pts. wt. soybean straw and 10-25 pts. wt. potato straw.
NOVELTY - Preparing tea tree mushroom nutrition agent comprises crushing rice straw and cottonseed hulls using a crusher, placing the crushed material into a mixed agitator, then adding water, carrying out fermentation process, then adding quicklime, corn protein powder, soybean meal and dairy manure, uniformly stirring the material, placing the material in a discharging device and a bag machine, sterilizing the placed material in a sterilizing boiler at high temperature for first time, then sterilizing for second time, and inoculating a strain into a nutrient medium, and growing a hairy fungus.    USE - The method is useful for preparing tea tree mushroom nutrition agent (claimed).    DETAILED DESCRIPTION - Preparing tea tree mushroom nutrition agent comprises crushing 30-65 wt.% of rice straw and 40-75 wt.% of cottonseed hull using a crusher having a length of 1-2 cm, placing the crushed material into a mixed agitator, then adding 80-90 wt.% of water, carrying out fermentation process for 10-15 days, then adding 5-5 wt.% of quicklime, 10-20 wt.% of corn protein powder, soybean meal, and 10-25 wt.% of dairy manure, uniformly stirring the material, placing the material in a discharging device and a bag machine, sterilizing the placed material in a sterilizing boiler at high temperature for first time, then sterilizing for second time, inoculating a strain into a nutrient medium and growing a hairy fungus at 18-20 degrees C and a humidity of 85-92 wt.%.
NOVELTY - Preparing tea tree mushroom nutrition base comprises crushing rice straw and cottonseed hulls using a crusher, placing the crushed material into a mixed agitator, then adding water, carrying out fermentation process, then adding quicklime, wheat bran, wheat straw, pig manure, soil and fertilizer to crush, uniformly stirring the material, placing the material in a discharging device and a bag machine, sterilizing the placed material in a sterilizing boiler at high temperature, and inoculating a strain into a nutrient medium, and growing hairy fungus.    USE - The method is useful for preparing tea tree mushroom nutrition base (claimed).    DETAILED DESCRIPTION - Preparing tea tree mushroom nutrition base comprises crushing 36-65 wt.% of rice straw and 32-38 wt.% of cottonseed hulls using a crusher having a length of 1-2 cm, placing the crushed material into a mixed agitator, then adding 80-90 wt.% of water, carrying out fermentation process for 10-15 days, then adding 5-10 wt.% of quicklime, 10-30 wt.% of wheat bran, 5-10 wt.% of wheat straw and 5-15 wt.% of pig manure, soil and fertilizer to crush, uniformly stirring the material, placing the material in a discharging device and a bag machine, sterilizing the placed material in a sterilizing boiler at high temperature for first time, then sterilizing for second time, and inoculating a strain into a nutrient medium, and growing hairy fungus at a temperature of 16-20 degrees C and a humidity of 85-92 wt.%.
NOVELTY - Preparation of seafood mushroom nutrients by taking 46-66 wt.% straw, 15-20 wt.% cottonseed, 5-15 wt.% quicklime, 15-20 wt.% sawdust, 14-20 wt.% crop straw, 2-6 wt.% corn powder and 3-10 wt.% accessories; crushing straw into 1-2 cm long, mixing with crushed cottonseed and sawdust in mixed agitator, adding 80-90 wt.% water; fermenting for 10-15 days; carrying out secondary fermentation, stirring, adding quicklime, corn powder and accessories, stirring uniformly; entering into bag machine, high temperature sterilizing, antivirus sterilizing; and packaging and inoculating with bacteria.    USE - Method for preparing seafood mushroom nutrients (claimed).    DETAILED DESCRIPTION - Preparation of seafood mushroom nutrients comprises:    (A) setting temperature at 15-20 degrees C, humidity at 90-95%, and nutrients proportion at 46-66 wt.% straw, 15-20 wt.% cottonseed, 5-15 wt.% quicklime, 15-20 wt.% sawdust, 14-20 wt.% crop straw, 2-6 wt.% corn powder and 3-10 wt.% accessories;    (B) crushing straw into 1-2 cm long, mixing with crushed cottonseed, and sawdust in mixed agitator, adding 80-90 wt.% water;    (C) fermenting for 10-15 days;    (D) carrying out secondary fermentation, stirring, adding quicklime, corn powder and accessories, stirring uniformly;    (E) entering into bag machine, high temperature sterilizing;    (F) antivirus sterilizing; and    (G) packaging and inoculating with bacteria at set temperature and humidity.
NOVELTY - Preparing Agaricus bisporus, straw mushroom nutritional medium comprises crushing straw, mixing rice straw, wheat straw, quick lime, dry dairy manure and auxiliary material in a mixer, adding water during the mixing process, heaped fermentation, carrying out secondary mixing process after fermentation, adding auxiliary material, stirring uniformly, sterilizing the obtained medium, inoculating the strain into the culture medium, culturing, and controlling the humidity to grow filamentous fungi.    USE - The method is useful for preparing A. bisporus, straw mushroom nutritional medium (claimed).    DETAILED DESCRIPTION - Preparing Agaricus bisporus, straw mushroom nutritional medium comprises (i) crushing straw to 1-2 cm, mixing 25-60% rice straw, 15-25% wheat straw, 1-5% quick lime, 10-20% dry dairy manure and 5-15% auxiliary material in a mixer, adding 80-90% water during the mixing process, (ii) carrying out heaped fermentation for 10-15 days, (iii) carrying out secondary mixing process after fermentation, adding 5-15% auxiliary material, and stirring uniformly, (iv) discharging obtained medium into a packing machine, sterilizing at a high temperature after placing into a boiler and sterilizing, (v) placing the packaged material at room temperature after sterilization to carry out cultivation, and sterilizing, and (vi) inoculating the strain into the culture medium, culturing at 18-22 degrees C, controlling the humidity at 90-95% to grow filamentous fungi.
NOVELTY - Biofertilizer comprises 10-20 pts. wt. straw, 7-11 pts. wt. clay, 5-8 pts. wt. calcium superphosphate, 3.5-6 pts. wt. zinc sulfate, 4.2-7 pts. wt. perlite, 1-3 pts. wt. ammonium citrate, 3.2-6.3 pts. wt. magnesium oxide, 4-6 pts. wt. ceramsite, 4-9 pts. wt. oyster, 3.5-6.4 pts. wt. radix stemonae powder, 3.1-6.8 pts. wt. biological black charcoal of straw, 4.3-7.6 pts. wt. chicken manure, 1.2-2.6 pts. wt. Bacillus mucilaginosus liquid, 0.6-2.2 pts. wt. gallnut, 1.1-1.8 pts. wt. microelement and 3.2-4.6 pts. wt. radix ilicis pubescentis.    USE - Biofertilizer for watermelon (claimed).    ADVANTAGE - The biofertilizer is cost-effective, ensures sweet taste of watermelon by increasing sugar content in the watermelon, and has protection function for loosening soil and good economic value.
NOVELTY - Producing organic fertilizer involves extracting realgar, garlic powder, tea root, myrobalam, sea clam shell, loquat leaf, cortex mori radicis, leaves, fructus evodiae, fructus amomi and radix clematidis thrice to obtain extract that is dried to get powder. The powder is mixed with plant ash to obtain traditional Chinese medicinal additive. Rotten chicken manure is decomposed in vacuum and then crushed to obtain fresh chicken manure. River sludge, bran, diatomite, bean dregs, fresh straw stick, dolomite powder, bentonite, flour, bone meal, grass meal, rice husk and plaster paste are mixed.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The method enables to produce organic fertilizer that improves soil granule structure.    DETAILED DESCRIPTION - Producing organic fertilizer involves extracting realgar, garlic powder, tea root, myrobalam, sea clam shell, loquat leaf, cortex mori radicis, leaves, fructus evodiae, fructus amomi and radix clematidis thrice to obtain extract that is dried to get powder. The powder is mixed with plant ash to obtain traditional Chinese medicinal additive. Rotten chicken manure is decomposed in vacuum and then crushed to obtain fresh chicken manure. River sludge, bran, diatomite, bean dregs, fresh straw stick, dolomite powder, bentonite, flour, bone meal, grass meal, rice husk and plaster paste are mixed with obtained additive to get another mixture that is fermented in a tank for 10-15 days in vacuum. The fermented product is granulated. Asphalt emulsion is sprayed on traditional Chinese medicinal additive layer of granule. The aqueous solution of potassium humate is sprayed on granules to obtain film that is dried in vacuum to get organic fertilizer.
NOVELTY - Bio-fertilizer comprises 0.1-0.2 pts. wt. Azotobacter powder, 0.1-0.2 pts. wt. Bacillus cereus powder, 0.1-0.2 pts. wt. Bacillus thuringiensis powder, 25-30 pts. wt. rice straw stick, 40-50 pts. wt. corn straw, 40-50 pts. wt. soybean straw, 8-10 pts. wt. monocalcium phosphate, 1-3 pts. wt. pyrophosphate, 2-8 pts. wt. potassium dihydrogen phosphate, 1-3 pts. wt. diammonium phosphate, 1-3 pts. wt. monocalcium phosphate, 1-2 pts. wt. monocalcium phosphate and 1-2 pts. wt. boric acid.    USE - Bio-fertilizer used for improving organism in soil (claimed).    ADVANTAGE - The bio-fertilizer improves quality of soil, suppresses soil-borne diseases, eco-friendly and has low cost, simple production process, and no residue.
NOVELTY - Preparing fertilizer involves inoculating Bacillus coagulans in molasses mash. The pH and metal ion concentration of mash is determined and then metal complexing agent is added. The molasses mash is heated at 90-100 degrees C for 30-360 minutes to obtain concentrated molasses mash. The pH of molasses mash is regulated to 7-8 by adding pH regulator. The molasses mash, aerobic bacteria and organic and inorganic filler are mixed to get mixture that is fermented for 12-48 hours, particularly 12-36 hours. The fermented product is degummed and granulated to obtain fertilizer.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method enables to prepare fertilizer that ensures improved product quality in low production cost.
NOVELTY - A sn-1 chloropropanol fatty acid ester is selectively synthesized by mixing aluminosilicate molecular sieve to iron salt solution, heating, hot filtering, vacuum drying to obtain aluminosilicate zeolite-loaded iron salt catalyst, pre-heating molten fatty acid and aluminosilicate zeolite-loaded iron salt catalyst, mixing, dropwise adding epichlorohydrin, reacting at 50-90 degrees C for 24-80 hours, suctioning off catalyst, washing with methanol, and concentrating filtrate.    USE - Selective synthesis of sn-1 chloropropanol fatty acid ester (claimed).    ADVANTAGE - Process is selective, simple, low cost, environment-friendly, and uses cheap and easy to obtain raw materials and catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a HPLC chromatogram of aluminosilicate zeolite-loaded iron salt catalyst synthesized chloropropanol monolaurate product.
NOVELTY - A bis(Cholorosulfonylimide) salt is prepared by reacting diclofenac sulfonimide and onium halide ion.    USE - Preparation of bis(Cholorosulfonylimide) salt (claimed).    ADVANTAGE - Preparation process is simple and environment-friendly and has low cost and improved yield. Product has improved purity.    DETAILED DESCRIPTION - A bis(Cholorosulfonylimide) salt is prepared by reacting diclofenac sulfonimide of formula (A) and onium halide ion of formula (M+X-)..    M+=onium cation; and    X-=halogen ion.
NOVELTY - Clorsulon preparation involves condensing benzaldehyde and chloroform, and then performing chlorination and elimination processes. The resulting product is reduced by using hydrazine hydrate, and then performing sulfonation, ammoniation, and purification processes to give the finished product clorsulon.    USE - Method for preparing clorsulon (claimed).    ADVANTAGE - The method prepares clorsulon in a simple and eco-friendly manner by avoiding toxic benzene and chlorine under mild reaction condition. The prepared product has good protection effect, high quality, good yield, and good industrial prospect.
NOVELTY - Valnemulin salt purification involves taking 1-15 wt.% aqueous solution of valnemulin salt, adding alkali for adjusting pH to 7-14, and then filtering to obtain filter cake. The obtained filter base is washed with solvent and then dried to obtain valnemulin base. The solvent is selected from water, methanol, ethanol or isopropanol. The obtained valnemulin base is dissolved in a solvent, and then water is also added dropwise with stirring, where the resulting mixture is crystallized, filtered, washed, and dried to obtain fine valnemulin base.    USE - Method for purifying valnemulin salt (claimed).    ADVANTAGE - The method gives purified valnemulin salt in a simple, cost-effective and eco-friendly manner with high yield.    DETAILED DESCRIPTION - Valnemulin salt purification involves taking 1-15 wt.% aqueous solution of valnemulin salt, adding alkali for adjusting pH to 7-14, and then filtering to obtain filter cake. The obtained filter base is washed with solvent and then dried to obtain valnemulin base. The solvent is selected from water, methanol, ethanol or isopropanol. The obtained valnemulin base is dissolved in a solvent, and then water is also added dropwise with stirring, where the resulting mixture is crystallized, filtered, washed, and dried to obtain fine valnemulin base. The solvent is selected from methanol, ethanol, isopropanol, n-butanol or other lower saturated monohydric alcohols. The obtained fine valnemulin base is added to water with an acid solution to adjust pH of the reaction system, and then dried to give pure salt of valnemulin solid product.
NOVELTY - Preparation of psoralen from radix fici hirtae extract comprises extracting radix fici hirtae, concentrating and drying.    USE - Method for preparing psoralen from radix fici hirtae extract (claimed) used for preventing bacteria, virus, tumor and coagulation, and regulating immunity.    ADVANTAGE - The method has no environmental pollution and easy implementation for industrial production. Psoralen has hormone-like pharmacological effects.
NOVELTY - Production of levamisole hydrochloride comprises dissolving L-tetraimidazole raw material in isopropanol, adding antioxidant, active carbon filtering, stirring under hydrogen chloride gas protective atmosphere until pH is 4-5, and separating.    USE - Method for production of levamisole hydrochloride (claimed).    ADVANTAGE - The method utilizes new and better isopropanol solvent and high boiling point acetone, does not require distilled water, ensures product high quality and yield, increases product stability and good product appearance, and it has less volatility and system loss, high recovery, low consumption and cost, less wastewater discharge, and no product agglomeration and macular generation.
NOVELTY - Liquid organic fertilizer preparation involves removing insoluble substance from the black liquor. The obtained liquor is treated for 30-120 minutes. The treated mixture is added with dilute acid or alkali regulating the pH of the mixture to 4-7. The mixture is fermented at 20-35 degrees C for 8-36 hours and 180 rotations per minute by adding 19 g/l glucose, 9 g/l yeast extract, 1.5 g/l dipotassium phosphate, 1.2 g/l magnesium sulfate. The fermented mixture is added with urea (0.019%-5%) containing nitrogen source. The mixture is filtered and then dried to obtain desired product.    USE - Method for preparing liquid organic fertilizer (claimed) used for sewage treatment and in modern agriculture.    ADVANTAGE - The method enables to prepare liquid organic fertilizer in a simple, eco-friendly and cost-effective manner, and ensures strong practicability by increasing stress resistance of crops.
NOVELTY - Genetically engineered succinic acid producing Escherichia coli BA601 (CCTCC NO: M2014210) strain is new.    USE - Used as genetically engineered succinic acid producing Escherichia coli BA601strain.    ADVANTAGE - The strain efficiently utilizes glucose for producing succinic acid, and can greatly promote the progress and development of succinic acid industry.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) constructing genetically engineered succinic acid producing Escherichia coli BA601 strain; and (2) use of Escherichia coli BA601 in fermentative production of succinic acid, comprising using two stage fermentation, aerobic phase to improve biomass, and anaerobic stage acid fermentation.
NOVELTY - Processing kitchen garbage involves pouring the kitchen garbage in a container for separating coarse and heavy impurities. Water is added to the kitchen garbage to separate the coarse impurities present in kitchen garbage, where the processed garbage is then treated aerobically. Heavy impurities are then removed from aerobically treated kitchen garbage, which is then degreased. The degreased kitchen garbage is then subjected to water to perform anaerobic digestion process.    USE - Method for processing kitchen garbage (claimed).    ADVANTAGE - The method enables to process kitchen garbage by effectively removing oil and other organic waste components from kitchen garbage in an eco-friendly manner.
NOVELTY - This utility new type relates to a one fertilizer production device, specifically is a one organic eco-fertilizer with microorganism production machine. Comprising transverse set with feeding and discharging wherein a wherein a, comprising in turn connected in series a front section, middle section and rear section, the front section and rear section is tapered tube are symmetrically set with a, the middle section is cylinder body, outside surface is set with an annular groove, the middle lower part is set with a card device of the pulley in the groove in the front and outside surface of rear section along the circumference uniform distribute a multi-column, and the other ring surface of inner gear ring matching with a locating column of a set, the locating column is inserted in a set in. This machine the teeth ring and track ring, structure is simple, the use life is long, a angle adjusting and driving mechanism a force.
NOVELTY - Application method of transplanting special fertilizer comprises mixing fertilizer and soil at mass ratio of 1-1.5:60-80 to obtain soil substrate, putting in seedling trays, scattering seed, covering to thickness of 2-2.5 cm, compacting, scattering 10-15 g fertilizer every 15-20 days and applying water mist. The fertilizer comprises sepiolite, sheep manure powder, humus, seaweed powder, stone powder, Angelica powder, plant ash and indole acetic acid.    USE - Method for applying transplanting special fertilizer used for promoting seedling root (claimed).    ADVANTAGE - The simple method promotes 4-8 roots.
NOVELTY - A mushroom cultivation corn core fermentation material comprises 60-70 wt.% corn core, 10-20 wt.% wood chips, 2-10 wt.% wheat bran, 2-10 wt.% rice bran, 1 wt.% gypsum, 1 wt.% lime, 1 wt.% phosphate fertilizer and 0.1 wt.% carbendazim.    USE - Mushroom cultivation corn core fermentation material.    ADVANTAGE - The scientific, reasonable and simple method has low investment cost. The material has quick effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cultivation of mushroom comprising:    (A) crushing corn core, dissolving lime, phosphate fertilizer and carbendazim in water, uniformly mixing, and adding additives;    (B) stacking culture material at width of 1.1-1.3 m and height of 1.1-1.3 m, making vent hole at center using stick, covering with agricultural film, fermenting, turning once every 3 days for 3 times when temperature reaches 55 degrees C, cooling, and adjusting pH to 4-5.5 using lime;    (C) selecting polyethylene bag, making front vent plug, tightly pressing, and binding;    (D) selecting shading cloth, sulfur fumigating and disinfecting, and ventilation cooling for 8-10 days every morning and evening for 1.5 hours if temperature reaches more than 28 degrees C; and    (E) fruiting, harvesting, peeling, binding with bamboo stick or reinforcing steel bar, soaking in water or nutrition liquid comprising 0.3-0.4% urea, 0.5-1% sucrose and 0.3-0.5% potassium dihydrogen phosphate for 12-16 hours, and reculturing.
NOVELTY - Organic fertilizer comprises 5-10 pts. wt. enzyme, 5-10 pts. wt. corn starch, 2-4 pts. wt. edible brown sugar, 10-14 pts. wt. wheat bran and 20-25 pts. wt. rice bran.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer has improved viscoelastic properties and compressive strength.
NOVELTY - A bio-organic fertilizer composition comprises 100 pts. wt. organic manure and 5-10 pts. wt. fermentation strain.    USE - Bio-organic fertilizer.    ADVANTAGE - The composition obviously increases fermentation manure viscoelasticity, is easy to granulate molding, improves compressive strength of organic fertilizer, prevents use of organic fertilizer in the process due to easy formation of powder and volatile loss, and is fully absorbed.
NOVELTY - Special organic fertilizer and its preparation method are claimed. The special organic fertilizer comprises 10-25 wt.% rapeseed cake, 20-35 wt.% distiller's grains, 30-40 wt.% quail manure, 2-6 wt.% rock phosphate powder, 6-10 wt.% tung oil, and 1-3 wt.% bacterial strains.    USE - As special organic fertilizer for tea.    ADVANTAGE - The special organic fertilizer is suitable to prepare in an environmentally-friendly manner.    DETAILED DESCRIPTION - Special organic fertilizer and its preparation method are claimed. The special organic fertilizer comprises 10-25 wt.% rapeseed cake, 20-35 wt.% distiller's grains, 30-40 wt.% quail manure, 2-6 wt.% rock phosphate powder, 6-10 wt.% tung oil, and 1-3 wt.% bacterial strains. The preparation method involves mixing the rapeseed cake, distiller's grains, quail manure, and tung oil, and adding water, uniformly stirring mixture and adding bacterial strain, performing aerobic fermentation for 10 days, adding fermented product to rock phosphate powder, and uniformly mixing, crushing, sieving and granulating obtained product.
NOVELTY - Preparing metal carbide syngas direct methanation catalyst comprises mixing molybdenum precursor, cobalt precursor and porous carbon substance in water to prepare a suspension, adjusting pH of the suspension, stirring to enable adsorption of cobalt and molybdenum precursor on the porous carbon substance, filtering the porous carbon material adsorbed with molybdenum precursor and cobalt precursor from the suspension, recovering obtained catalyst precursor and drying, calcining the recovered catalyst and carburizing the calcined catalyst precursor.    USE - The method is useful for preparing metal carbide syngas direct methanation catalyst (claimed).    ADVANTAGE - The catalyst has increased absorption of metal precursor, has high specific surface area, high reaction rate and poisoning resistance; has high durability; and improves carbon monoxide conversion and methane selectivity in direct methanation process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for metal carbide syngas direct methanation catalyst prepared by the above method.
NOVELTY - The heat exchanger (300) has a main portion that is comprised with a superheat vent which is connected with influx unit. Multiple foil modules are welded in top and bottom of heat exchange cell (200). A main foil is located at fixed interval to inner side from both sides, and the main major surface portion is positioned in the center of main foil. A planar section is positioned between main influx unit and the main major surface portion of main foil. The main influx unit is comprised with main inflow distributor plate for uniform flow distribution of exhaust gas of high temperature.    USE - Primary surface heat exchanger for solid oxide fuel cell (SOFC) generation system.    ADVANTAGE - The requirement of space is reduced, and the heat loss is decreased. The heat exchange efficiency is improved, and the operation of the SOFC stack is facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the primary surface heat exchanger.    Influx units (134,143)    Welding unit (150)    Catalytic combustor (160)    Heat exchanger cell (200)    Heat exchanger (300)
NOVELTY - The method involves arranging an electrolyte membrane between an anode and a cathode. Gas diffusion layers (2, 3) are reset with respect to a bipolar plate (1) and a membrane electrode assembly (4), where the gas diffusion layers comprise reaction fluid supply regions (2b, 3b), a reaction fluid exhausting region and a reaction fluid sealing region (9). A sealing material (5) is injected into the reaction fluid sealing region of the gas diffusion layers such that the gas diffusion layers are outwardly sealed. A spacer is attached between the bipolar plate and the membrane electrode assembly.    USE - Method for manufacturing a fuel cell arranged in a high voltage fuel cell stack of a fuel cell system.    ADVANTAGE - The method enables a precise attachment of a sealing material to fluid-conveying layers to the fuel cell and the fuel cell system under consideration of local compensation of material and manufacturing tolerances of individual components of the cell and/or the system. The method enables adjusting a seal height to the set seal height of the system during operation of the fuel cell system seal height, thus saving the sealing material, and hence manufacturing sealing lines in a simplified manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fuel cell system.    Bipolar plate (1)    Gas diffusion layers (2, 3)    Reaction fluid supply regions (2b, 3b)    Membrane electrode assembly (4)    Sealing material (5)    Reaction fluid sealing region (9)
NOVELTY - An ethanol from biomass feedstock is manufactured by making raw material suspension contain disinfectant before performing saccharification fermentation process in the process of carrying out saccharification fermentation process of raw material suspension containing biomass feedstock, and manufacturing ethanol.    USE - Manufacture of ethanol from biomass feedstock (claimed).    ADVANTAGE - Proliferation of microorganisms is suppressed efficiently and ethanol is produced efficiently.
NOVELTY - This utility new type relates to a rubbish transport device, in particular a one use in a fermentation of garbage transportation device. This utility new type is the purpose is provide a marsh gas a complete one life garbage fermentation using a transport device. A domestic garbage fermentation using one transportation device, comprising a roller of raw material and the raw material for the sliding of track, the raw material of the side upper wall with air hole. This utility new type and existing technology, it has following advantages: it can fully is a marsh gas, which avoids the waste of marsh gas resource.
NOVELTY - This new type utility claims composite carbon steel plate marsh gas ferment jar, a fermentation jar, jar, an air storage tank, a desulfurizing jar, an air storage tank and the fermentation jar are connecting, the air storage tank directly to gas cooker. This utility new type breaking past a fermentation jar and iron metal tank body is easy to rust and continuous use life is short, using new technology, new material for the tank body a innovation, so as to design a composite one carbon steel tank body, this marsh gas fermentation jar is added one layer polyethylene plastic plate in a tank body, so the corrosion resistance is greatly enhance, realize the heat preservation character, good leak tightness, corrosion and rust, convenient of install, use time can greatly delay the tank body a rust and prolongs use life, so as to reduce the use cost and increases the economic benefit and market popularization.
NOVELTY - This utility new type relates to a new-type biogas pneuma one pneuma collecting cover, a head round conical skirt section according to minimum taper design, a water sealing ring set with a pulling buckle bolt pole in the head of the conical skirt top part, the fixing hood, a hood top around a cloth groove, a groove hole with a bolt, water sealing ring around the bolt and a matched. Between the skirt and water seal so as to reduce a component of stress load, the hood opening and closing more intuitive, easily, conveniently and fast, and is convenient to store and transport. Each for a separate type anaerobic fermentation device top of seal, a gas collecting, use.
NOVELTY - Livestock and poultry dead kitchen garbage and comprehensive use for preparing industrial lipid part of system, comprising high temperature sterilizing hydrolysis device, a crusher, a closeness, storage jar, the first steam preheating device, water storage tank, a three phase separator, oil water separator, anaerobic ferment jar, an aeration pool, pond, deodorizing and industrial lipid. This utility new type is a large amount, fermenting period is short, treatment effect is good, the automatic degree high, a low cost, a process without peculiar smell, the kitchen garbage and dead livestock and poultry waste is valuable.
NOVELTY - The photovoltaic module (1) has a first photovoltaic group (3) housed in a support and containment structure (2) and comprising single photovoltaic cells (4). An electrolytic group is housed in the support and containment structure and having an electrolytic chamber for holding water containing electrolyte. Electrodes (8) are placed in the electrolytic chamber and connected to the photovoltaic cells of the first photovoltaic group, while an exit duct (9) is provided for the hydrogen and oxygen gases produced via electrolysis.    USE - Photovoltaic module for production of hydrogen.    ADVANTAGE - Provides a photovoltaic module for the conversion of solar energy into electricity and for the production of hydrogen gas via electrolysis, of which the photovoltaic module has structural and functional characteristics such as to perform the photovoltaic and hydrolysis function in an efficient manner with savings in terms of space, implementation and running costs and energy efficiency. The incorporation of the photovoltaic group and the electrolytic group in a single photovoltaic module, in particular in the same photovoltaic panel, the production of hydrogen occurs efficiently and with savings in terms of energy, space and running costs. This way, the filling and the recirculation of the water may take place automatically when the photovoltaic cells produce electricity and the electrolytic group produces hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a photovoltaic system.    DESCRIPTION OF DRAWING(S) - The drawing shows the exploded perspective view of the photovoltaic panel.    Photovoltaic module (1)    Support and containment structure (2)    First photovoltaic group (3)    Photovoltaic cells (4)    Electrodes (8)    Exit duct (9)
NOVELTY - The device has a vehicle frame whose instrument desk is provided with a controller, an alarm unit, a display unit and a switch. An upper part of a shell body (6) is formed with an opening end of an inner pipe (7) that is provided with a motor. An air inlet pipe is connected with an air outlet pipe. A lower end of the shell body is fixed with an exhaust port (11). A gas sensitive film is provided with an input terminal of an operation amplifier, where an output terminal of the operational amplifier is connected with a data collecting card. A pneumatic pump is connected with a control switch.    USE - Inner air quality detection device for a vehicle.    ADVANTAGE - The device achieves better air quality detection effect of the vehicle and monitors harmful air in the vehicle using a concentration monitor to send alarm information, thus providing a powerful support of the people health.    DETAILED DESCRIPTION - Operational amplifier is UPC4570 low noise operation amplifier chip. The data collecting card is data a MSP430F5438 collecting card. The controller is MSP430F149 low power consumption embedded MCU. The gas sensitive film is selected from detecting sulfide, hydrogen, alcohol, toluene, dimethylbenzene, carbon monoxide, carbon dioxide, propane gas and nitrogen oxide. An INDEPENDENT CLAIM is also included for an inner air quality detection method for a vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of an inner air quality detection device.    Shell body (6)    Inner pipe (7)    Exhaust port (11)    Transverse pipe (19)
NOVELTY - Obtaining ester optionally along with glycerol, comprises: obtaining endosperm from plant source and extracting oil from the endosperm; pretreating the oil and adding catalyst to the pretreated oil to obtain reaction mixture; treating the reaction mixture to obtain ester fraction and glycerol fraction, where the glycerol fraction is heavier than the ester fraction; separating the ester fraction from the glycerol fraction, obtaining and optionally quantifying ester from the ester fraction; and optionally obtaining and optionally quantifying glycerol from the glycerol fraction.    USE - The process is useful for obtaining ester optionally along with glycerol, where the ester is methyl ester that is useful as a biofuel, which is used as automotive fuel (all claimed) in diesel engine.    ADVANTAGE - The process: provides the yield of the ester and the glycerol is at ratio of 8:2 to 9:1, preferably 9:1 (claimed); and is simple, efficient and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for methyl ester obtained from the process.
NOVELTY - Filtering a gas comprises passing the gas through a highly alkalized liquid filter reagent comprising a humic and fulvic substance.    USE - The method is useful for filtering a gas, removing contaminants comprising carbon dioxide, sulfur oxide, nitrogen oxides, hydrogen sulfides, mercaptans, ammonia, radionuclides, toxic metals, particulates, volatile vapors, and organics from a gas stream, removing odorous chemicals such as ammonia and microbes in a chamber, preferably poultry litter, where microbes are clostridia and Salmonella (all claimed), and filtering and recycling harmful pollutants from gas sources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for removing odorous chemicals and microbes, comprising treating a chamber filled with a gas by spraying a highly alkalized liquid humic and fulvic filter reagent in the chamber, where the gas comprises odorous chemicals comprising ammonia and further comprises microbes and spores, and the treatment lowers levels of ammonia and at least partially kills the microbes and spores.
NOVELTY - Producing fermentable sugars from biomass, comprises preparation of a biomass-enzyme mixture comprising (i) pre-treated lignocellulosic biomass containing cellulose and/or hemicellulose and (ii) an enzyme composition comprising cellulase and/or hemicellulase enzymes; and saccharification comprising incubation of the biomass-enzyme mixture.    USE - The methods are used for producing fermentable sugars from biomass, and for producing a fermentation product (all claimed).    ADVANTAGE - The methods provide an improved efficiency of enzymatic hydrolysis of lignocellulosic biomass.    DETAILED DESCRIPTION - Producing fermentable sugars from biomass, comprises (a) preparation of a biomass-enzyme mixture comprising (i) pre-treated lignocellulosic biomass containing cellulose and/or hemicellulose and (ii) an enzyme composition comprising cellulase and/or hemicellulase enzymes; (b) a first saccharification comprising incubation of the biomass-enzyme mixture from step (a) for a sufficient time to achieve hydrolysis of at least 10% of the cellulose and/or hemicellulose and to produce partially-hydrolyzed biomass and hydrolysate liquor; (c) mechanical treatment of the partially-hydrolyzed biomass produced by step (b) to produce mechanically-disrupted, partially-hydrolyzed biomass; and (d) a second saccharification comprising incubation of the mechanically-disrupted, partially-hydrolyzed biomass produced by step (c) for a sufficient time to achieve hydrolysis of at least 60-100% of the cellulose and/or hemicellulose present in the pre-treated lignocellulosic biomass to fermentable sugars. An INDEPENDENT CLAIM is a process for producing a fermentation product.
NOVELTY - Producing pellets from a lignin composition, comprises: pre-treating lignocellulosic biomass into pre-treated biomass; separating the pre-treated biomass into a first liquid component comprising sugars and a first solid component comprising cellulose and the lignin composition; hydrolyzing the first solid component of the pre-treated biomass; separating the hydrolyzed biomass into a second liquid component comprising sugars and a second solid component comprising the lignin composition; and supplying the second solids component to a pelleting apparatus.    USE - The process is useful for producing lignin pellets (claimed), which are useful in the production of ethanol.    ADVANTAGE - The lignin pellets increase the efficiency and yield of cellulosic ethanol from biomass, are easy to handle, store and transport, create fewer problems with dust and in a combustion system (such as a solid fuel boiler), and has good combustible property due to lower moisture and increased airflow.    DETAILED DESCRIPTION - Producing pellets from a lignin composition, comprises: pre-treating lignocellulosic biomass into pre-treated biomass; separating the pre-treated biomass into a first liquid component comprising sugars and a first solid component comprising cellulose and the lignin composition; hydrolyzing the first solid component of the pre-treated biomass into a hydrolyzed biomass comprising sugars and the lignin composition; separating the hydrolyzed biomass into a second liquid component comprising sugars and a second solids component comprising the lignin composition; and supplying the second solids component comprising the lignin composition to a pelleting apparatus. The lignocellulosic biomass comprises cellulose, hemi-cellulose and lignin.
NOVELTY - Portable system (10) has bucket (12) comprising opening and handle (14), where lid (16) is configured to cover the opening in the bucket, the lid defines several holes (18), an air pump coupled to the lid, at least one air hose coupled to the air pump and received through one of the holes, at least one air stone coupled to the at least one air hose, and the air pump is operable to cause air bubbles to be expelled from the at least one air stone to facilitate aeration of a compost tea mixture contained by the bucket.    USE - The portable system is useful for brewing compost tea or liquid fertilizer which is used for fertilizing crops and gardens.    ADVANTAGE - The system is portable, and utilizes fish and animal waste for producing compost tea which is beneficial for growth of plants, flowers, vegetables, trees and bushes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for portable liquid fertilizer brewer which has the bucket having opening and handle, where the lid is configured to cover the opening in the bucket, the lid defines several air holes, air pump coupled to the lid, first air stone fluidly coupled to the air pump and arranged at a first depth within the bucket, second air stone fluidly coupled to the air pump and arranged at a second depth within the bucket, the second depth being deeper than the first depth, and the air pump is operable to cause air bubbles to be expelled from the first and second air stones to facilitate aeration of a liquid fertilizer mixture contained in the bucket.    DESCRIPTION OF DRAWING(S) - The drawing shows exploded perspective view of portable system for brewing compost tea.    Portable system (10)    Bucket (12)    Handle (14)    Lid (16)    Holes (18)
NOVELTY - Optimization of the production of biogas from anaerobic treatment of fermentable biomass, comprises anaerobically fermenting fermentable biomass in at least one fermenter (1). The fermentable biomass is subjected to an acidic hydrolysis before and/or after at least one fermenter in a separate device (2). A hydrolysis gas and a liquid and/or solid containing hydrolyzate is formed, and carbon dioxide and hydrogen sulfide-containing hydrolysis gas is separated from the separate device for acidic hydrolysis.    USE - The method is useful for optimization of the production of biogas from anaerobic treatment of fermentable biomass.    ADVANTAGE - The method has separate hydrolysis steps, which improves substrate utilization and process stability at high loading rates.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a device for optimizing the production of biogas from anaerobic treatment of fermentable biomass by the above mentioned method comprising at least one fermenter, and the separate device for acid hydrolysis before and/or after fermenter, where a fermentation suspension is produced by anaerobic fermentation and the separate device for acid hydrolysis has at least one removal device (3) for separating the hydrolysis gas; and    (2) a hydrolysis device (7), preferably for use in the method comprising a hydrolysis-container with at least one connecting device for connection to the fermenter, a device for supplying fermentable biomass, and the removal device for the hydrolysis gas.    DESCRIPTION OF DRAWING(S) - The figure shows schematic representation of the device for optimizing the production of biogas    Fermenter (1)    Separate device (2)    Removal device (3)    Second separate device (4)    Hydrolysis device (7)
NOVELTY - Biogas device (10) comprises: a hydrolysis tank (12), which is designed to carry out a hydrolysis on a biodegradable substrate, in which a hydrolysis gas containing carbon dioxide is produced during the hydrolysis; and a carbon dioxide discharge device (16), which discharges carbon dioxide contained in the hydrolysis gas from the hydrolysis tank. The carbon dioxide discharged from discharge device is fed to a power gas reservoir.    USE - Used as a biogas device.    ADVANTAGE - The biogas device controls the methane content of the biogas, and utilizes the products resulting during substrate degradation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for operating a biogas device, comprising discharging carbon dioxide contained in the hydrolysis gas from the hydrolysis tank and passing to an energy gas container.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas device.    Biogas device (10)    Hydrolysis tank (12)    Discharge device (16)    Separation device (18)    Methanogenic container (20)
NOVELTY - Method for preparing raw material for enzyme saccharification, involves heat pressing and pressurizing biomass feedstock comprising cellulose.    USE - The method is useful for preparing raw material for enzyme saccharification which is useful for preparing sugar for preparing ethanol and lactic acid (all claimed). The ethanol is useful as environmentally-friendly fuel. The method is also useful for preparing biodegradable plastics.    ADVANTAGE - The method prepares raw material having enzyme saccharification rate to 25% or more and suitable for long term storage, and is cost-effective as it reduces transport cost and volume density and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing sugar, involves subjecting the above-mentioned raw material to enzymatic saccharification;    (2) method for preparing ethanol and lactic acid, involves fermenting the sugar obtained the above-mentioned method; and    (3) raw material for enzyme saccharification comprising biomass feedstock comprising cellulose having moisture contents of 8-25 %mass.
NOVELTY - Composition comprises 60-65 wt.% manure chosen from pig manure, cow manure, and chicken manure, 18-23 wt.% sawdust, 3-5 wt.% dolomite, and 10-19 wt.% honeycomb enzyme. The honeycomb enzyme is prepared by mixing enzyme solution with honeycomb, and fermenting mixture for 10-20 days.    USE - The animal manure compost containing composition is useful for preventing and/or treating soil salinity (claimed).    ADVANTAGE - The composition is prepared easily.
NOVELTY - Manufacture of high-calorific fuel gas involves contacting ethanol and hydrogen in presence of methane and catalyst formed by carrying palladium and heteropolyacid on inorganic oxide support to obtain fuel gas containing ethane.    USE - Manufacture of high-calorific fuel gas used as town gas material.    ADVANTAGE - During efficient manufacture of fuel gas, time-dependent deterioration of catalyst is suppressed.
NOVELTY - The system has a linear piston pump, a piston pump that includes a tube such as a feed syringe assembly (15), a piston and an arm coupled to the piston. The piston pump is arranged to inject feedstock to a respective reactor. A beam or plate (2) is coupled to the arms of the piston pumps configured to linearly drive the pistons. A linear actuator is provided for driving the beam or plate. The beam or plate is configured to linearly drive the pistons at the same time.    USE - Reactor system such as bench-or laboratory scale reactor system for supplying feedstock such as wastewater, sewage, food waste and/or combination of liquids and solids (all claimed), and chemical or biochemical reactor system.    ADVANTAGE - The tumbler accuracy water levels that are pre-set to afford efficient tumbling are enhanced and by operator sample calibration after water changes or at pre-determined intervals system accuracy is maintained. All important accumulation of system error is ensured to be held minimum and that recorded data is viable. The feed rates of orders of magnitude of 10 or 100 milliliters performed day is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the reactor system.    Base frame (1)    Lifting beam (2)    Drive nut (5)    Drive shaft (6)    Feed syringe assembly (15)
NOVELTY - This new type utility claims one poultry corpse harmless process and a use device, comprising tube, motor and control cabinet, a tube set with a control cabinet, a motor set in a cabinet in, a top tube set with an ultraviolet sterilizing lamp, the upper part of two side tube set with a feeding tube, a hot air inlet pipe, the inner lower part of two side set with a discharging tube and an exhaust duct, wherein said tube set with mixing mechanism, the mixing mechanism including rotating shaft and multi-group mixing oar leaves, the electric machine drive mixing mechanism work, the control cabinet is set with a screen and PLC single chip, a ultraviolet lamp irradiation wavelength, sterilizing and mixing time, this utility new type through high temperature steam sterilizing and ultraviolet sterilizing double functions to harmless treatment of poultry body, through mixing fermentation the small poultry corpse valid conversion into stable quality of organic fertilizer, processing capacity, automatic degree high, b each of breeding and poultry processing enterprises.
NOVELTY - A pellet composition comprises a pelletizable mixture and a lubricant. The pelletizable mixture comprises combustible biomass and oil-retaining seed mash, preferably material derived from Camelina.    USE - Pellet composition e.g. animal feed pellets and fuel pellets (claimed) used in stoves.    ADVANTAGE - The pellet composition is manufactured efficiently and economically using by-products from production of biofuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of pellet composition, which involves forming pelletizable mixture from combustible biomass and oil-retaining seed mash, adding lubricant to the pelletizable mixture, drying the mixture, and pelletizing the dried mixture; and    (2) method of using by-products from production of biofuels.
NOVELTY - Fuel composition comprises a lower grade fuel component, and a microemulsion comprising at least one of a hydrous component, a renewable component and a polar component present in an amount effective for forming the fuel composition.    USE - The fuel composition, preferably biodiesel is useful in internal-combustion engines (claimed).    ADVANTAGE - The fuel composition exhibits enhanced lubricity, corrosion and water stability without the use of other additives and inhibitors, reduces carbon intensity in the internal combustion engines, reduces emissions of nitrogen oxide (NOx), particulate matter, and other criteria pollutants to the environments, can be formed spontaneously upon blending, and maintains clarity at low temperatures upon freeze-thawing for prolonged periods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for formulating a fuel composition useful in internal-combustion engines, comprising providing (102) a fuel, and forming (108) the fuel composition by adding the microemulsion to the fuel.    DESCRIPTION OF DRAWING(S) - The diagram shows a flow chart of a method for synthesizing and formulating a fuel composition for internal-combustion engines.    Providing a fuel (102)    Selecting alcohol component (104)    Providing microemulsion (106)    Forming the fuel composition by adding the microemulsion to the fuel. (108)
NOVELTY - The system (10) has a single piston (15) moved inside a transfer hopper (12) between first and second positions such that internal volume is varied between first value occupied in the first position and second value occupied in the second position. A control element (16) is moved from the first value to the second value by the piston when internal volume is in fluidic communication with first enclosure (E2). The control element is moved from the second value to the first value by the piston when the internal volume is in fluidic communication with second enclosure (E1).    USE - System for transferring a granular form solid material e.g. biomass, grains, cellulose particle and powder or chips, between enclosures into a gasification reactor (all claimed).    ADVANTAGE - The control element is moved from the first value to the second value by the piston when internal volume is in fluidic communication with the first enclosure, and the control element is moved from the second value to the first value by the piston when the internal volume is in fluidic communication with the second enclosure, thus avoiding risk of transfer of gas to a high pressure side toward a low pressure side during rotation of the chamber, and carrying out fluidic connections with the enclosures. The system is easy, economic and effective to use, and has low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for transferring a solid material into granular form to a gasification reactor between enclosures.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for transferring a granular form solid material between enclosures into a gasification reactor.    Enclosures (E1, E2)    System for transferring granular form solid material (10)    Transfer hopper (12)    Single piston (15)    Control element (16)
NOVELTY - Coconut husk fuel is solid fuel obtained by compression-molding of coconut husk as raw material.    USE - Coconut husk fuel (claimed).    ADVANTAGE - The coconut husk fuel has high calorific value, and is economical and environmentally-friendly. The coconut husk fuel produces minimum amount of ash when combusted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of coconut husk fuel.
NOVELTY - A Myceliophthora thermophila host cell expressing an alpha -xylosidase is new.    USE - The M. thermophila host cell and composition are useful for producing fermentable sugar, degrading biomass, and producing a biomass byproduct. The byproduct is ethanol (all claimed).    ADVANTAGE - The M. thermophila host cell and composition are used for improved and efficient biomass degradation. The M. thermophila host cell and composition are used for low cost fermentable sugar and biomass byproduct production with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a composition comprising the host cell above;    (2) a method for producing fermentable sugar by (a) incubating the host cell or composition above, and (b) obtaining the fermentable sugar; and    (3) a method for producing a biomass byproduct by (a) incubating the host cell or composition above to cause enzymatic hydrolysis of the biomass, (b) fermenting the fermentable sugars obtained after incubation with at least one fermenter organism, and (c) recovering the byproduct after fermentation.
NOVELTY - Preparing 5-chloro-N-((2R)-2-hydroxy-3-((4-(3-oxo-4-morpholinyl)-phenyl)amino)propyl)-2-thiophenecarboxamide intermediate (II), comprises (a) reacting a 5-chloro-thiophene-2-carboxylic acid oxiranylmethyl-amide compound (IV) with a 4-(4-amino-phenyl)-morpholin-3-one compound (V) in the presence of an acid catalyst containing an alkali metal, an alkaline earth metal or zinc metal to obtain (II).    USE - The process is useful for preparing 5-chloro-N-((2R)-2-hydroxy-3-((4-(3-oxo-4-morpholinyl)-phenyl)amino)propyl)-2-thiophenecarboxamide intermediate (II) in the preparation of rivaroxaban (I) (all claimed), which is useful as an antithrombotic agent. No biological data given.    ADVANTAGE - The process is capable of simply, safely, efficiently and economically preparing (II) in an eco-friendly manner with good yield and purity thus conveniently preparing (II) with high purity on a commercial scale.    DETAILED DESCRIPTION - Preparing 5-chloro-N-((2R)-2-hydroxy-3-((4-(3-oxo-4-morpholinyl)-phenyl)amino)propyl)-2-thiophenecarboxamide intermediate of formula (II), comprises (a) reacting a 5-chloro-thiophene-2-carboxylic acid oxiranylmethyl-amide compound of formula (IV) with a 4-(4-amino-phenyl)-morpholin-3-one compound of formula (V) in the presence of an acid catalyst containing an alkali metal, an alkaline earth metal or zinc metal to obtain (II). An INDEPENDENT CLAIM is included for preparing rivaroxaban of formula (I), comprising the step (a) as above per se, and converting (II) into rivaroxaban (I).
NOVELTY - Preparation of fatty acid alkylester involves performing hydrolysis reaction of water and a raw material containing fat at 200-280 degrees C and pressure of 30-80 bars, producing fatty acid and glycerin, separating glycerin and fatty acid, and performing esterification of separated fatty acid and alcohol at 200-350 degrees C and normal pressure of 35 bars.    USE - Preparation of fatty acid alkylester for biodiesel fuel.    ADVANTAGE - The fatty acid alkylester is produced economically without generating water as by-product and with high conversion ratio.
NOVELTY - Genetically modified yeast host cell comprising increased expression of acetyl-coenzyme A carboxylase, increased expression of at least one fatty acid synthase, and optionally reduced expression of at least one enzyme involved in or in the beta -oxidation pathway, is new.    USE - The genetically modified yeast host cell is useful for producing fatty acid, or fatty acid-derived compounds (claimed), where the fatty acid or fatty acid-derived compounds are used as fuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the genetically modified yeast host cell; and    (2) producing at least one fatty acid, and/or fatty acid-derived compounds, in a genetically modified yeast host cell, comprising culturing the genetically modified yeast host cell under suitable condition so that the culturing results in the genetically modified yeast host cell producing the fatty acids, and/or fatty acid-derived compounds.
NOVELTY - Adsorbent comprises 20-30 pts. wt. straw powder, 20-30 pts. wt. sawdust, 20-30 pts. wt. crushed bark, 5-10 pts. wt. sodium chlorite, 5-10 pts. wt. sodium hydroxide, 5-10 pts. wt. glacial acetic acid, 5-10 pts. wt. chitosan, 10-20 pts. wt. diatomite, 10-15 pts. wt. citric acid, 5-10 pts. wt. bleaching agent, 5-10 pts. wt. biological enzyme, and 20-30 pts. wt. microorganism including Arthrobacter, yeast and Bacillus, where the adsorbent comprises not greater than 200 million microorganisms.    USE - The adsorbent is useful in sewage treatment for removing heavy metals (all claimed).    ADVANTAGE - The adsorbent is cost-effective, and treats sewage effectively by promoting synergistic relationship among the microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the adsorbent in sewage treatment, where the sewage treatment is done by (a) mixing straw powder, sawdust, and crushed bark, boiling the mixture in water for 30-50 minutes, and sieving the boiled mixture through 40 mesh sieve, (b) passing the sewage into a pH value regulating tank, adding citric acid, and glacial acetic acid to adjust the pH value to 5-6, adding the mixture obtained in step (a), adding sodium hydroxide, and sodium chlorite, and stirring the mixture at 45-65 degrees C or less for 1 hour, (c) adding chitosan to the reaction tower filled with air, adding diatomite to the tower, and stirring the mixture, (d) adding biological enzyme and microorganism to the sewage tank, and stirring the mixture at 35-45 degrees C for 2-3 hours, and (e) adding bleaching agent to the treated sewage water, separating solid and liquid using a solid-liquid separator, and discharging the separated water.
NOVELTY - A hedgehog mushroom culture material comprises 30-35 wt.% straw stalk, 30-35 wt.% peanut shell powder, 10-15 wt.% soybean powder, 6-12 wt.% cake fertilizer, 6-12 wt.% white sugar, 1-2 wt.% gypsum powder, and 1-2 wt.% calcium superphosphate.    USE - Hedgehog mushroom culture material.    ADVANTAGE - The method is simple and has easy to obtain raw materials, low cost, high yield, and short growing period. The culture material is nutritious and rich in nitrogen, phosphorus, potassium, calcium, magnesium and organic matter; and has high quality, delicious taste and high straw coarse fiber and lignin content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of hedgehog mushroom culture material comprising cutting straw stalk into diameter of 6-8 mm; uniformly stirring straw stalk, peanut shell powder and soybean powder, drying, adding water, and pre-wetting until water content of 60-70%; adding cake fertilizer, white sugar and gypsum powder, uniformly stirring, stacking at 2-2.5 m wide and 1.5-2 m high rectangular pile, and covering with straw mat; turning for 5-6 times each for 2-5 days, fermenting, adding calcium superphosphate, adjusting pH to 6.5-6.7, and maintaining water content to 60-70%; and (5) putting into bag, filling, enclosing, and sterilizing at 120-130 degrees C for 2-2.5 hours.
NOVELTY - Fertilizer for special fruit trees, comprises 6-10 pts. wt. rice straw, 3-7 pts. wt. peat, 2.5-6 pts. wt. wheat bran, 3.5-8 pts. wt. pupae, 2.4-5.8 pts. wt. humic acid, 2.3-4.8 pts. wt. gypsum, 1.2-3.6 pts. wt. honey, 4.2-7.6 pts. wt. ammonium sulfate, 3-5 pts. wt. boron, 3.4-8.6 pts. wt. Aspergillus niger, 3.2-5.9 pts. wt. Lactobacillus agent, 4.2-8.1 pts. wt. sucrose, 2.5-4 pts. wt. organic fertilizer and 2.5-6 pts. wt. soluble-chitosan.    USE - The fertilizer is useful for special fruit trees (claimed).    ADVANTAGE - The fertilizer increases yield and quality of special fruit trees by improving texture, fertility and pH of soil.
NOVELTY - Method for producing white resveratrol-phenol-polyether laurate complex, involves using polyether, phenol, lauric acid, resveratrol and citric acid.    USE - The method and device are useful for producing white resveratrol-phenol-polyether laurate complex which is used for providing sterilizing effect against Staphylococcus aureus, Escherichia coli, fungi and molds. The white resveratrol-phenol-polyether laurate complex is useful in various products including food, makeup product, human body cleaning product, medicinal raw materials, health products, hair lotion, and face lotion (all claimed).    ADVANTAGE - The method is easy to perform, and causes no pollution as it generates no waste, and hence is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for producing white resveratrol-phenol-polyether laurate complex, which has reaction unit made of stainless steel, enamel or glass material, reaction kettle, and heating unit.
NOVELTY - Gasification of organic waste involves pressurizing and heating to-be-processed component containing organic waste and water, subjecting to hydrothermal reaction at 200-500oC in 1.5-50 MPa, contacting obtained product with porous granular catalyst containing metal at 200-500 degrees C in 1.5-50 MPa, decomposing organic waste, pressure-reducing or cooling, and carrying out gas-liquid separation of to-be-processed component containing decomposition product. The bulk density of porous granular catalyst is 1-8 g/cm3.    USE - Gasification of organic waste. Uses include but are not limited to waste plastics, waste rubber, shredder dust, livestock excrement, organic refuse, beer lees, sake lees, soy sauce cake, shochu-liquor lees, blood-mixed waste liquid, sewage sludge, and antigen antibody culture waste liquid.    ADVANTAGE - The organic waste is gasified by economical and efficient process. The catalyst has excellent durability for long period of time. The deterioration of catalyst is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasifier of organic waste, which has primary reaction layer for pressurizing and heating the to-be-processed product containing organic waste and water, and carrying out hydrothermal reaction, secondary reaction layer for contacting the to-be-processed product with activated carbon, decomposition-reaction layer for making decomposing organic waste, and splitter for performing gas-liquid separation of to-be-processed product containing decomposition product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasifier of organic waste.    Reactor (1)    Booster pump (2)    Relief valve (3)    Organic waste tank (4)    Gas-liquid separator (5)
NOVELTY - Production of noroxymorphone involves converting morphine to phenanthrofuran derivative (I) or (II), converting phenanthrofuran derivative to tetrahydrophenanthrene derivative (III) or (IV) in the presence of hydrogen peroxide and organic acid, and converting tetrahydrophenanthrene derivative to noroxymorphone. The organic acid and hydrogen peroxide are mixed and reacted for a specified induction time, before adding phenanthrofuran derivative.    USE - Production of noroxymorphone used in pharmaceutical composition for relieving pain, and treating drug addiction, opioid-induced constipation, and intestinal immobilization.    ADVANTAGE - The method enables efficient production of noroxymorphone from morphine with high yield, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Production of noroxymorphone involves converting morphine to phenanthrofuran derivative of formula (I) or (II), converting phenanthrofuran derivative to tetrahydrophenanthrene derivative of formula (III) or (IV) in the presence of hydrogen peroxide and organic acid, and converting tetrahydrophenanthrene derivative to noroxymorphone. The organic acid and hydrogen peroxide are mixed and reacted for a specified induction time, before adding phenanthrofuran derivative.    R1,R'1=1-20C alkyl, 1-20C aryl, 2-20C alkenyl, carbonyloxyalkyl having 1-20C alkyl, carbonyloxyaryl, carbonyloxyalkylaryl having 1-20C alkyl, or silyl of formula: Si(R4)3 (all optionally substituted);    R4=1-6C alkyl or phenyl (both optionally substituted);and    R2=optionally substituted 1-20C aliphatic or aromatic acyl.    An INDEPENDENT CLAIM is included for conversion of phenanthrofuran derivative to tetrahydrophenanthrene derivative.
NOVELTY - Pelletizing device for the preparation of pellets from biomass, comprises (a) a drying device (3) for drying biomass, preferably a fibrous biomass, preferably wood fibers and/or crushing biomass, (b) a pressing device for pressing pellets, and (c) a cooling device for cooling the pellets. A heat dissipation channel of the cooling device is connected with a heat supply channel (3a) of the drying device for supplying heat from the cooling device into the drying device.    USE - The pelletizing device is useful for the preparation of pellets from biomass.    ADVANTAGE - The device: reduces the moisture in biomass comprising bark, prior to combustion, and thus it ensures a high combustion temperature for avoiding harmful substances and for increasing the efficiency of combustion; and avoids the use of expensive filter screens.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing pellets, preferably wood pellets, preferably with the pelletizing device, comprising (i) drying biomass, preferably fibrous biomass, preferably wood fibers using the drying device, (b) pressing the biomass into pellets using the pressing device, (c) cooling the pellets with the cooling device, (d) removing heat from the cooling device to the drying device.    DESCRIPTION OF DRAWING(S) - The figure shows a flow diagram of the biomass processing device.    Large chopping machine (1)    Conveying device (2)    Drying device (3)    Heat supply channel (3a)    Tumbling sieve (5)
NOVELTY - Producing an organic growing medium from straw, comprises: (a) preparing straw humus; (b) preparing a helpful microorganism composition; (c) preparing humic acid; and (d) preparing an organic medium for growing vegetables.    USE - The process is useful for producing organic growing medium from straw, for growing sprout (claimed).    ADVANTAGE - The medium is a super clean medium for ensuring food safety, and contains sufficient nutrition, thus increasing growth and output of sprouts. The medium satisfies the requirement of micro-organic fertilizers allowed to be manufactured.
NOVELTY - The converter has a non-circular coaxial gasifier char tube (120) coaxially located from a top to a bottom of a downdraft gasifier (100). A biochar inlet valve (170) meters a biochar into the char tube. The gasifier includes a set of air inlet jets (140) to create a hot zone (150) in a reduction bell area (160) of the gasifier. The char tube is filled with highly reduced biochar carbon produced by a main chamber of the gasifier during operation of the gasifier. An extended hot zone is formed from air inlet nozzles (145) to bottom of the reduction bell during operation of the gasifier.    USE - Coaxial gas converter for use in a downdraft gasifier for producing hydrogen in energy and chemical industries.    ADVANTAGE - The converter provides high temperature radially from tips of the air jets, so that the converter is conformed around the jets, thus improving energy transfer, and hence preventing ash buildup, while enhancing hydrogen production in an efficient manner.    DETAILED DESCRIPTION - The char tube is selected from a group consisting of circular in cross-section shaped char tube, star-shaped shaped char tube and cross-shaped shaped char tube. An INDEPENDENT CLAIM is also included for a method for converting biomass to synthesis gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a coaxial gas converter in a downdraft gasifier.    Downdraft gasifier (100)    Non-circular coaxial gasifier char tube (120)    Air inlet jets (140)    Air inlet nozzles (145)    Hot zone (150)    Reduction bell area (160)    Biochar inlet valve (170)
NOVELTY - The method involves registering energy into fluid by a feed pump (2). The fluid is mixed in a reactor device (3) arranged with a reactor tube (31) and warmed by registered energy. The waste oil is processed, such that the composition containing hydrocarbon is obtained. The heated fluid is supplied to inlets of a vaporizer (41) and the composition containing hydrocarbon is vaporized. The composition containing hydrocarbon is provided with a boiling range from 170-390 degrees C and hydrocarbons are provided with 8-24 carbon atoms.    USE - Method for recovering composition containing hydrocarbon such as diesel oil from waste oil fluid.    ADVANTAGE - The residue compositions and residue flow rates are adapted efficiently during different operations. The yield of the composition containing hydrocarbon is increased effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a processing plant for recovering composition containing hydrocarbon from waste oil fluid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing plant for recovering composition containing hydrocarbon from waste oil fluid.    Feed pump (2)    Reactor device (3)    Reactor tube (31)    Vaporizer (41)    Capacitor (46)
NOVELTY - Producing biodiesel, comprises: (a) reacting a mixture comprising at least one fatty acid glycerol ester and at least one polyol in the presence of at least one zeolite at a temperature of 120-450 degrees C, to obtain biodiesel and (b) separating the biodiesel product obtained in the step (a).    USE - The method is useful for producing biodiesel (claimed).    ADVANTAGE - The method achieves conversion of fatty acid glycerol esters in simple and cost efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for biodiesel which is produced from the above mentioned method.
NOVELTY - Preparing organic fertilizer involves leaching and extracting sulfur, Apocynum venetum, Polygonum aviculare, cluster mallow fruit, fortune Eupatorium herb, Clerodendrum trichotomum, Glauber's salt, rhizoma smilacis glabrae, bark of tree of heaven, herba equiseti hiemalis and gordon euryale seed to obtain extract that is dried to obtain powder. Rotten chicken manure, corn and fresh chicken manure, river sludge, dairy manure, diatomite, bean dregs, lignin, fresh straw stick, powdered rock phosphate, bentonite grain, bone meal and seaweed powder are mixed.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that improves soil and acts for long time.    DETAILED DESCRIPTION - Preparing organic fertilizer involves leaching and extracting sulfur, Apocynum venetum, Polygonum aviculare, cluster mallow fruit, fortune Eupatorium herb, Clerodendrum trichotomum, Glauber's salt, rhizoma smilacis glabrae, bark of tree of heaven, herba equiseti hiemalis and gordon euryale seed to obtain extract that is dried to obtain powder. Rotten chicken manure, corn and fresh chicken manure, river sludge, dairy manure, diatomite, bean dregs, lignin, fresh straw stick, powdered rock phosphate, bentonite grain, bone meal, seaweed powder, rice hull, gypsum, vermiculite and water are mixed to obtain mixture. The obtained mixture is fermented in vacuum for 10-15 days, where obtained fermented product is granulated with asphalt emulsion obtained powder, shell, potassium humic acid and water. The obtained granules are dried to get product.
NOVELTY - The method involves connecting a light positive electrode (4) with an anode of a power supply (6). A light source (7) is connected with the light positive electrode. The light positive electrode is added with photoelectric chemical decomposition reaction solution (3). An electric conduction substrate (1) is formed with a semiconductor nanometer film (2). Pure water is added with activating agent and dispersing agent. A hydrogen and oxygen product is collected. The activating agent is formed with semiconductor nano-material. A conduction band bottom potential value is calculated.    USE - Light-electrochemically decomposing pure water preparation oxygen and hydrogen processing method.    ADVANTAGE - The method enables ensuring semiconductor nanomaterial and noble metal composite nano-material for pure water activating effect so as to prepare high purity hydrogen and oxygen in an efficient manner.    DETAILED DESCRIPTION - The activating agent is selected from group consisting of silicon, iron oxide, tungsten trioxide, Cadmium-sulfur and tin oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram illustrating a light-electrochemically decomposing pure water preparation oxygen and hydrogen processing method.    Electric conduction substrate (1)    Semiconductor nanometer film (2)    Photoelectric chemical decomposition reaction solution (3)    Light positive electrode (4)    Power supply (6)    Light source (7)
NOVELTY - Method for treating marine sewage using microbial agent involves (a) adding e.g. mixed microorganism to fermented rice bran, peat moss powder, and water, and performing culturing process, (b) adding e.g. fermented rice bran, peat moss powder, trehalose, and salt, (c) inoculating the microbial solution obtained in the step (a) to mixture, performing culturing process, and crushing and drying cultured product, and (d) adding the dried product into sewage treatment apparatus and performing sewage treatment process.    USE - The method is useful for treating marine sewage using microbial agent (claimed).    DETAILED DESCRIPTION - Method for treating marine sewage using microbial agent involves (a) adding 0.05-1 wt.% mixed microorganism to 0.125-0.15 wt.% fermented rice bran, 0.05-0.075 wt.% peat moss powder, 0.05-0.075 wt.% Lentinus edodes powder, 0.175-0.21 wt.% fermented rice husk powder, 0.015-0.025 wt.% molasses, 0.05-0.5 wt.% trehalose, 0.01-0.05 wt.% salt, and 100 t.% water, and performing culturing at 20-25 degrees C for 10-14 days to obtain microbial solution, (b) adding the 72.8 wt.% fermented rice bran, 28.7-35.7 wt.% peat moss powder, 28.5-47.47 wt.% L.edodes powder, 100 wt.% fermented rice husk powder, 15-25 wt.% trehalose, and 0.01-0.05 wt.% salt, (c) inoculating the microbial solution obtained in the step (a) to mixture obtained in the step (b), performing culturing process at 85-95 degrees C for 4-6 hours, crushing cultured product, and drying crushed product at 60 degrees C, and (d) adding the dried product into sewage treatment apparatus and performing sewage treatment. An INDEPENDENT CLAIM is included for microbial agent.
NOVELTY - The oxygen gas manufacturing machine (1) has a buzzer that is provided to block a power source if a pressure switch (7i) exceeds configuration pressure in gas in which a warning gas exhaust port (7d) supplies gas. A back fire prevention pipe (7a,8a) compares backfire which is able to flow in to gas exhaust ports (7c,8b,8c,8d) for buffering action of water for accident. The gas exhaust port indicates the gas pressure and supplies the gas to a combustor. A cleaning globe (7g,8g) is provided to emit the effluent after cleaning.    USE - Hydrogen and oxygen gas manufacturing machine.    ADVANTAGE - The fuel economy effect is provided effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolyzer tank of the hydrogen and oxygen gas manufacturing machine.    Oxygen gas manufacturing machine (1)    Back fire prevention pipe (7a,8a)    Gas exhaust ports (7c,8b,8c,8d)    Warning gas exhaust port (7d)    Cleaning globes (7g,8g)    Pressure switch (7i)
NOVELTY - Method for biological treatment of concentrated sludge using microbial agent involves (a) adding e.g. mixed microorganism to e.g. fermented rice bran, peat moss powder, Lentinus edodes powder and water, (b) adding e.g. fermented rice bran, peat moss powder, and trehalose, (c) inoculating the microbial solution obtained in the step (a) to mixture, performing culturing process, and crushing and drying cultured product, and (d) adding the dried product into concentrated sludge and performing treatment of concentrated sludge.    USE - The method is useful for biological treatment of concentrated sludge using microbial agent (claimed).    DETAILED DESCRIPTION - Method for treating marine sewage using microbial agent involves (a) adding 0.01-1 wt.% mixed microorganism to 0.50-1.5 wt.% fermented rice bran, 0.05-1.5 wt.% peat moss powder, 1.2-2.5 wt.% Lentinus edodes powder, 1.7-3.5 wt.% fermented rice husk powder, 0.5-2 wt.% molasses, 0.05-1.5 wt.% trehalose and 100 wt.% water to obtain microbial solution, (b) adding the 30-55 wt.% fermented rice bran, 25-47 wt.% peat moss powder, 20-35 L.edodes powder, 70-90 wt.% fermented rice husk powder, and 15-30 wt.% trehalose, (c) inoculating the microbial solution obtained in the step (a) into mixture obtained in the step (b), performing culturing process at 20-25 degrees C for 4 hours, crushing cultured product, and drying crushed product at 60 degrees C, and (d) adding the dried product into concentrated sludge and performing biological treatment of concentrated sludge. An INDEPENDENT CLAIM is included for microbial agent.
NOVELTY - The apparatus has an electrode unit (40) that is provided with electrode boards (60,70) which are provided with opposite polarity and are alternately arranged in preset intervals. The electrode unit is provided with a power supply unit (90) to supply power to electrode boards such that the water is received by an electrolyzer (20) is electrolyzed to produce hydrogen and oxygen. A center hole (63) is penetrated through the central portion. The electrode boards are extended upward in induction inclined surface (61) toward the central portion to form a slope in the outside.    USE - Apparatus for producing hydrogen and oxygen used as fuel supplied to internal combustion engine such as diesel engine and gas engine.    ADVANTAGE - The polarization phenomenon of the electrode plate is suppressed and the electric energy required for the electrolysis is reduced. The temperature of the water received inside the electrolyzer is uniformly maintained regardless of the domain. The freezing rupture is prevented. The electrolysis progressed to both electrode boards is prevented from being shorted with the iron and other metal material condensed in the water of the electrolyzer. The electrolysis is progressed and the chlorine other harmful material produced in the electrode plate is prevented. The hydrogen and the generated oxygen are mixed and the heat of the high temperature is generated with the stirring reaction in which the partial hydrogen and oxygen are reunited. The heating or the hot-water supply etc. is performed using the heat of the high temperature generated with the stirring reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for producing hydrogen and oxygen.    Electrolyzer (20)    Electrode unit (40)    Electrode boards (60,70)    Induction inclined surface (61)    Center hole (63)    Power supply unit (90)
NOVELTY - Producing an isomaltulose-containing composition from a sucrose-containing substrate, comprises: (a) contacting the sucrose-containing substrate with a particulate carrier-immobilized sucrose-isomerase biomass, and (b) obtaining an isomaltulose-containing composition. The carrier-immobilized sucrose-isomerase biomass exhibits a particle diameter of 100-900 mu m.    USE - The method is useful for producing an isomaltulose-containing composition from sucrose-containing substrate (claimed).    ADVANTAGE - The method allows large-scale production of isomaltulose and trehalulose with faster turnover rate and/or increased yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing a sugar alcohol-containing composition, comprising performing the steps (a) and (b), and carrying out catalytic hydrogenation of the resulting isomaltulose-containing composition.
NOVELTY - A pig feed producing method involves pouring 5 g yeast extract, 0.3 g magnesium sulfate and 200 g water to a container, stirring the mixture with hand for 3 minutes, blending the mixture together, fermenting the mixture in the container with a cover for 7 hours, adding 10 g alcohol into the mixture, adding 120 g yeast, 1 kg sugarcane bagasse, 1 kg soybean and 30 kg water to the mixture, fermenting the mixture for 3 days, stirring the mixture uniformly with hand stick, adding 1000 kg corn flour to the mixture, and stirring the mixture uniformly.    USE - Method for producing pig feed.
NOVELTY - A fermentation product is obtained taking fresh excrement, straw and straw stick at a weight ratio of 6:2:2, mixing fresh excrement, straw and straw stick in 105-135 ml EM bacteria ferment liquid natural to obtain a mixture, composting the obtained mixture for 15 day to obtain the fermentation product.    USE - Fermentation product for cultivating earthworm.    ADVANTAGE - The product has high nutrition value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for cultivating earthworm, which involves paving 40 kg fermentation product on an earthworm cultivation substrate, where earthworm cultivation density is 350-450 per square, controlling cultivation substrate temperature to 20-25 degrees C, controlling cultivation substrate humidity to 60-70%, and controlling pH value to 6-8.
NOVELTY - 1-(4 -((5-((4-(1H-1,2,4-Triazol-1-yl)phenoxy)methyl)-1,3,4-oxadiazole-2-yl)methoxy)phenyl)-1H-1,2,4-triazole (I) is new.    USE - (I) are useful in preparing fungicides and corrosion inhibitor (all claimed).    ADVANTAGE - The method: is simple and suitable for large-scale industrial production; has low production cost and less environmental pollution characteristics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - Fertilizer block comprises 80-100 pts. wt. fermented chicken manure, 40-50 pts. wt. modified starch, 30-40 pts. wt. mixture of powdered rock phosphate, zeolite powder and redstone powder in a respective mass ratio of 5:2:1, 20-40 pts. wt. biogas residues, 30-50 pts. wt. potassium sulfate, 20-40 pts. wt. mixture of oil cake and bean cake in a mass ratio of 1:3, and 10-30 pts. wt. potassium fulvate. The diameter of the fertilizer block is 12-15 cm.    USE - As fertilizer block.    ADVANTAGE - The fertilizer block exhibits rapid effect for a prolonged period of time, is prepared simply and cost-effectively, and convenient to use, and has slow-release property. The fertilization effect is prolonged by 75-85%, and the fertilization rate is increased by 65-80%.
NOVELTY - Organic fertilizer comprises traditional Chinese medicinal residues of antiviral medicine, where the fertilizer has organic matter of more than 70 wt.%, and nitrogen phosphorus potassium matter of more than 5 wt.%.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) crushing traditional Chinese medicine residues to obtain coarse powder, (b) mixing coarse powder with chicken manure, stirring uniformly and adding microbial inoculum to obtain fermentation mixture, (c) adding mixture obtained in the step (b) to fermentation tank, controlling the temperature to 60-70 degrees C, performing an aerobic fermentation for 20-36 days once the temperature reaches more than 70 degrees C, and collecting fermented product when the temperature reaches below 40 degrees C, (d) crushing fermented material, and sieving crushed material to obtain semi-finished organic fertilizer, (e) aging semi-finished organic fertilizer for 15-30 days, and (f) drying aged organic fertilizer for 1-5 days.
NOVELTY - Method for producing organic fertilizer, involves fermenting golden needle mushroom residues and poplar wood sawdust.    USE - The method is useful for producing organic fertilizer (claimed).    ADVANTAGE - The method is cost-effective.
NOVELTY - Fertilizer comprises mixture comprising urea, potassium phosphate and plant ash in respective mass ratio of 1:1:4, mixture comprising diesel oil and fermented corncob powder in a respective mass ratio of 5:1, calcium superphosphate, Spirulina powder, mixture comprising humus and crab shell powder in a respective mass ratio of 7:1, animal fats, and mixture comprising cortex moutan, radix salviae miltiorrhizae powder and glutamic acid in a respective mass ratio of 5:2:1.    USE - As fertilizer.    ADVANTAGE - The fertilizer is convenient to use and cost-effective, and provides fertilization rate up to 65-80% and efficiency up to 75-85%.    DETAILED DESCRIPTION - Fertilizer comprises 80-100 pts. wt. mixture comprising urea, potassium phosphate and plant ash in respective mass ratio of 1:1:4, 40-50 pts. wt. mixture comprising diesel oil and fermented corncob powder in a respective mass ratio of 5:1, 30-40 pts. wt. calcium superphosphate, 20-40 pts. wt. Spirulina powder, 30-50 pts. wt. mixture comprising humus and crab shell powder in a respective mass ratio of 7:1, 20-40 pts. wt. animal fats, and 10-30 pts. wt. mixture comprising cortex moutan, radix salviae miltiorrhizae powder and glutamic acid in a respective mass ratio of 5:2:1.
NOVELTY - Preparing fertilizer, by mixing fermented chicken manure, modified starch, rock phosphate, zeolite powder and redstone powder, mixing with biogas residue, potassium sulfate, diesel oil and soybean meal, adding potassium fulvate to the mixture, adding the mixture to kettle, heating, pouring the heated product into mold, cooling using cold water to obtain spherical blocks having diameter of 12-15 cm, coating outer surface of the blocks using molten sulfur, adding tung oil and packaging obtained product.    USE - The method is useful for preparing fertilizer (claimed).    ADVANTAGE - The method is simple. The prepared fertilizer is convenient to use.    DETAILED DESCRIPTION - Method for preparing fertilizer, involves mixing fermented chicken manure, modified starch, rock phosphate, zeolite powder and redstone powder, where the rock phosphate, zeolite powder and redstone powder are in ratio of 5:2:1, mixing with biogas residue, potassium sulfate, diesel oil and soybean meal, where the diesel oil and soybean meal are in mass ratio of 1:3, adding potassium fulvate to the mixture, adding the mixture to kettle, heating at 200-300 degrees C and 1.6 kg vapor pressure for 15-20 minutes, pouring the heated product into mold, cooling using cold water to obtain spherical blocks having diameter of 12-15 cm, coating outer surface of the blocks using molten sulfur to thickness of 2-3 mm, adding tung oil and packaging obtained product having diameter of 12-15 cm.
NOVELTY - Water retention fertilizer comprises 5-10 pts. wt. mixture comprising adsorption resin, clay and zeolite powder in a respective mass ratio of 1:2:4, 10-20 pts. wt. protein powder, 10-20 pts. wt. Chinese mosla herb powder, 40-50 pts. wt. and mixture comprising duck manure and vermiculite in a respective mass ratio of 20:1, 30-50 pts. wt. calcium dihydrogen phosphate, 1-2 pts. wt. phosphate solubilizing bacteria, 2-4 pts. wt. urea, and 1-2 pts. wt. mixture comprising fermenting bacteria, nitrogen-fixing bacteria and phytase in a respective mass ratio of 5:2:1.    USE - The water retention fertilizer is useful for promoting root growth of plants.    ADVANTAGE - The water retention fertilizer is convenient to use, reduces salt quantity in soil, enhances activity of microorganisms and enzymes in soil and neutralizes cations in the soil.
NOVELTY - Method for extracting cholesterol from egg yolk Oil, involves (a) placing the egg yolk oil in alumina/normal phase silica gel column, (b) eluting the sample using polar solvent, (c) concentrating the resulting eluate to obtain crude cholesterol, and (d) dissolving the crude cholesterol in aqueous solution of aliphatic alcohol, filtering the dissolved mixture and recovering product.    USE - The method is useful for extracting cholesterol from egg yolk oil (claimed).    ADVANTAGE - The method is simple, easy to operate, cost-effective and environmentally-friendly, and ensures high yield of good quality product.
NOVELTY - Method for monitoring aerobic fermentation process of sewage residue, involves (a) dehydrating sewage residue, mixing the dehydrated sewage residue with conditioning agent, and adding to fermenter, (b) inserting e.g. temperature probe, (c) installing oxygen sensors at one end of the suction pump, (d) installing transmitter and industrial display to the fermentor, (e) connecting inverter with programmable logic control, (f) setting detection time of e.g. oxygen, and (g) monitoring fermentation process.    USE - The method is useful for monitoring aerobic fermentation process of sewage residue (claimed).    ADVANTAGE - The method is less time-consuming and convenient.    DETAILED DESCRIPTION - Method for monitoring aerobic fermentation process of sewage residue, involves (a) dehydrating sewage residue, mixing the dehydrated sewage residue with conditioning agent to have moisture content of 60-65%, and adding the resulting mixture to a fermenter, (b) inserting temperature probe and suction pump probe into fermentation tank of the fermentor, (c) installing oxygen sensors at one end of the suction pump, and connecting ammonia sensor, hydrogen sulfide sensor to the inlet chamber, where the oxygen sensor, ammonia sensor, and hydrogen sulfide sensor are connected in series, (d) installing transmitter and industrial display, and programmable logic controllers to the fermenter, (e) connecting inverter, and blower with the programmable logic control using wire, (f) setting detection time of oxygen, ammonia, hydrogen sulfide with predetermined interval of time, and (g) monitoring the fermentation process, where the industrial display, programmable logic controller, blower, temperature probe, oxygen sensor, ammonia sensor, and hydrogen sulfide sensor are opened after the fermentation process.
NOVELTY - This utility new type claims a multifunctional marsh gas pool one automatic feeding vehicle, comprising a vehicle body and a hopper mounted in vehicle body a bottom hopper set with a open upper end wherein a semi-housing, housing and hopper inside connected, inner housing set with spiral conveying machine, a housing set with discharge wherein, wherein discharging end and a spiral conveying machine corresponding part, set with the one knife gate valve wherein the discharge. A knife gate valve further connect with the spreading device. This utility new type can finish for a add material of marsh gas pool, time saves time and labour force, working efficiency is also greatly increase the, and the utility new type can be used for field process for automatic fertilizing, through a size of leakage hole, fertilizing for process control, it greatly increase the fertilizer spreading efficiency, but also increase the fertilizer spreading quality, it has simple operation, reliable use, strong adaptability and high efficiency of work.
NOVELTY - The reactor has a reactor main body connected with a cover plate (1) that is fixed with a partition board (2). A center water inlet pipe (3) is engaged with the partition board. A side part of the cover plate is connected with an overflow pipe (6). An aeration head (7) is hinged with the reactor main body. An oxygen overflow pipe (10) is connected with a water pipe (11). A cylindrical device is provided with the reactor main body. A gas inlet pipe (4) is connected with an oxygen inlet pipe (9).    USE - Separate methane-denitrification reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a separate methane-denitrification reactor. '(Drawing includes non-English language text)'    Cover plate (1)    Partition board (2)    Center water inlet pipe (3)    Gas inlet pipe (4)    Overflow pipe (6)    Aeration head (7)    Oxygen inlet pipe (9)    Oxygen overflow pipe (10)    Water pipe (11)
NOVELTY - Method for preparing water-soluble fertilizer, involves mixing biomass from organic acids with urea solution to obtain solution containing amino acids, performing biomass pyrolysis reaction of calcium oxide powder, iron powder, copper powder, zinc powder and manganese powder with obtained solution to obtain calcium acetate solution, iron acetate solution, copper acetate solution, zinc acetate solution and manganese acetate solution, respectively, and uniformly stirring mixture.    USE - The method is useful for preparing water-soluble fertilizer (claimed) and sterilized product for preventing downy mildew, powdery mildew, gray mold, leaf spot, anthracnose, red rust, root rot and other fungal diseases, inhibiting growth of fungal spores in soil, and adjusting pH of the soil.    ADVANTAGE - The method improves yield and quality of crops.
NOVELTY - A Bacillus subtilis strain having CCTCC NO: M2014276, is new.    USE - Bacillus subtilis strain for preparing aquatic feed and microorganism composition that is utilized in aquaculture or sewage treatment (all claimed) for removing nitrite-nitrogen.    ADVANTAGE - The strain has better nitrite-nitrogen removal rate, and broad application prospects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a microorganism composition comprising Bacillus subtilis strain.
NOVELTY - A Pseudomonas fluorescens strain having CCTCC NO: M2014274 is new.    USE - Pseudomonas fluorescens strain for preparing microorganism composition that is utilized in water purification field such as aquaculture wastewater or sewage treatment field (all claimed) for energy efficient degradation of nitrite nitrogen, and for preparing aquaculture probiotics and sewage treatment agent.    ADVANTAGE - The strain has aerobic denitrification property, better nitrogen removal rate, and broad application prospects.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a microorganism composition comprising Pseudomonas fluorescens strain.
NOVELTY - Method includes preparation of ash and slag, mixing them with leaching solution, accumulation of biomass of microorganisms, bacterial leaching of rare earth and noble metals, separation of obtained suspension into sediment and clarified liquid with isolation of rare earth and noble metals from the latter. At the stage of accumulation of biomass of microorganisms saturated solution of calcium carbonate is added in amount 1-10% of leaching solution consumption. Bacterial leaching is performed in mode of multi-chamber floatation with aeration intensity 0.1-0.5 m3/m2.min. Intensity of aeration in each following chamber is reduced by 5-10% in comparison with the previous one. Bacteria of genus Acidithiobacillales are used as microorganisms. Floatation is performed with application of finely disperse aeration with average size of bubbles 20-30 mcm. Size of bubbles in any following chamber is increased by 10-15%.    USE - Chemistry.    ADVANTAGE - Increased extraction of rare earth and noble metals from ash and slag due to intensification of organism cultivation process.4 cl, 3 ex
NOVELTY - The device has a positive electrode compartment connected with a cathode room. An anion exchange film is formed on an anode room that is connected with an anode electrode. The cathode room is connected with a cathode liquid feed port. An aeration device is fixed with a cathode electrode and a bottom part of the cathode room. The anode electrode and the cathode electrode are connected with a resistor and a switch. The cathode electrode is formed with carbon paper, carbon cloth, graphite felt, stainless steel network and foam nickel.    USE - Microorganism fuel battery phenol and ammonia nitrogen degrading device.    ADVANTAGE - The device has better economic benefit and environmental protection effect, and removes phenol and ammonia nitrogen in sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a microorganism fuel battery phenol and ammonia nitrogen degrading device.
NOVELTY - The system has a level radiator (2) provided with an outlet of an anaerobic fermentation tank (4) and a sludge inlet that are connected together. The anaerobic fermenting tank is connected with a level radiator (6). The level radiator is connected with the sludge outlet that is connected with an anaerobic ammonia oxidizing tank (9). The level radiator is connected through a measuring pump (7) and a nitrite solution tank (8). The anaerobic ammonia oxidizing tank is connected through the measuring pump and the nitrite solution tank.    USE - High efficient recycling and low pollution discharge sludge processing system.    ADVANTAGE - The system has high economic benefit and low environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a high efficient recycling and low pollution discharge sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a high efficient recycling and low pollution discharge sludge processing system.    Level radiators (2, 6)    Anaerobic fermentation tank (4)    Measuring pump (7)    Nitrite solution tank (8)    Anaerobic ammonia oxidizing tank (9)
NOVELTY - The system has a system main body provided with an oil resin collecting device, a feeding separating system unit, a biological treatment system unit and a deodorization integrated sewage treatment system unit. A solid waste collecting device and the feeding separating system unit are connected with the deodorizing sewage integrated processing system unit. A malodorous pneumatic body is connected with the biological treatment system unit. The feeding separating system unit is provided with a hopper. The solid waste collecting device is provided with a sludge collecting pool.    USE - Kitchen waste processing system.    ADVANTAGE - The system has high working efficiency, large processing amount and high marsh gas quantity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a kitchen waste processing system.
NOVELTY - Recovering solvent in mesotrione production process comprises adding mesotrione, triethylamine and dichloroethane into a reaction container, uniformly mixing to obtain a mixed solution, adding water to the mixed solution, condensing the mixed solution, stirring the condensed mixed solution, slowly dropping dilute sulfuric acid to the stirred solution, adjusting pH value to 1-1.5, stirring the mixture for 15 minutes, decompressing and distilling the mixture under vacuum, and storing using a storage groove.    USE - The method is useful for recovering solvent in mesotrione production process (claimed).    ADVANTAGE - The method is capable of simply recovering solvent in mesotrione production process with improved water absorbing properties and reduced energy consumption and cost.    DETAILED DESCRIPTION - Recovering solvent in mesotrione production process comprises adding mesotrione, triethylamine and dichloroethane into a reaction container, uniformly mixing to obtain a mixed solution, adding water to the mixed solution, condensing the mixed solution, where the triethylamine and water have a volume ratio of 1:1-5, stirring the condensed mixed solution, slowly dropping 80-91% of dilute sulfuric acid to the stirred solution, where the triethylamine and dilute sulfuric acid have a molar ratio of 1:0.5-0.8, adjusting pH value to 1-1.5, stirring the mixture for 15 minutes, separating mesotrione dichloroethane solution, decompressing and distilling the mixture under vacuum to recycle moisture dichloroethane, and storing using a storage groove.
NOVELTY - Bio-organic fertilizer containing strains having high resistance to cadmium pollution comprises 4-6 pts. wt. core inoculant, 1-3 pts. wt. ionic antagonist and 91-95 pts. wt. refined organic fertilizer.    USE - The bio-organic fertilizer is useful for production of agricultural crops (claimed).    ADVANTAGE - The bio-organic fertilizer: comprises core inoculant, which ensures quick growth and colonization in the soil and multiplication to change the chemical form of the heavy metal cadmium in the soil to mix, passivation or detoxification; reduces soil environment mobility and bioavailability; enables direct absorption of heavy metal cadmium ions to microbial cell wall or intracellular metabolism; comprises ionic antagonist and refined organic fertilizer, which causes further cadmium reduction, purification and refining; and is safe.
NOVELTY - The device has a gas recovery device fixed with a double-room microorganism fuel cell system that is provided with an anode room and a cathode room. A positive ion exchange film is separated from the anode room that is fixed with a liquid anode and an anode electrode. The cathode room is provided with an aeration device, an ammonia gas exit and a cathode electrode. The aeration device is placed with the cathode room. The cathode electrode is connected with an outer circuit through an external circuit. An ammonia recovery unit is connected with the cathode room port through a pipeline.    USE - Microorganism fuel cell removal based sewage ammonia nitrogen recovery device.    ADVANTAGE - The device has better economic benefit and environmental protection benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a sewage ammonia nitrogen recovery method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a microorganism fuel cell removal based sewage ammonia nitrogen recovery device.
NOVELTY - Mitigating negative effects of fatty acid methyl ester (FAME) diluted in oil, involves epoxidation to remove carbon-carbon double bond (C=C), use of hydroboration and hydrosilylation reactions, use of Diels-Alder reaction, use of metathesis and oxidative cleavage reactions, use of transesterification reactions, decarboxylation of FAME and its oxidation products, use of slow-release thickener, decomposition of hydroperoxides, oxidatively chelating the catalytic metals, use of polyphosphazene bases, or thermal oxidation of FAME in the presence of nitrous oxide.    USE - The method is useful for mitigating negative effects of FAME used for the production of biodiesel.    ADVANTAGE - The method reduces the accumulation of FAME thus avoiding dilution of the lubricant and a subsequent loss in oil viscosity, improving engine performance such as oxidation control, cold flow properties, wear-control, sludge deposit control and component interaction, and decreasing costs for the consumer or fleet operator.
NOVELTY - Obtaining sweet gas, synthesis gas and sulfur from natural gas involves removing impurities from the natural gas so as to obtain pretreated natural gas; sweetening the pretreated natural gas by separation using membranes so as to obtain sweet gas and acid gases; ionizing the acid gases to separate them into sulfur and synthesis gas with remnants of acid gases; and neutralizing the synthesis gas with remnants of acid gases so as to generate synthesis gas.    USE - The method or system is useful for obtaining sweet gas, synthesis gas and sulfur from natural gas (claimed).    ADVANTAGE - The method is more efficient and can increase the interaction with CO2, and can decrease the size of the chain to crystallize to achieve higher gas flows. The hybrid plasma reactor provides at least three fundamental properties making it attractive for different applications: (i) the temperature and energy density greatly exceeds the conventional techniques; (ii) ability to produce active species with very low reaction to conventional techniques; and (iii) active species have high concentrations of power even when the volume of plasma remains at room temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for obtaining sweet gas, synthesis gas and sulfur from natural gas comprising a separator; a coalescing filter connected in parallel to the separator; membranes connected to the coalescing filter, such membranes are prepared from polyimide, polybenzimidazole, polyamides, polyethers, polyurethanes, polyureas, polymers, and its combinations; at least one hybrid double wall plasma reactor connected to membranes; and bubble columns connected to the hybrid plasma reactor and containing a neutralizing agent.
NOVELTY - The reactor has an oxidation state (4) formed in an air supply device (9). Nozzle openings are distributed on the air supply device. The oxidation state is opened into a reduction stage (3). A coaxial core (7) encloses an annular chamber (5). Two circumferential walls of the annular chamber are arranged with the nozzle openings of the air supply device for adding a nozzle ring. The air supply device is attached at the circumferential wall of the annular chamber by the coaxial core. An air line (8) is fixed within the coaxial core that receives a screw feeder.    USE - Reactor for gasification of biomass i.e. wood, (claimed).    ADVANTAGE - The annular chamber walls are arranged with nozzle openings of the air supply device for adding a nozzle ring so as to avoid entering of uncontrollable wrong air during oxidation state of the reactor, thus achieving better gasification condition with simple structural measures.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a reactor for gasification of biomass.    Reduction stage (3)    Oxidation state (4)    Annular chamber (5)    Coaxial core (7)    Air line (8)    Air supply device (9)
NOVELTY - The digester (1) has a receptacle for receiving a fermentable organic matter (5) and placed in an external silo (2), where fermentation of the organic matter leads to formation of biogas (6) above the organic matter, and the biogas is transformed into a digestate. The silo comprises inlets for the organic matter and outlets for the biogas. The receptacle comprises a flexible envelope (4) that is closed for containment of the organic matter and the biogas. The inlets and the outlets traverse through the envelope in a sealed manner. The envelope comprises a rectangular band.    USE - Digester i.e. methanizer, for use in an agricultural area for producing biogas i.e. methane and carbon dioxide mixture, and digestate i.e. biofertilizer, for heating and drying purposes in a farm building and a swimming pool.    ADVANTAGE - The digester is assembled in a simple, rapid, powerful and durable manner. The digester is designed such that the silo is robust and economic to use. The digester comprises an easily isolatable insulation. The digester does not utilize civil engineering and complex devices for the recovery of the biogas under security conditions, thus optimizing biological effectiveness of the digester.    DETAILED DESCRIPTION - The flexible envelope is designed as a flexible cover or a geomembrane that comprises a fabric or a geotextile coating. The fermentable organic matter is formed as liquid manure, manure, lawn shearings, residues or harvest surpluses such as small straws and silages. An INDEPENDENT CLAIM is also included for a method for assembling a digester.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of a digester.    Digester (1)    External silo (2)    Flexible envelope (4)    Fermentable organic matter (5)    Biogas (6)
NOVELTY - This utility new type claims a set one organic sewage treatment and producing a as a whole of the electrolytic pool. microorganism, microorganism comprising electrolytic pool shell (1), set with an anode electrode 8 and cathode electrode 4 microorganism electrolysis pool shell (1) inner, a cathode electrode 4 and an anode electrode 8 a through titanium 5 and titanium silk 7 connected with the external direct current stabilized voltage power supply 6 of low voltage end and high electric potential end is connected with microorganism electrolysis pool shell (1) of lower end side set with water inlet pipe 9, a water inlet pipe 9 and water distributor 10, microorganism electrolysis pool shell (1) is set with sludge discharge pipe 11 and valve 12, microorganism electrolysis pool shell (1) upper end surface set with a drain pipe 2, microorganism electrolysis pool shell (1) top end set with gas collecting pipe 3. This utility new type through sewage inlet pipe 9, removing organic matter sewage of oxygen injection microorganism electrolysis pool inner anode power generating microorganism growing as a nutrition source, an anode power generating microorganism for organic matter in sewage process of catabolism, produce CO2 in the same time of sewage treatment, H + and a. While the lower auxiliary, a cathode electrode 4 surface adhered electric activity of methane bacteria the anode power generating microorganism metabolic organic substance produce a CO2, H +, and a conversion is alkyl. This utility new type collecting sewage processing device, and generating a CO2 capture together, has simple structure and low construction cost, and it is easy to scale amplification. In addition, sewage orderly flows through the anode area and cathode area, which avoids the add electrochemically active methane bacteria culture medium on the cathode, and reduces the cost. Therefore, the energy using device has good application prospect in the aspect of organic sewage.
NOVELTY - A microorganism of Pseudomonas brassicacearum CECT 8162 strain or its mutant strain which maintains the ability to accumulate up to at least 20% of its dry weight in the form of lipids, is new.    USE - The microorganism is useful for obtaining triglyceride-rich microbial biomass, paraffins and biodiesel; and for making lipid composition from microbial biomass (all claimed).    ADVANTAGE - The microorganism not only can provide an economically viable alternative feedstock, but also can achieve sustainability criteria for biofuels.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method for obtaining a triglyceride-rich microbial biomass comprising: (i) culturing the microorganism in a culture medium comprising at least one carbon source and at least one nitrogen source, under conditions suitable for microorganism growth; and (ii) separating the microbial biomass of the culture medium, where the ratio carbon:nitrogen (C:N) in the culture medium is high;    (2) a triglyceride-rich microbial biomass obtainable by the method;    (3) a method for making a lipid composition from microbial biomass comprising extracting the lipid fraction of the microbial biomass;    (4) a method for obtaining paraffins comprising: (i) refining the lipids obtained by the method; and (ii) converting the refined mixture of lipids obtained in step (i) in paraffins; and    (5) a method for obtaining biodiesel comprising: (i) refining the lipids obtained by the method above; and (ii) converting the refined mixture of lipids obtained in step (i) in biodiesel.
NOVELTY - Method for preparing cellulose complex, involves transforming recombinant vector containing gene encoding chimeric endo beta -1,4-glucanase E (cCelE), gene encoding xylanase B (XynB) and gene encoding mini cellulose binding protein A (mCbpA) into a recombinant yeast, respectively, culturing the recombinant yeasts together, primarily forming a XynB-mCbpA complex, then forming cCelE-XynB-mCbpA complex, and collecting product.    USE - The method is useful for preparing cellulose complex which is used in brewery, bakery, alcohol production, feed production and probiotic development.    DETAILED DESCRIPTION - Method for preparing cellulose complex, involves (a) transforming recombinant vector containing gene encoding chimeric endo beta -1,4-glucanase E (cCelE) into a recombinant yeast, transforming recombinant vector containing gene encoding xylanase B (XynB) into a recombinant yeast and transforming recombinant vector containing gene encoding mini cellulose binding protein A (mCbpA) into a recombinant yeast, (b) culturing the above-mentioned recombinant yeasts together, and (c) primarily forming a XynB-mCbpA complex, then forming cCelE-XynB-mCbpA complex, and collecting formed product. An INDEPENDENT CLAIM is included for method (M1) for producing ethanol by simultaneous saccharification and fermentation of biomass, which involves culturing the above-mentioned recombinant yeast in a biomass and collecting produced ethanol.
NOVELTY - An alkcell or alkali-cellulase process to convert biomass (cellulosic material) to glucose using an alkali pretreatment followed by cellulase hydrolysis, involves using materials and methods amenable to implementation at or near the biomass growing or storage site, such that the process can be done in individual steps or by continuous process that uses mild temperatures not exceeding boiling of the water solutions employed in process, such that the temperatures can be achieved with thermal heating as with a gas fuel device such as a propane tank burner.    USE - In an alkcell or alkali-cellulase process to convert biomass (cellulosic material) to glucose (claimed), where the cellulosic material is agricultural waste like corn stover.    ADVANTAGE - The process uses materials readily available commercially that present limited hazard to operators of the process; can be operated manually or powered or both and with separate steps or in a continuous fashion; uses methods that can be implemented without technically sophisticated processes and thus is suitable for operation locally, i.e., near the biomass growing site; avoids the need and cost to transport unprocessed biomass distances to fermentation facilities outfitted to handle raw biomass; does not require extensive technical training of operators; and can be done in individual steps or by continuous process that uses mild temperatures not exceeding boiling of the water solutions employed in process.
NOVELTY - Method for making a product involves (a) determining the lignin content of a biomass feedstock, treating the biomass feedstock material with a process e.g. mechanical treatment, and steam explosion, and setting a process parameter of the process based on the lignin content or (b) providing a cellulosic or lignocellulosic material having several pendent carboxylic acid groups, mixing the material in a fluid that includes water to provide a dispersion that has a first pH, and adding base to the dispersion to increase its pH to a second pH higher than the first pH.    USE - The method is useful for making a product, preferably carboxylic acid, ester, salt, or their mixtures, fuel such as ethanol (all claimed) and food.    DETAILED DESCRIPTION - Method for making a product involves (a) determining the lignin content of a biomass feedstock, treating the biomass feedstock material with a process chosen from mechanical treatment, chemical treatment, radiation, sonication, pyrolysis, oxidation, steam explosion and their combinations and setting a process parameter of the process based on the lignin content or (b) providing a cellulosic or lignocellulosic material having several pendent carboxylic acid groups, mixing the material in a fluid that includes water to provide a dispersion that has a first pH, and adding base to the dispersion to increase its pH to a second pH higher than the first pH.
NOVELTY - Obtaining sweet gas (6), synthetic gas (15), and sulfur (10) from natural gas (1) comprises: removing impurities from the natural gas for obtaining pre-treated natural gas; sweetening the pre-treated natural gas through a separation using many membranes for obtaining sweet gas and acid gases (7); ionizing the acid gases to dissociate them into sulfur and synthetic gas with remnants of acid gases; and neutralizing the synthetic gas with remnants of acid gases for generating synthetic gas.    USE - The method is useful for obtaining sweet gas, synthetic gas, and sulfur from natural gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for obtaining sweet gas, synthetic gas, and sulfur from natural gas, comprising a separator, a coalescing filter connected in parallel to the separator, the membranes connected to the coalescing filter, where the membranes are made of polymers consisting of polyimides, polybenzimidazole, polyamides, polyethers, polyurethanes and/or polyureas, at least a hybrid plasma reactor connected to the membranes, and many bubbling columns connected to the hybrid plasma reactor which contains a neutralizing agent.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of method for obtaining sweet gas, synthetic gas, and sulfur from natural gas.    Natural gas (1)    Sweet gas (6)    Acid gases (7)    Sulfur (10)    Synthetic gas (15)
NOVELTY - This utility new type relates to one used for treating a rumen heave pneuma of multifunctional device, especially relating to a high, a middle rumen heave pneuma. Is mainly composed by the handle, a sleeve, a needle core, deflation valve and injection plug. Needle core and sleeve through screw thread connecting with the handle, deflation valve and injection piston through a screw thread connecting with the sleeve. The new-type of a feature is as follows: a connecting sleeve of the air valve control speed of a discharge to prevent discharging caused by too fast and suffer from other secondary disease (such as shock, etc.), at the same time, discharging protection cover of a valve for preventing a sliding sleeve, reduces the labour intensity of operator. Sleeve front end design 4 a hole, to time the pneuma rumen contents anti-blocking sleeve. Injection plug time needed for a rumen inner injection drug, with the sleeve through the screw thread connecting, a use, a rear interface, drug or rumen contents is not easy to leak, it reduces the pollution of puncturing part.
NOVELTY - A methane fermentation apparatus (10) comprises methane fermentation tank (14) which methane-ferments organic waste to produce biogas and has culture tank (22) which cultures phototrophic microorganism and retention-of-gas unit (16) which stores biogas produced by methane fermentation tank and has dissolution unit for dissolving carbon dioxide in biogas in a liquid. The liquid in which the carbon dioxide is dissolved is supplied by liquid supply unit (28) to the culture tank.    USE - A methane fermentation apparatus (claimed).    ADVANTAGE - Carbon dioxide which is originally discarded can be effectively used, decreasing carbon-dioxide emissions or amount of waste material. Carbon dioxide in biogas can be dissolved in a liquid by a simple structure. Culture of phototrophic microorganism can be accelerated more by supplying not only the liquid containing large amount of carbon dioxide but also a digestive liquid to a culture tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the methane fermentation apparatus. (Drawing includes non-English language text).    Methane fermentation apparatus (10)    Methane fermentation tank (14)    Retention-of-gas unit (16)    Culture tank (22)    Liquid supply unit (28)
NOVELTY - The method involves passing the material through a reactor chamber and heating to a material-based process temperature of 300-1000 degrees C. A degassing pressure is increased in the interior of the reactor chamber. A direct thermal treatment of materials is performed parallel to an indirect thermal treatment, starting from the outer surface of the reactor chamber by controlled and inwardly acting magnetic induction. The additional materials are returned by supplying heated permanent gas.    USE - Method for recovering raw materials from waste materials such as bituminous waste, hospital waste, sorted household waste, digestate from biogas plant, rapeseed meal, sunflower meal, renewable raw materials, animal waste and oil-contaminated sand, in sealed thermal reactor chamber for use in electronics industry.    ADVANTAGE - The faster recovery of raw materials is enabled . The more accurate and more efficient management of the necessary process temperatures and a need of insertion is no longer required.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for recovering the raw materials from the waste materials in a sealed thermal reactor chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the device for recovering raw materials from waste materials in sealed thermal reactor chamber. (Drawing includes non-English language text)
NOVELTY - The apparatus (100) has a first photo-catalyst electrode for producing chemical substance using oxidation reaction with respect to a component of electrolyte solution (130a) in reductive reaction, and a second photo-catalyst electrode in which oxidation reaction is performed with respect to another component of the solution in another reductive reaction. A control part (140) controls current density according to time fluctuation of energy such that electrode potential of the first electrode reaches oxidation or reduction potential of production reaction of the chemical substance.    USE - Apparatus for synthesizing chemical substance e.g. oxygen and hydrogen, dissolved in electrolyte solution e.g. sodium hydroxide solution, potassium hydrogen carbonate solution, sodium chloride solution and sulfuric acid solution. Can also be used for liquid fuel i.e. alcohol, organic hydride and water.    ADVANTAGE - The apparatus synthesizes the chemical substance by electrolytic synthesis using energy such that advancing of reaction other than objective reaction can be suppressed so as to provide highly efficient apparatus at low cost.    DETAILED DESCRIPTION - The second photo-catalyst electrode is a working electrode (110). The first photo-catalyst electrode is a counter electrode (120). The component is selected from a group consisting of water molecule, hydroxide ion, hydrogen ion and carbon-di-oxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an apparatus for synthesizing chemical substance dissolved in electrolytic solution.'(Drawing includes non-English language text)'    Apparatus for synthesizing chemical substance dissolved in electrolytic solution (100)    Working electrode (110)    Counter electrode (120)    Electrolyte solution (130a)    Control part (140)
NOVELTY - Producing biogas from non-pumpable biomass comprising multiple gas and liquid tight sealable fermenters (1), comprises collecting percolate resulting in the fermenters, and discharging the individually controlled fermenters, in which hygienized percolate is discharged in the individual fermenters.    USE - The method is useful for producing biogas from non-pumpable biomass (claimed).    ADVANTAGE - The method: ensures that hygienized and non hygienized percolate are in separate container; and prevents irregular accumulation of percolate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas plant for methanation of non-pumpable biomass, comprising gas and liquid tight sealable fermenters for the biomass, a biogas removal opening (2) in each fermenter, a percolate reservoir (3), a percolate removal device (4) from each fermenter which conveys the percolate obtained from it to percolate reservoir, a percolate distributor (5), which distributes the percolate from the percolate storage reservoir into each fermenter. The percolate reservoir comprises at least two percolate container, which are connected to one another via a connecting line, and a treatment unit is arranged in the connecting line for the passing percolate.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Fermenters (1)    Biogas removal opening (2)    Percolate reservoir (3)    Percolate removal device (4)    Percolate distributor (5)
NOVELTY - The process involves controlling synthesis gas ratio in a single step at constant temperature of electrochemical cell and under conditions of constant composition and concentration of inflow current, where the electrochemical cell is set to temperature among 500 Armstrong degrees Celsius and 900 Armstrong degrees Celsius. Inflow current is selected from current of light hydrocarbons and water vapor current or gaseous current containing alcohol. Entrance current is diluted in selected inert gas current of a list that includes nitrogen, helium, neon, argon, krypton and xenon.    USE - Process for producing synthesis gas in a petrochemical industry or fuel production industry.    ADVANTAGE - The process enables selecting inflow current from the current of light hydrocarbons and the water vapor current or gaseous current containing alcohol, thus producing the synthesis gas in the petrochemical industry in an easier and effective manner.    DETAILED DESCRIPTION - The process enables utilizing conductive anionic solid electrolyte (9) made of zirconium oxide, oxides of titanium, yttrium oxide stabilized with zirconium oxide, zirconium oxide stabilized with calcium and platinum.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electrochemical cell.    Electrode of work (1)    Quartz tube (8)    Conductive anionic solid electrolyte (9)    Conductive cationic solid electrolyte (10)    Gas entrance (11)
NOVELTY - The device (200) has a reactor i.e. tubular reactor, filled with aqueous media (118), where methanogenic microorganisms are present in the aqueous media. A feeding device is fixed with the reactor for introduction of hydrogen and carbon dioxide gaseous mixture. A reaction increase device enlarges a contact surface between the aqueous media with the methanogenic microorganisms and the gaseous mixture. A discharge equipment drives off gas i.e. methane gas, from the reactor. A return device e.g. shoot jet pump or compressor, reconducts part of the gas into the supply device.    USE - Device for producing methane by methanogenic microorganisms.    ADVANTAGE - The device can produce methane using methanogenic microorganisms in an effective and inexpensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing methane by methanogenic microorganisms.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a methane producing device.    Input line (102)    Valve (114)    Aqueous mediums (118)    Methane producing device (200)    Agitating kettle (202)
NOVELTY - Producing potable ethanol from Agave, by combining Agave bagasse with acid to form acid hydrolysis mixture, steam treating, cooling, combining cooled mixture and enzyme chosen from cellulase, hemicellulase, inulinase, and their combinations to form enzyme hydrolysis mixture, where the enzyme hydrolyzes at least one of cellulose, hemicellulose, and inulin present in the Agave bagasse into a water-soluble sugar, separating water-soluble sugar from hydrolysis mixture, and combining water-soluble sugar with fermentation mixture comprising fermentable sugar.    USE - The method is useful for producing potable ethanol from Agave which is used in tequila (all claimed) or as biofuel.    DETAILED DESCRIPTION - Method for producing potable ethanol from Agave, involves (a) combining Agave bagasse with an acid to form an acid hydrolysis mixture, steam treating the acid hydrolysis mixture, and cooling the steam treated mixture to obtain cooled mixture having a temperature sufficient for enzyme hydrolysis, and (b) combining the cooled mixture and an enzyme chosen from cellulase, hemicellulase, inulinase, and their combinations to form an enzyme hydrolysis mixture, where the enzyme hydrolyzes at least one of cellulose, hemicellulose, and inulin present in the Agave bagasse into a water-soluble sugar, separating the water-soluble sugar from the hydrolysis mixture, and combining the water-soluble sugar with a fermentation mixture comprising a fermentable sugar derived from an pina of Agave.
NOVELTY - Producing ethanol comprises: blending Agave bagasse and Agave leaves; steam treating the formed blended mixture; cooling the formed steam treated blended mixture; combining the cooled blended mixture and an enzyme comprising cellulase, hemicellulose and/or inulinase to thus form an enzyme hydrolysis mixture; combining the enzyme hydrolysis mixture with a fermentable sugar derived from an Agave pina and with a yeast to thus form a fermentation mixture; and fermenting the fermentation mixture to thus prepare a wort comprising ethanol.    USE - The method is useful for producing ethanol (claimed) which is useful in a distilled beverage or as a biofuel.    ADVANTAGE - The method increases production yield of ethanol.    DETAILED DESCRIPTION - Producing ethanol comprises: blending Agave bagasse and Agave leaves to form a blended mixture; steam treating the blended mixture to prepare a steam treated blended mixture; cooling the steam treated blended mixture to thus form a cooled blended mixture having a temperature sufficient for enzyme hydrolysis; combining the cooled blended mixture and an enzyme comprising cellulase, hemicellulose and/or inulinase to thus form an enzyme hydrolysis mixture; combining the enzyme hydrolysis mixture with a fermentable sugar derived from an Agave pina and with a yeast to thus form a fermentation mixture; and fermenting the fermentation mixture to thus prepare a wort comprising ethanol. The enzyme hydrolyzes at least one of a cellulose, a hemicellulose, or an inulin present in the Agave bagasse and the Agave leaves into a water-soluble sugar.
NOVELTY - Recovering oil, comprises: (a) converting a starch-containing material into dextrins with alpha -amylase; (b) saccharifying the dextrins using a carbohydrate source generating enzyme to form a sugar; (c) fermenting the sugar in a fermentation medium into a fermentation product using a fermenting organism; (d) recovering the fermentation product to form a whole stillage; (e) separating the whole stillage into thin stillage and wet cake; (e1) optionally concentrating the thin stillage into syrup; and (f) recovering oil from the thin stillage and/or optionally the syrup.    USE - The process is useful for recovering oil from thin stillage and/or syrup in the fermentation product production process (all claimed) such as ethanol production process, where the oil is useful in biodiesel production or other biorenewable products.    ADVANTAGE - The process economically increases the oil recovery yields from thin stillage and/or syrup in the fermentation product production process using protease.    DETAILED DESCRIPTION - Recovering oil, comprises: (a) converting a starch-containing material into dextrins with alpha -amylase, and optionally recovering oil during and/or after the step (a); (b) saccharifying the dextrins using a carbohydrate source generating enzyme to form a sugar; (c) fermenting the sugar in a fermentation medium into a fermentation product using a fermenting organism; (d) recovering the fermentation product to form a whole stillage; (e) separating the whole stillage into thin stillage and wet cake; (e1) optionally concentrating the thin stillage into syrup; and (f) recovering oil from the thin stillage and/or optionally the syrup. A protease having a thermostability value of more than 20% determined as relative activity at 80 degrees C/70 degrees C is present and/or added during the step (a) or the steps (d)-(e) and the step (e1).
NOVELTY - The device (10) has a pressing roll (4) which is arranged outside of ring roll (2) presses outer peripheral surface of ring roll. An adjustment unit (33A) relatively moves inscribed roll (3) and pressing roll along moving direction toward or away from each other to adjust center-to-center distance between rotation center of inscribed roll and pressing roll. To-be-squeezed object is arranged in space portion of ring roll and is directly squeezed by inner peripheral surface of ring roll and outer peripheral surface of inscribed roll.    USE - Squeezing device for squeezing liquid from liquid containing plant such as oil palm and sugarcane.    ADVANTAGE - The processing time of manufacturing fuel pellet is shortened, such that the cost of squeezing device is reduced reliably. The moisture content in residue is reduced. The efficient residue conveyance is performed.    DETAILED DESCRIPTION - A press unit presses press roll to inscribed roll side through ring wall portion of ring roll. A press roll rotation unit rotates press roll. A rotation transmission unit transmits rotation of press roll to ring roll by friction. A pressing target object supply unit supplies the pressing target object to space portion. A vibrating feeder conveys the pressing target object by vibration. A separation unit separates the residue of pressing target object mixed in squeeze. INDEPENDENT CLAIMS are included for the following:    (1) fuel-pellet manufacturing equipment has molding apparatus that compresses residue after pressing target object is squeezed by back stage of squeezing device for molding fuel pellet; and    (2) pressing method involves conveying the residue on outer side of space portion by airflow conveying unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic front view of the squeezing device.    Ring roll (2)    Inscribed roll (3)    Pressing roll (4)    Squeezing device (10)    Adjustment unit (33A)
NOVELTY - Electric power generating apparatus comprises combustion unit (1) having primary (1a) combustion unit and secondary combustion unit which burn biomass fuel that carries aging and aerobic fermentation of livestock excrement containing cattle feces, boiler (2) which generates steam by combustion heat from the combustion unit, and generator (3) having turbine (3a) rotated by the steam from the boiler to generate electric power.    USE - The electric power generating apparatus is useful in system for recycling livestock excrement containing cattle feces (all claimed).    ADVANTAGE - The electric power generating apparatus is simple and cost-effective to operate, consumes less power, utilizes the combustion ashes as fertilizer, and reduces burden of processing the livestock excrement.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for recycling livestock excrement, which comprises the electric power generating apparatus comprising livestock excrement, fuel production unit for producing biomass fuel from the livestock excrement, and heat transmitting unit which transmits heat from heat source (steam) of the boiler to the fuel production unit.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic block diagram of the electric power generating apparatus. (Drawing includes non-English language text)    Combustion unit (1)    Primary combustion unit (1a)    Boiler (2)    Generator (3)    Turbine (3a)
NOVELTY - A modified diatom strain in which a gene involved in lipid metabolism has been inactivated by a TAL-nuclease, a modular base-per-base specific nucleic acid binding domain (MBBBD)-nuclease or Clustered Regularly Interspaced Short palindromic Repeat (CRISPR)/Cas9 nuclease, is new.    USE - The modified diatom strain is useful for producing lipids and for further producing biofuel, a cosmetic or a food product (all claimed).    ADVANTAGE - The diatom produces an increased amount, storage and/or quality of lipids (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method for producing lipids by (a) cultivating a modified diatom strain above in an adapted culture medium; (b) optionally harvesting the diatoms; and (c) extracting the lipids from the diatom.
NOVELTY - The installation unit has a mechanization unit (6) for treatment of biogases, and a cogeneration unit (8) for delivering electricity and heat from the biogases. A hydroponic microalgae culturing unit (14) is provided for growing microalgae in photo-bioreactors supplied with a liquid phase (12) of organic residues of mechanization. A macrophytes culturing unit (22) is fed by the liquid phase and water (20) came-out from the microalgae culturing unit. The microalgae culturing unit receives carbon dioxide (30) collected in flue gases of a cogenerator.    USE - Installation unit for treatment and recovery of breeding effluents to produce biogas of effluents in an agricultural field.    ADVANTAGE - The macrophytes culturing unit is fed by the liquid phase and water came-out from the microalgae culturing unit, so that products can be concentrated and recovered so as to easily transport the products with reduced effort. The installation unit is designed, so that requirements of silos for mechanization can be avoided, thus ensuring better integration of the installation unit in landscapes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treatment and recovery of breeding effluents to produce biogas of effluents.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of an installation unit for treatment and recovery of breeding effluents to produce biogas of effluents.    Mechanization unit (6)    Cogeneration unit (8)    Liquid phase (12)    Hydroponic microalgae culturing unit (14)    Water (20)    Macrophytes culturing unit (22)    Carbon dioxide (30)
NOVELTY - Method (M1) for converting mushroom waste into raw material of organic fertilizer involves (a) collecting mushroom waste and crushing into fine powder, and (b) drying crushed powder to obtain dry mushroom waste, as main raw material of organic fertilizer.    USE - The method is useful for converting mushroom waste into raw material used for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer by cost-effective method, as the method utilizes mushroom waste, as the main raw material. The prepared organic fertilizer is nutritious and easily absorbed by plants, and has excellent fertilizer efficiency for prolonged time period, and improves the quality of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for producing organic fertilizer, which involves (a) mixing 400 kg raw material obtained in method (M1), 20 kg phosphorus fertilizer and 12 kg ammonium hydroxide uniformly, and (b) fermenting mixture for 7 days to obtain the product.
NOVELTY - A fertilizer comprises 50-100 pts. wt. plant straw, 30-50 pts. wt. green vegetable waste, 20-30 pts. wt. animal excrement, 20-40 pts. wt. river sand, 30-50 pts. wt. agricultural lime, 10-20 pts. wt. coal slag, 10-20 pts. wt. ferric hydroxide, 30-40 pts. wt. bone charcoal, 30-40 pts. wt. ammonium nitrate, 20-30 pts. wt. calcium superphosphate, and 20-30 pts. wt. potassium chloride.    USE - Fertilizer used for reducing heavy metal pollution in strawberry production (claimed).    ADVANTAGE - The method enhances fertilizer supply ability, increases strawberry yield and quality, and reduces lead, mercury, chromium and other heavy metal of residual in strawberry fruit and harmful chemical fertilizer and other organic waste.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of fertilizer comprising cutting plant straw into 2-4 cm length, spreading a layer of yarn cloth at the bottom of the first container, uniformly spreading with thickness of 20-25 cm plant straw, 3-6 cm river sand, 15-20 cm green vegetable waste and 3-5 cm agricultural lime, and maintaining temperature at 30-35 degrees C for 7-10 days; adding animal excrement, agricultural lime, coal slag, ferric hydroxide and bone charcoal, spreading with thickness of 15-20 cm plant straw, tightly wrapping with thin film, fermenting, stacking at more than 55 degrees C for 18-25 days, and taking off film; adding ammonium nitrate, calcium superphosphate and potassium chloride, uniformly mixing, filtering, stacking, and storing; and    (2) application of fertilizer comprising applying fertilizer in strawberry plant within 3-5 days during rainy days.
NOVELTY - A foliar fertilizer comprises 25-35 wt.% jasmine residue extract, 25-40 wt.% slag hops extract, 5-12 wt.% star anise extract, 2-5 wt.% monopotassium phosphate, 0.7-0.9 wt.% zinc chloride, 0.3-0.6 wt.% manganese(II) sulfate, 0.3-0.6 wt.% ferrous sulfate, 0.4-0.8 wt.% magnesium sulfate, 0.7-1 wt.% ammonium molybdate, and balance water.    USE - Foliar fertilizer used for tomato (claimed).    ADVANTAGE - The fertilizer is environment-friendly, has antibacterial effect, disease resistance and insecticidal effect, provides tomato nutrition component, does not contain any additive, and increases tomato yield and quality.    DETAILED DESCRIPTION - A foliar fertilizer comprises 25-35 wt.% jasmine residue extract, 25-40 wt.% slag hops extract, 5-12 wt.% star anise extract, 2-5 wt.% monopotassium phosphate, 0.7-0.9 wt.% zinc chloride, 0.3-0.6 wt.% manganese(II) sulfate, 0.3-0.6 wt.% ferrous sulfate, 0.4-0.8 wt.% magnesium sulfate, 0.7-1 wt.% ammonium molybdate, and balance water. The jasmine residue extract is prepared by crushing jasmine flower, adding 4-5 times water, 1-3 wt.% cellulose, 1-2 wt.% pectinase and 1-3 wt.% pepsin, soaking at 37-47 degrees C for 1-2 hours, heating to 75-85 degrees C, refluxing, extracting for 1-2 hours, and cooling. The slag hops extract is prepared by crushing hops slag, adding 3-4 times water, 1-2 wt.% cellulose, 1-2 wt.% pectinase and 1-2 wt.% pepsin, soaking at 37-46 degrees C for 1-2 hours, heating to 80-85 degrees C, refluxing, extracting for 1-2 hours, and cooling. The star anise extract is prepared by crushing star anise, adding 3-4 times 75-95 vol.% ethanol, 1-2 wt.% cellulase and 1-2 wt.% pectin, soaking at 45-55 degrees C for 1-2 hours, heating to 70-80 degrees C, refluxing, extracting for 1-2 hours, and cooling.
NOVELTY - A biological pesticide comprises 25-45 wt.% cedar castor cake, 5-10 wt.% cottonseed rice bran, 5-10 wt.% Humulus scandens, 10-20 wt.% Chinese medicine extraction residue, and 25-45 wt.% animal manure. The Chinese medicine extraction residue comprises radix isatidis, Salvia miltiorrhiza, and Astragalus membranaceus.    USE - Biological pesticide used for crop fertilizer.    ADVANTAGE - The biological pesticide has insecticidal and insect repellent effect and no residue at harvested crops, and can harvest crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of taking raw materials, stirring, mixing, putting into fermenting marsh gas tank, and fermenting at 18-45 degrees C for 3-15 days.
NOVELTY - A fertilizer comprises 60-100 pts. wt. plant straw, 30-50 pts. wt. green vegetable waste, 20-30 pts wt. animal excrement, 20-40 pts. wt. river sand, 30-50 pts. wt. quicklime, 10-20 pts. wt. blast furnace slag, 10-20 pts. wt. ferric hydroxide, 30-40 pts. wt. bone charcoal, 30-40 pts. wt. urea, 20-30 pts. wt. calcium superphosphate, and 20-30 pts. wt. potassium chloride.    USE - A fertilizer used for pomegranate (claimed).    ADVANTAGE - The fertilizer increases pomegranate yield, improves quality, and reduces heavy metal (e.g. lead, mercury, and chromium) residual amount, reducing environment pollution, and is inexpensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the fertilizer, comprising cutting plant straw into 2-4 cm length, covering container bottom with a layer of gauze, covering with a uniform thickness of 20-25 cm plant straw, spreading a river sand layer having a thickness of 3-6 cm, spreading a layer of green vegetable waste having a thickness of 15-20 cm, sprinkling quicklime having a thickness of 3-5 cm, and maintaining temperature at 30-35 degrees C; after 7-10 days, adding animal excrement, quicklime, blast furnace slag, iron hydroxide, and bone charcoal, covering with 15-20 cm plant straw, tightly wrapping with a thin film, fermenting, stacking at greater than or equal to 55 degrees C, maintaining for 18-25 days, and detaching film; adding urea, calcium superphosphate, and potassium chloride, uniform mixing, clearing impurities, filtering, and stack-storing; and    (2) applying 100-300 kg/mu fertilizer before and after flower budding; applying 300-500 kg/mu fertilizer during swelling; applying 300-500 kg/mu fertilizer during picking; and applying 50-100 kg/mu fertilizer during post-harvest.
NOVELTY - Grape organic eco-fertilizer comprises 71.9-92 pts. wt. inorganic fertilizer, 8-12 pts. wt. wine dregs, 1-4 pts. wt. antibiotic fertilizer, 1-4 pts. wt. water-retaining agent, 1-0.5 pts. wt. agricultural amino acid, 0.3-0.9 pt. wt. boric acid and 0.04-0.15 pt. wt. brassinolide.    USE - Grape organic eco-fertilizer.    ADVANTAGE - The grape organic eco-fertilizer increases yield, and increases growth rate to 31.34-42.54%.    DETAILED DESCRIPTION - Grape organic eco-fertilizer comprises 71.9-92 pts. wt. inorganic fertilizer, 8-12 pts. wt. wine dregs, 1-4 pts. wt. antibiotic fertilizer, 1-4 pts. wt. water-retaining agent, 1-0.5 pts. wt. agricultural amino acid, 0.3-0.9 pt. wt. boric acid and 0.04-0.15 pt. wt. brassinolide. The water-retaining agent is water absorbent resin, particularly low-crosslinked potassium polypropylene, crosslinked polyacrylamide, low-crosslinked sodium polyacrylate, polyvinyl alcohol, polyethylene oxide, hydrocarbons, carboxymethyl cellulose, hydroxypropyl cellulose, acidified xanthan fiber, carboxymethyl starch, starch xanthate, chitosan or alginic acid. An INDEPENDENT CLAIM is included for the preparation of grape organic eco-fertilizer comprising mixing wine dregs, adding water, fermenting for 130-150 days, drying to obtain less than 5% water content, passing over 5 mm mesh sieve, adding balance raw materials, crushing into 50 mm powder, mixing for 25-30 minutes, granulating, drying and cooling to room temperature.
NOVELTY - An electrolyte comprising solution of demineralized water (3), potassium carbonate and ascorbic acid (6) is electrolyzed, to obtain synthetic gas.    USE - Preparation of synthetic gas used as fuel for internal combustion engines (claimed).    ADVANTAGE - The method enables preparation of non-explosive and easily usable colorless and odorless synthetic gas having high calorific value.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of electrolytic system.    Carbon dioxide (2)    Demineralized water (3)    Ascorbic acid (6)
NOVELTY - Process for converting (100) hydrocarbon involves disproportionating a hydrocarbon feed (105) comprising 5C alkanes by contacting the hydrocarbon feed with a liquid catalyst in a reaction zone under disproportionation conditions to form a product mixture comprising 5 wt.% 4C alkane, and 5 wt.% 6C or more alkane in 30 minutes based on 5C alkanes in the hydrocarbon feed. The liquid catalyst comprises an unsupported ionic liquid and a carbocation promoter. The mass ratio of liquid catalyst and hydrocarbon feed is less than 0.75:1.    USE - Process for converting hydrocarbon (claimed).    ADVANTAGE - The method enables economical, quick and high conversion of hydrocarbon using reduced amount of ionic liquid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for disproportionation reaction mixture of hydrocarbon feed, which comprises 5C alkanes and the liquid catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining process for converting hydrocarbon.    Process for converting hydrocarbon (100)    Hydrocarbon feed (105)    Drying bed (110)    Reactor (115)    Regenerator (135)
NOVELTY - Hydrocarbon conversion process (P1) comprises isomerizing a hydrocarbon feed comprising normal 4C alkane or branched 4C alkane by contacting the hydrocarbon feed with a liquid catalyst in a reaction zone under isomerization conditions to form a product mixture having a ratio of branched 4C alkane to normal 4C alkane of at least 0.3:1 in 1 hour, where the liquid catalyst comprises an unsupported ionic liquid and a carbocation promoter, and a mass ratio of liquid catalyst to hydrocarbon feed is less than 0.75:1.    USE - The process is useful for converting hydrocarbon.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hydrocarbon conversion process (P2) comprising: isomerizing a hydrocarbon feed comprising normal 4C alkane by contacting the hydrocarbon feed with a liquid catalyst in a reaction zone under isomerization conditions to form a product mixture comprising at least 10 wt.% branched 4C alkanes in 1 hour based on the normal 4C alkane in the hydrocarbon feed, where the liquid catalyst comprises an unsupported ionic liquid and a carbocation promoter, where a mass ratio of liquid catalyst to hydrocarbon feed is less than 0.75:1.
NOVELTY - The method involves heating water of a hot water circuit by fluid coming from units placed upstream and/or downstream of fluidized-bed catalytic cracking (FCC) unit. The fluid is selected from overhead vapor of a fractionation column of a soft hydrocracking upstream unit of the FCC unit, vapors of head of stripor of the hydrocracking unit and effluent of a hydrodesulfurization (HDS) reactor (S) of a petrol hydro-treating unit when the hydro-treating unit is arranged downstream of the FCC unit after heat exchange with load of the reactor and load of a selective hydrogenation (SHU) reactor.    USE - Method for heating a reboiler of a propane/propylene column distillation system located downstream to a FCC unit.    ADVANTAGE - The method enables heating the water of the hot water circuit by fluid coming from the units placed upstream and/or downstream of FCC unit such that effective thermal integration is enabled, thus enabling economic separation of the propane and propylene by fractionation with the heat pump.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of a hot water circuit.    Propane/propylene separation columns (C-1-A, C-1-B)    Heat exchangers (E-1 - E-6)    HDS reactor (S)    Fluid flows (4a, 4b)    Propane flow (8)
NOVELTY - Method (M1) for producing methane from a halophyte substrate, comprises: providing a composition comprising the substrate in a saline medium; adding a culture comprising halophilic anaerobic archaea to the composition to digest the halophyte by anaerobic digestion; and then digesting the substrate with the culture to produce methane from it.    USE - The method is useful for producing methane from a halophyte substrate (claimed).    ADVANTAGE - The method produces methane that has less than 5 vol.%, preferably less than 1 vol.% of hydrogen sulfide (claimed) and has high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method (M2) for producing biofuels from a halophyte plant, comprising: growing the plant in a saline medium, where the plant comprises shoots, stems, roots and seeds; harvesting the seeds of the plant, where the harvesting is carried out by separating the seeds from the shoots, stems and roots, where the remaining shoots, stems and roots form a halophyte substrate; and then digesting the halophyte substrate to produce methane, where the methane is produced according to the method (M1).
NOVELTY - The apparatus (10) has a housing (12) for defining a pyrolysis chamber (14). The housing includes a solid waste inlet (16) for receiving solid or carbonaceous waste, a reagent inlet (18) for receiving chemical reagents and a gas outlet i.e. annular passage (54), in fluid flow communication with a gas-treatment apparatus. A gas conduit i.e. pipe, is placed in fluid flow communication with the gas treatment apparatus. Reagent inlets are connected to respective dosing devices (32) for regulating flow of the reagents from the dosing devices.    USE - Apparatus for treating solid or carbonaceous waste e.g. municipal waste, industrial waste, food waste, bio waste, wood waste, tire waste and medical waste (all claimed).    ADVANTAGE - The apparatus allows reagent stream to flow in a counter-current manner, so that high radial and axial gradients of static pressure can be created, thus facilitating lower emission rates to meet environmental standards, increasing efficiency of carburetion, combustion and clean-up of carbon monoxide and hydrocarbons and reducing nitrogen dioxide and carbon dioxide levels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating solid or carbonaceous waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of a waste treatment apparatus.    Apparatus for treating solid or carbonaceous waste (10)    Housing (12)    Pyrolysis chamber (14)    Solid waste inlet (16)    Reagent inlet (18)    Dosing devices (32)    Annular passage (54)
NOVELTY - Producing a fermentation product from readily fermentable sugar-material in a fermentation vat comprising a fermentation medium using a fermenting organism, comprises feeding the readily fermentable sugar material into the fermentation vat comprising a slurry of fermenting organism, and fermenting the readily fermentable sugar material into a desired fermentation product. A protease is added: before, during and/or after the feeding step; and/or during the fermentation step.    USE - The batch, fed batch, semi-continuous or continuous fermentation process is useful for producing a fermentation product such as ethanol, from a readily fermentable sugar-material (all claimed), where the ethanol is useful as a fuel for cars and as potable ethanol.    ADVANTAGE - The method is capable of reducing the foam generated by the fermenting organisms when producing the desired fermentation product from readily fermentable sugars using the protease, and producing the fermentation product with increased yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of a protease for reducing foam generated by fermenting organisms when producing a desired fermentation product from readily fermentable sugars.
NOVELTY - Use of glycerol or 3-5C sugar as a carbon source during culturing of Actinomycetes bacteria for the production of lipids by the bacteria, is claimed. The bacteria are cultured in a first medium enriched in phosphate and in a second medium containing low phosphate.    USE - The glycerol or 3-5C sugar (e.g. triose) is useful as a main carbon source during culturing of Actinomycetes bacteria (preferably Streptomyces) for the production of lipids by the bacteria, where the lipid is useful for: producing lubricants, surfactants, coatings, solvents, food ingredients and synthetic intermediates for oleochemicals (all claimed); producing biofuel; and production of methyl esters of vegetable oils.    ADVANTAGE - The glycerol or 3-5C sugar can economically produce biodegradable and non-toxic lipids with high yield and without using light and the production or accumulation of undesirable lipids.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a set of culture medium comprising glycerol or 3-5C sugar, comprising a first culture medium and a second culture medium;    (2) an assembly comprising first culture medium and a second culture medium each containing glycerol or 3-5C sugar, and at least one strain of Actinomycetes bacteria;    (3) producing lipids by Actinomycetes bacteria, comprising culturing bacterial in a first medium, and culturing the bacteria in a second medium;    (4) a lipid composition comprising lipid obtained by the method; and    (5) producing lubricants, surfactants, coatings, solvents, food ingredients and synthetic intermediates for oleochemicals, comprising culturing bacterial in a first medium, and culturing the bacteria in a second medium.
NOVELTY - A commodity is produced by using greater than or equal to 2 feedstock streams by processing feedstock stream into common intermediate and subsequently processing into final product.    USE - Production of commodity e.g. electrical energy, liquid fuel or liquefied fuel, methanol, dimethyl ether used for harvesting and transformation of oilseed biocrops, synthetic gasoline, diesel, kerosene, or jet fuel, or dimethyl ether fuel used as replacement for diesel-based prime movers and other machinery used in mining applications or used as replacement for carbonaceous soot, carbon monoxide sulfur, nitrogen oxide, and unreacted hydrocarbons (all claimed).    ADVANTAGE - The process enables safe and efficient dimethyl ether production.
NOVELTY - The method involves introducing calcium oxide, calcium sulfide and calcium carbonate containing thermal medium after absorption into a combustion tower (120). Decomposition-resistant hydrocarbon i.e. methane, in water, gasifying gas and off gas are made to react in presence of calcium oxide to decompose into carbon monoxide and hydrogen to set as synthesis gas. The off gas that does not become liquid fuel, while performing liquid fuel synthesis and heavy residue are returned to a fluidized-bed modification tower (130) or gasification tower (110).    USE - Gasification method for performing co-gasification of coal/biomass using an advanced three-tower type circulating fluidized bed in a gasification facility.    ADVANTAGE - The method enables performing liquid fuel synthesis such that the off gas and heavy hydrocarbon taking liquid fuel are introduced into the modification tower or gasification tower, so that the hydrocarbon components can be decomposed in the modification tower for synthesis of gas progress, thus re-absorbing the carbon dioxide with a low temperature sulfur absorber without generating hydrocarbons, and hence manufacturing high quality clean synthesis gas by simple scrubbing process by enabling a prolonged continuous operation, while achieving high efficient operation at low-cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an advanced three-tower type circulating fluidized bed gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a three-tower type circulating fluidized bed gasifier.'(Drawing includes non-English language text)'    Gasification tower (110)    Combustion tower (120)    Medium cyclone (125)    Fluidized-bed modification tower (130)    Liquid fuel synthesizer (160)
NOVELTY - Recovering ammonia gas comprises passing regenerated gas into ammonia washing tower, washing net ammonia, so that the ammonia content in regenerated gas is 5 wt.%; mixing the regenerated gas and ammonia with semi-water gas, adding into desulfurizing tower, and carrying out desulfurization; and discharging the semi-water gas into synthesis section.    USE - The method is useful for recovering ammonia gas (claimed).    ADVANTAGE - The method is economical, environmentally-friendly, and has low production cost.
NOVELTY - Preparing microwave plasma modified vanadium dioxide powder comprises adding M-type vanadium dioxide powder into the cavity of microwave plasma device, carrying out plasma surface modification, where the microwave plasma is methane and nitrogen gas, the flow ratio of mixed gas methane to nitrogen gas is 4-8:30-40, the microwave input power is controlled to 150-200 W, chamber pressure to 1.5-2 KPa, and the modifying time is 30-90 minutes.    USE - The method is useful for preparing microwave plasma modified vanadium dioxide powder (claimed).    ADVANTAGE - The modified vanadium dioxide powder has excellent thermochromic property, and can adjust the temperature according to the sunlight transmittance of smart glass.
NOVELTY - Preparing concentrated organic liquid fertilizer comprises: (i) cleaning vegetable peel, drying under sun and crushing via crusher; (ii) cleaning fruit peel, drying under cool place to obtain a mold, then crushing and mixing with vegetable peel powder; (iii) cleaning melons, drying to shrink, crushing and mixing with above mixture; (iv) mixing food residue and vegetable residue, mixing with above mixture; (v) placing the mixture in a container, adding 40-100 kg water, tightly closing, gently fermenting; and (vi) processing the fermentation broth to remove dregs, concentrating and filling.    USE - The method is useful for preparing concentrated organic liquid fertilizer (claimed).    DETAILED DESCRIPTION - Preparing concentrated organic liquid fertilizer comprises: (i) cleaning 30-40% vegetable peel, drying under sun for a day and crushing via crusher; (ii) cleaning 10-30% fruit peel, drying certain amount under cool place to obtain a mold, then crushing and mixing with vegetable peel powder; (iii) cleaning 5-15% melons, drying under natural sunlight for 2-3 days to shrink, crushing the melon and mixing with above mixture; (iv) mixing 5-15% of food residue and vegetable residue, then adding into above mixture and mixing; (v) placing the mixture in a container, adding 40-100 kg water, stirring, tightly closing the lid of the container, placing in a shady place and gently fermenting for 3 months; and (vi) collecting the fermentation broth, processing to remove dregs, concentrating the broth and filling.
NOVELTY - Organic fertilizer comprises 8% pine branches, 20% pine leaves, 5% citric acid residue, 5% fly ash, 5% oil soil slag, 3% shell powder, 5% sheep manure, 5% hot brick ash, 2% silkworm droppings, 10% cow dung, 12% biogas-liquid, 3% cottonseed meal, 3% kelp residue, 3% water, 10% nitrogenous fertilizer and 1% organic fertilizer fermenting agent.    USE - The fertilizer is useful for increasing rice yield (claimed); improving soil structure; promoting seedling on early-onset, and large root system.    ADVANTAGE - The fertilizer is economical; and facilitates deep rooting of rice, and rapid growth of rice.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising (i) preparing raw materials by crusher 8% pine branches and 20% pine leaves, to obtain raw material of 1.5 cm-long pieces; (ii) extracting citric acid residue, fly ash, oil soil slag, shell powder, sheep manure, hot brick ash, silkworm dropping, cow dung, biogas-liquid, cottonseed meal and kelp residue, and uniformly mixing; (iii) uniformly stirring 1% organic fertilizer and 3% fermentation agent with water, to obtain a fermentation broth; (iv) covering the field by paving a layer crushed pine leaves up to a thickness of 45 cm, sprinkling fermentation broth, then pouring a layer of biogas-liquid, and pouring a layer of mixed material of the step (ii), and spraying a fermentation broth, pouring a layer of biogas-liquid, and stacking by interleaving to a height of 2.5 m, covering tightly, and then allowing the leaves for 25 days, to obtain half composting material; (iv) uniformly overturning the semi-decomposed substance, and piling for 15 days, and packaging.
NOVELTY - Preparing bio-organic fertilizer using beer slag comprises drying beer slag and wood powder or mushroom residue powder mixed material, where the amount of wood powder or mushroom residue powder based on the beer slag volume is 50%, mixing at more than 105 degrees C, carrying out short time steam sterilization, reducing the temperature, inoculating Bacillus licheniformis and yeast, adding soluble sugar, aerobically fermenting, controlling the water content to be less than 45%, and drying until the material water content is less than 30%.    USE - The method is useful for preparing bio-organic fertilizer using beer slag (claimed).    ADVANTAGE - The method provides high quality fertilizer, which has high amount of nitrogen, multiple growth promoting substances, high decomposition degree, high probiotic content (2 hundred million/g) or more and has low bacteria content.    DETAILED DESCRIPTION - Preparing bio-organic fertilizer using beer slag comprises (a) drying beer slag until the water content is less than 50%, and wood powder or mushroom residue powder mixed material until the water content is less than 45%, where the amount of wood powder or mushroom residue powder based on the beer slag volume is 50%, (b) mixing at more than 105 degrees C, carrying out short time steam sterilization for 0.25-2 minutes, (c) reducing the temperature to 40 degrees C after sterilizing, inoculating Bacillus licheniformis and yeast, where the concentration of Bacillus licheniformis and yeast in the material is respectively not less than 50000000 cells/g and 5000000 cells/g, adding 5 Kg/per cubic material soluble sugar, and (d) aerobically fermenting at not greater than 60 degrees C, controlling the water content to be less than 45%, and drying until the material water content is less than 30%.
NOVELTY - Preparing selenium-enriched organic fertilizer comprises (i) crushing selenium ore and sieving with 80-200 meshes sieve, (ii) adding mineral powder into the compost, adding soluble sugar and mixing uniformly, (iii) adding Acetobacter, adjusting moisture content of compost to 60-75%, anaerobic fermenting and composting, (iv) adjusting compost carbon and nitrogen ratio to 20-30:1, (v) adding Bacillus licheniformis, adding urea, and aerobic fermenting, and (vi) adjusting compost temperature to less than 45 degrees C and moisture content to less than 40%, crude crushing and aging.    USE - The method is useful for preparing selenium-enriched organic fertilizer (claimed).    ADVANTAGE - The method reduces production cost, and is simple and ensures easy operation. The fertilizer realizes easy absorption of selenium.    DETAILED DESCRIPTION - Preparing selenium-enriched organic fertilizer comprises (i) crushing selenium ore in a large plant crusher, crushing using a crusher and sieving with 80-200 meshes sieve, where the selenium content is not less than 150 mg/kg, (ii) adding mineral powder into the compost, where the adding amount is 1-10 kg per ton of compost, adding soluble sugar accounting for 10-100 kg/ton of compost, and mixing uniformly, (iii) adding Acetobacter accounting for not less than 200000/g raw material, adjusting moisture content of compost to 60-75%, anaerobic fermenting and composting under pH of less than 5 for at least 15 days, (iv) adjusting compost carbon and nitrogen ratio to 20-30:1, (v) adding Bacillus licheniformis accounting for not less than 500000/g raw material, adding 1-25 kg urea per ton of compost, and aerobic fermenting at 55 degrees C for at least 7 days, and (vi) adjusting compost temperature to less than 45 degrees C and moisture content to less than 40%, crude crushing and aging for at least 20 days.
NOVELTY - Environmentally friendly wheat fertilizer comprises nitrogen-phosphorus-potassium (of ratio 12-18-5), greater than or equal to 10% organic substance, less than or equal to 5% humic acid, Azotobacter CCTCC M95040, potassium bacteria ACCC10013 and Bacillus megaterium ACCC10010 with total viable count of greater than or equal to 0.2 hundred million/g.    USE - Used as environmentally friendly wheat fertilizer.    ADVANTAGE - The fertilizer has good absorption rate, meets wheat production requirements, eliminates chemical pollution, and improves soil fertility.
NOVELTY - Preparing seafood mushroom nutrition base comprises setting temperature, humidity, component distribution ratio and technological process, where the component comprises straw, corn powder, quicklime, sawdust, crop straw, soybean powder and auxiliary material, the technique process is e.g. crushing crop straw and sawdust, entering into mixed agitator, adding water, carrying out stack fermentation, after fermentation of the material, second time stirring, and adding quicklime, adding corn powder, soybean powder and auxiliary material, stirring uniformly and sterilizing.    USE - The method is useful for preparing seafood mushroom nutrition base (claimed).    DETAILED DESCRIPTION - Preparing seafood mushroom nutrition base comprises setting temperature, humidity, component distribution ratio and technological process, where the temperature is 15-20 degrees C, humidity is 90-95%, the component comprises 40-50% straw, 2-6% corn powder, 5-15% quicklime, 15-25% sawdust, 16-20% crop straw, 14-25% soybean powder and 8-10% auxiliary material, the technique process is (i) crushing the straw to a length of 1-2 cm long fiber, crushing crop straw and sawdust, entering into mixed agitator, during mixing process, adding 80-90% water, (ii) carrying out stack fermentation for 10-15 days, (iii) after fermentation of the material, second time stirring, and adding 5-15% quicklime, at the same time, adding corn powder, soybean powder and auxiliary material, and stirring uniformly, (iv) from the discharging device, entering into a bag machine, placing in a boiler, and high temperature sterilizing, (v) base material of upper bag after sterilizing, placing in a cultivation room and sterilizing two times, and (vi) inoculating strains in base material containing bag, maintaining the indoor temperature at 15-20 degrees C, humidity at 90-95% to grow hairy fungus.
NOVELTY - Controlled-release biological fertilizer composition comprises 1-3 pts. wt. ammonium nitrate, 2-6 pts. wt. calcium nitrate, 1-3 pts. wt. potassium mineral powder, 7-13 pts. wt. stone powder, 25-35 pts. wt. carbon powder, 0.1-0.2 pts. wt. caterpillar fungus powder, 0.1-0.2 pts. wt. Japanese chafer Bacillus powder, 1-7 pts. wt. ammonium dihydrogen phosphate, 3-8 pts. wt. monocalcium phosphate, 4-8 pts. wt. monopotassium phosphate, 2-8 pts. wt. dipotassium hydrogen phosphate, 0.1-0.2 pts. wt. Aeromonas powder, 0.1-0.2 pts. wt and Candida powder.    USE - Controlled-release biological fertilizer composition.    ADVANTAGE - The controlled-release biological fertilizer composition has reduced water solubility for slow release of fertilizer in soil, and ensure reduced loss of nutritional element, and shows long-term fertilizing effect and stability.    DETAILED DESCRIPTION - Controlled-release biological fertilizer composition comprises 1-3 pts. wt. ammonium nitrate, 2-6 pts. wt. calcium nitrate, 1-3 pts. wt. potassium mineral powder, 7-13 pts. wt. stone powder, 25-35 pts. wt. carbon powder, 0.1-0.2 pts. wt. caterpillar fungus powder, 0.1-0.2 pts. wt. Japanese chafer Bacillus powder, 1-7 pts. wt. ammonium dihydrogen phosphate, 3-8 pts. wt. monocalcium phosphate, 4-8 pts. wt. monopotassium phosphate, 2-8 pts. wt. dipotassium hydrogen phosphate, 0.1-0.2 pts. wt. Aeromonas powder, 0.1-0.2 pts. wt. Candida powder , 0.1-0.2 pts. wt. Rhodococcus powder, 0.1-0.2 pts. wt. mushroom powder, 0.1-0.2 pts. wt. humic acid, 0.1-0.2 pts. wt. amino acid and 0.1-0.2 pts. wt. chitin.
NOVELTY - Preparing ecological organic fertilizer comprises (i) crushing green waste into less than 5 mm diameter wood fiber raw material, (ii) fermenting wood fiber raw material in a fermenting pool for 30-40 days, (iii) composting and aging the fermented raw material in a sunshine house and secondary heating, (iv) turning the raw material for once in every 10 days, where the total turning time is 3 times, and (v) ecological processing after 60-70 days.    USE - The method is useful for preparing ecological organic fertilizer (claimed).    ADVANTAGE - The fertilizer: does not contain weed seed, insect eggs and harmful chemical components; improves soil fertility, has drought resistance property and water retention capacity; improves plant growth conditions, increases beneficial microorganism content in soil, is good for root growing and plant nutrient absorption; and increases resistance to diseases.
NOVELTY - Fermenting organic fertilizer base material comprises adding 100 pts. wt. organic manure and 5-10 pts. wt. fermentation strain into a reaction container, uniformly mixing, stacking the mixture having a length of 3 m and a width of 1.5 m, fermenting the stacked mixture for 24 hours under aerobic conditions, maintaining the fermented mixture for 36 hours, accumulating the mixture, again maintaining the accumulated mixture for 48 hours, stacking the mixture, and maintaining for 72 hours.    USE - The method is useful for fermenting organic fertilizer base material (claimed).    ADVANTAGE - The method is capable of easily fermenting the organic fertilizer base material with increased viscoelasticity and compressive strength.
NOVELTY - Production of organic fertilizer involves preparing raw material utilizing 30-70 wt.% edible mushroom, 20-60 wt.% sheep manure, 5-30 wt.% soybean meal, 0-5 wt.% hoof horn powder, 0-5 wt.% ox hair powder, 3-10 wt.% bone powder, 0-0.5 wt.% microorganism and 0.1-1 wt.% fermentation promoting agent. All components are dried, crushed and sieved to obtain powder, and then fermentation promoting agent is sprayed on the powder and then mixed uniformly to obtain a mixture. The mixture is piled up to form a strip or trapezoid shaped product in bottom of a sealed plastic bag.    USE - Method for producing organic fertilizer (claimed) for increasing yield and quality of crop.    ADVANTAGE - The method is cost-effective, enables to produce organic fertilizer that improves structure of soil, suppresses soil-borne diseases, promotes degradation of pesticide, chemical residue and heavy metal pollutant, and has wide industrial applicability.    DETAILED DESCRIPTION - Production of organic fertilizer involves preparing raw material utilizing 30-70 wt.% edible mushroom, 20-60 wt.% sheep manure, 5-30 wt.% soybean meal, 0-5 wt.% hoof horn powder, 0-5 wt.% ox hair powder, 3-10 wt.% bone powder, 0-0.5 wt.% microorganism and 0.1-1 wt.% fermentation promoting agent. All components are dried, crushed and sieved to obtain powder, and then fermentation promoting agent is sprayed on the powder and then mixed uniformly to obtain a mixture. The mixture is piled up to form a strip or trapezoid shaped product in bottom of a sealed plastic bag. Fermentation is performed in the sealed plastic bag in presence of microorganism without supplying oxygen at 65 degrees C for 24 hours, and then at 55-65 degrees C for 9 days to obtain a fermented product. The fermented product is crushed and dried, and then 5 kg bentonite is added in 1 ton of fermented product. The fermented product and bentonite are dried and granulated, and then stored to obtain final product.
NOVELTY - The apparatus has a drive motor for rotating an agitating blade part that is connected to a suspension accommodating chamber to provide rotational centrifugal force to the suspension accommodating chamber. A vacuum chamber accommodates the suspension accommodating chamber and the agitating blade part. A heater heats a film. An inner side of the suspension accommodating chamber is provided with a planar part. A control unit controls rotate time and rotating speed of the drive motor, vacuum degree of the vacuum chamber and heating temperature and heating time of the heater.    USE - Apparatus for manufacturing a fuel anode of a solid oxide fuel cell (claimed).    ADVANTAGE - The apparatus effectively forms multiple air gaps with different amounts and sizes in the film. The apparatus installs the film to a fuel anode of a fuel cell, so that fuel cell efficiency can be improved. The apparatus forms large air gap in an outer portion of the fuel anode and a small air gap in an inner-side portion of the fuel anode so as to easily perform injection of hydrogen gas and improve reaction area of oxygen ion and reactivity of the oxygen ion.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for manufacturing a fuel anode of a solid oxide fuel cell    (2) a fuel anode of a solid oxide fuel cell    (3) a solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an apparatus for manufacturing a fuel anode of a fuel cell.'(Drawing includes non-English language text)'
NOVELTY - The system has a fermentation system in fluid communication with an evaporation system to receive treated liquid component, where the fermentation system comprises ethanologen to ferment sugars into ethanol. An ion exchange system comprises a resin bed that comprises resin i.e. ion exchange chromatography type resin, for binding multiple inhibitors e.g. furfural and hydroxymethylfurfural. The biomass comprises lignocellulosic material, where the lignocellulosic material is selected from one of corn cobs, corn plant husks, corn plant leaves and corn plant stalks.    USE - System for producing ethanol from pre-treated biomass e.g. lignocellulosic material such as corn cobs, corn plant husks, corn plant leaves and corn plant stalks (all claimed), during production of fermentation product i.e. beer, in a cellulosic ethanol production facility.    ADVANTAGE - The system can treat a component of lignocellulosic biomass that has been pre-treated and separated to remove inhibitors from the component prior to fermentation in order to facilitate pentose fermentation resulting in an efficient production of ethanol. The system provides multiple features to facilitate improvement in the efficiency and yield of cellulosic ethanol from biomass, and can reduce or manage formation of inhibitors by adjusting pre-treatment conditions such as pH, temperature and time. The system can concentrate the C5 sugars in the C5 stream to improve efficiency of fermentation in order to improve titer of ethanol for distillation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an apparatus for treating liquid component of pre-treated biomass.
NOVELTY - A porous film comprises a polylactic acid-type resin, and has a porosity of 1-80%. When the porous film is heated at 20 degrees C/minute, at least one melting peak is observed at 190-250 degrees C as measured using differential scanning calorimeter. The sum total of heat-absorption amount of melting peak at 190-250 degrees C is 3-20 J/g.    USE - Porous film is used for agricultural-and-forestry materials (e.g. mulch films and fumigation sheets), sanitary materials (e.g. moisture-permeable waterproof films of bed sheets, pillow cases, sanitary towels, and paper diapers), and industrial materials (e.g. packaging materials, bags used for foodstuffs, vegetables and fruits, garments, sheets used for cell culture, clothing used in rainy weather, gloves, garbage bags, compost bags, bags used for various industrial commodities, and separators).    ADVANTAGE - The porous film has excellent moisture permeability, flexibility, bleeding resistance, workability, water vapor transmission rate, handleability, and heat resistance.
NOVELTY - The production apparatus (10) has an electrolysis cell (14) which forms a cathode (12) in one side of a solid oxide electrolyte (11), and forms an anode (13) in other side of the solid oxide electrolyte. A fixing unit (15) fixes the end of the electrolysis cell, by which the fixed space is maintained from the other end of the electrolysis cell. An open end portion (17) forms a flow path (16) which guides the leakage of gas from the cathode side or the anode side to the opposite pole side.    USE - Hydrogen production apparatus.    ADVANTAGE - The open end portion is formed in a flow path which guides the leakage of gas from the cathode side or the anode side to the opposite pole side of the solid oxide electrolyte, such that the influence of gas leakage is minimized. The high soundness is achieved effectively by simplified structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the hydrogen production apparatus. (Drawing includes non-English language text)    Hydrogen production apparatus (10)    Solid oxide electrolyte (11)    Cathode (12)    Anode (13)    Electrolysis cell (14)    Fixing unit (15)    Flow path (16)    Open end portion (17)
NOVELTY - Conditioner comprises 5-15 wt.% of carbon source, 2-10 wt.% of nitrogen source, 0.5-3 wt.% of organic acid, 20-30 wt.% of a microbe culturing agent, and balance of water. The microbe culturing agent is made of a carrier. The carrier comprises 30-40 wt.% of calcium silicate, 50-68 wt.% of rice bran and 2-10 wt.% of dry distiller's grains with solubles.    USE - The conditioner is useful for improving soil for cultivation of crop (claimed) such as Chinese cabbage.    ADVANTAGE - The conditioner reduces salt content and damages of the soil, thus improving the productivity of the crops.
NOVELTY - This utility new type claims a fertilizer stacking one, belonging to fertilizer production machinery device field, this fertilizer stack turning machine comprising supporting frame, a rotating disk and turning device, this rotating disk comprising a disk and motor, supporting frame mutually between the connection is set with rotating shaft of a electric machine base, motor set with a motor base up, this turning device comprising a bracket, a rotary motor and turn pile head, wherein bottom edge of two end a rotating connection and two end support frame of bracket and support frame of the rotating connection and rotating connection of motor base and supporting frame are located on the same one straight line strip, and the other end and the electric machine base fixing connection, this end part is further set with a rotating rod, a rotating electrical machine set with 3 a, a bracket set with mounting plate, rotating electrical machine rotating shaft in centre position, and the base is set with a mounting plate a, turn stack head set with a rotating shaft of rotating electrical machine a can for fertilizer turning process.
NOVELTY - This utility new type belonging to the waste water treatment field, provide a one animal fermentation liquid production waste water processing device of liquid fertilizer, comprising a reactor main body, ammonia nitrogen gas-liquid absorption unit and the microalgae seed incubator air inlet unit, reactor main body set with a waste water inlet, and the bottom air inlet unit connecting the upper part and the micro-algae culture unit connecting the top outlet connecting pipe between the ammonia nitrogen gas-liquid absorption unit divided into liquid with converse suction protecting room and ammonia nitrogen-liquid absorbing room, protecting liquid reverse absorbing room and ammonia nitrogen-liquid absorbing room with a gas guide pipe connected. This new type utility claims device is one of a circulation, semi closed, a multistage circulation use and microalgae biomass production of b and c, a the liquid fertilizer production process in a produce of waste water high in ammonia nitrogen concentration, and the application b the production of microalgae and the microalgae pure culture, in a sewage standard discharge, protect environment of at the same time, realize the efficient recycling of sewage use.
NOVELTY - A one kitchen garbage aerobic fermentation device this utility new type claims a horizontal stir cavity by a semi cylindrical, a speed reducer, a stir shaft, agitator blade, stir blade, a support shell and a system compose. Stir cavity of inner mounting travel switch and a rotating shaft, a rotating shaft mounted with agitator blade, agitator blade mounted with stir blade, through two side travel switch of speed change rotating direction of the agitator blade to rotate back and forth in the cavity of inner semi cylindrical. A limiting amount of a material add a stir shaft lower boundary line, stir chamber of volume use rate is more than 90%. This utility new type device has simple structure, small occupied space is small, the cost is low, efficiency is high, the stir stir effect is good.
NOVELTY - This utility new type relates to a house, comprising one fan-ring shaped residential building main body, glass greenhouse and basement, fan-ring shaped residential building main body set with the glass greenhouse, fan-ring shaped residential building main body lower part set with a basement. This utility new type is beneficial effects as follows: 1, fan-ring shaped residential building main body due to external construction, capacity of the arc, anti-seismic ability is better than the traditional square building, residential use prolongs the service life. 2, the fan annular residential building main body set with a glass greenhouse roof, a fully use resource, increasing agricultural product, at the same time increase virescence coverage rate, reducing municipal heat island effect. 3, the storage space is also a basement for edible fungi planting and increase economic income. 4. The glass greenhouse edible fungi can arrange a large amount of personnel employment, which solves the problem of not trans employment. 5. Marsh gas pool can process domestic sewage, a people provide fuel, a glass greenhouse supply fertilizer.
NOVELTY - This utility new type relates to a one pig and pig field, comprising pig, clean system and sewage treatment system, ' farm comprising a pigsty, a fence, piggery transverse a direction into a plurality of pig, pig fence side is, the other side is wall; side per a pig column close to the inner wall is set with one discharging groove, the discharging groove is paved with a drain joint plate, a clean system including spray head, water pump and water storage tank; the sewage processing system comprising the compost pool, solid-liquid separating machine, UASB pool, a biochemical pool A/0, flocculating and precipitating pool, a steam-water separator, and the pneuma. This utility new type of live pig and the pig field outside further is equipped with a clean and sewage treatment system can conveniently realize daily clean and a dirt of inner pig of pig farm, is energy-saving, environment-friendly, green, clean and so on.
NOVELTY - The method involves placing one or more electrodes (107) against one surface of the diaphragm such that the opposing ends of electrode are at or beyond the perimeter edge of one surface of diaphragm. The other electrodes are placed against other surface of diaphragm such that opposing ends of other electrodes are at or beyond opposing perimeter edge of other surface of diaphragm. Each electrode is affixed at perimeter edge of diaphragm surface against which electrode is placed to make diaphragm electrode array (105) suitable for use in electrolyzer apparatus (117).    USE - Method for making diaphragm electrode array suitable for use in electrolysis apparatus used for electrolytic splitting of water into hydrogen gas and oxygen gas.    ADVANTAGE - Since separate streams of hydrogen and oxygen are produced in the cathode and anode compartments of the electrolyzer apparatus that is directed to flow in opposite directions and with subterranean placement of the gas flow streams, the potential hazards for producing and handling large quantities of combustible gases are minimized effectively. Hence, the maintenance is made simple and the downtime of the electrolyzer apparatus is reduced for reducing over potential, and increasing electrical energy conversion efficiency to hydrogen energy.    DESCRIPTION OF DRAWING(S) - The drawings show exploded and assembled views of the electrolyzer apparatus comprising continuous zone hemi-enclosures.    Hemi enclosure (101)    Second hemi enclosure (103)    Electrode array (105)    Electrodes (107)    Electrolyzer apparatus (117)
NOVELTY - A partially-oxidized syngas composition comprises 70 mol% hydrogen and carbon monoxide, 0.1-1 mol% ethane, 1-50 ppm (mol) acetylene, 10-100 ppm (mol) ethylene, 0.1-50 ppm (mol) hydrogen cyanide and 3-30 mol% carbon dioxide. The molar ratio of hydrogen and carbon monoxide is 0.4:1-1.5:1.    USE - Partially-oxidized syngas composition (claimed).    ADVANTAGE - The partially-oxidized syngas composition efficiently contributes to conservation of syngas values during cleanup operation. The conversion of biomass to oxygenated organic compound is economically carried out during syngas cleanup operation, by simple process.
NOVELTY - The apparatus (1) has an electrolysis cell stack apparatus (2) provided with an electrolysis cell stack for generating gas containing hydrogen from the gas containing water vapor. The fuel cell stack apparatus (3) is provided with a fuel cell stack (11) arranged with multiple fuel cells (10). The gas containing the hydrogen is generated with the electrolysis cell stack apparatus and supplied to the fuel cell stack apparatus. A vaporizer (16) is arranged for generating gas containing water vapor supplied to electrolysis cell stack apparatus positioned near the fuel cell stack.    USE - Hybrid apparatus used in hybrid system (claimed).    ADVANTAGE - The temperature distribution of fuel cell stack apparatus is improved, and generating efficiency of hybrid apparatus is improved. Hence, the reliability of the hybrid system is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hybrid system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hybrid apparatus.    Hybrid apparatus (1)    Electrolysis cell stack apparatus (2)    Fuel cell stack apparatus (3)    Fuel cell (10)    Fuel cell stack (11)    Vaporizer (16)
NOVELTY - Agent comprises aerobic and anaerobic sewage treatment agents. The aerobic treatment agent comprises 10-20 pts. wt. of sodium chloride, 15-30 pts. wt. polymerized aluminum chloride, 10-30 pts. wt. polyacrylamide, 5-10 pts. wt. bleaching agents, 5-10 pts. wt. biological enzyme, 5-15 pts. wt. nitrifying bacteria, 10-20 pts. wt. denitrifying bacteria, and 10-20 pts. wt. photosynthetic bacteria. The anaerobic treatment agent comprises sodium chloride, polymerized aluminum chloride, polyacrylamide, bleaching agents, glacial acetic acid, enzyme, yeast, and Bacillus bacteria.    USE - The agent is useful for treating beer industrial wastewater (claimed).    ADVANTAGE - The agent treats the beer industrial wastewater with good stability and synergistic effect in an economical manner.    DETAILED DESCRIPTION - Agent comprises aerobic and anaerobic treatment agents. The aerobic treatment agent comprises 10-20 pts. wt. of sodium chloride, 15-30 pts. wt. polymerized aluminum chloride, 10-30 pts. wt. polyacrylamide, 5-10 pts. wt. bleaching agents, 5-10 pts. wt. biological enzyme, 5-15 pts. wt. nitrifying bacteria, 10-20 pts. wt. denitrifying bacteria, and 10-20 pts. wt. photosynthetic bacteria. The anaerobic treatment agent comprises 10-20 pts. wt. sodium chloride, 15-30 pts. wt. polymerized aluminum chloride, 10-30 pts. wt. polyacrylamide, 5-10 pts. wt. bleaching agents, 5-15 pts. wt. glacial acetic acid, 5-20 pts. wt. enzyme, 10-20 pts. wt. yeast, and 10-20 pts. wt. Bacillus bacteria.
NOVELTY - Fertilizer comprises 3-8 pts. wt. royal jelly, 2.5-6 pts. wt. yeast, 3.5-7 pts. wt. gypsum, 3-5 pts. wt. humic acid, 5-9 pts. wt. ammonium nitrate, 3.2-5.8 pts. wt. sodium humate, 0.6-1.4 pts. wt. zinc sulfate, 2.4-5.2 pts. wt. potassium dihydrogen phosphate, 3-8 pts. wt. egg shell powder, 2.1-4.6 pts. wt. peat soil, 3.2-4.8 pts. wt. sawdust, 4.5-8 pts. wt. poultry manure, 2.3-3.5 pts. wt. Bacillus licheniformis and 0.3-0.9 pt. wt. lactic acid.    USE - Fertilizer.    ADVANTAGE - The fertilizer: provides plant with increased growth and development and nutrients needed for plants growth; improves the soil condition; and promotes rapid rooting.
NOVELTY - Aqueous polyurethane hydrophilic chain extender (I), is new.    USE - Aqueous polyurethane hydrophilic chain extender (I).    ADVANTAGE - (I) can be simply and easily prepared with reduced cost in an eco-friendly manner.    DETAILED DESCRIPTION - Aqueous polyurethane hydrophilic chain extender of formula (I), is new.    R1, R2 = hydrocarbyl.    An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - An aerosol comprises 0.05-1.2 pts. wt. flavor, 0.5-5 pts. wt. imidazoline amphoteric surfactant, 0.2-5 pts. wt. alkyl glycoside, 3-15 pts. wt. triethanolamine, 0.2-5 pts. wt. cocamidopropyl betaine (CAB-35), 0.5-2 pts. wt. sodium benzoate, 0.2-3 pts. wt. sodium nitrite, 280-330 pts. wt. deionized water and 15-30 pts. wt. propane and butane.    USE - Aerosol is used for cleaning heavy oil dirt in cooker hood, oven and other kitchen utensils.    ADVANTAGE - The aerosol has excellent heavy oil removal dirt efficiency and cleaning effect, without damaging the cleaning component surface.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of aerosol, which involves uniformly mixing flavor, imidazoline amphoteric surfactant, alkyl glycoside, triethanolamine, cocamidopropyl betaine, sodium benzoate, sodium nitrite, deionized water, and propane and butane.
NOVELTY - Bioreactor comprises a sealed vertical cylindrical tank mounted on the supports, the loading and unloading pipes, a pipe for removing biogas. The tank is provided with a bottom in the form of a truncated cone, covered with heating tape, the tank itself is also wrapped with heating tape and provided with a dome having the shape of a truncated cone facing with the smaller base upwards. Inside the tank the mixing device is mounted, which is a three-tiered paddle mixer made in the form of steel plates of rectangular cross section fixed crosswise on a vertical shaft (10), equipped immovably by fixed blades (11) in the form of flat steel plates of rectangular section, mounted parallel to the shaft. The upper paddles (7) of the mixer are mounted perpendicular to the shaft axis, each paddle is provided with a blade mounted perpendicularly on it, directed downwards, and the middle and lower paddles of the mixer repeat the shape of the tank bottom, the blades of which are attached to the paddles, and directed upwards. The middle paddles (8) of the mixer have one blade each, and the lower paddles (9) - three or more blades located with a gap over the entire surface of the paddle.    USE - Agriculture.    ADVANTAGE - Increased productivity of the bioreactor and increase in the yield of biogas.3 dwg
NOVELTY - Method for processing pure straw anaerobically with zero-emission of biogas, involves (a) pre-treating raw straw, (b) regulating carbon/nitrogen ratio in pretreated straw by feeding carbon and nitrogen source, (c) fermenting residue obtained from pretreated straw and isolating biogas, (d) aerobically nitrifying biogas and removing chemical oxygen demand (COD), and (e) obtaining 100 % biogas from straw feed and continuing anaerobic pretreatment, and denitrifying biogas for 1-5 times.    USE - The method is useful for processing pure straw anaerobically with zero-emission of biogas (claimed).    ADVANTAGE - The method saves energy and resource, specifically water and is cost-effective and performed for long period of time.
NOVELTY - Chicken manure and peat, taken in the ratio of 50:50, are shredded to particle-size composition of less than 10 mm. The shredded components are stirred and alkalified with 0.5% aqueous solution of potassium hydroxide in an amount of 1.5 l per 1 kg of the mixture at 20-22 degrees C for 24 hours. Wheat bran is added into the resulting primary biofertiliser in an amount of 3 wt % and stirred. The first stage of the mixture bioconversion is carried out at 36-39 degrees C for 96 hours. Then the second stage of bioconversion is carried out at 55-60 degrees C for 24 hours. At that every 24 hours the mixture is purged with air in the longitudinal and transverse directions for 30 minutes.    USE - Agriculture.    ADVANTAGE - Increased efficiency of application by improving the survival of microorganisms, increase in biological activity of the soil, and improvement of consumer properties of the biofertiliser obtained.2 cl, 2 dwg, 3 tbl, 2 ex
NOVELTY - Biological process of Sarcophaga peregrina fly larvae is carried out by crushing unsuitable fresh tobacco leaves into granules with grain diameter of 2-3 cm to prepare into culture material; putting Sarcophaga peregrina fly larvae in the culture material and allowing to hatch for biological conversion process of unsuitable fresh tobacco leaves into biological organic fertilizer; and aging fly maggot to obtain biological protein. The culture material comprises 60-85% unsuitable fresh tobacco leaves, 0-25% bran, 5% bran powder, 5% sawdust, and 5% fish meal.    USE - Method for biological process of Sarcophaga peregrina larvae (claimed).    ADVANTAGE - The method requires less operation space, has reduced cost on crushing of tobacco leaves and low energy consumption, and can produce biological protein and high-quality biological organic fertilizer.
NOVELTY - Biological process of green bottle fly larva is carried out by crushing unsuitable fresh tobacco leaves into granules with grain diameter of 2-3 cm to prepare into culture material; putting green bottle fly larva in the culture material and allowing to hatch for biological conversion process of unsuitable fresh tobacco leaves into biological organic fertilizer; and aging green bottle fly maggot to obtain biological protein. The culture material comprises 60-85% unsuitable fresh tobacco leaves, 0-25% bran, 5% bran powder, 5% sawdust, and 5% fish meal.    USE - Method for biological process of green bottle fly larva (claimed).    ADVANTAGE - The method requires less operation area, has reduced cost on crushing of tobacco leaves and low energy consumption, and can produce biological protein and high-quality biological organic fertilizer.
NOVELTY - An ornithine conversion liquid obtained during enzymatic conversion of arginine to ornithine is filtered using nanofiltration membrane (a) having molecular weight cutoff of 300-1000 Da, to obtain filtrate. The filtrate is further filtered using nanofiltration membrane (b) having molecular weight cutoff of 50-100 Da, to obtain ornithine-containing filtrate. Then, acid and active carbon for decolorizing are added to filtrate and crystallized salt, to obtain ornithine hydrochloride.    USE - Preparation of ornithine hydrochloride from ornithine conversion liquid obtained during enzymatic conversion of arginine to ornithine, used for preparing urea used as fertilizer.    ADVANTAGE - The method safely and reliably provides ornithine hydrochloride without using ethanol.
NOVELTY - Fractionating a lignocellulosic biomass, comprises subjecting the lignocellulosic biomass to an organosolv step, and treating the biomass with a treatment liquid at a temperature of 100-160 degrees C. The treatment liquid comprises 20-70 wt.% of non-hydroxylic organic solvent comprising an ether and/or a carbonyl moiety, 20-80 wt.% of water, and 0.5-100 g of acid per kg biomass.    USE - The method is useful for fractionating a lignocellulosic biomass (including herbaceous biomass and/or softwood or hardwood) (all claimed), where the biomass is useful for the production of biofuels, chemicals, performance products and energy.    ADVANTAGE - The method ensures efficient and economical fractionation of the lignocellulosic biomass thus increasing delignification of the biomass without side-reactions, preferably reducing hemicelluloses degradation, improving cellulose hydrolysis and increasing the nativity of the obtained lignin.
NOVELTY - The aerator has a mixing unit (92) that is installed in front of casing. The discharge hole of mixing unit is formed in radial direction. An impeller (93) is installed inside mixing unit and fastened to driving shaft (9135) to generate flow in radial direction of mixing unit. Intake holes (941) are formed in housing. An auxiliary intake unit (96) is extended forwards from impeller to be inserted into extension tube unit. The auxiliary intake unit is rotated together with impeller for providing fluid inside air inflow unit with intake force.    USE - Aerator.    ADVANTAGE - The air intake force is doubled, so the aeration is efficiently improved even at deep level. The wastewater treatment efficiency is improved by the aerator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the aerator.    Mixing unit (92)    Impeller (93)    Auxiliary intake unit (96)    Intake holes (941)    Driving shaft (9135)
NOVELTY - Culture material and its preparation are claimed. The culture material comprises 10-20 wt.% sawdust, 5-40 wt.% rice bran, 12-27 wt.% sugarcane bagasse, 16-30 wt.% wheat bran, 3-8 wt.% corn powder and 1-5 wt.% calcium carbonate. Method for preparation of the material, involves (a) weighing the above-mentioned raw materials, mixing weighed raw materials, drying mixed material, and crushing dried material and stirring uniformly for 5 minutes, and (b) adjusting water content of crushed material to obtain mixed culture material.    USE - The culture material is useful for cultivating Agrocybe aegerita (claimed).    ADVANTAGE - The culture material increases nutritional value and yield of A.aegerita and is cost-effective.    DETAILED DESCRIPTION - Culture material and its preparation are claimed. The culture material comprises 10-20 wt.% sawdust, 5-40 wt.% rice bran, 12-27 wt.% sugarcane bagasse, 16-30 wt.% wheat bran, 3-8 wt.% corn powder and 1-5 wt.% calcium carbonate. Method for preparation of the material, involves (a) weighing the above-mentioned raw materials, mixing weighed raw materials, drying mixed material, and crushing dried material and stirring uniformly for 5 minutes, and (b) adjusting water content of crushed material to obtain mixed culture material, until the water content reaches 65 plus minus 1%, where the pH is 4-5. An INDEPENDENT CLAIM is included for method of using the above-mentioned culture material, which involves obtaining polypropylene bags, bagging mixture into bag within 1 hour of pre-wetting the culture material, stamping bag, where each bag contains 1300-1400 g culture material, and the space left above culture material in pack is 18 cm, making hole, and tying collar of bag tightly to plug bag.
NOVELTY - Wastewater treatment system comprises cesspit (1), pressure filter (2), fermentation tank (3), sedimentation tank (4), filter tank (5), sterilizing tank (6), and water tower (7).    USE - The wastewater treatment system is useful for processing wastewater to produce recycled water used as water for flush toilet and watering plants and trees, and organic fertilizer.    ADVANTAGE - The system processes wastewater simply, and increases use rate of wastewater.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of wastewater treatment system.    Cesspit (1)    Pressure filter (2)    Fermentation tank (3)    Sedimentation tank (4)    Filter tank (5)    Sterilizing tank (6)    Water tower (7)
NOVELTY - Bromfenac sodium preparation involves reacting 7-(4-bromobenzyl)-1H-indole with an electrophilic substitution reagent in N,N-dimethylformamide or dimethyl sulfoxide to give bromobenzyl derivative (I). The obtained bromobenzyl derivative is treated with 2-methoxyethanol in presence of phosphoric acid to give 7-(4-bromobenzyl)-2,3-dihydro-1H-indol-2-one. The obtained 7-(4-bromobenzyl)-2,3-dihydro-1H-indol-2-one is hydrolyzed with sodium hydroxide and methylene chloride to give 2-amino-2-(3-(4-bromobenzyl)phenyl)acetic acid.    USE - Method for preparing bromfenac sodium (claimed).    ADVANTAGE - The method prepares bromine diclofenac sodium reaction in a simple and eco-friendly manner with high yield and product quality.    DETAILED DESCRIPTION - Bromfenac sodium preparation involves reacting 7-(4-bromobenzyl)-1H-indole with an electrophilic substitution reagent in N,N-dimethylformamide or dimethyl sulfoxide to give bromobenzyl derivative of formula (I). The obtained bromobenzyl derivative is treated with 2-methoxyethanol in presence of phosphoric acid to give 7-(4-bromobenzyl)-2,3-dihydro-1H-indol-2-one. The obtained 7-(4-bromobenzyl)-2,3-dihydro-1H-indol-2-one is hydrolyzed with sodium hydroxide and methylene chloride to give 2-amino-2-(3-(4-bromobenzyl)phenyl)acetic acid. The obtained2-amino-2-(3-(4-bromobenzyl)phenyl)acetic acid is added in an organic alcohol solvent and sodium hydroxide salt solution, and then cooled to crystallize to give bromine diclofenac sodium.    X=Br or Cl.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting high-performance liquid chromatographic diagram of bromine diclofenac sodium preparartion. (Drawing includes non-English language text).ReagentPHOSPHORIC-ACID (DCR#000063)METHYLENE-CHLORIDE (DCR#000027)N-BROMOSUCCINIMIDE (DCR#000224)SUCCINCHLORIMIDE (DCR#000199)SODIUM HYDROXIDE (DCR#000002)ProducedBROMFENAC SODIUM (DCR#139464)
NOVELTY - The device has a SBR reaction unit (12) is fixed with a magnetic force rotor stirrer (6). An inner part of a rotor (7) is fixed with an active sludge reactor. The SBR reaction unit is connected with an aeration unit (3) and a sampling unit (4). The aeration unit is fixed with a pneumatic pump through silicon glue tube. An adhesive sand block (8) is located in the SBR reaction unit that is mounted with an overflow pipe (13). A pH value probe (10) is connected with the SBR reaction device through a reserved hole.    USE - Rapid aerobic starvation municipal sewage short-range nitration test device.    ADVANTAGE - The device ensures aerobic starvation nitrite-oxidizing environment different starvation sensitivity and reduces aeration time, and has stronger starvation maintaining ability, better growing environment, simple operation, low investment cost and high stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rapid aerobic starvation municipal sewage short-range nitration test method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a rapid aerobic starvation municipal sewage short-range nitration test device.    Aeration unit (3)    Sampling unit (4)    Magnetic force rotor stirrer (6)    Rotor (7)    Adhesive sand block (8)    PH value probe (10)    SBR reaction unit (12)    Overflow pipe (13)
NOVELTY - An epidemic disease preventing method involves cleaning and forming a male group and a female group. House and sheep manure cleaning process is performed. Pathogenic bacteria and parasite in excrement are killed. Pathogen killing process is performed. Aluminum hydroxide injecting process is performed. Carbon spore seedling process is performed. Multi-shuttle dry powder injecting process is performed. Swine and Brucella abortus freezing is performed, followed by performing comprehensive preventing process periodically, cleaning medicated bath with dipterex solution.    USE - Method for preventing epidemic disease in sheep.    ADVANTAGE - The method enables preventing epidemic disease with improved prevention effect, and valid control of important disease.    DETAILED DESCRIPTION - An epidemic disease preventing method involves managing the sheeps by improving sanitation, feeding male and female cluster, separating according to species, age, breeding purposes, physical strength and weakness, performing cleaning, stacking, and fermentation for killing fecal pathogens and parasites or eggs, disinfecting sheeps by preventing brucellosis, sheep pox, sheep scabies, bluetongue, and tuberculosis, eliminating the sheep suffering from disease, and taking important measures for preventing epidemic diseases. Aluminum hydroxide injecting process is performed for 4 months. Goat epidemic pleuropneumonia aluminum hydroxide injection process is performed for 5 month. Carbon spore seedling process is performed for 3-9 months. Multi-shuttle dry powder injecting process is performed for 3 months. Swine and Brucella abortus freezing and drying process is performed. Lamb aluminum hydroxide is produced for 20-30 days during seedling time according to s local parasitic popular rule, followed by performing comprehensive preventing process periodically, cleaning medicated bath with dipterex solution.
NOVELTY - 3-((S)-1-methylamino-ethyl)-phenol (I), is new.    USE - (I) is useful as an intermediate for synthesis of rivastigmine (claimed).    ADVANTAGE - (I) can be prepared with high production rate and yield in an eco-friendly and cost-effective manner.    DETAILED DESCRIPTION - 3-((S)-1-methylamino-ethyl)-phenol of formula (I), is new. An INDEPENDENT CLAIM is included for preparation of (I).
NOVELTY - The system has an ecological base whose bottom is provided with water pipeline (2) that is vertically connected with an exit of a releasing device (3). The ecological base is provided with a sewage body along a flow direction. The sewage body is fixed with an oxygen source unit (1). An end of the water pipeline is connected with the of sewage body along the flow direction. An end of the oxygen source unit is connected with an air outlet. Another end of the oxygen tube is connected the releasing device. A total oxygen supply tube (4) is connected with a branch oxygen supply tube (5).    USE - Town sewage treatment plant tail water purification system.    ADVANTAGE - The ecological base supplies fresh water body and a nutrient so as to improve growth of a micro-organism. The system provides better treatment effect for organic matter in polluted water body, thus reducing organic matter content in waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a town sewage treatment plant tail water purification system.    Oxygen source unit (1)    Water pipeline (2)    Releasing device (3)    Total oxygen supply tube (4)    Branch oxygen supply tube (5)
NOVELTY - A fotemustine is prepared by performing amination of 1-aminoethyl phosphoric acid diethyl ester and carmustine in reaction medium, obtaining organic compound, and performing nitrosation of organic compound in which reaction medium is water.    USE - Preparation of fotemustine (claimed).    ADVANTAGE - Preparation process has high product purity and yield and is environment-friendly.    DETAILED DESCRIPTION - A fotemustine is prepared by performing amination of 1-aminoethyl phosphoric acid diethyl ester and carmustine in reaction medium to obtain (1-(3-(2-chloro-ethyl)-ureido)-ethyl)-phosphonic acid diethyl ester, and performing nitrosation of the obtained compound, in which reaction medium is water.
NOVELTY - This utility new type provide a one porous ceramsite biological filter tank. Water leakage grid plate separation set with filter cavity of biological filtering chamber and the lower layer to the upper layer of the water in tank body, the top part of said biological filter chamber is set with water inlet, inner cavity is set with multi-hole porcelain granule biological filter layer, a porous ceramsite filter layer by a suspension in water in a, c macro-pore structure of multi-hole porcelain granule distribute, set with a water outlet and a sludge collecting filter cavity in. Using porous ceramsite filter layer filter, intercepting suspended substance and as a microorganism growth carrier, realize the effect of a physical filter and biological filter. And a suspension on the multi-hole porcelain granule in water, impurity of the table layer absorbing the water in a separate precipitation, filter layer and is easy to clean. With the traditional technology, it has environment-friendly, efficient, small floor area, large load and so on.
NOVELTY - This utility new type claims a one operation is simple, the floor space is small, the process of ship sewage treatment device of sewage inner ship, comprise by glass steel of inner embedded steel framework is made of a box, through support leg of the bottom fixed on the ship floor up, a top end of tank opening, the upper part of a box set with one inclined a filter network, one set with filter screen along the inclined direction of a sliding plate on the upper part of filter screen, in turn set with plant zeolite processing area, biological enzyme treatment area and settling zone at the lower part of filter screen, with bottom set with a spiral groove on the inner wall of a precipitation zone, the upper part of settling zone set with the water tube, the bottom of settling zone set with pipe. This utility new type processing process is simple, operation management maintenance is convenient.
NOVELTY - Wastewater treatment cabinet comprises a cabinet body that is set with a three phase separator, where the three phase separator of the cabinet body is divided into the lower area and the upper area of sludge precipitation zone. The top side of cabinet body is set with a marsh gas discharging pipe. The upper area of sludge precipitation zone is set with a water tube. A sludge settling zone is set with a water inlet tube.    USE - Wastewater treatment cabinet.    ADVANTAGE - The wastewater treatment cabinet enables to treat wastewater in an efficient manner.
NOVELTY - The device has an artificial marsh tank (1) that is provided with five layers such as gravel layer, an aerobic microbe layer, a coal slag layer, an immobilized microorganism anaerobic layer and residue layer. The aerobic microbe layer is mounted with an aeration pipe (10-a) and an aeration branch tube (13-a). The aeration pipe is mounted with a gas valve (11-a) and a gas flow meter (12-a). A water outlet unit is connected with the artificial marsh tank. A side wall and bottom of the artificial marsh tank are provided with a barrier layer.    USE - Immobilized microorganism aerobic and anaerobic sewage treatment device.    ADVANTAGE - The immobilized microorganism aerobic and anaerobic treatment are performed to artificial wetland. The effect of microorganism is improved.    DETAILED DESCRIPTION - The gravel layer is provided with a water inlet pipe (10-b) and a cloth water branch tube (13b). The water inlet tube is mounted with a liquid valve door (11-b) and a liquid flow meter (12-b). The immobilized microorganism anaerobic layer is mounted with an immobilized microorganism component (5) mounting with an immobilized microorganism plate (6).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the immobilized microorganism aerobic and anaerobic sewage treatment device.    Artificial marsh tank (1)    Immobilized microorganism component (5)    Immobilized microorganism plate (6)    Aeration pipe (10-a)    Water inlet pipe (10-b)    Gas valve (11-a)    Liquid valve door (11-b)    Gas flow meter (12-a)    Liquid flow meter (12-b)    Aeration branch tube (13-a)    Cloth water branch tube (13b)
NOVELTY - Treating pig farm manure comprises preparing organic fertilizer by adding pig (or other animal manure) and crushed crop waste into fast processing tank, controlling the humidity at 50-60%, adding ferment bacteria to optimise C:N ratio, heating, mixing, then activating ferment bacteria, circulating oxygen, allowing to fully reproduce and ferment, after 8 hours, carrying out aerobic fermentation at 80-120 degrees C for 24 hours in the fermentation tank.    USE - The method is useful for treating pig farm manure (claimed).
NOVELTY - A special fertilizer for walnut comprises: 6-10 pts. wt. urea, 8-12 pts. wt. diammonium phosphate, 12-16 pts. wt. potassium sulfate, 32.3-36.3 pts. wt. acidified bone powder, 28-32 pts. wt. manure and furfural residue, 7.1-7.3 pts. wt. trace element, and 1.4-1.8 pts. wt. micronutrient element.    USE - As special fertilizer for walnut (claimed).    ADVANTAGE - The present fertilizer greatly increases whole crop yield and quality of Chinese walnut, increases disease resistance of crop, prolongs the fertilizer release cycle, reduces fertilizer loss, enhances stress resistance of crops, provides large amount of organic substances to soil, and gradually improves environment of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of fertilizer involving mixing urea, diammonium phosphate, potassium sulfate, trace element, and fermenting agent, crushing into 30-40 meshes, then adding acidified bone powder and manure and furfural residue, and extruding and granulating in a traditional way to obtain the fertilizer.
NOVELTY - This utility new type provide the one a terrestrial heat self heating horizontal undercurrent aritificial wetland sewage treatment system, heat preservation in wetland bed distribute with at least two group circulating geothermal heating module, heat preservation wetland bed two side connecting a buried insulating porous cloth water component and multi-hole water outlet component, heat preservation wetland bed and four wall paved heat insulating plate, a heat insulation heat preservation stone at the bottom of wetland bed arranged filler in filler is planted with wetland plant cold-resistant. The condition of rich geothermal resource, little high grade energy consumption of low, the low grade heat energy extraction aritificial wetland bed to maintain a higher temperature, it has a good heat preservation effect in winter, to increase matrix microorganism and plant physiological activity of the sewage purification effect aritificial wetland lower increase in winter of cold state. Structure is simple, it does not need complex management and nursing staff, and the maintenance cost is low, a widely used in winter in cold area domestic sewage and cultivation waste water, polluted water body of purification treatment, it has a wide development prospect.
NOVELTY - This utility new type provide a one for removing heavy metal in a sewage treatment device, comprise one tank body, a tank body with a water inlet connecting tube, a tank body upper end connecting with the water tube, a tank body by lower bottom in turn set with sand primary filter layer, microorganism absorbing layer, filter cloth and a active carbon absorbing layer, said microorganism absorbing layer set with surface attached with microbe of sphere. This utility new type has following beneficial effects: this utility new type overcomes the disadvantages of the traditional metal ion removing method exist high cost, complex operation, difficult process for a low concentration waste water and so on, by using microorganism treatment way using multi-grade filter and of absorbing method, the process water can reach the recycling standard, at the same time for a potential heavy metal resource recovery process.
NOVELTY - This new type utility claims one a low dissolved oxygen magnetic biochemical treatment system, in turn comprise of a lean oxygen pool, oxygen-enriched pool and sedimentation tank, a sedimentation tank is divided into inner separate area and slurry area, said area connecting the water tube, a lean oxygen pool a water inlet tube, a rich oxygen pool bottom part set with an aeration device, the aeration device fan further comprise drums separator, entrance of the magnetic drum separator through surplus sludge tube connecting to a separate water area bottom exit through a magnetic return tube connecting to said oxygen-poor pool, inner reflux pump, the inner reflux pump entrance of a oxygen-enriched pool, a lean oxygen pool exit. This utility new type practical based on a primary biochemical process system a mix the magnetic carrier, magnetic separate and low dissolved oxygen nitration advanced technology, increase effect of removing nitrogen and phosphorus in waste water at the same time, increase of the water quality of the waste water.
NOVELTY - Method for preparing lignocellulosic bioethanol involves collecting wastewater generated during preparation of torrefied pellet, after torrefaction of lignocellulosic biomass, and fermenting with yeast at 25-32 degrees C to obtain the product.    USE - The method is useful for preparing lignocellulosic bioethanol (claimed).    ADVANTAGE - The preparation method is sustainable and suitable for large-scale production of lignocellulosic bioethanol.
NOVELTY - System for preparing a fuel from biomass and petroleum fraction, comprises pyrolysis system for producing a renewable fuel oil from the biomass, a refinery system comprising a conversion unit to co-process the renewable fuel oil and the petroleum fraction as reactants in the presence of a catalyst, delivery system to deliver the renewable fuel oil to an injection point of the conversion unit, and a control system to control the delivery of renewable fuel oil to the refinery system.    USE - The system is useful for preparing a fuel from biomass and petroleum fraction (claimed). The system includes refinery fluid catalytic cracker unit, coker, field upgrader system, hydrocracker, and/or hydrotreating unit.    ADVANTAGE - The system enables to prepare fuel with high yield.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of fluid catalytic cracker unit.    Renewable oil (101)
NOVELTY - Use of Candida santamaria (CGMCC 2959) and Trichosporon akiyoshidainum (CGMCC 3150) is claimed, in treatment of organic wastewater residues.    USE - The C.santamaria and T.akiyoshidainum are useful for treating organic wastewater residues (claimed).    ADVANTAGE - The C.santamaria and T.akiyoshidainum exhibits increased resistance with respect to low temperature and high salt conditions.
NOVELTY - Extracting m-cresol from p-cresol mixture involves taking 50-90% m-cresol content, 10-50% p-cresol of cresol mixture and urea into reaction kettle, urea and cresol mixture middle of mol ratio is 1-1.30:1, stirring at 85-110 degrees C, forming transparent penetrate, cooling transparent solution at 20-25 degrees C, maintaining temperature, stirring for 2 hours, separating out solid to obtain filter cake, adding solvent to filter cake, mixing at 20-25 degrees C, stirring and washing, filtering, washing filter cake multi-time repeatedly, separating oil phase solution, decompressing and rectifying.    USE - For extracting m-cresol from p-cresol mixture (claimed).    ADVANTAGE - The method is cheap and easily obtained raw materials, low cost, obtains m-cresol content is more than 99.8%, it can satisfy drug level vitamin E production of standard. Extraction rate of the method is more than 60%, the solvent has low toxicity, and can be a repeated use, a waste liquid and zero emission, reduces the pollution for environment.    DETAILED DESCRIPTION - Extracting m-cresol from p-cresol mixture involves a) taking 50-90% m-cresol content, 10-50% p-cresol of cresol mixture and urea into reaction kettle, urea and cresol mixture middle of mol ratio is 1 to 1.30:1, stirring at 85-110 degrees C, forming transparent penetrate, b) cooling the transparent solution at 20-25 degrees C, maintaining the temperature and stirring for 2 hours, separating out a solid, to obtain filter cake, adding solvent to filter cake, mixing at 20-25 degrees C, stirring and washing, filtering, washing filter cake multi-time repeatedly until a filter cake to obtain middle methyl phenol content is not greater than 99.8%, a mix solvent is selected from 2-4C alcohol, and tetrahydrofuran, 1,4-dioxane, or benzene; adding filter cake in water, at 20-25 degrees C to stir for 1-4 hours, standing and layering, separating oil phase solution, decompressing and rectifying to obtain more than 99.8% of mcresol.
NOVELTY - The system (100) has a power source that is electrically coupled to cathode and anode. A pump (106) is fluidly coupled with reservoir and electrolysis chamber and is configured to pump electrolysis fluid through reservoir. A first electrolysis product is pumped into cathode fluid pathway and into first electrolysis product gas collector through cathode apertures where electrolysis occurs. A second electrolysis product is pumped into anode fluid pathway and into second electrolysis product gas collector through anode apertures where electrolysis occurs.    USE - Electrolysis system for use in water electrolysis, for producing gaseous products from liquid reaction materials.    ADVANTAGE - By reducing and avoiding these major sources of resistance, efficiency of the resulting system is significantly increased. By eliminating the need for a membrane, the distance between the electrodes are reduced as compared to requirements where a membrane is present, which further reduces the total resistance by reducing the resistance associated with the electrolyte path. The variability of wind limits wind power to no more than about 15% of the generation mix in order to ensure grid stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis system.    Electrolysis system (100)    Inlet (104)    Pump (106)    Polar plate (108)    Separator (112a)
NOVELTY - Plant growth regulator composition obtained by crushing wood waste to a predetermined size to form sawdust, adding soil, rice husk, rice straw, barley straw and native grass to sawdust, fermenting at a constant temperature, and softening sawdust compost by spraying microbial agent, is claimed.    USE - Used as plant growth regulator composition.    ADVANTAGE - The plant growth regulator composition can be easily produced, stored and transported, is environmentally friendly, and is safe and economical.
NOVELTY - The system has a driver device (220) e.g. step motor, for driving a movable electrical contact bridge (108) along a conductive track (110). A measuring device measures an electrical output of a power source. A controller determines a number of electrolysis cells (202-210) to be operated based on the measured electrical output of the power source to cause movement of the driver device to drive the contact bridge to a point accordance with the determined number of cells to form an electrical circuit including the determined number of electrolysis cells in series with the power source.    USE - Hydrogen generation system for generating clean hydrogen by electrolysis of water from a volatile power source e.g. solar and wind power sources, in stationary and mobile applications.    ADVANTAGE - The system can efficiently increase and decrease capacity of an electrolysis stack, and can be operated at desired efficiency with fluctuating electricity in different formats. The system reduces utilization rate of sensors, controllers and/or switches to control electrolysis units so as to reduce complexity and manufacturing cost of the hydrogen generation system.    DETAILED DESCRIPTION - The electrical output is electrical current or voltage of the power source. An INDEPENDENT CLAIM is also included for a method for generating hydrogen from a volatile power source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an electrical structure of a hydrogen generation system.    Electrolysis stack (106)    Movable electrical contact bridge (108)    Conductive track (110)    Electrolysis cells (202-210)    Driver device (220)
NOVELTY - Livestock and poultry dead kitchen garbage and comprehensive use system, comprising high temperature sterilizing hydrolysis device, a crusher, a storage jar, primary magnetic sorting device, a crushing separating device, the first stir mix device, solid-liquid separating device, the second stir mix device, auxiliary material conveying device, water storage tank, a three phase separator, oil water separator, anaerobic ferment jar, an aeration pool, pond, closeness horizontal double-layer tube aerobic fermentation jar, closeness horizontal aerobic fermentation jar, crushing and screening device, a chamber, an air supply device, discharge device, homogenizing storage chamber, organic fertilizer packaging device and industrial lipid. This utility new type is a large amount, fermenting period is short, treatment effect is good, the automatic degree high, a low cost, a process without peculiar smell, the kitchen garbage and dead livestock and poultry waste is valuable.
NOVELTY - Livestock and poultry dead kitchen garbage and comprehensive use system of preparing organic fertilizer part, comprising high temperature sterilizing hydrolysis device, a crusher, a closeness, storage jar, primary magnetic sorting device, crushing device, a crushing separating device, the first stir mix device, using reclaimed fibre waste use device, solid-liquid separating device, the second stir mix device, auxiliary material conveying device, the first steam preheating device, closeness horizontal double-layer tube aerobic fermentation jar, closeness horizontal aerobic fermentation jar, crushing and screening device, a chamber, an air supply device, discharge device, homogenizing storage chamber, organic fertilizer packaging device and deodorizing tower. This utility new type is a large amount, fermenting period is short, treatment effect is good, the automatic degree high, a low cost, a process without peculiar smell, the kitchen garbage and dead livestock and poultry waste is valuable.
NOVELTY - Livestock and poultry dead pests without industrial lipid and biological organic fertilizer part of chemical processing system, comprising high temperature sterilizing hydrolysis device, a crusher, a closeness, oil water slag separator, mixed stir device, auxiliary material conveying device, closeness horizontal double-layer tube aerobic fermentation jar, closeness horizontal aerobic fermentation jar, crushing, homogenizing storage cabin, sundries cabin, biological organic fertilizer packaging device, industrial lipid storage tank, an air supply device, discharge device and deodorizing tower. This utility new type is a large amount, fermenting period is short, treatment effect is good, the automatic degree high, a low cost, a process without peculiar smell, the dead livestock and poultry waste is valuable.
NOVELTY - Kitchen garbage residue prepare a edible mushroom a rod system, comprising the first belt conveyor, a second belt conveyor, a crusher, a third belt conveyor, a mixed stirrer, a hoisting machine, a type fermentation jar, sterile air generator, a steam generator, a mixer and, this utility new type has simple structure, using kitchen garbage to one as a raw material, a source is very wide, it reduces a the preparation cost of edible mushroom a rod, this utility new type using sterile air process heat, increase the fermentation and a mixed effect so as to increase the quality of a rod.
NOVELTY - This utility new type claims a one solid oxide fuel cell power supply system, including S0FC cell stack, connecting to S0FC anode of storage battery with a fuel of high pressure gas bottle, and connecting to S0FC cell stack cathode is air power supply unit, through intermittent change storage with high pressure air bottle is alkyl, hydrogen as a fuel for generation of a S0FC cell stack, power output end of S0FC cell stack connecting to one, output end of a supercharger to one inverter, output end of inverter connect to electric device and electric device for power supply directly, without need to set battery. This utility new type by S0FC cell stack generation after through inverter directly a device use, without using a battery, power supply structure is simpler and the generation efficiency is high, the tail pneuma only contains water vapour and carbon dioxide, for there is no environment pollution, and maintenance period can reach 10-50 times of electric generator is diesel oil.
NOVELTY - A dead one livestock and poultry and kitchen garbage comprehensive processing system, comprising high temperature sterilizing hydrolysis device, a sand wheel grinding crusher, storage jar, primary magnetic sorting device, a crushing separating device, the first stir mix device, solid-liquid separating device, the second stir mix device, auxiliary material conveying device, water storage tank, a three phase separator, oil water separator, anaerobic ferment jar, an aeration pool, pond, closeness horizontal double-layer tube aerobic fermentation jar, closeness horizontal aerobic fermentation jar, crushing and screening device, a chamber, an air supply device, discharge device, homogenizing storage chamber, organic fertilizer packaging device and industrial lipid. This utility new type processing amount is large, a good effect, automatic degree high, a low cost, especially for livestock and poultry dead of high temperature hydrolysis and crushing work, processing compare completely to ensure the particle size of material is not more than 0.5 cm, the kitchen garbage and dead livestock and poultry waste is valuable, the production has great market value of organic fertilizer and industrial lipid.
NOVELTY - This utility new type is a one mobile power supply vehicle, comprising vehicle body and set with set with a door in a fuel cell generation device inner the vehicle body, a vehicle body, a fuel generation device comprising a supporting body, the supporting body set with a radiating device and operation display device, a radiating device and the operation device to the body of a vehicle door. And the existing technology, this utility new type mobile power supply vehicle, through the position of operation device and a radiating device and a distribute, it has convenient operation and heat character is good.
NOVELTY - This utility new type relates to tower-shaped integrated sewage treatment device, a core of this device using engineering strain. of traditional active sludge, and using special carrier fixed engineering strain, the structure comprising a tower body, a cloth water system, an aeration system, biological reaction area and precipitation separating system, a cloth water system set with a tower body bottom of the cloth water system and biological reaction area through sieve plate, lower sieve plate set with aeration system outside the tower body set with aeration pipe and back-flushing pipe, an aeration pipe and aeration system connected, a back-flush pipe and cloth water system connected, a precipitate separating system comprising a precipitation zone, a water pipe, a precipitation zone set with a biological reaction area, mud discharging pipe and the bottom of settling zone connected, a drain pipe set with a pipe. This utility new type engineering strain to substituted of traditional active sludge, great increase of the sewage processing efficiency and saves the floor area, at the same time is convenient to maintain and repair and reduces the operation cost.
NOVELTY - Livestock and poultry dead and kitchen garbage comprehensive processing system, comprising high temperature sterilizing hydrolysis device, a sand wheel grinding crusher, storage jar, primary magnetic sorting device, a crushing separating device, the first stir mix device, solid-liquid separating device, the second stir mix device, auxiliary material conveying device, water storage tank, a three phase separator, oil water separator, anaerobic ferment jar, an aeration pool, pond, closeness horizontal double-layer tube aerobic fermentation jar, closeness horizontal aerobic fermentation jar, crushing and screening device, a chamber, an air supply device, discharge device, homogenizing storage chamber, organic fertilizer packaging device and industrial lipid. This utility new type processing amount is large, a good effect, automatic degree high, a low cost, especially for livestock and poultry dead of high temperature hydrolysis and crushing work, processing compare completely to ensure the particle size of material is not more than 0.5 cm, the kitchen garbage and dead livestock and poultry waste is valuable, the production has great market value of organic fertilizer and industrial lipid.
NOVELTY - A device for transforming refuse into compost, comprises a first reducing mechanism in the hopper operable to grind the refuse; and a transfer mechanism disposed in a conduit extending upwardly from the hopper to an outlet in the upper portion of the cabinet.    USE - The device is used for transforming refuse into compost (claimed).    ADVANTAGE - The composting devices are effective in producing compost in a continuous way. The combination of two separate chambers, hopper and the container, makes the overall composting process faster and more efficient by sequentially transforming the refuse into compost in two separate chambers.    DETAILED DESCRIPTION - A device for transforming refuse into compost, comprises a cabinet; a hopper at an upper portion of the cabinet and having an opening through the cabinet configured to receive refuse; a first reducing mechanism in the hopper operable to grind the refuse; a transfer mechanism disposed in a conduit extending upwardly from the hopper to an outlet in the upper portion of the cabinet; a motor beneath the hopper and the transfer mechanism and operably connected to the first reducing mechanism and the transfer mechanism to operate the first reducing mechanism and the transfer mechanism; and a container removably mounted within the cabinet adjacent the motor and beneath the outlet to receive ground refuse from the outlet, where the container is accessible from outside the cabinet.
NOVELTY - A hydrogen manufacturing system has separator for separating sulfuric acid and iodinic acid produced in Bunsen reactor, metal electrodes arranged on the side of separator along vertical direction, surface-determinant potential measurement portion for measuring potential difference between metal electrodes which are adjacent to each other, and interface determiner for determining position of interval of the metal electrodes in which potential difference is formed.    USE - Hydrogen manufacturing system (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for separation of sulfuric acid and iodinic acid produced in Bunsen reactor.
NOVELTY - The method involves abutting extension portion extended from base end of standing-up element provided in one surface of base material with respect to cathode side separator or anode side separator. Interval between the anode side separator and the cathode side separator along lamination direction is set at a range in which deformation of the standing-up element exceeds an elastic deformation range and falls within a plastic deformation range without allowing base ends that move in conjunction with the deformation to come into contact with cathode side separator or anode side separator.    USE - Method for manufacturing fuel cell (claimed).    ADVANTAGE - The deformation of the standing-up element is optimized. The load received by the standing-up element is made to increase.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating a state which considers expansion of another stacking element and setting height of standing-up element of deformation absorption element of the fuel cell. (Drawing includes non-English language text)
NOVELTY - Seed coating comprises: (A) adhesive compounds; and at least one of (B) a fertilizer compound, (C) an inoculum comprising micro-organisms, (D) a biostimulant compound, (E) a water absorber and (F) a filler.    USE - The seed coating is useful for improving the initial growth of the plant. No biological data given.    ADVANTAGE - The coating allows for effective modification of shape and/or size of the seed of e.g. maize, wheat, barley and oats, thus improving or promoting the growth of the plant.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a seed comprising a layer of the coating;    (2) a method for obtaining coated seeds, comprising preparing the above compounds (A)-(F) intended to form the seed coating, and applying the obtained compounds (A)-(F) to the seed of the coating layer; and    (3) a device comprising a storage unit containing the seed and the compounds (A)-(F), an application unit for generating a coating layer on the seed, a processing unit for drying and removing an excess or non deposited coating on the seeds, and a conditioning unit for the coated and dried seed.
NOVELTY - Process for continuous flow of liquid phase nitration of alkyl benzene compound involves reacting alkyl benzene compound with nitrating agent in micromixer and tubular reactor at 10-60 degrees C for 30 seconds to 30 minutes at atmospheric pressure to obtain nitro alkyl benzene.    USE - Process for continuous flow of liquid phase nitration of alkyl benzene compound used for producing 4-nitro-o-xylene used as raw material for manufacturing pharmaceutical intermediates, vitamin B2, vitamin B12 and 3,4-dimethylaniline.    ADVANTAGE - The process enables quick and efficient continuous flow of liquid phase nitration of alkyl benzene compound at low temperature, with reduced energy consumption, and produces 4-nitro-o-xylene with high yield and selectivity. The process is zero-effluent process, facile, environmentally-friendly and easily manageable.
NOVELTY - Drought-resistant potato special organic fertilizer comprises Paenibacillus polymyxa strain fermentation liquid.    USE - Used as drought-resistant potato special organic fertilizer.    ADVANTAGE - The fertilizer makes full use of waste resources, reduces the environmental pollution, solves the problem of carrier materials needed for the production of bio-organic fertilizer, reduces continuous cropping soil-borne disease, improves disease prevention effect and increases potato yield by using less dosage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing drought-resistant potato special organic fertilizer comprising mixing uniformly 80 mesh sieved organic material carrier and Paenibacillus polymyxa strain fermentation liquid, after packaging, under the condition of 20-30 degrees C, allowing to stand for 7-10 days to obtain fertilizer.
NOVELTY - Manufacturing fertilizer comprises crushing plant ash into 80-120 meshes powder, adding sepiolite, sheep manure, shell powder, humus, seaweed powder and stone powder to the crushed powder, uniformly mixing, heating the mixture at 150-200 degrees C, holding the heated mixture at room temperature for 4 hours, cooling the mixture at room temperature, fermenting the cooled mixture for 15-18 days, stirring the fermented mixture, adding Angelica powder and indoleacetic acid to the stirred mixture, uniformly mixing, adding 52-55% of water to the mixture, machining the mixture, and drying.    USE - The method is useful for manufacturing fertilizer (claimed), which is useful for promoting seedling root.    DETAILED DESCRIPTION - Manufacturing fertilizer comprises taking plant ash and then crushing into 80-120 meshes powder, adding sepiolite, sheep manure, shell powder, humus, seaweed powder and stone powder to the crushed powder, uniformly mixing, heating the mixture at 150-200 degrees C, holding the heated mixture at room temperature for 4 hours, cooling the mixture at room temperature, fermenting the cooled mixture for 15-18 days, stirring the fermented mixture, adding Angelica powder and indoleacetic acid to the stirred mixture, uniformly mixing, adding 52-55% of water to the mixture, machining the mixture into a granule size of 5 mm, and drying.
NOVELTY - Fertilizer comprises 35-43 pts. wt. urea, 30-35 pts. wt. diammonium phosphate, 15-18 pts. wt. potassium chloride, 1-2 pts. wt. zinc sulfate, 5-8 pts. wt. micronutrient fertilizer, 30-40 pts. wt. wheat straw, 5-8 pts. wt. fulvic acid, and 25-30 pts. wt. humic acid.    USE - The fertilizer is useful for continuous cropping in wheat and corn (claimed).    ADVANTAGE - The fertilizer has increased soil microbial content and reduced cropping obstacle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer comprising adding urea, diammonium phosphate, potassium chloride, zinc sulfate, micronutrient fertilizer, wheat straw, fulvic acid and humic acid into a reaction container, uniformly mixing, adding 50-55% of water to the mixture, composting the mixture, fermenting the composted mixture for 10-12 days, where urea, diammonium phosphate and potassium chloride are present in an amount of 3-5 pts. wt., maintaining the temperature at 36-42 degrees C, granulating the mixture, and drying.
NOVELTY - Fertilizer composition comprises mixture of organic and inorganic fertilizer components such as 200-700 pts. wt. sisal saponin extract, 100-300 pts. wt. monoammonium phosphate, 80-150 pts. wt. potassium chloride, and 80-120 pts. wt. urea.    USE - As fertilizer composition.    ADVANTAGE - The composition exhibits synergistic effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves (a) drying sisal until moisture content reaches 10%, and pulverizing dried sisal, (b) crushing monoammonium phosphate, and potassium chloride, adding crushed mixture to pulverized sisal, and (c) granulating the mixture and drying the granulated mixture.
NOVELTY - Solanaceous vegetable seedling substrate comprises fermentation bed waste material, vermiculite and peat mixture, added with 0.5 kg phosphorus pentoxide/cm2.    USE - Used as Solanaceous vegetable seedling substrate.    ADVANTAGE - The substrate utilizes waste material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing solanaceous vegetable seedling substrate, comprising: (i) cleaning the fermentation bed waste material of pigsty, then adjusting nitrogen and moisture content to (16-25):1 and 50-60% respectively; (ii) stacking the fermentation bed waste material to ferment, turning once for every two days until it matures to 80 plus minus 2%; (iii) mixing the fermented material with vermiculite and peat; (iv) uniformly stirring the mixture with a stirrer, adding phosphorus pentoxide; and (v) uniformly mixing the mixture via blender.
NOVELTY - Fertilizer granule comprises core layer comprising 4-8 pts. wt., preferably 5 pulverized straw, 2-6 pts. wt., preferably 5 crushed wooden meal, 10-12 pts. wt., preferably 10 clay, cellulose degrading bacteria, nitrogen fixing bacteria and phosphate solubilizing bacteria and covering layer comprising 3-6 %, preferably 3 % gelatin solution.    USE - Fertilizer granule used in agriculture for processing biological waste material in soil.    ADVANTAGE - The fertilizer granule is beneficial for agricultural production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer granule, which involves:    (A) mixing and crushing pulverized straw, wooden meal and clay;    (B) sterilizing obtained mixture;    (C) mixing cellulose degrading bacteria, nitrogen fixing bacteria and phosphate solubilizing bacteria with obtained mixture to obtain another mixture;    (D) granulating obtained mixture; and    (E) coating obtained granule with 3-6 % gelatin solution to obtain fertilizer granule.
NOVELTY - Lotus fertilizer comprises 70-80 pts. wt. organic fertilizer, 15-25 pts. wt. inorganic fertilizer, 1-5 pt(s). wt. trace elements, 0.1-0.3 pt. wt. fermentation bacteria, 1-2 pt(s). wt. enzymes, 2-7 pts. wt. humic acid and 0.5-1 pt. wt. chitosan oligosaccharide.    USE - Lotus fertilizer.    ADVANTAGE - The lotus fertilizer can be prepared without any heavy metals, hence eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer comprising: weighing organic fertilizer, inorganic fertilizer, trace elements, fermentation bacteria, enzyme, humic acid and chitosan oligosaccharide; mixing fermentation bacteria with water in a weight ratio of 1:5-20 to obtain a diluted broth; adding organic fertilizer into the diluted broth, mixing, stacking the mixed piles, turning the piles and fermenting the pile for 10-15 days to obtain a fermented product; adding enzymes for second fermentation, drying at low temperature and grinding; adding inorganic fertilizer, trace elements, humic acid, chitosan oligosaccharide and biological bacteria, and granulating the mixture.
NOVELTY - Tea fertilizer comprises 6-14 pts. wt. ammonium bicarbonate, 3-8 pts. wt. humic acid, 2-6 pts. wt. sodium chloride, 2.5-6 pts. wt. ammonium molybdate, 2-4 pts. wt. soil modifier, 3.5-8 pts. wt. yeast, 4.2-7 pts. wt. radix sophorae flavescentis, 7-11 pts. wt. potassium sulfate, 2.5-4.8 pts. wt. disodium hydrogen phosphate, 4.2-7.6 pts. wt. Bacillus and 3.2-6.8 pts. wt. Lactobacillus.    USE - Tea fertilizer.    ADVANTAGE - The fertilizer increases quality and taste of tea, and increase the absorption rate and disease resistance property of the tea plant.
NOVELTY - Microorganism fertilizer comprises 1-3 pts. wt. ammonium persulfate, 0.5-2 pts. wt. ammonium phosphate, 1-2 pts. wt. potassium chloride, 6-10 pts. wt. chicken manure, 5-9 pts. wt. rice bran, 1-4 pts. wt. boric acid, 1.2-3 pts. wt. pyrophosphate, 3-7 pts. wt. cypress, 0.6-1 pts. wt. borax, 3-5 pts. wt. Bacillus stearothermophilus, 2-6 pts. wt. plant lactic acid, 0.6-1.5 pts. wt. bonding agent and 3-6 pts. wt. Effective microorganism (RTM: Anaerobic organisms).    USE - Microorganism fertilizer used for improving soil and increasing soil fertility.    ADVANTAGE - The microorganism fertilizer increases utilization rate of fertilizer and is eco-friendly.
NOVELTY - The apparatus (100) comprises multiple electrolysis cells (10a,10b) each accommodates diaphragm of solid oxide electrolyte having oxygen ion permeability. The hydrogen and oxygen electrodes are adjacent to respective surface of diaphragm. A cell container (21) forms hydrogen side space with diaphragm into which hydrogen produced as reaction product is made to flow out of hydrogen recovery opening. The electrolysis cell and mutually adjacent electrolysis cell are arranged mutually parallelly so that direction which goes to hydrogen recovery opening is mutually opposing from fuel intake.    USE - Hydrogen production apparatus.    ADVANTAGE - As the heat conduction leads the air between the opposing surfaces, the temperature difference of an opposing portion is eliminated. Therefore the equalization of temperature is achieved. Since the hydrogen reaction rate and temperature distribution in both cell stacks are uniformized, the cell stack efficiency is improved and the stress of each portion in a cell stack is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the structure of the hydrogen production apparatus.    Electrolysis cells (10a,10b)    Hydrogen recovery pipe (17)    Oxygen discharge pipe (19)    Cell container (21)    Hydrogen production apparatus (100)
NOVELTY - Improved process for preparing palonosetron hydrochloride (HCl) involves: (a) hydrogenating salt of 2-(1-azabicyclo(2.2.2)oct-3-yl)-2,4,5,6-tetrahydro-1H-benz(de)isoquinolin-1-one using hydrogenation catalyst, in water to obtain palonosetron free base; (b) optionally isolating the palonosetron free base; and (c) converting the palonosetron free base into palonosetron HCl using a source of HCl in the presence of acetone or isopropanol or a mixture of acetone and organic solvent.    USE - The improved process is useful for preparing palonosetron HCl (claimed).    ADVANTAGE - Improved and environment-friendly process is provided for preparing palonosetron HCl with good stability, purity and yield, where the process avoids the use of corrosive agents like perchloric acid.    DETAILED DESCRIPTION - Improved process for preparing palonosetron hydrochloride (HCl) involves: (a) hydrogenating salt of 2-(1-azabicyclo(2.2.2)oct-3-yl)-2,4,5,6-tetrahydro-1H-benz(de)isoquinolin-1-one of formula (II) using hydrogenation catalyst, in water to obtain palonosetron free base of formula (III); (b) optionally isolating the palonosetron free base; and (c) converting the palonosetron free base into palonosetron HCl of formula (I) using a source of HCl in the presence of acetone or isopropanol or a mixture of acetone and organic solvent.    x=salt.
NOVELTY - Potassium salt flotation involves grinding low grade potassium salt containing ore, where the mass content of potassium is not less than 64.90%. The obtained material is placed in a flotation machine, where the potassium salt is potassium-magnesium alum or potassium chloride. Positive ion collector (120-160 grams per ton of potassium salt containing ore) is added to the obtained material to obtain the potassium chloride ore concentrate, where the floatation time is 6-8 minutes. The negative ion collector is added in the flotation machine.    USE - Method for flotation of potassium salt (claimed).    ADVANTAGE - The method is simple, eco-friendly and cost-effective, and has improved recovery rate of potassium ions.    DETAILED DESCRIPTION - Potassium salt flotation involves grinding low grade potassium salt containing ore, where the mass content of potassium is not less than 64.90%. The obtained material is placed in a flotation machine, where the potassium salt is potassium-magnesium alum or potassium chloride. Positive ion collector (120-160 grams per ton of potassium salt containing ore) is added to the obtained material to obtain the potassium chloride ore concentrate, where the floatation time is 6-8 minutes. The negative ion collector is added in the flotation machine, where the potassium-magnesium alum is potassium-magnesium alum, anhydrous potassium-magnesium alum and epsomite. The obtained material is processed for 4-6 minutes to obtain flotation concentrate. The obtained potassium chloride ore concentrate and flotation concentrate are mixed with fresh water, where the mass ratio of a mixture of the obtained potassium chloride ore concentrate and flotation concentrate, and fresh water is 1:0.65-0.80, respectively. The obtained mixture is stirred at normal temperature for 2 hours. The obtained material is filtered, and then dried to obtain potassium magnesium sulfate fertilizer.
NOVELTY - Preparing fertilizer involves adding Bacillus into molasses and then fermenting to obtain fermentation liquid. pH value and metal ion concentration are measured and then metal complexing agent is added into fermentation liquid and then heated at 90 degrees C for 30-360 degrees C to obtain the molasses alcohol (35-95%). pH regulator is added into molasses alcohol to obtain mixture and then pH value (7-8) is maintained. The mixture is put into anaerobic fermentation pool and then anaerobic bacteria is added.    USE - Fertilizer.    ADVANTAGE - The fertilizer is economic, eco-friendly and improves crop quality.    DETAILED DESCRIPTION - Preparing fertilizer involves adding Bacillus into molasses and then fermenting to obtain fermentation liquid. pH value and metal ion concentration are measured and then metal complexing agent is added into fermentation liquid and then heated at 90 degrees C for 30-360 degrees C to obtain the molasses alcohol (35-95%). pH regulator is added into molasses alcohol to obtain mixture and then pH value (7-8) is maintained. The mixture is put into anaerobic fermentation pool and then anaerobic bacteria is added. The mixture is fermented for 12-48 hours and then organic filler and inorganic fertilizer are added to obtain another mixture. The mixture is fermented for 12-36 hours and then spray dried to obtain dried material. The material is granulated and then beneficial biological flora is added to obtain the product.
NOVELTY - Fertilizer preparation involves mixing anionic adsorbent, ginger powder and zeolite powder. Dairy manure, peat soil and chicken manure are mixed according to mass ratio of 5:1:1. Humus and potassium chloride are mixed in the ratio of 9:1. Phosphate and potash decomposing bacteria, dehydroacetic acid, and potassium humate are mixed. Ginger powder and zeolite powder are crushed, and then mixture of humus and potassium chloride is added. The obtained mixture is mixed with dairy manure, peat soil and chicken manure uniformly. Potassium humate is added to the obtained material. The obtained material is covered.    USE - Method for preparing fertilizer used for reducing salinity of soil (claimed).    ADVANTAGE - The method enables to prepare the fertilizer that is cost-effective and has improved the basicity of the soil.    DETAILED DESCRIPTION - Fertilizer preparation involves mixing anionic adsorbent, ginger powder and zeolite powder. Dairy manure, peat soil and chicken manure are mixed according to mass ratio of 5:1:1. Humus and potassium chloride are mixed in the ratio of 9:1. Phosphate and potash decomposing bacteria, dehydroacetic acid, and potassium humate are mixed. Ginger powder and zeolite powder are crushed, and then mixture of humus and potassium chloride is added. The obtained mixture is mixed with dairy manure, peat soil and chicken manure uniformly. Potassium humate is added to the obtained material. The obtained material is covered using plastic film cover. The obtained material is fermented for 10-12 days. Anion absorbent, phosphorus potassium solution and methylacetopyranone is added to the obtained material, where the water content of material is 63-65%. The obtained material is processed in an extruder and dried to obtain the desired product.
NOVELTY - Using cationic and water retaining fertilizer involves utilizing rod-shaped fertilizer. The rod shaped fertilizer is inserted into the end part of the exposed surface, which is selected from corn starch. Water is added to the obtained material, and then heated to 70-75 degrees C for 1 hour. The obtained material is cooled to 45 degrees C to obtain paste. The paste is sprayed using a pressure sprinkle device on the ground surface to obtain thin film. Rod shaped fertilizer is inserted into the other part of the exposed surface. The fertilizer components are sprayed.    USE - Method for using cationic and water retaining fertilizer (claimed) for enhancing activity of microorganism and enzyme in soil, improving the salinity of soil, and promoting growth of plant root.    ADVANTAGE - The method is simple and convenient.    DETAILED DESCRIPTION - Using cationic and water retaining fertilizer involves utilizing rod-shaped fertilizer. The rod shaped fertilizer is inserted into the end part of the exposed surface, which is selected from corn starch. Water is added to the obtained material, and then heated to 70-75 degrees C for 1 hour. The obtained material is cooled to 45 degrees C to obtain paste. The paste is sprayed using a pressure sprinkle device on the ground surface to obtain thin film. Rod shaped fertilizer is inserted into the other part of the exposed surface. The fertilizer components are sprayed on the surface of the obtained material, where the fertilizer composition comprises absorbing resin clay and zeolite powder in the mass ratio of 1:2:4, a mixture of egg white, Chinese Mosla herb powder, duck manure and vermiculite powder, and a mixture of calcium biphosphate, calcium phosphate-solubilizing bacteria, urea, fermentative bacteria, nitrogen-fixing bacteria and phytase.
NOVELTY - Emodin and tert-butoxide are dissolved in water, and reacted at 90-100 degrees C for 4-6 hours. Hydroquinone is added to mixture, irradiated with microwaves, then mixture is transferred to closed container, and reaction is continued at 120-140 degrees C for 8-12 hours. Then, inorganic acid is added to reaction mixture to adjust pH to 3-4, filtered, washed and dried, to obtain crude hypericin. The crude product is mixed with iodosylbenzene and dissolved in acetone, reacted, filtered, filtrate is collected, evaporated, washed, filtered and recrystallized, to obtain hypericin.    USE - Synthesis of hypericin (claimed).    ADVANTAGE - The method efficiently and economically provides hypericin, with high yield and high purity.    DETAILED DESCRIPTION - Emodin and tert-butoxide are dissolved in water, and reacted at 90-100 degrees C for 4-6 hours under nitrogen protection. Hydroquinone is added to mixture, irradiated with microwaves, then mixture is transferred to closed container, and reaction is continued at 120-140 degrees C for 8-12 hours. Then, inorganic acid is added to reaction mixture to adjust pH to 3-4, filtered, washed and dried, to obtain crude hypericin. The crude product is mixed with iodosylbenzene and dissolved in acetone, reacted at 45-55 degrees C for 4-8 hours, reaction mixture is filtered, filtrate is collected, evaporated, washed, filtered and recrystallized, to obtain hypericin.
NOVELTY - Preparation of S-pregabalin by chemical-splitting method involves splitting racemic pregabalin by using L-pyroglutamic acid as resolving agent in an alcohol solution as organic solvent, acid-hydrolyzing mixture of S-pregabalin salt and L-pyroglutamic acid, crystallizing, washing, acid-hydrolyzing, removing resolution agent, adjusting pH to neutral, and distilling.    USE - Preparation of S-pregabalin by chemical splitting method (claimed).    ADVANTAGE - The method efficiently and economically provides S-pregabalin, with high purity by simple process without causing pollution to the environment.
NOVELTY - Mother liquor is placed in column, distilled, and aqueous solution of methanol and ammonium chloride is separated. Top of the column contains ammonia in methanol solution, and bottom of the column contains aqueous solution of ammonium chloride, amino acid and methenamine. Sodium hydroxide-containing methanol solution is added to top of the column, and sodium hydroxide is removed. The liquid discharged from the bottom of the column is dehydrated, and concentrated to obtain ammonium chloride solution. Ammonium chloride solution is cooled and precipitated to obtain ammonium chloride.    USE - Processing of amino acid-mother liquor (claimed).    ADVANTAGE - The method enables processing of amino acid-mother liquor without discharging wastewater by environmentally-friendly process.    DETAILED DESCRIPTION - Mother liquor is placed in distillation column, distilled under reduced pressure, and aqueous solution of methanol and ammonium chloride is separated. Top of the column contains 5-12% ammonia in methanol solution, and bottom of the column contains an aqueous solution of ammonium chloride, amino acid and methenamine. Sodium hydroxide-containing methanol solution is added to top of the column, and sodium hydroxide is removed. The liquid discharged from the bottom of the column is introduced into vacuum flasher, dehydrated, and concentrated to obtain ammonium chloride solution. Ammonium chloride solution is subjected to slow cooling process and precipitated to obtain ammonium chloride.
NOVELTY - Device comprises a substrate container (1) comprising a peripheral wall (4) and a bottom (12), in which the peripheral wall is aligned along a vertical axis, and at least one agitator (3) comprising a shaft (8) which projects into substrate container from vertically and horizontally deviating mounting angle. The agitator comprises at least two stirring blades, radially extending on both sides of the shaft and twisted to each other. The blades are spaced apart in the longitudinal extension of the shaft and are disposed on the shaft.    USE - The device is useful for mixing the contents of a substrate container (claimed).    ADVANTAGE - The device: adjusts the operation conditions of the biogas plant in simple manner; and has good maintenance.    DETAILED DESCRIPTION - Device comprises a substrate container (1) comprising a peripheral wall (4) and a bottom (12), in which the peripheral wall is aligned along a vertical axis, and at least one agitator (3) comprising a shaft (8) which projects into substrate container from vertically and horizontally deviating mounting angle. The agitator comprises at least two stirring blades, radially extending on both sides of the shaft and twisted to each other. The blades are spaced apart in the longitudinal extension of the shaft and are disposed on the shaft. The length of the agitator blades, their axial position and the mounting angle are provided in the shaft such that their rotation circles overlap in terms of the level of liquid in the container substrate. The agitator blades exhibit rectangular profile radially extending up to their end portions. The end portions exhibit angled portions with respect to the extension direction of the profile.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the rotational circuit.    Substrate container (1)    Agitator (3)    Wall (4)    Shaft (8)    Bottom (12)
NOVELTY - This utility new type claims a one ammonia nitrogen sewage processing system (AMOXP), through research and engineering practice for biological denitrification of nitrogen which combine, in engineering application in low investment, good effect, high efficiency, simple operation, low energy consumption, realize the full range of nitrogen without pollution circulation. The structure a, comprise a three part, the first unit, second unit and third unit, which are serially connected, the volume ratio of a 2: 1: 3. The first unit and a connected water inlet, the first unit and second unit upper part by the water hole connected, second unit and third unit a part by the water hole connected, second unit and third unit bottom reflux by a connected, at the same time the first unit and third unit and the bottom aeration system, the aeration system and fan connecting device, set with a bottom of a third discharge unit. end of the process operation temperature a normal temperature.
NOVELTY - This utility new type provides a natural oxygen increasing one type of biological filter tower, wherein, comprising water inlet pipe, rotating nozzle, biological film filter bed, biological bed tower body, wherein natural ventilation, water collecting tank. Using natural ventilation wherein a through tower top waste water drop flow down air flow, a sewage, air and b attached filler of a biological film phase fully contact, namely the needed processing waste water entering into the water inlet tube, the rear rotary nozzle uniform cloth water, entering into biological bed tower body, biological film filter bed, wherein the natural air entering into a natural wind supply oxygenation of waste water, purifying water degraded biological film filter bed, self-discharging rear to collecting water tank collecting or entering into the next processing unit. Through more than improved, natural oxygen increasing type biological filter tower of a a energy-saving, the over-ground type structure, the construction speed is fast, the energy consumption operation cost is low, it is convenient to maintain and maintenance and so on.
NOVELTY - Preparing (S)-5-hydroxymethyl-cyclopent-1-enol compound comprises performing reduction reaction of (R)-2-hydroxy-cyclopent-2-enecarboxylic acid compound in the presence of solvent.    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method is capable of economically preparing (I) under a mild reaction condition with improved yield in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing (S)-5-hydroxymethyl-cyclopent-1-enol compound of formula (I) comprises performing reduction reaction of (R)-9-cyclopentyl-9H-purine compound of formula (II) in the presence of solvent.    R2 = monovalent group of formula (Ia);    R21 = pyridyl or 6-10C-aryl (both optionally substituted by 1-3C-alkyl, halo or 1-3C-alkoxy);    Y1 = optionally substituted 3-9 membered ring to connect with Si bond to form a optionally substituted 4-10-membered carbocyclic ring, or Y1 is optionally substituted 3-9 membered ring to connect with heteroatoms comprising Si, O, S or N to form a optionally saturated 4-10-membered ring or 1-3C-alkyl;    P1 = (-C(CH3)(O-R9)-CH2-R8);    R8 = 1-6C-linear or branched alkyl or H;    R9 = linear or branched 1-6C-alkyl, trimethylsilyl, triethylsilyl, triphenylmethyl or tert-butyldimethylsilyl; and    R10 = linear or branched 1-4C-alkyl.
NOVELTY - Preparing 6-amino-1-((1S)-2-oxocyclopentyl)benzimidazol-4-one compound comprises performing reduction reaction of (R)-9-cyclopentyl-9H-purine compound in the presence of a solvent.    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method is capable of economically preparing (I) with high efficiency and yield under a mild reaction condition in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing 6-amino-1-((1S)-2-oxocyclopentyl)benzimidazol-4-one compound of formula (I) comprises performing reduction reaction of (R)-9-cyclopentyl-9H-purine compound of formula (II) in the presence of solvent.    R2 = monovalent group of formula (Ia);    R21 = pyridyl or 6-10C-aryl (both optionally substituted by 1-3C-alkyl, halo or 1-3C-alkoxy);    Y1 = optionally substituted 3-9 membered ring to connect with Si bond to form a optionally substituted 4-10-membered carbocyclic ring, or Y1 is optionally substituted 3-9 membered ring to connect with heteroatoms comprising Si, O, S or N to form an optionally saturated 4-10-membered ring or 1-3C-alkyl;    P2 = monovalent group of formula (Ib) or (Ic), 1-6C-alkoxy, 1-6C-alkyl, trimethyl or ethoxymethyl;    R4, R5 = linear or branched 1-6C-alkyl, H, halo or nitro;    R6 = H or linear or branched 1-6C-alkoxy; and    X = 1-6C-linear or branched alkyl or halo.    An INDEPENDENT CLAIM is included for a method-1 for preparing 9-cyclopentyl-9H-purin-2-ylamine compound of formula (III) comprising performing acetal exchange reaction of 9-cyclopentyl-9H-purin-2-ylamine compound of formula (IV) and ester compound of formula (V) in the presence of an acid and a solvent.
NOVELTY - Dicationic ionic liquid as solvents in the preparation of regenerated collagen protein, is claimed.    USE - The dicationic ionic liquid is useful as solvents in the preparation of regenerated collagen protein (claimed).    ADVANTAGE - The dicationic ionic liquid rapidly and simply dissolves collagen protein without any pollution and with increased dissolution efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for collagen protein dissolution method comprising mixing vacuum dried pure collagen powder, defatted pigskin powder and waste leather powder with the dicationic ionic liquid and heating the mixture at 80-140 degrees C under stirring.
NOVELTY - This utility new type is sludge aerobic fermentation of rotary ventilating device, wherein comprising rotary main shaft and vertical to fixed mounting inner jar body in a rotating main shaft is a multiple of a stir air wings, rotating main shaft by jar body outside pipeline of a high pressure fan, rotating shaft and stir air wings are a hollow ventilation cavity and mutually connected, stir ventilation feather wing is a cross is a triangular plate, rear plate piece part with a vent hole, the upper air hole fixed with a protective plate. This utility new type is beneficial effect is, valid solves the sludge aerobic fermentation ventilation cloth pipe multi-device, easy to block pipeline defect and so on, in the sludge drying process uniform, ordered of ventilation, ventilation satisfying requirement of sludge aerobic fermentation process. Ventilation process in the main shaft drives a sludge inner rotary wings, wing rear part cause space, gas flow in a vent hole to prevent the material entering into air hole cause blockage, for sludge aerobic fermentation process uniformity.
NOVELTY - This utility new type new marsh gas happen device, comprising reinforced concrete or brick concrete building of marsh gas tank, marsh gas tank set with a feeding and discharging wherein wherein, marsh gas tank of the inner upper wall mounting soft storage bag material, the cavity of the inner tank is also set with separating wall. Because of using reinforced concrete or brick concrete building of marsh gas tank, the whole device has a good structure intensity, it can support weight of the structure itself, and has a certain anti-impact ability. In addition, mounting soft storage bag material corrosion effect is in a tank of inner wall, it can avoid of marsh gas and organic matter in long-term contact corrosion, so as to cause leakage and produce safety hidden trouble. Furthermore, a is further set with the separating wall, prolongs the organic matter in a residence time to make a sufficient time of anaerobic fermentation process, produce maxinum of economic value. This utility new type structure is simple, construction and maintenance is convenient, the cost is low, and it has wide a applicability.
NOVELTY - This utility new type claims a force pushing one flow anaerobic reactor, the inner mounting fermentation tank fermentation tank body in outside, and the inner fermentation tank and fermentation tank coaxial set outside, the inlet mounting fermentation tank body outside wall of lower part in outside, the feeding and feeding tube wherein a, a material wherein a middle part mounted in the fermentation tank body inner bottom wall, the discharging and discharging tube wherein a, a fermentation Opening mounted upper part of fermentation tank body in outside, air outlet mounted in the upper part of the fermentation tank cover, an exhaust port and a gas discharge pipe connection. This utility new type is beneficial effect is: use feeding a thrust force, a marsh gas lifting force action such as pushing material liquid a, then use gravity and gas pressure of pushing effect, solves the problem that the straw fiber raw material marsh gas ferment discharging height is difficult.
NOVELTY - This utility new type relates to used for solid-liquid double-phase ferment jar is straw producing ethyl alcohol, comprising solid zymohydrolysis jar 1 and liquid fermentation jar 2, through pipeline 5 connecting the solid enzymolysis jar 1 include jar cover 3 and the tank body 4, air outlet 9, enzyme solution inlet (10) and slag 12, set with a stir stick 7, stir stick 7 a set with spiral slurry leaves 6, stir stick 7 and the outside of motor 8 a, the liquid fermentation jar 2 with a gas inlet 16, a liquid outlet 19 and a pH buffer device 22, the top part is set with pressure table 13, a thermometer 14, liquid fermentation jar pH meter 15, the bottom set a heating device 26, liquid fermentation jar 2 a double wall structure, interlayer in double layer wall is set with water inlet 17 and water outlet 18, 2 is further set with a liquid wherein a 25, a liquid wherein a 25 through a liquid inlet pipeline 24 and liquid fermentation jar 2 a, a liquid inlet pipeline 24 is set with valve 23.
NOVELTY - A float sludge crushing circulation of autotrophic denitrification nitrogen granule sludge reactor, comprising reactor main body and an external control device, a reactor main body from lower to upper set with cloth water discharging unit, reaction unit, float sludge crushing unit, collecting unit, circulation unit and a water outlet unit, a cloth water unit set with mud water inlet, an aeration head and a sludge, float sludge crushing unit comprising gas collecting room, spraying pipe and baffle plate; circulation unit set with flow guide clapboard, reducing pipe, water outlet unit comprising overflow hole, in the water groove is set with ring outside circulation unit, and external connected water outlet of an external control device comprising relay and liquid level control valve. This utility new type is beneficial effect is: use aeration rest pneuma and autotrophic denitrification nitrogen gas implication of a for removing a removing floating a sludge surface of bubble, breaking a sludge inner bag, realize the collecting-crushing-sedimentation-return of a floating a sludge).
NOVELTY - Synthesis of zinc oxide nanoparticles from plant source by combustion method is claimed.    USE - Manufacture of zinc oxide nanoparticles used in biomedical, optical and electronic applications.    ADVANTAGE - The zinc oxide nanoparticles having high purity, porosity and efficacy against bacterial and fungal organisms are produced economically and quickly by simple experimental set-up without affecting the environment.
NOVELTY - A low temperature-resistant nitrifying bacteria enriched culturing method involves inoculating activated sludge with nitrification ability to aeration pool for sewage treatment, and culturing the nitrifying bacteria.    USE - Method for enriched culturing low temperature-resistant nitrifying bacteria.    ADVANTAGE - The method enables enriched culturing low temperature-resistant nitrifying bacteria in a simple manner with short time, stable property, good effect, high stability, easy flora source and convenience for popularizing application, overcoming complex problems caused by existing low temperature nitrobacteria inoculum preparation, long low temperature domestication time and difficulty in maintaining long-term advantages.
NOVELTY - The system has a power device (1), a material inlet (2), a material outlet (6) and a box-shaped main portion (7) with a liquid level observation window (8). The power device is set on one end of the main portion and material outlet is set on other end of the main portion. The liquid level observation window is set on the side surface of main portion. An aeration device is set in the interior of main portion and has an aeration machine (9), an aeration machine air inlet pipe (3), an aeration process machine (4) and a de-foaming machine (5).    USE - Treatment system of organic waste from municipal sludge, livestock and domestic garbage.    ADVANTAGE - The organic waste treatment system has simple structure and is convenient to use. The service life of the organic waste treatment system is prolonged. The cost is reduced. The human health is promoted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic waste treatment process of organic waste treatment system.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the organic waste treatment system.    Power device (1)    Material inlet (2)    Aeration machine air inlet pipe (3)    Aeration process machine (4)    De-foaming machine (5)    Material outlet (6)    Box-shaped main portion (7)    Liquid level observation window (8)    Aeration machine (9)
NOVELTY - This utility new type provide the a one can filter a solid residue in sewage to ensure filler to maximize the efficiency of microorganism used for sewage treatment of biological trickling filter. It comprising main tank body, water chamber set with ventilation port and a sewage inlet, a sewage inlet connecting with the first water chamber of spray head, water chamber set with a sewage exit, a ventilation port is used for mounting of the inner main tank body outside air of the first air discharging device, is connected with water chamber corresponding to a main tank body of a side wall mounting is used for the external air suction inner main tank body of second ventilation device, wherein the sewage inlet connecting with transverse connecting pipe, a transverse end of a pipe is inclined upward inclination of the inclined mounting with a filter screen, filter network up to the front one section with inclined guide tube, guide tube with a total inlet sewage port, lower filter screen front through fast joint is connected with sewage box, the sewage box by transparent material.
NOVELTY - Double anaerobic pool for preparing marsh gas system, a solid waste organic matter by anaerobic pool (A) and organic waste water anaerobic processing pool (B), wherein the solid organic waste anaerobic pool (A) and organic waste water anaerobic processing pool (B) through liquid pipe (4) and water pump II (5) is connected, a solid waste organic matter anaerobic pool (A) starting time of produce, through liquid pipe (4) and water pump II (5), a solid waste organic matter anaerobic pool (A) in a liquid, the organic waste water anaerobic processing pool (B) of the pump inlet process organic waste water anaerobic pool (B) in, and then processing organic waste water anaerobic pool (B) overflow tube (1) a solid waste organic matter anaerobic pool (A), forming circulation. With the existing technology, this utility new type can be a large amount of solid organic waste and waste water and machine for preparing marsh gas, reduces the resource waste and can ensure a solid waste organic matter anaerobic pool one time start is successful.
NOVELTY - This new type utility claims one plastic biogas tank with a floating slag removing device. It mainly by floating residue collecting hopper, scum temporary storage pool and bag-shaped U-type tube, the slag temporary storage pool mounting edge on the outer side of methane tank floating residue collecting hopper and bag-shaped U type pipe mounting inner fermentation room of the tank, U-type pipe of bag-shaped one end from extending pressure entering into the fermentation chamber between the rear upper water then enters the slag temporary storage pool, U type pipe set with bag-shaped manifold, bag-shaped U type pipe the other end of the floating residue collecting hopper at the bottom through a flexible connecting piece form a floating residue collecting hopper is set with the bag-shaped U-shaped tube type of one-way valve, one side floating residue collecting hopper of a float component, so that floating residue collecting with floater component inclines a certain angle. A scum collecting bucket multi-with water filtering small hole and a floating slag shell piece. This utility new type device structure is simple, it can finish a floating residue collecting operation, increase raw material conversion rate, increase.
NOVELTY - Manufacture of epirubicin (I) involves deprotecting N-trifluoroacetyl-14-O-tert-butyldimethylsilyl epirubicin using deprotection agent chosen from tetrabutylammonium fluoride, hydrofluoric acid and potassium fluoride (preferably, tetrabutylammonium fluoride) in a solvent which is dichloromethane or acetonitrile, and hydrolyzing N-trifluoroacetyl group of N-trifluoroacetyl-14-O-tert-butyldimethylsilyl epirubicin.    USE - Manufacture of epirubicin (claimed).    ADVANTAGE - The method enables efficient and economical manufacture of epirubicin with high yield and high purity, and suppresses pollution caused by bromination reaction.    DETAILED DESCRIPTION - Manufacture of epirubicin of formula (I) involves deprotecting N-trifluoroacetyl-14-O-tert-butyldimethylsilyl epirubicin using deprotection agent is chosen from tetrabutylammonium fluoride, hydrofluoric acid and potassium fluoride (preferably, tetrabutylammonium fluoride) in a solvent which is dichloromethane or acetonitrile, and hydrolyzing N-trifluoroacetyl group of N-trifluoroacetyl-14-O-tert-butyldimethylsilyl epirubicin. An INDEPENDENT CLAIM is included for N-trifluoroacetyl-14-O-tert-butyldimethylsilyl adriamycin.
NOVELTY - Detecting tumor cells comprises providing a device, the device comprising: a substrate surface; and first aptamer probes attached to the substrate surface; contacting cells with the first aptamer probes attached to the substrate surface; adhering one or more of the cells to the substrate surface; and measuring a non-uniformity parameter, a Hausdorff distance, a change in the number of pseudopods, and/or a shape of at least one adhered cell.    USE - The method and device are used for detecting tumor cells (claimed). The device may be used in wide variety of applications requiring sensitive protein and cell detection, including, but not limited to, forensics, early disease detection, disease progression monitoring (such as in response to therapy and/or medicinal agents), legal matters (such as paternity and criminal proceedings), defensive biohazard detection, and immigration issues (such as establishing blood relationships).    ADVANTAGE - A nanotechnology-based low-power, rapid, inexpensive, recyclable, and sensitive electrical detection device, system, and method of low concentrations of proteins and cells with no external sample preparation or labeling or other chemical modification of the sample; and biosensors for proteins and cells, including cancer cells, that integrate sensing, characterization, comparative analysis and decision making all on-board a single chip, while sustaining or increasing sensitivity and specificity, are provided.
NOVELTY - The engine mechanism has a rotor housing (Rh) fed with water (H2O). Water is transformed into water vapor using heat of the rotor housing. Carbon (C) is supplied to water vapor. Synthesis gas, preferably carbon monoxide (CO), is generated as result of endothermic reaction between carbon and water vapor using exhaust heat following a combustion process. The synthesis gas is stored in a gas storage tank (MT) for later supply to the engine.    USE - Engine mechanism for rotary piston engine vehicle. Can also be used for ships, boats, munitions or weapons, locomotives, construction machine, and rockets.    ADVANTAGE - The synthesis gas which replaces hydrogen can be stored at low pressure in the appropriate tank so as to avoid risk of gas explosion in event of vehicle accident. Since synthesis gas is used as fuel, the engine mechanism contributes to lessening of global warming and greenhouse gas emissions and reduced dependence on fossil fuels, and also allows the engine to omit need for radiator and cooling water piping. Forestry and agriculture industries are promoted since carbon is derived from plants or waste foodstuffs.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic side view of a rotary piston engine vehicle having a rotary piston engine operating on synthesis gas, and the schematic perspective view of the rotary piston engine. (Drawing includes non-English language text).    Carbon (C)    Carbon monoxide (CO)    Water (H2O)    Gas storage tank (MT)    Rotor housing (Rh)
NOVELTY - Producing lime residue involves putting lime into a machine and then stirred uniformly and placed into a microwave belt type sterilizing machine to sterilize lime at 60-100 degrees C under low temperature. The obtained lime is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material, and then dried, cooled and packaged to obtain the final product. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55) and leaching liquid (2-15).    USE - Method for producing lime residue used for providing nutrition to soil (claimed) and growth and development of plant.    ADVANTAGE - The method is ecofriendly, enables to produce lime residue that provides nutrition of nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Producing lime residue involves putting lime into a machine and then stirred uniformly and placed into a microwave belt type sterilizing machine to sterilize lime at 60-100 degrees C under low temperature. The obtained lime is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material, and then dried, cooled and packaged to obtain the final product. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and high water absorbing resin (0.5-5).
NOVELTY - Processing attapulgite involves stirring acidified attapulgite, where obtained attapulgite is dried in microwave at 60-100 degrees C for sterilization. The dried attapulgite is cooled and then packed. Attapulgite comprises (in wt.%): acidified attapulgite (10-35), acidified slurry (15-50), high viscosity attapulgite clay (2-15), peat (2-15), biogas slurry (2-10), plant fiber (1-10), vermiculite (0.5-5), perlite (0.5-5) and super absorbent resin (0.1-5).    USE - Method for processing attapulgite (claimed) used for providing nutrition to plant and reducing pathogenic bacteria and harmful pest.    ADVANTAGE - The method enables to process attapulgite in simple and eco-friendly manner.
NOVELTY - The device has a main body filled with polycaprolactone (PCL) granule particle. Average diameter of the PCL granule particle is 3-3. 5 mm. Specific surface area of the PCL granule particle is 0. 87m2/L. Real density of the PCL granule particle is 1.12 kg/L. Fill density of the PCL granule particle is 0.74kg/L.    USE - PCL sewage denitrification treatment device.    ADVANTAGE - The device ensures better nitrogen removing effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a PCL sewage denitrification treatment device.
NOVELTY - Resolution of racemic amino alcohol to obtain optically pure amidogen D-tartrate and optically pure amidogen hydrochloride involves reacting 2 eq of amidogen racemic alcohol and 1 eq of tartaric acid dissolved in D-alcohol, under ice cooling, adding 1 eq of concentrated hydrochloric acid at room temperature, stirring continued until the reaction is complete; washing the filter cake with alcohol and drying to obtain (1R, 4S)-tartaric acid salt of D-amino alcohols; collecting the filtrate after spin-dried, and recrystallizing with alcohol, to obtain (1S, 4R)-amidogen hydrochloride.    USE - For resolution of racemic amino alcohol to obtain optically pure amidogen D-tartrate and optically pure amidogen hydrochloride (claimed), which is useful for preparation of abacavir and dacarbazine.    ADVANTAGE - The method allows preparation of product (i.e. optically pure amidogen D-tartrate and optically pure amidogen hydrochloride) with high yield, high purity and stable quality, has little environment pollution, low cost and allows easy industrial production, and the prepared optical pure amidogen alcohol D-tartrate and optical pure amidogen hydrochloride can be directly used for preparation of abacavir and dacarbazine, without desalting.    DETAILED DESCRIPTION - Resolution of racemic amino alcohol to obtain optically pure amidogen D-tartrate having formula (III) and optically pure amino alcohol hydrochloride having formula (IV) involves reacting 2 eq of amidogen racemic alcohol and 1 eq of tartaric acid dissolved in D-alcohol, under ice cooling, adding 1 eq of concentrated hydrochloric acid at room temperature, stirring continued until the reaction is complete; washing the filter cake with alcohol and drying to obtain (1R, 4S)-tartaric acid salt of D-amino alcohols (III); collecting the filtrate after spin-dried, and recrystallizing with alcohol, to obtain (1S, 4R)-amidogen hydrochloride (IV).
NOVELTY - Fondaparinux decanoate derivatives (I) are new.    USE - Used as a fondaparinux decanoate derivative (I).    ADVANTAGE - The method: produces a high yield and high purity product without purification step; and is carried out in a simple and cost efficient manner.    DETAILED DESCRIPTION - Fondaparinux decanoate derivatives of formula (I) are new.    R = substituted benzyl;    R1 = substituted alkyl; and    R2 = H+, Na+, K+ or Ca2+.    INDEPENDENT CLAIMS are also included for:    (1) a fondaparinux derivative of formula (II);    (2) preparation of (I);    (3) preparing (II) by sulfonating (I) at 50 degrees C in pyridine with sulfur trioxide/pyridine for 18 hours; and    (4) preparing fondaparinux sodium decanoate comprising catalytically hydrogenating (II) using palladium hydroxide or palladium on carbon catalyst in methanol and water.
NOVELTY - Generating one or more cellulosic-renewable identification numbers, comprises: thermally processing a cellulosic biomass to form a renewable fuel oil; and co-processing the renewable fuel oil with a petroleum fraction as reactants in a refinery conversion unit to form a cellulosic-renewable identification number-compliant fuel.    USE - The process is useful for generating one or more cellulosic-renewable identification numbers form a cellulosic-renewable identification number-compliant fuel, preferably a transportation fuel, a diesel fuel, a jet fuel, a gasoline, a heating oil (all claimed), liquid petroleum gas (LPG) and light cycle oil (LCO), where the fuel is useful in an internal combustion engine of a vehicle.    ADVANTAGE - The process is capable of generating the cellulosic-renewable identification number-compliant fuel with high yield and flash point via rapid thermal processing of the cellulosic feedstock.
NOVELTY - The process involves subjecting carbon monoxide to water-gas shift conversion in presence of a hot carbon dioxide sorbent and water vapor by contacting part of pyrolysis gas obtained by condensing a gaseous stream before recycling gas to subject a biomass feedstock in a pyrolysis reactor (5). A spent sorbent is supplied to a regenerator (7) to regenerate the sorbent and to obtain hot regenerated carbon dioxide sorbent, where subjecting of carbon monoxide is performed by mixing the hot regenerated carbon dioxide sorbent with a part of the pyrolysis gas or with another gaseous stream.    USE - Process for converting a forestry and agricultural waste stream biomass feedstock into a liquid hydrocarbon product i.e. pyrolysis oil.    ADVANTAGE - The process ensures that a small part of pyrolysis gas is typically purged so as to avoid too large pyrolysis gas recycle. The process enables obtaining hydrogen needed in a hydrode-oxygenation step by sorption-enhanced water-gas shift conversion of pyrolysis gas produced in the technique in an efficient and quick manner.    DETAILED DESCRIPTION - The pyrolysis gas is water-gas shifted pyrolysis gas. The gaseous stream is a hydrogen-rich gaseous stream.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating a process for converting a biomass feedstock into a liquid hydrocarbon product in regeneration of supplying steps of solid stream and spent sorbent.    Pyrolysis reactor (5)    Regenerator (7)    Condensing zone (11)    Pyrolysis oil (12)    Pyrolysis gas (13)
NOVELTY - This utility new type claims a one life garbage harmless processing system, comprising garbage sorting mechanism, the anaerobic and aerobic biological organic fertilizer mechanism, waste incineration and flue gas purifying mechanism mechanism, sorting mechanism, the anaerobic and aerobic biological organic fertilizer mechanism, waste incineration and flue gas purification mechanism through conveying belt mechanism are integrally connected, garbage sorting mechanism and a garbage anaerobic and aerobic made biological organic fertilizer mechanism, burning mechanism connecting the smoke purification and waste incineration mechanism connecting mechanism. The processing system by conveyor belt are integrally connected, automatic operation, labour and time, can the household garbage systematization process, there is no tail, can most of the domestic garbage, organic matter is made of biological organic fertilizer, the plastic film a; furnace with a hot air and marsh gas combustion-supporting, furnace high temperature, complete combustion, a dioxin splitting the flue gas purification mechanism set with a smoke pneuma cooler, capable of preventing the dioxin formation, for environment-friendly, without second pollution, the system is especially fit town and in small municipal use.
NOVELTY - The system has a condensation unit (7) that cools the cathode waste gas discharged from the cathode of fuel cell stack (1), and condenses water content. The condensation unit is a first heat exchanger (13) heat-exchanged with the cathode waste gas by using the oxidizing agent gas of oxidizing agent gas supply line (23) as a coolant. An adjustment unit adjusts the quantity of the water content condensed by the condensation unit independently of the oxidizing agent gas volume supplied to the fuel cell stack is provided.    USE - System for generating fuel cell power.    ADVANTAGE - Since the air temperature and electric power generation amount change, the water of a quantity required for an electric power generation is recoverable. Hence, the fuel cell power generation system with high generating efficiency is provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the direct methanol type fuel cell power generation. (Drawing includes non-English language text)    Fuel cell stack (1)    Condensation unit (7)    First heat exchanger (13)    Oxidizing agent gas supply line (23)    Cathode waste gas line (24)
NOVELTY - Application of bulk fertilizer comprises digging pits, burying straw crop chunks, adding fertilizer A, burying cereal crops, adding fertilizer B, burying grass and leguminous crop, and adding fertilizer C. Fertilizer A comprises 80 pts. wt. fermented chicken manure, 40 pts. wt. modified starch, 30 pts. wt. phosphate rock, red powder and zeolite powder mixture, 20 pts. wt. biogas, 20 pts. wt. diesel and soybean meal mixture and 10 pts. wt. fulvic acid.    USE - Method applying bulk fertilizer used for extending fertilizer effect (claimed).    ADVANTAGE - The method is simple, fast and convenient.    DETAILED DESCRIPTION - Application of bulk fertilizer comprises digging pits, burying straw crop chunks, adding fertilizer A, burying cereal crops, adding fertilizer B, burying grass and leguminous crop, and adding fertilizer C. Fertilizer A comprises 80 pts. wt. fermented chicken manure, 40 pts. wt. modified starch, 30 pts. wt. phosphate rock, red powder and zeolite powder mixture, 20 pts. wt. biogas, 20 pts. wt. diesel and soybean meal mixture, 30 pts. wt. potassium sulfate and 10 pts. wt. fulvic acid. Fertilizer B comprises 100 pts. wt. fermented chicken manure, 50 pts. wt. modified starch, 40 pts. wt. phosphate rock, red powder and zeolite powder mixture, 40 pts. wt. biogas, 50 pts. wt. potassium sulfate, 40 pts. wt. diesel and soybean meal mixture, and 30 pts. wt. fulvic acid. Fertilizer C comprises 90 pts. wt. fermented chicken manure, 45 pts. wt. modified starch, 35 pts. wt. phosphate rock, red powder and zeolite powder mixture, 40 pts. wt. potassium sulfate, 30 pts. wt. biogas, 30 pts. wt. diesel and soybean meal mixture, and 20 pts. wt. fulvic acid.
NOVELTY - Preparing iridium oxide catalyst comprises (a) dissolving sodium hydroxide in deionized water, adding chloroiridic acid to obtain first solution; (b) placing the first reaction solution in an oil bath, cooling the reaction to room temperature with stirring, to obtain second solution; (c) adding an acid into the second solution, adjusting the pH, centrifuging, and drying, to obtain iridium hydroxide; and (d) calcining the mentioned iridium hydroxide in an air atmosphere.    USE - The iridium oxide catalyst is useful for electrolysis of water (claimed).    ADVANTAGE - The preparation method is simple and has controllable conditions. The catalyst has high catalytic activity and stability, achieves oxygen dissolution reaction area specific activity of 84.37 mA/cm2.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for iridium oxide catalyst, prepared as mentioned above.
NOVELTY - Preparing alkaline fertilizer comprises adding bean dregs, chicken manure and traditional Chinese medicine into a reaction container, uniformly mixing, adding 0.5 kg of ammonium bicarbonate, 0.15 kg of potassium chloride, 0.025 kg of zinc sulfate, 2.5 kg of human waste, 1 kg of cattle manure, 5 kg of pig manure and 20 kg of rutile powder to the mixture, uniformly stirring the mixture, covering the mixture using a thin film, fermenting the mixture for 20-25 days, placing the mixture into a plastic bottle, embedding the plastic bottle in soil, screwing the bottle, and slowly permeating.    USE - The method is useful for preparing alkaline fertilizer (claimed).    ADVANTAGE - The method simply and conveniently prepares the alkaline fertilizer with reduced cost.    DETAILED DESCRIPTION - Preparing alkaline fertilizer comprises adding bean dregs, chicken manure and traditional Chinese medicine having a ratio of 12:6:100 (preferably 6:4:100) into a reaction container, uniformly mixing, adding 0.5 kg of ammonium bicarbonate, 0.15 kg of potassium chloride, 0.025 kg of zinc sulfate, 2.5 kg of human waste, 1 kg of cattle manure, 5 kg of pig manure and 20 kg of rutile powder to the mixture, uniformly stirring the mixture, covering the stirred mixture using a thin film, fermenting the mixture for 20-25 days, placing the fermented mixture into a plastic bottle, embedding the plastic bottle in soil, screwing the bottle, and slowly permeating.
NOVELTY - Synergistic complex fertilizer comprises 0.1-100 pts. wt. synergistic agent, 0.3-7000 pts. wt. biological preparation, 1-200 pts. wt. calcium sulfate, 5-500 pts. wt. sodium silicate, 2-8000 pts. wt. complex fertilizer. The synergistic agent is composed of potassium humate, polyaspartic acid salts, chitosan, non-ionic polyacrylamide, polypropylene potassium and polysilicon potassium. The biological preparation is composed of e.g. nitrogen-fixing bacteria, phosphate-solubilizing bacteria, potassium-solubilizing bacteria, and photosynthetic bacteria.    USE - Used as synergistic complex fertilizer.    ADVANTAGE - The fertilizer can effectively improve use rate and water retention rate, promotes crop growth, increases anti-cropping effect, provides resistance to disease, and is environmentally friendly.    DETAILED DESCRIPTION - Synergistic complex fertilizer comprises 0.1-100 pts. wt. synergistic agent, 0.3-7000 pts. wt. biological preparation, 1-200 pts. wt. calcium sulfate, 5-500 pts. wt. sodium silicate, 2-8000 pts. wt. complex fertilizer. The synergistic agent is composed of potassium humate, polyaspartic acid salts, chitosan, non-ionic polyacrylamide, polypropylene potassium and polysilicon potassium. The biological preparation is composed of nitrogen-fixing bacteria, phosphate-solubilizing bacteria, potassium-solubilizing bacteria, photosynthetic bacteria, actinomycetes and saccharomycetes, and Bacillus. The viable count of beneficial microorganism is more than 2000000000/g.
NOVELTY - Grape fertilizer comprises 75-85 pts. wt. organic fertilizer, 5-15 pts. wt. inorganic fertilizer, 3-10 pts. wt. trace elements, 0.1-0.5 pts. wt. composite fermentation bacteria, 1-2 pts. wt. enzymatic microorganism, 2-6 pts. wt. humic acid, 1-5 pts. wt. amino acid and 1-2 pts. wt. Pseudomonas strain HN103 components.    USE - Used as grape fertilizer.    ADVANTAGE - The fertilizer is environment-friendly (claimed); utilizes agricultural waste as raw materials; provides the nutrients required by grape plant; and solves the production of heavy metals and organic pollutant matter.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising (i) taking organic fertilizer, inorganic fertilizer, trace elements, composite fermentation bacteria, enzymatic microorganism, humic acid, chitosan oligosaccharide and biological bacteria shell; (ii) uniformly mixing composite fermentation bacteria and water in a weight ratio of 1:5-50, and diluting the bacterial liquid; (iii) adding organic fertilizer into the diluting liquid, uniformly mixing, stacking into pile, circulating, fermenting for 10-15 days to meet the basic decomposition of state, to obtain first-stage fermentation product; (iv) adding enzymatic microorganisms into the first-stage fermentation product, completely decomposing while fermenting, drying at low temperature, and crushing to obtain second-level fermentation product; and (v) adding inorganic fertilizer, trace elements, humic acid, chitosan oligosaccharide and biological bacteria shell, and uniformly mixing, and granulating into spherical product, and sorting the product.
NOVELTY - Purifying carbon nanotubes comprises (a) providing a carbon nanotube substrate, (b) primarily washing the carbon nanotube substrate with an acid, preferably aqueous acid having at least one of acid radical anions (A1) and (b2) optionally washing of the intermediate product obtained in step (b) with an additive-free solvent, (c) secondarily washing the carbon nanotube substrate with a solution having replacement anions (A2), (c2) optionally further washing the product obtained in step (c) with an additive-free solvent, and (d) isolating the purified carbon nanotubes.    USE - The method is useful for purifying carbon nanotubes, which are useful for production of: composites for packaging or transport material of electronic components; batteries, preferably lithium ion batteries; and electrodes for electrochemical processes or fuel cells (all claimed).    ADVANTAGE - The method simply, rapidly and economically purifies the carbon nanotubes with high yields, low amorphous carbons and good electrical conductivity.    DETAILED DESCRIPTION - Purifying carbon nanotubes comprises (a) providing a carbon nanotube substrate, (b) primarily washing the carbon nanotube substrate with an acid, preferably aqueous acid having at least one of acid radical anions (A1) and (b2) optionally washing of the intermediate product obtained in step (b) with an additive-free solvent, (c) secondarily washing the carbon nanotube substrate with a solution, where the solution has replacement anions (A2) of the acid radical anions (A1) of the acid of different type, and the mole fraction of the replacement anions (A2) in the solution is greater than the mole fraction of the anions (A1) in the solution in step (c), (c2) optionally further washing the product obtained in step (c) with an additive-free solvent, and (d) isolating the purified carbon nanotubes.
NOVELTY - An L-aspartate oxidase variant having an amino acid sequence of which a 302nd amino acid in a defined sequence of 540 amino acids (SEQ ID NO. 1), given in the specification, is substituted with another amino acid, is new.    USE - The L-aspartate oxidase variant is useful for transforming a microorganism, where the microorganism is useful for producing quinolinate and nicotinic acid (all claimed).    ADVANTAGE - Quinolinate may be effectively produced by culturing a microorganism including a L-aspartate oxidase variant that the feedback regulation by nicotinic acid or NAD. Nicotinic acid is released. These methods using the microorganism may solve the problems from the conventional chemical synthesis methods, regarding environmental issues due to generation of catalyst byproducts, high-energy consumption and use of non-renewable resources, and the problem of low yield with the conventional biosynthesis methods. These methods may efficiently produce quinolinate and nicotinic acid in an environmental-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a polynucleotide comprising a nucleotide sequence that encoding an amino acid sequence which a 302nd amino acid in an amino acid sequence represented by SEQ ID NO. 1 is substituted with another amino acid;    (2) a vector comprising the polynucleotide of (1) which is operably linked to a regulatory sequence;    (3) a microorganism comprising the polynucleotide of (1);    (4) a method of producing quinolinate by culturing the microorganism of (3) in a medium; and recovering quinolinate from the cultured medium; and    (5) a method of producing nicotinic acid by culturing the microorganism of (3) in a medium; and conducting a decarboxylation reaction by adding an acid to the cultured medium.
NOVELTY - Improvement of soil aggregate structure using special fertilizer comprises inserting fertilizer in soil, adding corn starch and water, heating at 70-75 degrees C for 1 hour, cooling to 45 degrees C and spraying. Special fertilizer comprises adsorbent, heavy calcium carbonate, water retention agent, chicken manure, peat soil, calcium dihydrogen phosphate, solubilizing bacteria, urea, fermenting bacteria, Bacillus and phytase.    USE - Method for improving soil aggregate structure using special fertilizer (claimed), promoting plant growth and reducing salt quantity in soil.    ADVANTAGE - The method is simple and convenient.
NOVELTY - Dispersible tablet comprises (in pts.wt.): amoxicillin and clavulanate potassium powder (100), film coating agent (10-20), and filler (20-40).    USE - Dispersible tablet.    ADVANTAGE - The dispersible tablet is prepared in a simple, convenient, and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing dispersible tablet, which involves:    (A) mixing amoxicillin and clavulanate potassium powder with coating agent uniformly to obtain mixed product;    (B) adding filler in the obtained product in adequate amount to obtain resultant product;    (C) adding disintegrating agent, lubricant or flavoring agent uniformly to obtain final product; and    (D) tableting the obtained product to obtain desired product.
NOVELTY - Skin exfoliant comprises silk fibroin gel and carbonized rice husk powder at 10 ml:1 g-10 ml:1.5 g ratio.    USE - Skin exfoliant.    ADVANTAGE - The skin exfoliant has simple preparation and good exfoliating effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of skin exfoliant comprising adding 0.1-0.8 wt./vol.% sericin solution to 4-10 wt./vol.% fibroin protein and/or adding carboxymethyl chitosan solution as gel accelerator, uniformly mixing to obtain 0.1-0.5 wt./vol.% solution, standing at 20-80 degrees C to obtain silk fibroin gel, adding rice husk into a clean flat ceramic basin, high temperature carbonizing at 160-220 degrees C for 3-10 hours, cooling, grinding to obtain rice husk carbide powder, sieving by 80-100-mesh sieve, homogeneously mixing the prepared silk fibroin gel and carbonized rice husk to prepare into paste, and obtaining the product.
NOVELTY - The device has dehydration tower (1), methyl alcohol removing tower (2), pressurized column (3), methanol reflux column (4), condenser (5), reflux tank (6), return pump (7) and reboiler (8) which are connected in turn through pipeline. The bottom of reboiler is set with dehydration discharge pipe and discharging pump. The bottom of methyl alcohol removing tower is also set with a discharging pipe and a discharging pump. The return pump outlet is connected to tower top set with branch pipe. The pressurizing tower is connected with methanol reflux column.    USE - Methylal refining process device for production of glyphosate by-product using glycine method.    ADVANTAGE - The methylal refining process is performed so that waste discharge and environment pollution are reduced, and the production of glyphosate by-product is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methylal refining process method for production of glyphosate by-product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the methylal refining process device for production of glyphosate by-product.    Dehydration tower (1)    Methyl alcohol removing tower (2)    Pressurized column (3)    Methanol reflux column (4)    Condenser (5)    Reflux tank (6)    Return pump (7)    Reboiler (8)
NOVELTY - Use of adsorbent is claimed for treating biological wastewater in a fixed bed reactor.    USE - Used for treating biological wastewater fixed bed reactor (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fixed bed reactor, which comprises water inlet, water outlet, absorbing layer, supporting layer, and inner reactor.
NOVELTY - The system has a main pipe provided with a dry pipe that is provided with a side pipe. A branch pipe is connected with the dry pipe along horizontal direction. A top surface of the branch pipe is formed with a cloth water hole and an inclined cloth water hole. The inclined cloth water hole is matched with the cloth water hole. An angle is formed between the inclined cloth water hole and the branch pipe for about 45 degrees. A bottom part of the branch pipe is formed with a drain hole. A mud discharge pipe is provided with a water outlet valve.    USE - Rural biological filter domestic sewage chamber-free reverse flushing cloth water system.    ADVANTAGE - The system is simple to mount, convenient to manage and simple in structure, and has convenient modular design, high uniformity, better fine processing effect and low energy consumption, and accurately controls a cloth water unit parameter and avoids blockage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rural biological filter domestic sewage chamber-free reverse flushing cloth water system controlling method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a rural biological filter domestic sewage chamber-free reverse flushing cloth water system.
NOVELTY - Preparing potassium-enriched solution involves mixing feldspar ore powder and calcium salt with water and then ground in a mill for 20 hours to obtain a solid-liquid mixture. The solid-liquid mixture is filtered to obtain final product.    USE - Method for preparing potassium-enriched solution (claimed).    ADVANTAGE - The method is simple, enables to prepare potassium-enriched solution which is activated at low temperature, and has wide industrial applicability.
NOVELTY - Recycling method involves utilizing salvage water hyacinth and then selecting root, stem part and leaves. The selected material is qualified and then the qualified material is cut into block. The salvage water hyacinth leaves and stem part are kept to obtain biomass and then water hyacinth stems and manure are mixed with water into marsh gas pool for anaerobic fermentation. The obtained material is stirred to obtain biogas liquid and biogas residue and then the obtained material is added with another portion of water hyacinth stems after dehydration and drying.    USE - Recycling method used for water salvage water hyacinth and animal manure material (claimed).    ADVANTAGE - The method enables to recycle water salvage water hyacinth and animal manure material with high efficiency, good environment for earthworms and higher yield and better quality of earthworm.    DETAILED DESCRIPTION - Recycling method involves utilizing salvage water hyacinth and then selecting root, stem part and leaves. The selected material is qualified and then the qualified material is cut into block. The salvage water hyacinth leaves and stem part are kept to obtain biomass and then water hyacinth stems and manure are mixed with water into marsh gas pool for anaerobic fermentation. The obtained material is stirred to obtain biogas liquid and biogas residue and then the obtained material is added with another portion of water hyacinth stems after dehydration and drying, where the weight ratio of water hyacinth stemsand biogas 2:1-3:1. The obtained material is fermented to obtain full maturity product and then the fermented product and water hyacinth biological carbon are mixed in weight ratio of 15:1-10:1 as the earthworm bait material. The obtained material is feeded into bed for breeding earthworms and then earthworms and earthworm manure are collected.
NOVELTY - Biological organic fertilizer additive comprises (in pts.wt.): bran (50), silkworm excrement (50), oligosaccharides (10), yeast (1) and water (150).    USE - Biological organic fertilizer additive.    ADVANTAGE - The biological organic fertilizer additive ahs good nutrition element, and ensures long fertilizer efficiency and fast growth of fruit and vegetable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological organic fertilizer additive, which involves:    (A) adding silkworm excrement and bran into in a fermentation jar;    (B) pouring the water into the fermentation jar for to leach for 5 hours;    (C) standing the fermentation jar 20-30 minutes;    (D) adding dry yeast and chitosan into the fermentation jar for carrying out fermentation for 30 days for forming acid; and    (E) filtering the fermentation liquid to obtain the finished product.
NOVELTY - Fertilizer fermentation device comprises fermenting pool (1), where fermentating pool is provided with discharge port (9) and track (2). The track is mounted transversely on moving platform (3). The platform is provided with wheel (4) and driving motor (19). The platform is provided between first hydraulic pressure jar (18) and roller (6). The roller and driving motor are connected with stir pole, where stir pole is provided with material plate. The material plate is provided with cross beam (10), which is mounted below baffle material door (11).    USE - Fertilizer fermentation device.    ADVANTAGE - The fertilizer fermentation device is efficient and enables continuous production of fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fertilizer fermentation device.    Fermenting pool (1)    Track (2)    Moving platform (3)    Wheel (4)    Roller (6)    Discharge port (9)    Cross beam (10)    Baffle material door (11)    Hydraulic pressure jar (18)    Driving motor (19)
NOVELTY - Organic fertilizer comprises (in pts.wt.): sawdust and red stone mass ratio (20:1) mixture (400-500), animal viscera powder (30-50), crab shell powder (80-120), calcium superphosphate (50-80), bentonite and boric acid mass ratio (100:1) mixture (40-60), calamine powder (10-30) and clover powder (80-120).    USE - Organic fertilizer used for improving selenium content in crop (claimed).    ADVANTAGE - The organic fertilizer increases crop production by 35% as compared to traditional fertilizer and selenium content by 18-22%.
NOVELTY - Organic fertilizer comprises (in pts.wt.): bran (25-35), fermented silkworm excrement (25-40), high temperature-treated chicken manure (10-15), phosphate fertilizer (5-10) and potassium fertilizer (5-10).    USE - Organic fertilizer used for growing fruits and vegetables.    ADVANTAGE - The organic fertilizer shortens culture time and reduces cultivation cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) fermenting silkworm excrement with chitosan oligosaccharide and dry yeast for 15 days to obtain fermented silkworm excrement;    (B) fermenting crushed sugarcane leaves with wetting agent, filter, calcium superphosphate, rice bran and gypsum to obtain bran;    (C) heating chicken manure with brown sugar, metal complexing agent and water;    (D) mixing bran, fermented silkworm excrement, high temperature-treated chicken manure, phosphate fertilizer and potassium fertilizer to obtain mixture; and    (E) granulating obtained mixture to obtain organic fertilizer that is dried.
NOVELTY - Organic fertilizer comprises (in pts.wt.): bran (25-35), fermented silkworm excrement (25-40), high temperature-treated fish scale (10-15), phosphate fertilizer (5-10) and potassium fertilizer (5-10).    USE - Organic fertilizer used for growing fruits and vegetables.    ADVANTAGE - The organic fertilizer shortens culture time and reduces cultivation cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) fermenting silkworm excrement with chitosan oligosaccharide and dry yeast for 15 days to obtain fermented silkworm excrement;    (B) fermenting crushed sugarcane leaves with wetting agent, filter, calcium superphosphate, rice bran and gypsum to obtain bran;    (C) heating fish scale with brown sugar and water;    (D) mixing bran, fermented silkworm excrement, high temperature-treated fish scale, phosphate fertilizer and potassium fertilizer to obtain mixture; and    (E) granulating obtained mixture to obtain organic fertilizer that is dried.
NOVELTY - Bio-organic fertilizer comprises (in wt.%): water soluble nitrogen, phosphate and potash fertilizer (10-25), bio-filler (15-25), biological bacteria (1-5), ferrous sulfate (1-3), humic acid (1-15) and balanced amount of molasses alcohol waste liquid.    USE - Bio-organic fertilizer used for planting lotus (claimed) and preventing lotus root decay disease.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer , which involves fermenting raw materials for 16-28 hours, where fermented product is stirred and then dried to obtain product.
NOVELTY - Liquid culture composition comprises Bacillus subtilis powder (10-30 g), potassium dihydrogen phosphate (1-2 g) and indomethacin (0.5-1 g), where the content of Bacillus subtilis in Bacillus subtilis powder is 1x 1010- 1x 1012 unit/g.    USE - Liquid culture composition for Forsythia seedlings (claimed) for root promoting, for promoting side root, and for promoting growth.    ADVANTAGE - The liquid culture composition shows improved soil fertilization and permeability.
NOVELTY - Special fertilizer comprises (in pts.wt.): Bacillus mucilaginosus liquid (20), Bacillus subtilis liquid (10-20), beans (40-50), corn (35-45), potassium nitrate (1-7), urea (2-6), anhydrous sulfuric acid (1-5), borax (2-8), matrine (0.1-0.5) and gibberellin, (0.2-0.8).    USE - Special fertilizer for solanaceous vegetable (claimed).    ADVANTAGE - The special fertilizer improves quality of solanaceous vegetable, increases yield and reduces plant diseases and insect pests.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing special fertilizer, which involves using Bacillus mucilaginosus liquid, Bacillus subtilis liquid, beans, corn, potassium nitrate, urea, anhydrous sulfuric acid, borax, anhydrous sulfuric acid, matrine and gibberellins.
NOVELTY - Fertilizer synergistic biological additive preparation involves utilizing microbial agent, red clover sugar syrup (200-400 milliliter) and water. The obtained mixture is fermented, where the microbial agent is stored in liquid culture medium (10-30 milliliter). Microbial agent is prepared by inoculating microorganism microbial inoculum of Bacillus megaterium and Bacillus cereus in liquid culture medium. The obtained culture medium is cultured, and then activated to obtain microbial agent. Fresh alfalfa and sugar is weighed. The weighed sucrose is dissolved in water.    USE - Method for preparing fertilizer synergistic biological additive (claimed).    ADVANTAGE - The method enables to produce the product that has improved phosphorus content in soil, phosphorus absorption and crop yield.    DETAILED DESCRIPTION - Fertilizer synergistic biological additive preparation involves utilizing microbial agent, red clover sugar syrup (200-400 milliliter) and water. The obtained mixture is fermented, where the microbial agent is stored in liquid culture medium (10-30 milliliter). Microbial agent is prepared by inoculating microorganism microbial inoculum of Bacillus megaterium and Bacillus cereus in liquid culture medium. The obtained culture medium is cultured, and then activated to obtain microbial agent. Fresh red clover plant and sugar is weighed. The weighed sucrose is dissolved in water. The obtained sucrose solution is mixed with red clover plant, and then mixed with water (1 liter) to obtain red clover sugar syrup. The obtained microbial agents and red clover sugar syrup are mixed with water at 30 degrees C for 24 hours, and then filtered through a double gauze filter. The volume of the mixture is adjusted to 1 liter using water to obtain biological additive.
NOVELTY - Fertilizer comprises (in pts.wt.): urea (35-43), diammonium phosphate (35-42), potassium chloride (18-25), corn core (30-40), fulvic acid (5-8) and humic acid (25-30).    USE - Fertilizer used as base fertilizer for planting wheat (claimed).    ADVANTAGE - The fertilizer is cost-effective and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing corn core, fulvic acid, humic acid with urea, diammonium phosphate and potassium chloride uniformly;    (B) adding water (50-55%) to the obtained material;    (C) fermenting the obtained material for 10-12 days at 36-42 degrees C;    (D) adding the remaining urea, diammonium phosphate and potassium chloride to the fermented fertilizer;    (E) mixing the obtained mixture uniformly;    (F) granulating the obtained material; and    (G) drying the obtained material to obtain the desired product.
NOVELTY - Fertilizer comprises (in pts.wt.): adsorbent (5-10), calcium carbonate (10-20), water retention agent (10-20), mass ratio of chicken manure and peat soil 20: 1 (40-50), monocalcium phosphate (1-2), urea (3-4), and mass ratio of fermentation bacteria, Bacillus and phytase (5:2:1) (1-2).    USE - Fertilizer used for improving soil aggregate structure (claimed) and promoting growth of plant root.    ADVANTAGE - The fertilizer enhances water retention ability and activity of microorganism and reduces salt content in soil.
NOVELTY - Organic fertilizer comprises (in pts.wt.): mixture of clay and sepiolite in the mass ratio of 4:1 (5-10), dehydroacetic acid (10-20), grass seed (10-20), dry cow dung (40-50), a mixture of sawdust and straw legume powder in the mass ratio of 1:5 (30-50), phosphate solubilizing bacteria (1-2), rock phosphate (2-4) and fermenting bacteria (1-2).    USE - Organic fertilizer used for improving soil salinity (claimed).
NOVELTY - Preparation of beta -hydroxyethylsulfonyl sulfate aniline involves sulfonating acetanilide and chlorosulfonic acid in presence of chlorinated inhibitor, performing chlorination reaction with thionyl chloride, obtaining chlorosulfonated compound, and sequentially carrying out reduction reaction, condensation reaction and esterification reaction.    USE - Preparation of beta -hydroxyethylsulfonyl sulfate aniline (claimed).    ADVANTAGE - The method provides beta -hydroxyethylsulfonyl sulfate aniline by an environmentally-friendly process with reduced generation of chloroacetanilide by-products.
NOVELTY - Neohesperidin as starting material is subjected to hydrogenation reaction using methanol and ethanol as reaction medium, and sodium borohydride and potassium borohydride as reducing agent, heated and solvent is evaporated to obtain crude neohesperidin dihydrochalcone.    USE - Synthesis of neohesperidin dihydrochalcone (claimed).    ADVANTAGE - The method provides neohesperidin dihydrochalcone with high yield and high quality, by simple, economical and environmentally-friendly process.
NOVELTY - Fruit tree soil conditioner comprises 1.2-3.6 wt.% siliceous petrochemical powder, 5.8-9.2 wt.% amino acid powder, 10.6-17.8 wt.% potassium dihydrogen phosphate, 10.6-19.8 wt.% diammonium phosphate, 3.6-7.6 wt.% boron/zinc/potassium/calcium, 15.8-42.3 wt.% potassium, 7.8-13.6 wt.% biochemical fulvic acid, 16.8-23 wt.% crushed soybean and 3.2-6.6 wt.% urea.    USE - Fruit tree soil conditioner.    ADVANTAGE - The fruit tree soil conditioner is efficient and provides high quality fruits. It softens and loosens soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of fruit tree soil conditioner comprising mixing raw materials, fermenting for 7-15 days, performing enzymolysis, diluting, and performing foliar spraying for every 30-60 days.
NOVELTY - An estrogen-degrading Serratia marcescens with preservation number CGMCC No. 1.12941 is new.    USE - An estrogen-degrading Serratia marcescens for treating sewage and solid wastes i.e. feces (claimed).    ADVANTAGE - The product can be applied directly in water and manure to be treated, and has high degradation rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of estrogen-degrading S. marcescens small bead immobilized repairing inoculant.    DESCRIPTION OF DRAWING(S) - The drawings show transmission electron micrographs of estrogen-degrading Serratia marcescens colony.
NOVELTY - Obtaining lignocellulosic residues involves treating bagasse feedstock with hydro-ethanolic in a sealed reactor at 160-200 degrees C for 30-90 minutes to obtain pretreated-solution. The pretreated-solution is then reacted with deionized water to obtain precipitated material. The precipitated material is dissolved in buffer, and then treating with cellulase to obtain an enzymatic hydrolyzed solution comprising residues such as xylooligosaccharide, lignin and glucose as desired lignocellulosic residues.    USE - Method for obtaining lignocellulosic residues from bagasse feedstock (claimed).    ADVANTAGE - The method enables to obtain lignocellulosic residues such as xylooligosaccharide, lignin and glucose by promoting saccharification efficiency in an eco-friendly and economical manner.
NOVELTY - Preparation of fertilizer comprises taking 3 fresh broken egg shell, 500 g crushed hay, 900 g rice water, 900 g fermented cow manure and 1 kg plant ash, feeding into container, sealing, fermenting for 10-25 days, adding 5 kg rice water, fermenting for 5-8 days, filtering, recrystallizing to obtain 13-18 g crystals, packing, sealing and storing in dark room.    USE - Method for preparing fertilizer used for indoor flowering plant (claimed).    ADVANTAGE - The method can change allocation of raw materials based on soil pH to meet different kinds of flowers need.
NOVELTY - Fertilizer for indoor flower nursery, and its production method and use, are claimed. The fertilizer comprises fresh broken egg shell, crushed hay, rice water, waste milk, fermented chicken and ash. The fertilizer is prepared by uniformly mixing the raw materials in wide-mouth container, sealing container with plastic film, placing container in sun for 10-25 days until no bubbles is formed, injecting fresh air into the container, further adding rice water to the container, fermenting, filtering mixture, recrystallizing filtrate, sealing and storing product.    USE - Te fertilizer is useful for indoor flower nursery (claimed).    ADVANTAGE - The fertilizer improves growth of plants.    DETAILED DESCRIPTION - Fertilizer for indoor flower nursery, and its production method and use, are claimed. The fertilizer comprises 4 fresh broken egg shell, 0.5 kg crushed hay, 900 g rice water, 100 g waste milk, 500 g fermented chicken and 1 kg ash. The fertilizer is prepared by uniformly mixing the raw materials in wide-mouth container, sealing container with plastic film, placing container in sun for 10-25 days until no bubbles is formed (for fermentation), injecting fresh air into the container, further adding 5 kg rice water to the container, fermenting for 5-8 days, filtering mixture, recrystallizing filtrate, sealing and storing product. The fertilizer is mixed with 20-30 g charcoal residue, and applied to plant.
NOVELTY - Method for converting an algal biomass to a carbon-based chemical, involves contacting the algal biomass with a microbial culture for a period of time at an initial temperature and an initial pH, thus producing an amount of the carbon-based chemical.    USE - The methods are useful for converting an algal biomass to a carbon-based chemical and producing lactic acid from algal biomass material. The carbon-based chemical is carboxylic acid, preferably lactic acid or its salt or ester, or alcohol, preferably ethanol (all claimed).    ADVANTAGE - The method is cost-effective to perform, consumes less time, reduces risk of contamination from other microorganisms, and utilizes easily available components.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing lactic acid from algal biomass material converting the algal biomass material to lactic acid in a single step process, which involves (a) culturing and growing algae in a liquid medium to a desired algae biomass, (b) combining a microbial culture and the algal biomass, and (c) fermenting the algal biomass under conditions and for a period of time sufficient to produce lactic acid, or its salt or ester, and optionally (d) isolating the lactic acid, or its salt or a ester.
NOVELTY - The method comprises introducing a drying gas into a biomass containing oxidation-sensitive recyclable materials and then drying. The oxidation-sensitive recyclable materials are unsaturated fatty acid that is omega 3 fatty acid and omega 6 fatty acid. The drying step is accomplished in a fluidized bed at a temperature of 45-95 degrees C, preferably 50-60 degrees C. The drying gas has an oxygen content of less than 20 wt.%, preferably 8-13 wt.%. The biomass is in the form of a fermentation broth with a solids content of 10-50 wt.% (preferably 20-40 wt.%), and is transferred into a granulate.    USE - The method is useful for drying a biomass, which is useful in a feed or food (claimed) for humans and animals such as fish i.e. salmon fish and shellfish.    ADVANTAGE - The dried biomass has desired particle size and improved strength.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a particulate biomass.
NOVELTY - Manufacture of mesoxalic-acid compound (2) or its hydrate involves reacting malonic acid compound (1) with chlorine dioxide.    USE - Manufacture of mesoxalic-acid compound or its hydrate e.g. mesoxalic-acid diester used in pharmaceutical and agrochemical applications, and for manufacturing pyrazin-2-one-3-carboxylic acid ester derivative.    ADVANTAGE - The method enables safe, economical and environmentally-friendly manufacture of mesoxalic-acid compound, using easily-available chlorine dioxide having excellent handleability.    DETAILED DESCRIPTION - Manufacture of mesoxalic-acid compound of formula (1) or its hydrate involves reacting malonic acid compound of formula (1) with chlorine dioxide.    R=alkyl, cycloalkyl, aryl or heteroaryl (all optionally substituted), or H.
NOVELTY - Pleurotus eryngii cultivation material comprises 10-20% sawdust, 35-40% rice bran meal, 12-27% bagasse, 16-30% wheat bran, 3-8% corn powder and 1-5% calcium carbonate. The preparation of the cultivation material comprises drying and mixing the raw materials to obtain mixed culture material for 5 minutes, pre-wetting and controlling the water content, stirring for at least 15 minutes until the water content is 65 plus minus 1% at a pH of 4-5 to obtain mixed culture material, extracting oil and removing solvent.    USE - Pleurotus eryngii cultivation material comprising rice bran meal.    ADVANTAGE - The culture material: ensures production rate and color of Pleurotus eryngii; and increases the nutritional value of P. eryngii. The method is simple; consumes less energy; can be carried out at room temperature; carries out defatting of rice bran meal at low temperature conditions with low residual oil, high protein content and high nitrogen dissolution index.
NOVELTY - Strawberry environmentally-friendly fertilizer comprises 70-80 pts. organic fertilizer, 10-25 pts. inorganic fertilizer, 0.5-1 pts. trace elements, 0.1-0.3 pts. complex fermentation strains, 1-2 pts. fermentation bacteria, 3-7 pts. humic acid, 3-7 pts. amino acid and 0.2-0.7 pts. antibiotic.    USE - Used as strawberry environmentally-friendly fertilizer.    ADVANTAGE - The fertilizer solves the problem of crop nutrient supply, and limits the propagation of pathogenic microorganisms.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising (i) taking the mentioned components; (ii) mixing the complex fermentation strain with water in the weight ratio of 1:5-50, to obtain diluted strain solution; (iii) adding organic fertilizer into the diluted strain solution, mixing, stacking in piles, turning and flipping, and fermenting for 10-15 days, to obtain primary fermented product; (iv) adding the fermentation bacteria into the fermented product, fermenting, drying at low-temperature, and pulverizing to obtain secondary fermented material; and (v) adding inorganic fertilizer, trace elements, humic acid, amino acids and antibiotic into the secondary fermented material, mixing, granulating in a ball mill, and sorting.
NOVELTY - Aerobic fermentation sludge treatment involves obtaining oxygen flow rate in an oxygen tube by using a sensor corresponding to a recovery feeding tube through connected aeration groove in an aeration section. The sensor is set with a feeding tube, where segment control system uses another dissolve oxygen sensor. The oxygen content is compared to a predetermined target oxygen content respectively, where the flow rate of target is adjusted through oxygen pipe according to oxygen content.    USE - Method for treating aerobic fermentation sludge (claimed).    ADVANTAGE - The increases homogeneity and fermentation effect.
NOVELTY - This new type utility claims one for butylene skeleton isomerization of a raw material extracting concentration device, comprising orderly connected a feeding mixer, the selective hydrogenation reactor, butane tower feed buffer tank and said isobutyl tower, wherein, a feeding mixer set with a raw material entrance and gas entrance, in the different butane tower feed buffer tank set with a flash device, and the outlet frame of the said butane tower heterogeneous of isobutyl inlet connected. A the active chemical property of 1.3-butadiene hydrogenation a n-butene and butane, which can reduce the energy consumption, at the same time, most-1 isomerization to-2, butene loss can be reduced in a subsequent of said isobutyl tower, increase olefin. At the same time, because of using the selective hydrogenation reactor, isobutyl tower can reduce the tower disk number, reducing the reflux ratio, futher saves the energy consumption.
NOVELTY - Inorganically-enhanced, bioorganic fertilizer with reduced bioorganic odor, comprises dried granules of one or more organic materials containing disinfected biosolids and nutrient mixture, where e.g. the (a) dried granules have dryness of more than 90%, and diameter of 3.5 mm and are coated with material to reduce dust formation, (b) the disinfected biosolids contain no active pathogens and organisms, and (c) the odors in the disinfected biosolids have been substantially reduced or eliminated during processing with the nutrient mixture.    USE - The inorganically-enhanced, bioorganic fertilizer is useful for treating biosolids, preferably organic-containing sludges and alkaline materials and converting them into useful inorganic-organic nutrient fertilizers.    ADVANTAGE - The fertilizer reduces odor from disinfected biosolids.    DETAILED DESCRIPTION - Inorganically-enhanced, bioorganic fertilizer with reduced bioorganic odor, comprises dried granules of one or more organic materials containing disinfected biosolids and nutrient mixture, where the (a) dried granules have dryness of more than 90%, and diameter of 3.5 mm and are coated with material to reduce dust formation, (b) the disinfected biosolids contain no active pathogens and organisms, (c) the odors in the disinfected biosolids have been substantially reduced or eliminated during processing with the nutrient mixture, (d) the nutrient mixture comprises nitrogen and one or more calcium, phosphorus, potassium, sulfur or iron, and (e) the nutrient mixture is reacted with chemical components of the organic materials such that the fertilizer does not require further modification or supplementation before use.
NOVELTY - This utility new type relates to a one propylene propane separating tower energy-saving heat exchange system, including separating tower (1), and the top outlet of the separating tower with a propylene conveying pipeline (2), the bottom of a separating tower set with propane mixture discharging pipeline (3), wherein the discharging pipeline (3) of a reboiler outlet (4) of tube pass entrance, the reboiler (4) pass outlet through a return pipeline (5) connecting the separating tower (1) of lower part of the reboiler (4) of the shell side entrance a steam turbine machine (6) of the steam outlet, the reboiler (4) shell side outlet of a condensed liquid discharging pipeline (7). And the existing technology, this utility new type the inner steam turbine machine and a separating tower through pipeline combine together, waste heat of exhaust valid use the steam turbine the produce of the propane mixture heating, energy saving and consumption reducing effect is good, and a two stage heat exchanger is omitted, device investment is reduced, at the same time a condensed water greatly saves dosage of exhaust gas, to power a 35000kw steam turbine machine of example, each for a save condensed water 9000 tons.
NOVELTY - The method involves conducting and storing a partial flow of sample gas i.e. carbon di-oxide, over a first molecular sieve i.e. zeolite, for long or short periods of time in a continuous manner or non-continuous manner. The sample gas is passed through a suitable catalyst in a second molecular sieve. Organic components i.e. methane components, of to-be detected gas sample in the catalyst are cracked, and the organic components are stored, where the catalyst includes Palladium-aluminum or iron-aluminum compounds.    USE - Method for qualified and quantitative distinction of fossil and biomass fuels in flue gas obtained from power plants based on C14 content in a laboratory.    ADVANTAGE - The organic components of the gas sample in the catalyst are cracked, and the organic components are stored, thus ensuring harmless, simple and inexpensive handling of an absorber designed as the molecular sieve, and simply dispatching and dividing the molecular sieve. The method ensures that the gas is bubbled in weak caustic soda so that the carbon dioxide is bound and technically treated in the laboratory for determining the proportionate C-14 portions.
NOVELTY - Fermenter (1) comprises: a bottom plate, walls and ceiling comprising: at least one substantially vertically oriented charging opening (3) for filling and removal of biomass (7); a gas charging opening in the closed state and liquid-tight-sealing closure; at least one heater arranged in the bottom plate with heating tubes, which can be flowed through by a heat carrier medium; and a percolate collection device (4) with collecting troughs in the bottom of the fermenter. The heating tubes are arranged in the collecting troughs.    USE - The fermenter is useful for producing biogas from biomass by the dry fermentation process (claimed).    ADVANTAGE - The fermenter: contains easily operating percolate collection device, and heater which has long life; and produces biogas in simple and cost efficient manner.    DESCRIPTION OF DRAWING(S) - The figure shows a sectional side view of the front part of an open fermenter.    Fermenter (1)    Biogas-removal opening (2)    Charging opening (3)    Percolate collection device (4)    Biomass (7)
NOVELTY - This new utility model claims of one of calcium chloride and potassium, natural gas as raw material realize resource comprehensive use and production system, including potassium hydroxide device, potassium carbon device, alkyne device, calcium carbide alkyne device, chlorine ethylene device, polyvinyl chloride device, synthesis ammonia device of urea device, methanol device, empty device and supply heat center. The utility model use new petroleum and natural gas as main raw material production PVC, each production device is tightly combined, products, and of the whole device, waste gas and waste residue can be one of the following device of raw material, resource can make full use, will eliminate pollutants in production process and technology, from radically at reducing or eliminate of pollute, realization of maximum and three-waste discharge and minimize the circulation economic model of resource use efficiency.
NOVELTY - A crystalline Form III or IIIa of fidaxomicin having powder X-ray diffraction pattern as given in specification, is new.    USE - In the pharmaceutical composition (claimed) as antibiotic agent.    ADVANTAGE - The polymorphic forms of fidaxomicin is prepared by environmentally-friendly, cost-effective, and industrially applicable manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Form IIIa of fidaxomicin.
NOVELTY - Method for preparing organic phosphorus fertilizer, involves pretreating raw materials, performing aerobic fermentation and aging to obtain product. The raw material comprises 70-95 wt.% pig manure, organic material decomposition agent having viable count of 50 million cells/g and phosphorus-containing acids to regulate pH to 5.5-8.5, where the organic material decomposition agent comprises (a) mixture of Bacillus subtilis, Aspergillus niger, (b) phosphate-solubilizing Bacillus sp. in a ratio of 80:1:19, and (c) manganese sulfate.    USE - The method is useful for preparing organic phosphorus fertilizer which is used for providing growth promoting effect.    ADVANTAGE - The method prepares product with reduced unpleasant odor, and exhibits increased phosphorus utilization rate and humus content and improved ventilation ability.    DETAILED DESCRIPTION - Method for preparing organic phosphorus fertilizer, involves pretreating raw materials, performing aerobic fermentation and aging to obtain product. The raw material comprises 70-95 wt.% pig manure with organic substance content of more than 60% and moisture content of 50-70%, organic material decomposition agent having viable count of 50 million cells/g and phosphorus-containing acids to regulate pH to 5.5-8.5, where the organic material decomposition agent comprises (a) mixture of Bacillus subtilis, Aspergillus niger, (b) phosphate - solubilizing Bacillus sp. in a ratio of 80:1:19, and (c) manganese sulfate.
NOVELTY - Biofertilizer is preparing by performing solid fermentation of raw materials using activated solution, where effective number of viable cells in activated solution is 4-30x 108 cells/ml and the ratio of activated solution with respect to fermenting raw material is 1-5 l/100 kg. The fermenting raw material comprises 30-50 pts. wt. grape skin, 30-50 pts. wt. mushroom residue, 10-20 pts. wt. furfural residue, 3-6 pts. wt. plant ash and 0.2-0.8 pts. wt. inorganic salt.    USE - The biofertilizer is useful as basal application or top dressing fertilizer (claimed).    ADVANTAGE - The biofertilizer has high viable count.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biofertilizer, which involves obtaining activated solution using activated strain, taking the fermenting raw material, mixing, adding water until moisture content reaches 40-50%, sterilizing, adding the activated solution, stirring uniformly, spreading to thickness of 30-40 cm, fermenting at 30 plus minus 5 degrees C under humidity of 50-70% for 3-4 days, turning once in every 6-12 hours, and drying until moisture content reaches less than 15% to obtain product.
NOVELTY - Organic fertilizer and its preparation method, are claimed. The organic fertilizer comprises 45-70 wt.% chicken manure, 5-20 wt.% rice bran, 15-35 wt.% straw, 0.1-4 wt.% effective microbial liquid, 0.1-2 wt.% corn powder and 0.5-4 wt.% wheat bran. The organic fertilizer is prepared by taking the above-mentioned raw materials, mixing uniformly, adding water until moisture content reaches 60-70%, compacting, fermenting and drying until moisture content reaches 30%.    USE - As organic fertilizer and its preparation method.    ADVANTAGE - The organic fertilizer is prepared rapidly and required in reduced dosage amount. The method is suitable for large-scale production, does not require screening process, and provides high yield of more than 90%.    DETAILED DESCRIPTION - Organic fertilizer and its preparation method, are claimed. The organic fertilizer comprises 45-70 wt.% chicken manure, 5-20 wt.% rice bran, 15-35 wt.% straw, 0.1-4 wt.% effective microbial liquid, 0.1-2 wt.% corn powder and 0.5-4 wt.% wheat bran. The organic fertilizer is prepared by taking the above-mentioned raw materials, mixing uniformly, adding water until moisture content reaches 60-70%, compacting to a height of 0.5-1.2 m, performing primary anaerobic fermentation at 45-75 degrees C for 3-10 days, reducing the temperature to 20-30 degrees C, performing aerobic fermentation at 30-40 degrees C for 2-3 days and turning for 2-3 times, and drying until moisture content reaches 30%.
NOVELTY - Method for preparing and providing organic fertilizer for blueberry, involves taking weeds and straw to obtain manure, taking rapeseed and Camellia oleifera, pressing to separate oil and cake fertilizer, piling prepared manure and cake fertilizer, stacking to perform primary fermentation, covering using a plastic film, arranging waterproof sheets on sides, fermenting, mixing, stacking, fermenting to obtain a fertilizer, forming furrows, removing soil around blueberry plant, filling with the fertilizer, and providing fertilizer during later autumn or early spring.    USE - The method is useful for preparing and providing organic fertilizer for blueberry (claimed).    ADVANTAGE - The method prepares fertilizer with reduced fermentation time of 20-30 days, reduces expense with respect to fertilizer, and increases yield to more than 15%.    DETAILED DESCRIPTION - Method for preparing and providing organic fertilizer for blueberry, involves (a) taking weeds and straw which are used as food for agricultural livestock and poultry, mixing to obtain manure, taking rapeseed and Camellia oleifera, and pressing to separate oil and cake fertilizer, (b) piling prepared manure and cake fertilizer to height of height of 1.5-2 m and stacking to perform primary fermentation, where bottom layer is provided with manure to thickness of 25-35 cm, and a layer a cake fertilizer is provided above the bottom layer to thickness of 2-3 cm, covering using a plastic film, arranging waterproof sheets on sides, fermenting for 30 days, mixing the manure and cake fertilizer in a ratio of 10:1, stacking, and fermenting for 30-50 days to obtain a fertilizer, and (c) forming furrows on both side of blueberry plant with depth of 30-35 cm and width of 25-30 cm, removing soil around plant, filling with the fertilizer, and providing 3-5 kg fertilizer for 3 year old plant and 7-10 kg fertilizer for 5 year old plant during later autumn or early spring.
NOVELTY - Preparing carbon-based selenium fertilizer, by (a) washing straw or sludge, crushing, passing through 20-30 mesh sieve, sintering and drying to obtain biochar, (b) culturing yeast or Bacillus sp. in medium and washing, (c) mixing sodium selenite, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, magnesium sulfate, calcium chloride, zinc sulfate, ferrous sulfate, disodium EDTA, nitrogen source, glucose and water and (d) soaking the biochar in product obtained in step (b), adding the product obtained in step (c), and incubating for 10-25 hours.    USE - The method is useful for preparing carbon-based selenium fertilizer (claimed).    ADVANTAGE - The prepared fertilizer completely provides nitrogen, phosphorus and microelements to crops, improves soil property and yield and quality of the crops, and is environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing carbon-based selenium fertilizer, involves (a) washing straw or sludge with water, drying the washed product, crushing the dried product, passing the crushed product through 20-30 mesh sieve, sintering obtained product at 200-400 degrees C for 3-5 hours, cooling to room temperature, passing the cooled product through 20-40 mesh sieve, washing with water, and drying the washed product to obtain biochar, (b) culturing yeast or Bacillus sp. in medium, incubating and washing the incubated product using saline, (c) mixing sodium selenite, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, magnesium sulfate, calcium chloride, zinc sulfate, ferrous sulfate, disodium EDTA, nitrogen source, glucose and water in mass ratio of 30:(70-80):(70-80):(6-12):(6-12):(2-6):(2-6):(6-12):(20-35):(10-25):800, and adjusting pH of the mixture to 7-7.5, and (d) soaking the biochar in product obtained in step (b), adding the product obtained in step (c) to the soaked product, sealing, and incubating for 10-25 hours.
NOVELTY - This new utility model claims of one of organic garbage disposer, wherein comprising: main body and heating wind device, the main body comprises shell and stirring, the shell comprises the opposite lower side of the feeding port and discharging port and defining out inner side face of one inner groove, the stirring element is pivoted in the inner groove and setting; the heating wind device according to wind process orderly comprises oxygenator, heater, and several respectively and heater and connected in slot of the body and communicated the spraying pipe, the spraying pipe is provided with several perforation, the organic garbage processor for organic garbage holding in closeness state, when, by producing the oxygenator air through the heater after changing into one predetermined temperature of hot air, and by entering into the jet pipe in perforation of groove, and the temperature, humidity and oxygen content and adjust in groove.
NOVELTY - This utility new type claims a fruit peel litter one fermentation device, comprising bucket body and inner container, inner container set with a bucket body, bucket body upper end mounted with a rubber seal pad is a bucket cover, the bucket body and the inner container bottom is set with four a whole line of waist drum spring a bucket body, a bucket cover set on the this pneuma valve wherein, pump head, handle and stir, the bucket body and the inner container is further set with a cover and a connection rod mechanism, a bucket body outside side set with a connecting pole mechanism and a pedal, a bucket body of one side set with a one stop switch, stop switch comprising baffle pole and spring, the gear pole and connecting pole connecting mechanism, and the end and inner bag outside wall tangential to set with a rod with a hollow pipe and absorbing pump head and stir handle connection of the bottom end rod is set with a stainless steel blade inner container, inner container one side set with a scave line, one is a structure and reasonable structure, low manufacturing cost low, good seal, ferment effect is stable and has a stir and a closing function of fruit peel litter fermentation device.
NOVELTY - Agricultural organic waste anaerobic fermentation a marsh gas reaction device, comprising producing the acid fermentation reactor and producing a phase reactor, a further exist between the filter device, wherein the acid fermentation reactor using continuous stir kettle reactor, the reactor using a high aspect ratio is expanding granule sludge bed anaerobic reactor is 9: 1 to 10: 1, filtering device mounted with a material is nylon filter network or polyethylene filter screen is filter material, filter screen aperture size is 0.5 mm to 3 mm, the acid fermentation reactor, a filter, a phase reactor total volume ratio is 2.5: 3.5: 1: 1, the utility model is new type can increase agricultural organic waste in a degradation efficiency, device and pipeline blockage technology bottle neck in anaerobic fermentation system, in the low temperature environment for the anaerobic fermentation system caused by fluctuation of interference, increase speed of operation stability and produce marsh gas of system.
NOVELTY - This utility new type relates to one a sewage treatment device, specifically is sleeve-type catalyzed iron filler autotrophic denitrification device, comprising outside cylinder, inner cylinder and a top cover, the top cover in outside the top part of a cylinder wall of inner cylinder is provided with a through water hole, inner cylinder mounted in outside cylinder and inner and outside cylinder coaxial, inner bottom through annular mounting plate is mounted in the inner wall of outside cylinder a, mounting plate and outside the bottom; outside cylinder, inner cylinder and mounting plate form an annular area of a catalyzed iron filler fill area, a inner cylinder is provided with a water inlet pipe, water outlet pipe, mounting plate and outside the bottom of the gap connecting with pipe, inner cylinder is provided with inner agitator blade. In the device in the catalyzed iron filler would not sediment deposition, agitator blade through stir of inner cylinder in the catalytic iron filler fill water power condition and the mass transfer effect of inner area to a reaction, at the same time the valid microorganism in sedimentation of filler area, a denitrification reaction can continuously valid process.
NOVELTY - A one aerobic granule sludge integrated sewage treatment device, comprising a water inlet pipe, an aeration system and sludge discharging pipe, a cylindrical pool body, pool body centre set with conical reaction barrel, a conical reaction barrel periphery set with cylindrical clapboard, taper reaction tube is the first reaction room, between the tapered cylinder and cylindrical clapboard of reaction space is a space between the second reaction room, cylindrical clapboard cylindrical pool body and a third reaction room, each reaction room set with multi-layer screen is horizontal arrangement, the bottom conical reaction barrel set with water-gas mixed nozzle, a water-gas mixed nozzle connecting with air inlet pipe, a water-gas mixed short tube lower end set with circular water inlet cavity, a water outlet horizontal pipe and the round table set with water inlet cavity, a water inlet pipe mounted with a nozzle outlet, a cylindrical pool body lower end set with cone bottom and discharging pipe connecting through hole, a cylindrical pool body inner wall in a set with the water groove. This utility new type construction is simple and convenient construction, small floor area, convenient operation, good water quality, low cost and operation cost is low.
NOVELTY - Betulin sulfation is carried out in 1,4-dioxane with the mixture of sulphamic acid and urea at a temperature of 70-75 degrees C for 3.0-3.5 hours, the product isolation is carried out by cooling the reaction mass, dilution with water, extraction with butyl or isoamyl alcohol, rinsing with water, treating the alcohol extract with subsequent concentration of the alcohol layer and isolation of the target product.    USE - Biotechnology.    ADVANTAGE - Broadening the range of sulphating reagents for betulin sulfation, improvement of environmental friendliness of the method, expansion the range of sulfated derivatives of betulin.4 cl, 4 ex
NOVELTY - Method for producing organic compost, involves weighing e.g. tung tree nutshell, microbial inoculum, and decomposing agent, cleaning weighed raw materials respectively, and crushing cleaned raw materials, mixing crushed tung tree nutshell and water, mixing flue-cured tobacco stem with mixture, adding urea and decomposing agent, mixing uniformly, adding mixture layer by layer, fermenting mixture and turning mixture for 2-3 times, and accumulating mixture, mixing mixture using hand, and packing fermented product in dark brown color bag.    USE - The method is useful for producing organic compost (claimed), which is useful for cultivating plantation crop, improving soil condition and increasing fertility soil.    ADVANTAGE - The prepared organic compost is cost-effective and enables to increase quality of flower and crop.    DETAILED DESCRIPTION - Method for producing organic compost, involves (a) weighing 1200-1400 kg tung tree nutshell, 400-430 kg tung tree oil, 600-800 kg flue-cured tobacco stem, 10-11 kg urea, 400 ml microbial inoculum, and 200 g decomposing agent, (b) cleaning weighed raw materials respectively, and crushing cleaned raw materials using crusher, (c) mixing crushed tung tree nutshell and water, or soaking crushed tung tree nutshell in water to obtain mixture, (d) mixing flue-cured tobacco stem with mixture obtained in step (c), adding urea and decomposing agent, mixing uniformly, adding mixture layer by layer, fermenting mixture, turning mixture for 2-3 times, during turning mixture, and adding tung tree oil to mixture, and (e) accumulating mixture for 70-90 days, mixing mixture using hand, and packing fermented product in dark brown color bag.
NOVELTY - A hydrogen carrier comprises a hydrogen storage portion in the main chain and/or side chain of an organic polymer. The hydrogen storage portion turns into a redox-active portion while generating hydrogen molecules in the presence of a catalyst. The redox-active portion stores hydrogen obtained from reduction and contact with a proton source to become a hydrogen storage portion.    USE - Hydrogen carrier is used in production of hydrogen (claimed).    ADVANTAGE - The hydrogen carrier has excellent storage stability and transportability under a normal-pressure environment, handleability and reusability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of hydrogen, which involves preparing hydrogen carrier, and generating hydrogen by contacting catalyst with the hydrogen carrier.
NOVELTY - An electrolytic membrane comprises polymer (P1) having hydrophilic segment (A1) and hydrophobic segment (B1), and polymer (P2) which does not have sulfonic acid group. The polymer (P2) has hydrophobic segment (B1') which is compatible with segment (B1) and 0-50 wt.% segment (B2) different from segment (B1') with respect to the whole polymer (P2). The electrolytic membrane has water contact angle of 45-120 degrees .    USE - Electrolytic membrane is used for polymer electrolyte fuel cell (claimed) for production of hydrogen gas.    ADVANTAGE - The electrolytic membrane has excellent transparency, electric power generation characteristics, water-repellent property, adhesiveness with electrode, and dimensional stability during wet-and-dry cycle time. The battery containing the membrane does not include foreign material. The fuel cell containing the electrolytic membrane suppresses flooding, and has excellent electric power generation characteristics and durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for membrane-electrode assembly, which has a gas diffusion layer, catalyst layer, electrolytic membrane, catalyst layer and gas diffusion layer, which are laminated in order.
NOVELTY - Method for performing intercropping of mulberry and alfalfa, involves selecting suitable intercropping pattern for the mulberry and alfalfa, determining spacing and density between the above-mentioned crops, creating ridge, cultivating the mulberry in the ridges, and intercropping the alfalfa in the ridges.    USE - The method is useful for performing intercropping of mulberry and alfalfa (claimed).    ADVANTAGE - The method enables nitrogen fixation by alfalfa which is required for growth of the mulberry, controls soil erosion as the crops have developed root system, is environmentally-friendly, does not use toxic pesticide, and promotes photosynthesis.
NOVELTY - Fertilizer comprises 9-15 pts. wt. monoammonium phosphate, 1.1-2.3 pts. wt. copper sulfate, 8-14 pts. wt. ammonium sulfate, 1.5-6 pts. wt. fulvic acid, 2.2-3.8 pts. wt. chlorothalonil, 6-10 pts. wt. potassium sulfate, 2.5-6 pts. wt. soluble chitosan, 2.4-5.8 pts. wt. Bacillus subtilis, 4.2-8 pts. wt. calcium oxide, and 1.1-2.4 pts. wt. chelating agent.    USE - The fertilizer is useful for vegetables (claimed).    ADVANTAGE - The non-toxic fertilizer can improve nutrition content of vegetables, loosen soil and improve soil structure, and is eco-friendly.
NOVELTY - Flower-specific biological fertilizer comprises 6-14 pts. wt. chicken manure, 3.5-8 pts. wt. calcium biphosphate, 1.3-4.8 pts. wt. pyrophosphate, 0.6-1.4 pts. wt. boric acid, 4-8 pts. wt. weevil powder, 2.5-6 pts. wt. limestone, 3.2-6.8 pts. wt. ammonium hydroxide, 3.5-9 pts. wt. chicken manure, 3.6-8 pts. wt. manganese sulfate, 4.2-8.5 pts. wt. iron oxide, 4.2-8.4 pts. wt. wheat bran, 3.5-8 pts. wt. rice bran, 3.6-8.7 pts. wt. Stellera chamaejasme, 3.1-8.2 pts. wt. Bacillus subtilis, and 1.3-3.5 pts. wt. magnesium chloride.    USE - Flower-specific biological fertilizer.    ADVANTAGE - The fertilizer can extend the flowering period, increases the viewing effect, and has good economic and social value.
NOVELTY - Method for preparing water-soluble liquid organic fertilizer, involves (a) adding 100 million/cm3 yeast and 100 million/cm3 lactic acid bacteria, respectively into liquid fertilizer stock solution, uniformly mixing solution, adding filler and performing biological anaerobic fermentation for 48 hours, (b) inoculating 1 billion/cm3 Bacillus into obtained mixture, adding nitrate, boron, zinc and ammonium fertilizers to the mixture, and performing aerobic fermentation for 24 hours, and (c) adding 20 kg/m3 chitin to the mixture, and uniformly stirring the mixture.    USE - The method is useful for preparing water-soluble liquid organic fertilizer (claimed).    ADVANTAGE - The method is simple to perform.
NOVELTY - Bazedoxifene acetate intermediate is prepared by condensing p-hydroxybenzaldehyde and 1-(2-chloroethyl)hexahydro-1H-azepine salt in polar aprotic solvent under presence of base to obtain intermediate, directly mixing resulting product with protic solvent, and reducing product using reducing agent.    USE - Preparation of bazedoxifene acetate intermediate (claimed).    ADVANTAGE - Process is one-pot, fast, safe, simple, environment-friendly, reduces cost, and has mild conditions, high conversion rate and product yield, and high purity products.    DETAILED DESCRIPTION - Bazedoxifene acetate intermediate of formula (3) is prepared by condensing p-hydroxybenzaldehyde of formula (6) and 1-(2-chloroethyl)hexahydro-1H-azepine salt of formula (5) in polar aprotic solvent under presence of base to obtain intermediate of formula (4), directly mixing resulting product with protic solvent, and reducing product using reducing agent. INDEPENDENT CLAIMS are included for:    (1) preparation of bazedoxifene acetate intermediate of formula (2) from bazedoxifene acetate intermediate (3) which involves reacting bazedoxifene acetate intermediate (3) with ester solution of hydrogen chloride; and    (2) preparation of 4-(2-(imino-1-cyclohexyl) ethoxy)benzyl chloride hydrochloride of formula (1) from bazedoxifene acetate intermediate (2) which involves reacting obtained bazedoxifene acetate intermediate (2) with chlorinating agent.
NOVELTY - A Enterobacter hormaechei QDN01 strain preserved in China Center for Type Culture Collection with preservation number of CCTCC NO: M2013670, is new.    USE - Enterobacter hormaechei QDN01 strain for use in bio-deodorant that is utilized for removing ammonia, peculiar smell and odor from industrial waste water, livestock excrement and animal dung for manure.    ADVANTAGE - The strain has better ammonia deodorization stability and capacity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a bio-deodorant comprising the Enterobacter hormaechei QDN01 strain adsorbed on bentonite, after adding brown sugar    (2) a method for deamination and deodorizing chicken manure, which involves using the strain adsorbed on bentonite, while adding brown sugar, to obtain bio-deodorant, adjusting carbon and nitrogen ratio to 20-30:1 in chicken using starch, spreading the bio-deodorant in manure in shed uniformly, and treating for 3 days, and evaluating deodorizing effect.
NOVELTY - A Cordyceps militaris mycelium powder comprises Cordyceps Militaris (Cordyceps militaris) YCC-RY-O2, having CGMCC NO: 9350.    USE - For improving fibrinolytic and antioxidant function (claimed).    ADVANTAGE - The method has simple operation and low cost; requires short period of time and is easy to implement; is environment0friendly; uses inexpensive reagents; and is suitable for large-scale production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the Cordyceps militaris mycelium powder involving (i) taking Cordyceps militaris, and seeding in PDA liquid seed culture medium, and shaking at 22-25 degrees C, at speed of 120-180 revolutions per minute (rpm) and culturing for 4-8 days, to obtain Cordyceps militaris seed solution; (ii) adding bean in water, performing high pressure sterilization, and after cooling to room temperature, seeding Cordyceps militaris seed solution with 1-8% inoculum, then fermenting at 22-28 degrees C and culturing for 4-8 days; and (iii) then vacuum freeze drying cordyceps militaris beans under low-temperature condition, and finally crushing to 80-120 mesh, to give final product.
NOVELTY - A Bacillus pumilus SNR-3 strain preserved in China General Microbiological Culture Collection Center, Accession Number CGMCC NO. 7126, deposit date January 11, 2013, is new.    USE - Bacillus pumilus SNR-3 strain for removing nitrate and nitrite in contaminated water (claimed).    ADVANTAGE - The strain culture removes heavy metal pollution in convenient, simple, and cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a use of Bacillus pumilus SNR-3 strain for removing nitrate and nitrite in contaminated water by inoculating culture of Bacillus SNR -3 in Cadmium ion and/or copper ion containing nitrogenous wastewater, performing growth process through aerobic denitrification, while use of biological removal of water adsorption of Cadmium ion and/or copper ion heavy metal, and adsorbing located intracellular, so as to achieve the purpose of the removal of heavy metals.
NOVELTY - Special organic fertilizer of tea comprises 20-50 pts. wt. fresh chicken manure, 40-70 pts. wt. fresh cow dung, 5-30 pts. wt. fresh pig manure, 0.5-2.5 pts. wt. calcium hydrogen phosphate, 0.0007-0.0030 pts. wt. aluminum salt, 5-20 pts. wt. inorganic fertilizer, 0.05-0.25 pts. wt. inoculants and 0.03-0.08 pts. wt. rotten livestock and poultry dry excrement powder.    USE - The special organic fertilizer is useful for promoting growth and improving quality of tea (claimed).    ADVANTAGE - The special organic fertilizer increases organic aluminum content in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) mixing fresh chicken manure, cow dung, pig manure and calcium hydrogen phosphate, adjusting pH of the mixture, adding the inoculants to the mixture and performing aerobic fermentation, (b) gradually increasing temperature to 50-60 degrees C during fermentation, and stopping fermentation after 2-3 days, (c) crushing mixture, and storing mixture for 3-5 days, (d) adding aluminum salt to dry livestock and poultry excrement powder, uniformly mixing materials, and fermenting mixture at 60-70 degrees C, (e) maintaining mixture at 40-50 degrees C, and (f) adding other raw materials into mixture, quantifying and packaging product.
NOVELTY - Invention relates to farm industry and biotechnology, in particular, to manufacture of biologically active additives for farm animals and poultry. The acellular probiotic represented by a biologically active complex contains a mixture of sterile culture liquids of bacteria of Lactobacillus plantarum 8 RAZ (VKPM No B-11007) strain and Bacillus subtilis M-8 (VKPM No B-1948) strain taken at a volume ratio of 1:1; the prebiotic is represented by a liquid sterile autolysate of micellium of fungi of Fusarium sambucinum MKF-2001-3 (VKPM F-867) strain; the dry biologically active additive is represented by dry biomass of fungi of Fusarium sambucinum MKF-2001-3 (VKPM F-867) strain. The complex is applied without preliminary mixing of the probiotic, prebiotic and/or the biologically active additive; each component is directly introduced into the fodder or drinking water in doses depending on animals species and age.    USE - Food industry.    ADVANTAGE - Invention allows to increase animals performance and the organism natural resistance, compensate for deficit of amino acids, vitamins, microelements in animals and poultry feeding rations and normalise the digestive tract microflora.15 cl, 19 tbl, 9 ex
NOVELTY - Monoammonium phosphate fertilizer composition preparation involves performing pulping of paddle and white manure in 2-5:1 ratio. The obtained material is kept at 50-80 degrees C, and then mixed with sulfate and phosphorus (0.5-2:1). The obtained material is performed for acidolysis by adding sulfuric acid. The obtained material is performed for solid-liquid separation to obtain white manure acid hydrolyzate and phosphogypsum. The obtained material is mixed with wet process phosphoric acid, and then the obtained material is mixed with phophorous pentaoxide (15-20%).    USE - Method for preparing monoammonium phosphate fertilizer composition (claimed).    ADVANTAGE - The method enables to prepare monoammonium phosphate fertilizer composition in simple and cost-effective manner that is eco-friendly in nature.    DETAILED DESCRIPTION - Monoammonium phosphate fertilizer composition preparation involves performing pulping of paddle and white manure in 2-5:1 ratio. The obtained material is kept at 50-80 degrees C, and then mixed with sulfate and phosphorus (0.5-2:1). The obtained material is performed for acidolysis by adding sulfuric acid. The obtained material is performed for solid-liquid separation to obtain white manure acid hydrolyzate and phosphogypsum. The obtained material is mixed with wet process phosphoric acid, and then the obtained material is mixed with phophorous pentaoxide (15-20%). The obtained material is mixed with phosphoric acid and liquid ammonia reaction to obtain the finished product.
NOVELTY - Production of nutritive soil involves compressing phosphorus and potassium composite-containing tailings to sheet form with thickness of 5-30 mm, conveying product to microwave sterilization machine for low-temperature sterilization, drying, and cooling. The tailing comprises phosphorus and potassium composite, acidified sludge, high-viscosity attapulgite clay, ceramic, pulverized peat, biogas, pulverized plant fiber, vermiculite, expanded perlite and superabsorbent.    USE - Production of nutritive soil (claimed).    ADVANTAGE - The method efficiently and economically provides nutritive soil which improves the normal growth of plants, by removing pathogens and harmful pests.    DETAILED DESCRIPTION - Production of nutritive soil involves compressing phosphorus and potassium composite-containing tailings to sheet with thickness of 5-30 mm, conveying product to a microwave sterilization machine for low-temperature sterilization, drying at 60-100 degrees C for 30-120 minutes, cooling and obtaining product having moisture content of 15% or less. The tailing comprises 15-35% phosphorus and potassium composite, 25-55% acidified sludge, 2-15% high-viscosity attapulgite clay, 2-15% ceramic, 2-15% pulverized peat, 2-15% biogas, 1-10% pulverized plant fiber, 0.5-5% vermiculite, 0.5-5% expanded perlite and 0.1-5% superabsorbent.
NOVELTY - A healthcare product comprises 1-5 pts. wt. buckwheat extract, 1-3 pts. wt. red yeast, and 0.1-5 pts. wt. mulberry extract.    USE - Healthcare product, i.e. powder, tablet, capsule, granules or granular tea used for preventing or treating high blood sugar and high blood fat (all claimed).    ADVANTAGE - The healthcare product can restrain or reduce blood sugar and blood fat, and it has simple preparation method and great medical and healthcare function.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of healthcare product comprising:    (A) steaming off tartary buckwheat to activate enzyme, adding 6-15 times water, extracting to 70-100 degrees C for 2-4 times every 30-120 minutes/extraction, combining extracts, filtering, and concentrating filtrate to 50-100 degrees C to obtain concentrate having relative density of 1.02-1.15;    (B) adding 60-90 wt.% 90-98% ethanol, standing at 0-20 degrees C for 6-48 hours, and filtering;    (C) recovering ethanol, concentrating filtrate to 60-90 degrees C to obtain concentrate having relative density of 1.15-1.30, drying to 60-90 degrees C under reduced pressure, and crushing to obtain buckwheat total flavonoid extract; and    (D) adding red yeast powder, mixing, adding mulberry extract, mixing, drying, and crushing.
NOVELTY - Production of diatomite compressed nutritional soil comprises adding diatomite and compressed nutritional soil into a mixer, uniformly stirring, conveying into microwave drying sterilizing machine for sterilizing and drying, controlling the moisture content, conveying into heat-insulating sterilizing library, continuously sterilizing and drying, cooling and packaging to obtain the product including acidified diatomite, acidified mud, high-viscosity attapulgite clay, broken stone-shaped attapulgite flower ceramic, crushed peat, biogas residue, plant fiber and expanded vermiculite.    USE - Production of diatomite compressed nutritional soil (claimed) used for reducing pathogenic bacteria and pests harmful for plant and protecting the ecological environment.    ADVANTAGE - The diatomite compressed nutritional soil contains nitrogen, phosphorus, potassium, organic matter and multiple elements for plant growth, and enables the normal growth and development of plant.    DETAILED DESCRIPTION - Production of diatomite compressed nutritional soil comprises adding diatomite and compressed nutritional soil having thickness of 5-30 mm into a mixer, uniformly stirring, conveying into microwave drying sterilizing machine through a belt type conveyor for sterilizing and drying at 60-100 degrees C for 30-120 minutes, controlling the moisture content at less than or equal to 15%, conveying into heat-insulating sterilizing library, continuously sterilizing and drying, cooling and packaging to obtain the product comprising 15-35 wt.% acidified diatomite, 25-55 wt.% acidified mud, 2-15 wt.% high-viscosity attapulgite clay, 2-15 wt.% broken stone-shaped attapulgite flower ceramic, 2-15 wt.% crushed peat, 2-15 wt.% biogas residue, 1-10 wt.% plant fiber, 0.5-5 wt.% expanded vermiculite, 0.5-5 wt.% expanded perlite, and 0.1-5 wt.% high water-absorbing resin.
NOVELTY - Production of nutritive soil composition involves providing raw materials of nutritive soil composition into a mixer, stirring, adding resultant mixed material to a compression machine, forming nutritive soil composition sheet, controlling thickness of resultant product to 5-30 mm, transferring resultant product to a microwave belt-type sterilizing machine, subjecting to low-temperature sterilization process, drying at 60-100 degrees C for 30-120 minutes, obtaining sterilized and dried product with moisture content of less than 15%, heating, cooling, and packaging.    USE - Production of nutritive soil composition (claimed).    ADVANTAGE - The method enables production of environmentally-friendly nutritive soil composition that provides sufficient amount of nutrients required for normal growth and development of plants, and reduces infestation of harmful pathogenic bacteria and pests in the plants.    DETAILED DESCRIPTION - Production of nutritive soil composition involves providing raw materials of nutritive soil composition into a mixer, stirring, adding resultant mixed material to a compression machine, forming nutritive soil composition sheet, controlling thickness of resultant product to 5-30 mm, transferring resultant product to a microwave belt-type sterilizing machine, subjecting to low-temperature sterilization process, drying at 60-100 degrees C for 30-120 minutes, obtaining sterilized and dried product with moisture content of less than 15%, heating, cooling, and packaging. The raw material of nutritive soil composition includes 15-35 wt.% acidified attapulgite clay tailings, 25-55 wt.% acidified sludge, 2-15 wt.% high-viscosity attapulgite clay, 2-15 wt.% slurry of gravel-shaped attapulgite ceramic, 2-15 wt.% pulverized peat, 2-15 wt.% biogas residue, 1-10 wt.% crushed plant fiber, 0.5-5 wt.% expanded vermiculite, 0.5-5 wt.% expanded perlite and 0.1-5 wt.% superabsorbent resin.
NOVELTY - This utility new type relates to a one organic fertilizer fermenting device, include fermentation tank, the fermentation tank body comprise outer shell and inner layer shell, an outer layer shell and the inner layer shell is set with electric heating wire, a fermentation tank body set with temperature controller, the temperature controller and the electric heating wire, bottom top part of the fermentation tank body set with marsh gas collecting box, a methane collecting box set with several air inlet, one side gas collecting box set with a marsh gas air outlet, low fermentation tank side wall part set with biogas residue and biogas slurry exit exit, ferment tank body middle part set with stir shaft, fermentation tank lower end set with fixed motor, said electric machine and the stir shaft. This utility new type of beneficial effects as follows: animal litter for a fermentation process, which not only increases the utilization rate of animal excrement, at the same time, can according to need a fermentation tank of inner body temperature, stir the tank body set with excrement temperature uniformity, and uniform fermentation of shaft, marsh gas for a collection, or to generate electricity, the excrement;
NOVELTY - Fertilizer composition preparation involves producing spiral algae fertilizer by fermenting spiral algae and manure by using lactic acidlactobacillus fermentation liquid. Urea, boric acid, potassium sulfate, wheat bran, soybean dreg, organic selenium and phosphorus are added to the obtained material. Phosphorus fertilizer are mixed to the obtained material, and then ground them. Nano-ceramics particle are added to the obtained material to obtain the finished product.    USE - Method for preparing fertilizer composition used for cropping sugarcane (claimed).    ADVANTAGE - The method enables to prepare fertilizer composition, ensures improved absorption and yield.
NOVELTY - Production of fluorine-containing compound (I) involves reacting ester group-containing compound (II) with fluorination agent at less than 100 degrees C.    USE - Production of fluorine-containing compound used in plant-protecting and pharmaceutical composition.    ADVANTAGE - The method provides fluorine-containing compound with high selectivity and yield, by environmentally-friendly process with reduced energy consumption.    DETAILED DESCRIPTION - Production of fluorine-containing compound of formula: R-CF2-O-Ar' (I) involves reacting ester group-containing compound of formula: R-C(O)-O-Ar' (II) with fluorination agent at less than 100 degrees C.    R=fluorinated alkyl, optionally substituted aryl or heteroaryl;and    Ar'=optionally substituted aryl or heteroaryl.
NOVELTY - A cefradine combination drug comprises 60-140 pts. wt. cefradine, 2-14 pts. wt. borneol, 6-20 pts. wt. vitamin E, and 3-12 pts. wt. sodium carbonate.    USE - For preparing cefradine combination drug (claimed). The cefradine combination drug may be used for the treatment of infections, e.g. susceptible strains causing acute pharyngitis, tonsilitis, otitis media, bronchitis and pneumonia, respiratory tract infection, urinary tract infection and skin soft tissue infection; the cefradine is also protected from oxidation and peroxide formation in manufacturing, storage, transportation and use, and side effects such as head pain, emesis, diarrhea, abdominal distension, and constipation are reduced; the drug dosage is reduced, giving a liver-protecting effect (claimed).    ADVANTAGE - The prepared cefradine combination drug has good stability, and good curative effect. The method is safe, energy-saving and environment-friendly.    DETAILED DESCRIPTION - A cefradine combination drug comprises 60-140 pts. wt. cefradine, 2-14 pts. wt. borneol, 6-20 pts. wt. vitamin E, and 3-12 pts. wt. sodium carbonate. The cefradine combination drug is prepared by taking cefradine, 5-15 times of water for injection, mixing respectively, adding borneol, vitamin E, and sodium carbonate, dissolving completely, ultra filtering the obtained solution, washing the filtrate, adjusting the pH value of 6.5-7.6, steam sterilizing at 121 degrees C, cooling the sterilized solution to 20-22 degrees C, adding sodium hydroxide solution drop wise and stirring to the solution, adjusting the liquor with a pH value of 6.5-7.6, and filtering.
NOVELTY - Preparing N-acetylphenothiazine comprises adding acetic acid (A mole) and phosphorus oxychloride (B mole) to a reaction container and grinding uniformly, then adding phenothiazine (C mole), and continuing the grinding until the reaction is complete to obtain the product, where the ratio of A, B and C is (1-1.2):(1-1.2):1; and allowing the product to stand the product, washing, filtering, drying the filter cake, and recrystallizing to obtain N-acetylphenothiazine.    USE - The method is useful for preparing N-acetylphenothiazine (claimed).    ADVANTAGE - The method: has mild reaction conditions and short reaction time; does not require solvent; is simple and convenient; produces little pollution to the environment; requires only grinding reaction; and provides the product with high yield of more than 93%.
NOVELTY - A 2-(benzyl(2-phenylethyl-carbamoyl-methyl)amino)acetic acid (I), is new.    USE - New 2-(benzyl(2-phenylethyl-carbamoyl-methyl)amino)acetic acid is used as intermediate for preparing 4-benzyl-1-phenethyl-piperazine-2,6-dione used in preparation of medicament against Schistosoma japonicum (all claimed).    ADVANTAGE - The 2-(benzyl(2-phenylethyl-carbamoyl-methyl)amino)acetic acid is prepared efficiently and economically with high purity by consuming reduced amount of energy without causing pollution to environment.    DETAILED DESCRIPTION - A 2-(benzyl(2-phenylethyl-carbamoyl-methyl)amino)acetic acid of formula (I) or its salt, is new. INDEPENDENT CLAIMS are included for the following:    (1) preparation of 2-(benzyl(2-phenylethyl-carbamoyl-methyl)amino)acetic acid (I), which involves reacting 2-(benzyl(carboxy)amino)acetic acid and 4-benzylmorpholine-2,6-dione and then acylating with beta -phenethylamine in aprotic organic solvent; and    (2) preparation of 4-benzyl-1-phenethyl-piperazine-2,6-dione, which involves reacting compound (I) and dehydrating agent and alkaline substance.
NOVELTY - Synthesis of (hetero)aromatic diazene compound (I) involves reacting nitrobenzene/nitropyridine derivative (II) with organic alkali, in presence of organic solvent, using modified carbon nano-tube as catalyst.    USE - For synthesis of (hetero)aromatic diazene compound (claimed), useful for synthesizing antioxidant, dye, drug, light material, additive, adhesive, plastic agent and food auxiliary agent.    ADVANTAGE - The method is green and environment-friendly; has low cost, mild operation condition; and produces product with high yield.    DETAILED DESCRIPTION - Synthesis of (hetero)aromatic diazene compound of formula (I) involves reacting nitrobenzene/nitropyridine derivative of formula (II) with organic alkali, in presence of organic solvent, using modified carbon nano-tube as catalyst.    R=H, mercapto, halo, 1-4C alkyl, 1-4C alkoxy or halogenated 1-4C alkoxy; and    X=C or N.    An INDEPENDENT CLAIM is also included for the preparation of the catalyst.
NOVELTY - Purifying penciclovir involves mixing crude penciclovir with aluminum oxide and methyl sulfoxide, where the obtained product is filtered to obtain a filtrate, which is dissolved in monohydric alcohol solvent under stirring condition. The dissolved product is filtered, and then crystallized to obtain (R)-9-(4-hydroxy-2-(hydroxymethyl)butyl)guanine, which is then re-crystallized to obtain purified penciclovir.    USE - Method for purifying penciclovir (claimed).    ADVANTAGE - The method enables to purify penciclovir so as to obtain a highly purified (99.9%) product, and also has wide industrial applicability. The obtained penciclovir is easily regenerated in the lab and prepared in a simple, convenient and cost-effective manner with no pollution.
NOVELTY - Preparing felbinac, comprises (i) taking bromine acid and phenylboronic acid as raw materials, in the presence of alkali catalyst, adding pure water as a solvent, and reacting in presence of air, and filtering the reaction liquid, to obtain filter liquid; (ii) adding water into the filter liquid, stirring, heating the filtered liquid at 70-80 degrees C, and filtering to obtain a white solid matter; and (iii) dissolving white solid matter by adding ester, drying by adding a drying agent, washing ester with water, remove the drying agent by filtration, and evaporating the washing liquid, and drying.    USE - The method is useful for preparing felbinac (claimed).    ADVANTAGE - The method is rapid, environmental friendly, and suitable for large-scale industrial production; does not produce any toxic materials; has simple synthesis and treatment processes, mild synthesis conditions, easy separation and purification procedures, and high yield; produces product: not sensitive to air humidity, and with high water solubility, and high catalytic activity; and shortens the reaction steps.    DETAILED DESCRIPTION - Preparing felbinac, comprises (i) taking bromophenylacetic acid and phenylboronic acid as raw materials, in the presence of an alkali catalyst, and adding pure water as a solvent, and reacting in presence of air at 15-60 degrees C for 2-10 hours, stopping the reaction, and filtering the reaction liquid, to obtain the filter liquid; (ii) adding water into the filter liquid, stirring, heating the filtered liquid at 70-80 degrees C, and filtering to obtain a white solid matter; and (iii) dissolving the white solid matter by adding ester, drying by adding a drying agent, washing ester with water, remove the drying agent by filtration, and allowing the washing liquid to evaporate, and drying to obtain the product, where the catalyst is palladium dichloride diglycine complex.
NOVELTY - (5-Halo-2-methylphenyl)(5-(4-fluorophenyl)thiophen-2-yl)methanone (II) is dissolved in an organic solvent, reacted in presence of Bronsted acid or Lewis acid, and reaction mixture is cooled to -10 degrees C to 10 degrees C. Then, metal borohydride reducing agent is added, reacted at 0-10 degrees C for 3-5 hours, warmed to 50-80 degrees C, reaction is continued for 12-15 hours, cooled to 0-10 degrees C, quenched with water, and extracted using dilute acid, to obtain crude product. The obtained crude product is purified by recrystallization, to obtain canagliflozin intermediate 2-(4-fluorophenyl)-5-((5-halo-2-methylphenyl)methyl)thiophene (I).    USE - Preparation of canagliflozin intermediate 2-(4-fluorophenyl)-5-((5-halo-2-methylphenyl)methyl)thiophene useful as intermediate for preparing diabetes mellitus drug (claimed).    ADVANTAGE - The method efficiently provides 2-(4-fluorophenyl)-5-((5-halo-2-methylphenyl)methyl)thiophene, without generating pungent smell and without causing pollution to environment.    DETAILED DESCRIPTION - (5-Halo-2-methylphenyl)(5-(4-fluorophenyl)thiophen-2-yl)methanone of formula (II) is dissolved in an organic solvent, reacted in presence of Bronsted acid or Lewis acid, and reaction mixture is cooled to -10 degrees C to 10 degrees C. Then, metal borohydride reducing agent is added, reacted at 0-10 degrees C for 3-5 hours, warmed to 50-80 degrees C, reaction is continued for 12-15 hours, cooled to 0-10 degrees C, quenched with water, and extracted using dilute acid, to obtain crude product. The obtained crude product is purified by recrystallization, to obtain canagliflozin intermediate 2-(4-fluorophenyl)-5-((5-halo-2-methylphenyl)methyl)thiophene of formula (I).    X=bromo or iodo.
NOVELTY - A microbial agent comprises 15-35 mass parts Bacillus subtilis, 10-20 mass parts Bacillus laterosporus, 30-50 mass parts Candida lipolytica, 10-20 mass parts green Trichoderma viride and 15-35 mass parts Aspergillus niger.    USE - Microbial agent for degrading kitchen rubbish of naval ship (claimed).    ADVANTAGE - The microbial agent is simple, convenient and inexpensive to use.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following: (1) a method for utilizing a microbial agent for degrading kitchen rubbish of naval ship, which involves mixing microbial agent and kitchen rubbish of naval ship at a mass ratio of 1: 300-500, and fermenting at 28-40 degrees C for 36-72 hours (2) a method for preparing a microbial agent, which involves taking 15-35 mass parts Bacillus subtilis, 10-20 mass parts Bacillus laterosporus, 30-50 mass parts Candida lipolytica, 10-20 mass parts green Trichoderma viride and 15-35 mass parts Aspergillus niger as cultured plant, inoculating the cultured plant in 10% liquid culture medium for activation of cultured plant, placing 60-75 vol.% cultured plant in fermentation culture medium for fermentation process to obtain fermentation liquid, absorbing the fermentation liquid with carrier to obtain single fungus powder of each strain such as Bacillus subtilis, Bacillus laterosporus, Candida lipolytica, green Trichoderma viride and Aspergillus niger with effective viable number of 5X108 cells/g, where the carrier comprises diatomite, bran and rice bran at a mass ratio of 1-1.5:0.5-1.5:2-3.
NOVELTY - Bio-fertilizer comprises 20-30 pts. wt. Sorghum stalk, 20-30 pts. wt. cornstalk, 20-40 pts. wt. manioc waste, 10-20 pts. wt. plant ash, 10-20 pts. wt. fruit and vegetable waste, 20-50 pts. wt. animal excrement, 5-10 pts. wt. effective microorganism, 0.001-0.003 pts. wt. cellulase and remainder purified water.    USE - The bio-fertilizer is useful for increasing soil fertility.    ADVANTAGE - Environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the bio-fertilizer, which involves mixing Sorghum stalk, cornstalk, manioc waste, plant ash and fruit and vegetable waste to obtain plant-based raw materials, stacking a layer of plant-based raw materials, dissolving effective microorganism and cellulase in purified water, spraying mixture on stacked material, mixing uniformly, stacking layer of animal excrement, covering top surface with a layer of grasses, sequentially stacking 8-10 layers of raw materials, covering with black plastic film, sealing, performing first round of anaerobic fermentation for 5-10 days, inserting thermometer into stacked material for measuring temperature during fermentation, where if the temperature reaches 50 degrees C, the black plastic film is opened, mixing compost and allowing compost to absorb oxygen, covering compost after mixing, fermenting at 40 degrees C, turning compost for 5-6 times after the first round of fermentation, covering compost, turning compost, when the temperature reaches 50 degrees C, cooling mixture and performing anaerobic fermentation for 15- 20 days.
NOVELTY - Use of sulfur compound having carbon-sulfur-carbon bond for reducing loss in oxidative stability of lubricating oil composition for crankcase of internal combustion engine when internal combustion engine is fuelled with biofuel, is claimed.    USE - Use of sulfur compound having carbon-sulfur-carbon bond for reducing loss in oxidative stability of lubricating oil composition for crankcase of internal combustion engine, when internal combustion engine is fuelled with biofuel (claimed).    ADVANTAGE - The sulfur compound effectively reduces loss in oxidative stability of lubricating oil composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for improving resistance to oxidation of lubricating oil compositions used to lubricate engines fuelled with biofuel, which involves adding predetermined amount of the sulfur compound to the lubricating oil composition.
NOVELTY - A hydrogen separation body comprises porous body and hydrogen separation layer with which hydrogen separation metal which selects and permeates only hydrogen in pore of porous body among gases containing hydrogen is filled. Ratio ( epsilon / tau ) of filling rate ( epsilon ) which is the parameter showing the ratio of the filling of hydrogen separation metal in hydrogen separation layer with zigzag-coefficient ( tau ) which is the parameter showing the grade of the length of the permeable path of hydrogen in the thickness direction of hydrogen separation layer is 0.2-0.6.    USE - A hydrogen separation body for hydrogen production apparatus (claimed).    ADVANTAGE - The hydrogen separation body has high hydrogen-permeation performance and coating-film-peeling resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the required angle during path bending.
NOVELTY - A fuel cell unit (900) comprises fuel cell module (901) which is assembly of single cell which produces electric power according to electrochemical reaction of reformed gas from fuel and oxygen, modifier (921) which has catalyst which generates reformed gas from fuel, container (923) which has structure which contacts fuel cell module and modifier, and heating area in which entrance side of reformed gas in fuel cell module and heat generation by electrochemical reaction is large and thermal absorption area which is a site which introduces fuel into modifier may adjoin each other.    USE - A fuel cell unit for fuel cell system used for hybrid electric power generation system (all claimed).    ADVANTAGE - Thermal stress by temperature nonuniformity accompanying electrochemical reaction is reduced, and reliability of fuel cell is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fuel cell system; and    (2) hybrid electric power generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the flow of fuel in fuel cell unit.    Fuel cell unit (900)    Fuel cell module (901)    Modifier (921)    Modification fuel supply device (922)    Container (923)
NOVELTY - Bifunctional enzyme has amino acids (SEQ ID NO: 1). The bifunctional enzyme comprises a xylosidase, a linker and a xylanase. (ftp://ftp.wipo.int/pub/published_pct_sequences/publication).    USE - Bifunctional enzyme used for degrading lignocellulosic portions of biomass for obtaining xylose (all claimed).    ADVANTAGE - The bifunctional enzyme synergistically catalyzes lignocellulosic portions of the biomass to obtain xylose in a single operation, where the obtained xylose undergoes bioconversion process to produce biofuel in a cost-effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for a method of producing bifunctional enzyme, which involves:    (1) ligating DNA fragment with xylanase-xylosidase activity into plasmid, and then cloning plasmid for protein expression in desired Escherichia coli strain; and    (2) a method for obtaining xylose, which involves utilizing a bifunctional enzyme that disrupts hemicellulose-rich matter to obtain desired residue.    .
NOVELTY - Application of selenium-enriched fertilizer comprises determining fertilizing plot selenium content, adding selenium-enriched fertilizer and fertilizing for 25-30 days. Selenium-enriched fertilizer comprises organic fertilizer, cow dung, spinach leaf, floating aquatic plant dry powder, fermented wood, clay, medical stone powder, phellodendron powder, Lophatherum gracile, cattle manure and pig manure.    USE - Application of selenium-enriched fertilizer (claimed).    ADVANTAGE - The method is simple. The fertilizer is simple.
NOVELTY - Preparing long-term sustained release antimicrobial anti-mildew material comprises (i) dissolving glucose in deionized water, formulating into solution, placing in a hydrothermal reaction kettle, reacting, centrifuging, washing with deionized water and absolute ethanol, and drying to obtain carbon microspheres; (ii) adding carbon microspheres into aqueous zinc acetate solution, ultrasonicating, aging, centrifuging, washing, calcining, to obtain hollow mesoporous zinc oxide microspheres; and (iii) immersing hollow mesoporous zinc oxide microspheres organic mildew preventive solution and drying.    USE - The material is useful for antimicrobial anti-mildew treatment in leather, textile, paper making and furniture fields (claimed).    ADVANTAGE - The anti-mildew material has no toxicity, is non-polluting, and has thermal stability.    DETAILED DESCRIPTION - Preparing long-term sustained release antimicrobial anti-mildew material comprises (i) dissolving glucose in deionized water, formulating into 0.5-1.5 mol/l solution, placing in a hydrothermal reaction kettle at 140-180 degrees C, reacting for 8-20 hours, completing the reaction, centrifuging the resulting mixture, washing with deionized water and absolute ethanol, respectively, and drying in a dry box for 24 hours, to obtain carbon microspheres; (ii) adding 0.1-0.5 g carbon microspheres into 0.5-1 mol/l aqueous solution of zinc acetate, ultrasonicating for 30-60 minutes, aging for 8-16 hours, centrifuging, washing with deionized water and absolute ethanol 3 times, drying, calcining at 400-500 degrees C for 2-4 hours, to obtain hollow mesoporous zinc oxide microspheres; and (iii) immersing 0-20 mg hollow mesoporous zinc oxide microspheres in 0.5-3 g/ml organic mildew preventive solution for 12-48 hours, and drying at room temperature.
NOVELTY - Manufacture of additive comprises drying herba schizonepetae, herba scutellariae and Gardenia, crushing, sieving, adding yeast and rice sprout, stirring for 40 minutes, fermenting at 45 degrees C for 3 days, mixing protein powder, glucose, lipase and fortune eupatorium herb, granulating, coating, packaging and storing at 18 degrees C.    USE - Method for manufacturing additive used for strengthening livestock immunity (claimed).    ADVANTAGE - The additive is simple. The manufacturing method is simple and environment-friendly.
NOVELTY - Antibacterial wound dressing comprises antibacterial superfine fiber film (1), calcium alginate fiber non-woven cloth (2) and supporting protection layer (3).    USE - Antibacterial wound dressing.    ADVANTAGE - The wound dressing is slow release, porous and has reduced toxic side effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of antibacterial wound dressing comprising mixing acetic acid solution and antibacterial medicine powder, dissolving, adding chitosan, polyethylene glycol and ethylene, stirring, electrostatic spinning, adding glutaric dialdehyde solution, drying for 12-36 hours, weaving, adding adhesive and calcium alginate fiber, sticking and cutting.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of antibacterial wound dressing.    Antibacterial superfine fiber film (1)    Calcium alginate fiber non-woven cloth (2)    Supporting protection layer (3)
NOVELTY - The device has a steam chamber (2) connected with a permeable chamber (1). The permeable chamber and the steam chamber are formed by oxygen-permeable material. An oxygen-permeable chamber (3) is connected with the steam chamber. Potential difference of the permeable chamber is lower than potential difference of the steam chamber. Potential difference of the oxygen-permeable chamber is greater than the potential difference of the steam chamber. A reaction room is provided with an inner pipe set (4), a sleeve (5) and an outside pipe set (6).    USE - Permeable water decomposing hydrogen preparing device.    ADVANTAGE - The device has high hydrogen production efficiency and better synergistic effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a permeable water decomposing hydrogen preparing device.    Permeable chamber (1)    Steam chamber (2)    Oxygen-permeable chamber (3)    Inner pipe set (4)    Sleeve (5)    Outside pipe set (6)
NOVELTY - Chicken manure processing device comprises a mixing unit, a dehydrating unit, a steam sterilizing unit and an exhaust gas absorption unit (11), where the mixing unit and the dehydrating unit are connected with the steam sterilizing unit, which is provided on the surface of the dehydrating unit. The exhaust gas absorption unit is provided in the inside of the mixing unit and the dehydrating unit. The mixing unit comprises a stir bucket (1), a driving motor (2), a packing auger blade (3), and a feeding port (4). Waste gas absorption unit comprises an ammonia absorber and sulfur dioxide absorber.    USE - Chicken manure processing device.    ADVANTAGE - The chicken manure processing device is cost-effective, eco-friendly and has simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a chicken manure processing device.    Stir bucket (1)    Driving motor (2)    Packing auger blade (3)    Feeding port (4)    Exhaust gas absorption unit (11)
NOVELTY - Fertilizer preparation involves crushing corncob grain, sweet potato leaves and bean straw stick. Chicken manure and pig manure mixture, celery and spinach leaves are mixed in the mass ratio of 2:3. Grassy straw, corncob grain, bentonite and peat soil, rhizome coptidis powder are added in a fermentation pool. Water is added to the obtained material, and then covered using a plastic film. The obtained mixture is fermented for 25-30 days. Chicken manure and pig manure mixture, and enzyme are poured into fermenting pool, and then fermented for 10-12 days.    USE - Method for preparing fertilizer used for improving selenium in soil (claimed).    ADVANTAGE - The method enables to produce the product that has improved selenium content and crop absorption rate of soil.    DETAILED DESCRIPTION - Fertilizer preparation involves crushing corncob grain, sweet potato leaves and bean straw stick. Chicken manure and pig manure mixture, celery and spinach leaves are mixed in the mass ratio of 2:3. Grassy straw, corncob grain, bentonite and peat soil, rhizome coptidis powder are added in a fermentation pool. Water is added to the obtained material, and then covered using a plastic film. The obtained mixture is fermented for 25-30 days. Chicken manure and pig manure mixture, and enzyme are poured into fermenting pool, and then fermented for 10-12 days. Selenium and selenium additive as sodium selenite are added to the obtained material, and then stirred uniformly. The obtained material is dried for 3 days, where the water content of obtained material is 45-55%. Microelement is added to the obtained material, and then stirred uniformly. The obtained material is extruded in an extruder, and then granulated. The obtained material is dried to obtain the desired product.
NOVELTY - Organic fertilizer preparation involves pre-processing cow dung as raw material raw material through heat radiation and water evaporation, where the water content of raw material is 50-65%. Solid urea (1-5 kilograms per cubic meter) is added to the mixed raw material. Bacillus subtilis and Aspergillus niger is added to the obtained material, where the ratio of Bacillus subtilis and Aspergillus niger is 20-50:1, respectively. The obtained mixture is fermented at 45 degrees C, where the water content is less than 40%.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method is simple, and enables to produce the product that is cost-effective and eco-friendly.    DETAILED DESCRIPTION - Organic fertilizer preparation involves pre-processing cow dung as raw material raw material through heat radiation and water evaporation, where the water content of raw material is 50-65%. Solid urea (1-5 kilograms per cubic meter) is added to the mixed raw material. Bacillus subtilis and Aspergillus niger is added to the obtained material, where the ratio of Bacillus subtilis and Aspergillus niger is 20-50:1, respectively. The obtained mixture is fermented at 45 degrees C, where the water content is less than 40%. Bacillus licheniformis strain is added to the obtained material, and then crushed. The obtained material is sieved, and then fermented for 1 month to obtain the desired product.
NOVELTY - Fertilizer drainage regulator comprises a top tank and a motor that is connected to an external power supply wire, where the motor drives the rotating screw threaded rod for moving in upward direction. A bottom tank is provided, which is equipped at lower side of the tank top. The motor also drives the thread stick downwards.    USE - Fertilizer drainage regulator.    ADVANTAGE - The fertilizer drainage regulator effectively regulates the moisture content of the fertilizer.
NOVELTY - Fertilizer compression drainage regulator comprises a support, a tank and a bottom tank, where the bottom tank is set at the center position of the regulator, where a water leakage hole is formed in the bottom tank. The support is welded and fixed at lower side of the bottom tank. A cylinder is set with a pole.    USE - Fertilizer compression drainage regulator.    ADVANTAGE - The fertilizer compression drainage regulator is easy to use and ensures simple structure, and effectively regulates fertilizer compression drainage.
NOVELTY - Device comprises a sludge fermentation groove (1) which is mounted with a walking bridge. The walking bridge frame is mounted with walking back and forth part of a stir device (2). The stir device is provided with terminal (3) and the bracket end (4) is mounted in a transmission chain of the terminal. The transmission chain is provided with multi-blades (6) and the multi-blades are hinged with bracket end. The lower part of the other end of stir device is rotated around the hinge point of the bracket end.    USE - Device used for fermenting compost (claimed).    ADVANTAGE - Device has simple structure and saves more than 50% energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a compost fermenting device.    Sludge fermentation groove (1)    Stir device (2)    Terminal (3)    Bracket end (4)    Multi-blades (6)
NOVELTY - Organic fertilizer fermenting device comprises a tube (1), supporting frame (2) and heating unit, where the tube is connected to supporting frame and heating device through the guide heat oil pipe (15). The guide heat oil pipe is connected to a cylinder body. The heat preservation material (18) is located between the outside wall (17) and inner container of fermenting device. The oil pipe is connected with the oil pump and a heating oil tank. The heating unit bag is provided with the high temperature oil furnace and is connected to the oil pump.    USE - Organic fertilizer fermenting device.    ADVANTAGE - The organic fertilizer fermenting device has a closed structure, removable vertical mixing arm and good heat preservation effect, reduces footprints and resistance, and improves product quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an organic fertilizer fermenting device.    Tube (1)    Supporting frame (2)    Guide heat oil pipe (15)    Outside wall (17)    Heat preservation material (18)
NOVELTY - Preparing composite substrate involves mixing banana, pineapple stem leaves and chicken manure to obtain mixture. Trichoderma, Bacillus subtilis, Aspergillus niger and Streptomyces are added into mixture and then fermented for 8-15 days to obtain fermentation material. The fermentation material is dried and then crushed to obtain banana pineapple fertilizer. Coconut husk is added into fertilizer and then polyvinyl alcohol is added to mixture. Boric acid solution is sprayed on mixture and then cured to obtain the product.    USE - Composite substrate used for promoting growth of vegetable seedling.    ADVANTAGE - The composite substrate has good physical properties, permeability, and nutrient contents.
NOVELTY - Fertilizer comprises (in pts.wt.): charcoal (25-35), liquid organic fertilizer (8-12), humus (8-10) and mushroom waste (45-55).    USE - Fertilizer used for promoting growth of plant and controlling pest.    ADVANTAGE - The fertilizer loosens soil, improves moisture content of soil and absorbs heavy metal.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing raw materials and then adding vinegar to obtain mixture;    (B) fermenting mixture at 50 degrees C for 4-8 days and then turning the fermented material; and    (C) fermenting fermented material at 60 degrees C for 4-8 days and then turning fermented material to obtain the product.
NOVELTY - Culture material comprises (in pts.wt.): pine wood chips (25-35), cotton seed hull (5-10), rapeseed cake (5-10), sand (10-20), pine needle (5-10), wheat straw stick (5-10), glucose (0.5 1), calcium superphosphate (0.2-0.3) and magnesium sulfate (0.2-0.4), and prepared by mixing pine wood meal, cotton seed hulls, rapeseed cake, pine needle and wheat straw stick to obtain granule. The granule is mixed with sand, glucose, calcium superphosphate and magnesium sulfate in indole acetic acid aqueous solution to obtain product.    USE - Culture material used for growing pine mushroom (claimed).
NOVELTY - Granular soil fertilizer preparation involves taking adsorbent, calcium, water retention agent, chicken manure and peat soil, calcium dihydrogen phosphate, solubilizing bacteria, urea, fermenting bacteria and Bacillus phytase. The calcium is ground, and then mixed with chicken manure and peat soil. The obtained material is fermentee with Bacillus phytase for 10-12 days. The fermented material is mixed with calcium dihydrogen phosphate, urea and water. The obtained material is extruded to obtain the finished product.    USE - Method for preparing granular soil fertilizer (claimed).    ADVANTAGE - The method enables to prepare granular soil fertilizer in simple manner.
NOVELTY - Preparing organic fertilizer involves mixing clay, sepiolite, methylacetopyranone, dairy manure, wooden meal, bean straw stick powder and powdered rock phosphate to obtain mixture. The obtained mixture is fermented for 10-12 days. The fermented product is extruded to obtain product.    USE - Method for preparing organic fertilizer used for improving soil (claimed).
NOVELTY - Organic fertilizer comprises a mixture of bentonite and sea shell powder (5-10), calcium propionate (10-20), spirulina powder (10-20), dry cow dung (40-50), mixture of wooden meal and food debris (30-50), solubilizing bacteria (1-2), calcium superphosphate (2-4) and fermenting agent (1-2).    USE - Organic fertilizer used for enhancing microbial activity of soil (claimed).    ADVANTAGE - The organic fertilizer enables efficiently enhancing microbial activity of soil.
NOVELTY - Using organic fertilizer involves utilizing rod shaped fertilizer. The fertilizer is inserted to the one side of the ridge to form saline soil. Corn starch is heated with water at 70-75 degrees C for 1 hours. The obtained material is cooled to 45 degrees C. The obtained paste is sprayed using a pressure spraying apparatus on the surface to obtain thin film. The fertilizer is inserted to the other side of the ridge, where the fertilizer comprises sepiolite clay, methylacetopyranone, seeds, dried cow dung, sawdust, straw legume powder, phosphate solubilizing bacteria, phosphate rock, fermentative bacteria.    USE - Method for using organic fertilizer for improving soil (claimed) and reducing salt quantity of soil, enhance activity of microorganism and enzyme in soil and promoting growth of plant root.    ADVANTAGE - The method is simple and convenient.
NOVELTY - Manufacturing organic fertilizer involves mixing acidic bentonite and clam shell powder in mass ratio of 6:1 to obtain a mixture. The mixture is mixed with calcium propionate, spirulina powder, dry dairy manure, wooden meal and food debris in mass ratio of 1:5 and then fermentation is carried out for 10-12 days in presence of water (63-65%) to obtain a product. The product is extruded in an extruder and then dried to obtain final product.    USE - Method for manufacturing organic fertilizer (claimed) for promoting growth of plant root.    ADVANTAGE - The method enables to manufacture organic fertilizer that enhances microorganism activity of soil and reduces soil salinity.
NOVELTY - The extraction rectification device has an extraction agent recovery tower (5) whose top is set with a first outlet extracting agent recovery tower and bottom is set with a second outlet extracting agent recovery tower. A light component tower of a light-constituent removing tower (1) is removed. A second outlet is connected to a heavy component tower raw material inlet of a heavy component tower (2). A heavy component tower raw material outlet is connected to an extracting rectifying tower raw material inlet of first extraction rectifying tower (3).    USE - Extraction rectification device for separating propane and propylene.    ADVANTAGE - The extraction rectification device has simple structure, low investment, good separation effect of propane and propylene. Good social benefit is obtained. The energy consumption of the extraction rectification device is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for extraction rectification method for separating propane and propylene.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the extraction rectification device. (Drawing includes non-English language text)    Light-constituent removing tower (1)    Heavy component tower (2)    Extraction rectifying tower (3)    Regular filler (4)    Extraction agent recovery tower (5)
NOVELTY - The method involves performing condenser cooling process by using low temperature fuel refrigerant, where the refrigerant contains liquid helium, liquid oxygen, liquid nitrogen and liquid propane. Harmful substance produced during low temperature liquid phase is separated to reduce combustion emission of the harmful substance. A condenser is connected with a refrigerating device. Liquefied natural gas is added to a combustion part to support low temperature fuel oxidizing agent.    USE - Method for separating combustion waste gas from a low temperature fuel zero-carbon burner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a zero carbon burner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for separating combustion waste gas from a low temperature fuel zero-carbon burner.
NOVELTY - The system has a fuel cell module (FCM) (5) for generating power. A bottoming cycle power block (BCPB) (15) is provided through which motive fluid circulates to generate the power. A waste heat heat-transfer unit (WHHTU) (12) transfers heat from exhaust gases (EG) of the FCM to BCPB motive fluid to produce a desired combined power level from the FCM and the BCPB. A controller (17) transmits a control signal (C) to a flow control component (22) to cause the power level of the BCPB to increase when detected heat data indicates a value that increases above a predetermined threshold.    USE - System for generating power from fuel cell waste heat in a hybrid fuel cell-based power plant, a combined fuel cell-Rankine cycle power plant and a hybrid fuel cell-ORC power plant.    ADVANTAGE - The hybrid fuel cell-based power plant profitably employs fuel cells for a period of time generally beyond normal life span. The system increases power output and efficiency of the hybrid fuel cell-based power plant. The system efficiently utilizes the waste heat of the fuel cell for generating additional power in the power plant.    DETAILED DESCRIPTION - The BCPB is an organic rankine cycle (ORC) power block and a steam rankine cycle power block. The heat data is temperature data and heat flux data. The flow control component is a diverter i.e. bypass valve of BCPB, and a pump of WHHTU. An INDEPENDENT CLAIM is also included for a method for controlling output power of a combined fuel cell-Rankine cycle power plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a hybrid fuel cell-based power plant.    Control signal (C)    Exhaust gas (EG)    FCM (5)    WHHTU (12)    BCPB (15)    Controller (17)    Flow control component (22)
NOVELTY - An electrolytic cell has an anodic compartment and a cathodic compartment partitioned by a cation-exchange membrane (100) and provided with unit for feeding and discharging an alkaline solution. The anodic compartment contains an anode (300) for oxygen (500) evolution, and cathodic compartment contains a cathode (310) for hydrogen (510) evolution and comprising a porous web in intimate contact with membrane through a catalytically-activated layer containing at least one noble metal chosen from platinum and palladium.    USE - Electrolytic cell used in electrolyzer for electrolysis of alkali solution (all claimed) e.g. caustic soda and potash for producing hydrogen.    ADVANTAGE - The electrolytic cell is safe and economical. Hydrogen having high purity is produced by electrolysis method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) electrolyzer; and    (2) electrolysis method in cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional side view of electrolysis cell.    Cation exchange membrane (100)    Anodic wall (200)    Anode (300)    Cathode (310)    Oxygen (500)    Hydrogen (510)    Anodic current collector (600)
NOVELTY - An active auxiliary agent comprises bagasse, peanut cake, cornmeal and yeast secondary fermentation, active substance extract, 10-20 wt.% small organic molecules extract, 20-40 wt.% oligosaccharide, 30-50 wt.% fulvic acid, 35-40 wt.% surfactant, 0-5 wt.% filler, and trace element.    USE - Active auxiliary agent used for fertilizer (claimed).    ADVANTAGE - The auxiliary agent improves fertilizer and soil properties, regulates growing condition of crops, increases crop nutrient absorption ability, fertilizer use efficiency and grain yield, and reduces fertilizer environment pollution.
NOVELTY - Manufacturing liquid fertilizer using cattle blood comprises: crushing the cattle blood; adding protease into crushed blood; adding the blood with protease into a reactor and reacting by heating; and cooling the reaction blood.    USE - The method is useful for manufacturing liquid fertilizer (claimed).    ADVANTAGE - The liquid fertilizer includes amino acids, has rapid and long-lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for liquid fertilizer, prepared by above mentioned method.
NOVELTY - This new type utility claims a solar energy light heat circulation one garbage treatment device, including depot, wherein the material, wherein the discharging gas and thermal circulation treatment system, thermal circulation gas system comprising a gas collecting processing device, a return pipe, gas injection device, collecting device and reflux pipe is connected with a gas injection device and reflux pipe are connected, the depot is set air inlet, a top mounted with a photo-thermal collecting plate, garbage material wherein the garbage material is provided wherein a depot of . This utility new type use solar energy photo-thermal effect of air and heat circulation principle promoting decomposing of waste, increase the fermentation efficiency, valid for a household garbage processing process and reduce a pollution for environment.
NOVELTY - This new type utility claims one in a sewage treatment process microorganism active temperature control system, comprising a tube type heat exchanger, one collecting the condensed water of steam condensate recovery main pipeline of a steam inlet pipe in a pipe range inner tube type heat exchanger, a steam pipe of tube connected the condensing water cooling pool, inner one collecting station waste water of sewage water collecting regulating pool through one lifting the waste water conveying pump to tube type heat exchanger of the shell side of the water inlet pipe, the water pipe of the shell side connected pressure oxygen pool. B sewage and water collecting regulating pool between the station set with one sewage station for a waste water filter of a hydraulic machinery. This system through collecting each produce a workshop steam condensed water, through waste heat of steam condensed water, which is used for heating sewage treatment anaerobic process waste water of section, so as to increase the anaerobic process section microorganism of biological activity, increase efficiency of microorganism treatment.
NOVELTY - This new utility model belongs to sewage treatment area, of one of industrial sewage processing device, comprising in turn connected with the grid well pipe, sediment pool, the first filter pool, microorganism reaction pool, between the second filter pool, the sterilizing pool and dechlorinating pool, the first filter pool and microorganism reaction pool is set with micro-computer water quality with acid alkali controller, used for pH value to avoid excessive floating microorganism to cause damage, the filtering pool and on the second pipeline between the disinfecting pool set with plate frame filter, used for collecting microorganism and fermentation product for preparing fungus fertile. This new utility model using physical chemistry method and microorganism method mutually combined, effective of removing each kind of impurities and material of industrial sewage of chemistry, and effective recycling use of waste, implementation of the waste as treasure.
NOVELTY - This utility new type provide taurine with a pipeline cooling desalting device. It is by spiral conveying machine (1), cooling interlayer (2), a feeding flow rate controller (3), a speed reducing motor (4), a cooling water inlet valve (5), cooling water outlet valve (6), a feeding pipe (7), a discharge valve (8), a centrifugal device (9), a liquid discharging valve (10), a spiral shaft (11) compose. This utility new type has simple structure, convenient operation, rational process, compact structure, small floor area, cooling separating effect is good, loss, the energy consumption is low.
NOVELTY - One of marsh gas production equipment, including one, provided with double sealed structure in on group, two group sealed structural form of closeness space is fermentation chamber, wherein the inner tunnel is set with track, used for fermentation material converying lorry is driven by driving mechanism of walking on the track inside, via corresponding open door using the lorry through transition chamber enter into the fermentation is indoor, a water inlet pipe in the fermentation room also set with to fermentation material supply used for dividing the water and liquid discharging pipe used for discharging waste liquid is used for extraction and the marsh gas exhaust pipe, one water inlet pipe and passes through the tunnel end well and water supply pipeline of each external connect, also equipped with used for discharging, waste liquid discharging pipe by the waste liquid after fermentation of wherein said the discharging lorry. The device by using fermentation room closeness set in laneway in the fermentation chamber and two side respectively provided with one individual can regulate and control the transition chamber, make lorry through transition chamber enter into ferment indoor, the scheme investment cost low, the safety performance is good, and increase fermentation effect.
NOVELTY - This utility new type relates to a hydraulic pressure type marsh gas anaerobic one, including the marsh gas anaerobic tank, a biogas anaerobic happen happen inside a tank forming a cavity, a stir device, hanging the marsh gas anaerobic happen inside a tank, mixer lifting device, mounted inside a happen in marsh gas anaerobic tank, and a stirrer lifting device driving a stir device by a working position at the marsh gas anaerobic tank happen at the bottom of lifting maintenance window to the marsh gas anaerobic happen tank top wall, a control cabinet, a stir and a device, used for a work of a stir device. This utility new type using a stirrer lifting device driving a stir device by a working position located at the marsh gas anaerobic tank happen at the bottom of lifting maintenance window to the marsh gas anaerobic happen tank top wall, so, maintenance operation is convenient, and the cost is greatly reduced, so as to make the whole marsh gas anaerobic tank happen more efficient.
NOVELTY - Ecological recycling treatment of waste bacteria stick comprises removing waste bacteria stick plastic film, burying under canopy of fruit trees to allow moisture and nutrients penetrate the waste bacteria stick, activating mycelial growth, germinating to increase production of new strains, harvesting and sprinkling with fermentation agent in the pit cover to allow self-fermentation and organic fertilizer absorption for 3-4 months.    USE - Method for carrying out ecological recycling treatment of waste bacteria stick (claimed) used for improving soil structure.    ADVANTAGE - The method is environment-friendly.
NOVELTY - Use of biogas residue for fermenting feed, comprises (i) mixing egg-laying chicken feed with multi-dimensional factors, and fermenting by adding biogas residue; (ii) mixing egg-laying chicken feed with trace elements, and fermenting using biogas residue; and (iii) mixing egg-laying chicken feed with protein powder, and feeding chicken, and carrying out fermentation by adding biogas residue, where the amount of protein powder added accounts to 2-3%, and the biogas residue used during fermentation is biogas materials, corn, red stone powder, polypeptides, calcium powder, lipase or bitter orange.    USE - The feed is useful for increasing immunity in chicken poultry, and egg production.    ADVANTAGE - The method is simple, and utilizes easily available raw materials.    DETAILED DESCRIPTION - Use of biogas residue for fermenting feed, comprises (i) mixing egg-laying chicken feed with multi-dimensional factors, while feeding chicken, and carrying out fermentation by adding biogas residue, where the multi-dimensional factors are rich in vitamin A and vitamin D, and the amount of multi-dimensional factors added, is 0.2-0.3%; (ii) mixing egg-laying chicken feed with trace elements, while feeding chicken, and carrying out fermentation using biogas residue, where the trace elements are rich in copper, iron, zinc, selenium, molybdenum and manganese, and the amount of trace elements added accounts to 0.15-0.2%; and (iii) mixing the egg-laying chicken feed with protein powder, and while feeding chicken, and carrying out fermentation by adding biogas residue, where the amount of protein powder added accounts to 2-3%, and the biogas residue used during fermentation is biogas materials, corn, red stone powder, polypeptides, calcium powder, lipase, bitter orange, amino acid, Lophatherum gracile, root of kudzu vine, rhizoma cibotii, dragon's bone, malt and garlic oil.
NOVELTY - Hydrogenation of 4C fraction, comprises dissolving the 4C fraction in an absorbent to obtain a feed mixture, mixing the feed mixture with hydrogen gas, introducing a hydrogenation catalyst A into a first-stage reactor, performing hydrogenation reaction, mixing the reaction effluent with hydrogen gas, introducing hydrogenation catalyst B into a second-stage reactor, performing hydrogenation reaction, and separating liquid reaction effluent in the second-stage reactor from the absorbent to obtain 4C fraction hydrogenation product.    USE - The method is useful for the hydrogenation of 4C fraction (claimed).    ADVANTAGE - The method ensures efficient and economical hydrogenation of 4C fraction with high catalyst hydrogenation activity.
NOVELTY - Preparing 4-(1-hydroxy-1-methylethyl)-2-propyl-1H-imidazole-5-carboxylate, comprises (A) reacting alpha -chloro diethyl oxaloacetate with a salt of butanamidine (I) in the presence of an organic base to obtain diethyl 4-propylcyclopenta-1,3-diene-1,2-dicarboxylate (II), and (B) reacting (II) with a Grignard reagent (III) to give 4-(1-hydroxy-1-methylethyl)-2-propyl-1H-imidazole-5-carboxylate.    USE - The method is useful for preparing 4-(1-hydroxy-1-methylethyl)-2-propyl-1H-imidazole-5-carboxylate (claimed).    ADVANTAGE - The method is capable of preparing the 4-(1-hydroxy-1-methylethyl)-2-propyl-1H-imidazole-5-carboxylate with high yield and mild reaction condition in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing 4-(1-hydroxy-1-methylethyl)-2-propyl-1H-imidazole-5-carboxylate, comprises (A) reacting alpha -chloro diethyl oxaloacetate with a salt of butanamidine of formula (I) in the presence of an organic base to obtain diethyl 4-propylcyclopenta-1,3-diene-1,2-dicarboxylate of formula (II), and (B) reacting (II) with a Grignard reagent of formula (CH3MgX) (III) to give 4-(1-hydroxy-1-methylethyl)-2-propyl-1H-imidazole-5-carboxylate.    X = halo, preferably Br.
NOVELTY - Synthesizing metronidazole comprises taking 2-methyl-5-nitroimidazole and ethylene oxide as raw material and then mixing, subjecting the mixture to hydroxylation reaction, diluting the hydroxylated mixture with water and then neutralizing, separating solid and liquid from the neutralized mixture to obtain a crude product of metronidazole, wetting the crude product to obtain purified crystals of metronidazole, subjecting the crystals to solid-liquid separation, and washing the obtained solid material with purified water and then drying to obtain metronidazole.    USE - The method is useful for synthesizing metronidazole (claimed).    ADVANTAGE - The method is capable of synthesizing the metronidazole in an economical and environmentally-friendly manner.
NOVELTY - Extracting scopolamine comprises processing fresh raw material by heating it in oven, crushing hot mixture and then collecting coarse powder, adding bio-enzyme to powder and then performing enzymolysis, adding certain volume of water to enzymolyzed product and then filtering to obtain hydrolysates, placing hydrolysates in Soxhlet extractor and then extracting using solvent, refluxing extract to obtain crude extract of scopolamine, introducing crude extract into macroporous resin column to obtain liquid extract and then eluting, and concentrating the eluate under reduced pressure.    USE - The method is useful for extracting scopolamine (claimed).    ADVANTAGE - The method is capable of easily extracting the scopolamine in an efficient manner.    DETAILED DESCRIPTION - Extracting scopolamine comprises processing fresh raw material by heating it at 60-70 degrees C for 1-3 hours in an oven, crushing the hot mixture into 40-60 meshes and then collecting coarse powder, weighing a certain amount of coarse powder, adding 30-70 pts. wt. of bio-enzyme to the powder and then performing enzymolysis, adding a certain volume of water to the enzymolyzed product and then filtering to obtain coarse powder hydrolysates, placing the coarse powder hydrolysates in a Soxhlet extractor and then extracting using a solvent including alcohol, refluxing the extract to obtain a crude extract of scopolamine, introducing the crude extract into macroporous resin column to obtain a liquid extract and then eluting to obtain eluate, and concentrating the eluate under reduced pressure.
NOVELTY - The device has reinforcing rib plate and aeration pedestal which are provided with aeration system. The ball valve and pipe portion are provided with discharge system (8). The tube portion and fan are provided with longitudinal axis of tank main portion. The end of tank main portion is provided with pulley. A middle portion is equipped with shaft. A lifting oil cylinder (17) is connected with mesh cover plate. The aeration groove (16) is connected with reinforcing rib plate.    USE - Automatic hydraulic flip-organics aerobic oxidant resources (OAR) processing device.    ADVANTAGE - The automatic hydraulic flip-OAR processing device ensures low energy consumption, high efficiency, simple structure, small floor space and simple operation in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic hydraulic flip-OAR processing device.    Machine frame (1)    Ceiling (2)    Spraying system (3)    Discharge system (8)    Aeration groove (16)    Lifting oil cylinder (17)
NOVELTY - The system has air blower intelligent control unit which includes display screen and work program logic controller (5). The work display screen (6) and program logic controller are connected through lead. The air blower is connected with fermentation process monitor portion. A transducer (11) is connected with oxygen sensor (12), gas sensor and sulfureted hydrogen sensor (15). The oxygen sensor, gas sensor and sulfureted hydrogen sensor are located on air inlet chamber. The suction probe (8) is connected with air program logic controller.    USE - Portable sludge aerobic fermenting intelligent diagnosis system.    ADVANTAGE - The portable sludge aerobic fermenting intelligent diagnosis system is provided to realize intelligent timing precision quantitative blower and adjust the sludge aerobic fermentation in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the portable sludge aerobic fermenting intelligent diagnosis system.    Work program logic controller (5)    Work display screen (6)    Suction probe (8)    Transducer (11)    Oxygen sensor (12)    Sulfureted hydrogen sensor (15)
NOVELTY - The device has a frame (1) that is set with two rows of fermentation tank that is set with multiple layer fermenting chamber (3). A reverse turning bed (8) is provided in the bottom of fermenting chamber and the frame is set with a turning control device. The reverse turning bed is connected with the support frame. The outer side of frame is set with an air blower (4) that is connected with a draught fan (5) through an air pipe (6). The frame is set with a distributor (9) in middle portion. A belt machine (7) is provided in the outer side of the frame.    USE - Tower-type aerobic composite device used for treatment of sludge.    ADVANTAGE - The automation degree is improved, energy consumption is reduced, floor area and construction period are reduced and working environment is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the aerobic composite device.    Frame (1)    Fermenting chamber (3)    Air blower (4)    Draught fan (5)    Air pipe (6)    Belt machine (7)    Reverse turning bed (8)    Distributor (9)
NOVELTY - P-anisic acid preparation involves taking proper amount of rough sulfate turpentine oil for fractionating to obtain coarse anise camphor, and then treating the obtained large anise camphor crystals are separate to get a high purity large anise camphor. The separated high purity large anise camphor is added in sodium hydrogen sulfite solution in a reaction kettle with ozone introduction to get aldehyde sodium sulfite adduct.    USE - Method for preparing p-anisic acid (claimed) used for medicine, food and cosmetic industry.    ADVANTAGE - The method prepares p-anisic acid with high yield and high purity in a simple and eco-friendly manner without using toxic and harmful solvent under mild reaction condition.    DETAILED DESCRIPTION - P-anisic acid preparation involves taking proper amount of rough sulfate turpentine oil for fractionating to obtain coarse anise camphor, and then treating the obtained large anise camphor crystals are separate to get a high purity large anise camphor. The separated high purity large anise camphor is added in sodium hydrogen sulfite solution in a reaction kettle with ozone introduction to get aldehyde sodium sulfite adduct. The obtained adduct is added in sodium hydroxide solution and hydrogen peroxide solution with stirring at 65-85 degrees C for 5.0-9.0 hours to obtain reaction product. The obtained reaction product is treated with hydrochloric acid solution to obtain the aniseed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the p-anisic acid preparation method. (Drawing includes non-English language text).
NOVELTY - Synthesizing isoquinoline salt (I), comprises selecting substituted aromatic hydrocarbon, alkynes and hyaluronic acid as raw material and then reacting in a presence of transition metal catalyst and organic solvent.    USE - The method is useful for synthesizing (I) (claimed), which is useful in fine chemicals, medicine, pesticide, spices and optoelectronic industries.    ADVANTAGE - The method is capable of economically synthesizing (I) under mild reaction condition with high purity and yield and without pollution.    DETAILED DESCRIPTION - Synthesizing isoquinoline salt of formula (I), comprises selecting substituted aromatic hydrocarbon compound of formula (II), alkynes compound of formula (R2-CC-R3) and acid as raw material and then reacting in transition metal catalyst and organic solvent.    R1-R3 = 6-60C-aryl (preferably 6-20C-aryl), linear or branched 1-40C-alkoxy (preferably linear or branched 1-4C-alkoxy), halo, furanyl, phenyl, phenoxy, halo, pyridinyl, pyridyl, OH, nitro, amino, linear or branched 1-40C-ester (preferably linear or branched 1-6C-acyl or sulfonic acid) (all optionally substituted), H, or linear or branched 1-40C-aliphatic hydrocarbyl (preferably linear or branched 1-4C-alkyl).
NOVELTY - The reactor has a parallel clapboard reactor body divided into five chambers. A baffle plate is connected with the first chamber. A flow area is connected with a single cellular cell pool. An anode film and a cathode film are connected with a clamping slot through a titanium wire. The clamping slot is linked with a small hole. An external voltage stabilizing power source is connected with the five chambers. A rubber plug seal is connected with the anode film and the cathode film. A water sample collecting pipe is connected with a sludge sampling tube.    USE - Electric auxiliary microorganism fermenting hydrogen anaerobic baffle plate reactor.    ADVANTAGE - The reactor is simple in structure, and has high volume utilization rate. The reactor reduces working time, and performs integrated waste water treatment and production operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an electric auxiliary microorganism fermenting hydrogen anaerobic baffle plate reactor.
NOVELTY - The method involves performing a prior culture domestication process in an active sludge oxidation ditch reactor. First sample i.e. germ, is stored in a first storage box. A destructive test is performed in an inner side of the active sludge oxidation ditch reactor. Second sample i.e. fungus, is stored in a second storage box. Gradient gel electric pulse wave form is generated. A microorganism diversity detection process is performed on the first sample and the second sample. Microorganism diversity detection result is obtained. Active sludge expansion process is performed.    USE - Active sludge expansion method.    ADVANTAGE - The method ensures realizing high precision value and high reliability and preventing microorganism population of sludge expansion angle.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an active sludge expansion method.'(Drawing includes non-English language text)'
NOVELTY - This utility new type relates to a one family vegetable fertilizer generator, a device comprising a main body, the main body top part opening and set with a top cover, the top cover and the main body form seal system, a main body inner part by up to lower orderly comprising solid containing room, soil room and liquid , a solid containing room set with the bottom of the first network-shaped support plate, a the first network-shaped supporting plate set with several the first mesh, the bottom of said humic soil room set with second network-shaped support plate, a the second network-shaped supporting plate set with several second mesh, a wall of the humic soil room and liquid fertilizer room are set with connected inner the main body outside two side of taking door is, extract the door and the main body is set with seal, the water wherein a set with a wall of the liquid lower end, the water outlet is set with a valve. This generator can be a kitchen garbage in a fermentation, a cross and a fertilizer used in home ferment of vegetable, the convenient use, green and environment-friendly, safe and it saves cost.
NOVELTY - One a municipal organic waste is a use device, relating to one a municipal organic waste is a device, set with cover is mixed with fermentation pool in a municipal green belt (6) (4), the mixed fermentation pool (4) one side set with the machine room (9), a spiral conveyor (11) of conveying pipeline (13) in a mixed fermentation pool (4) at the bottom of one side, (9) inner of electrical machine (12) drives the spiral conveyor (11), the utility model is new type environmental sanitation department through a green department combined in a green belt. mixed fermentation pool, the vegetable, fruit, vegetable, remaining in the green area of leaves into the mixed fermentation pool, the green department need time for green fertilizer, a directly after fermentation of the mixed organic substance a scattering to green belt in the time when the mixed organic substance amount is large, a contact free farmers for agricultural production, this utility new type effectively reduces the occupied by organic matter garbage landfill.
NOVELTY - One for domestic garbage of the fermentation cabin device, comprising has to use for domestic garbage for fermentation process of fermentation cabin device main body, wherein fermentation cabin device is set with main body and the suction pipe (4), set up for gas pipe and air suction pipe (4) is connected (5), set up for gas processing device, an air suction pipe and air pipe (5) is connected (4) set up for net distribution present, through air suction pipe (4) is composed of gas collecting large network, by gas treatment device for waste gas processing harmless treatment, again not directly discharge in air or to use air pump to pump body collecting gas, collecting gas range so large, collecting gas small cost.
NOVELTY - This utility new type refers to a agricultural waste crushing one fertilizing device, comprising crushing cavity and the left side set with bottom of transmission squeegee roller bracket, transmission squeegee roller bracket is set with squeegee roller fixed bracket, a fixed bracket is set with a fixed extrusion extruding wheel set with a transmission, a crushing cavity right inner side wall a and the left side connecting with a motor bracket, a motor bracket set with the first drive motor, the drive motor and the first transmission connection with driving belt extruding, crushing cavity right side upper part set with a stir between crushing cavity and stir chamber connecting with a pipe, stir chamber right side set with a second driving motor, the second driving motor left side vertical to two stir shaft is connected with the lower part stir chamber set with a filter screen. This utility new type device for aiming at the agricultural waste treatment process, a waste into agricultural fertilizer implementation and use, according to need and convenient use, reduces the agricultural waste for environment of pollution and improve the source of agricultural fertilizer.
NOVELTY - This utility new type claims a one for municipal sludge biology compost process of automatic production system, comprising a feeding buffer pool, reactor and separator, the top is open and the reactor set with distributing device, a feeding buffer pool of material wherein the first collecting transmission device to a distributor, the bottom reactor set with scraper, lower scraper set with second collecting transmission device, second collecting transmission device to a separator, a distributor and a scraper set b through the first reactor top and bottom guide rail and a second guide rail fixing, a distributor and scraper through the first guide rail and second guide rail the back and forth movement of the distributing device, scraper, collecting the first transmission device, second collecting transmission device directly or indirectly a and c. This utility new type is one automatic is a municipal sludge biology compost system, it has safety and environment-friendly, saves manpower, production efficiency is high and so on.
NOVELTY - This utility new type under one relates to a straw organic fertilizer quick fermentation kettle, wherein the speed fermentation kettle with kettle body is cylindrical (1), kettle body (1) set with heater. The beneficial effect is as follows: a is straw fermenting supplementary heat, greatly shortens the fermenting time, especially using solar energy heat storage device and a heat recovery device fermenting steam exploded wood fibre straw, saves a lot of fuel, which ensures the heat supply, reduces the fermentation cost, after to the front spring sowing a continuous fermentation fertilizer-making, as a device of a straw fertilizer.
NOVELTY - This utility new type relates to a one granule compound fertilizer production line, comprising a mixed, granulating system, a screen, wherein the raw material in turn by a, mixed stirrer, crusher raw material, granulating disk, then orderly entering into drying cylinder, a cooling cylinder, a level one, level two, at last orderly entering into finished product machine, machine, a packaging machine. Each process a distributing reasonable, controllable character increase, using granule compound fertilizer method and granulating device, and simplify technology, reduces the cost, and granulation process using mixing, full integration of drying, cooling the coated and integrated cost is only a normal compound fertilizer granulation is cost. And increasing the silencing dust-removing device in a source line, valid solves the dust pollution and ensures the product quality reaches the national standard.
NOVELTY - This utility new type claims a methyl alcohol water reforming one generation air conditioner system, the air conditioner system comprising: a hydrogen, generation device, air conditioner device, hydrogen through a water methanol reforming hydrogen preparation to obtain a hydrogen supply to generation a generation, a electric energy for air conditioner device operation. The air conditioning device is a movable type air conditioner device, without need to outdoor machine; a movable type air conditioner device is used for leading the outdoor connecting pipe, comprising a mobile air conditioner comprising a compressor, an exhaust fan, an electric heater, an evaporator, an air cooling fin-type condenser, a ventilation system, wherein, the ventilation system comprising closeness cover, a heat exchange chamber, a blowing pipeline, a supplementing device and fan, which is used for extracting the outdoor air, and the inner room by the air of the cooling. This utility new type claims a methyl alcohol water reforming generation air conditioner system, without extra power supply, air conditioner system operation.
NOVELTY - This utility new type claims a one for a indoxacarb intermediate a washing kettle, washing the reaction kettle is the bottom of a cone of the reaction kettle, the bottom of the taper is set with discharge wherein a reaction kettle, the reaction kettle is a tapered bottom and horizontal position of inclined angle is 45 degrees, the bottom and a side wall of the reaction kettle is set with jacket layer, a thickness of the jacket layer is 13cm-15cm, the part in the reaction kettle is set with anchor agitator blade, the utility model is new type aiming at prepare acidified water of indoxacarb intermediate washing using a special kettle bottom conical bottom of reaction kettle, and also with a jacket cone, which is good for reaction after the kettle body. liquid heat preservation, one operation batch standing water diversion of operation time is greatly shortened, at the same time oil water separating effect, saves a lot of cost and waste water in carried oil less and is easy to process.
NOVELTY - A kind of one hydraulic pressure wave to deliver power and electrolytic hydrogen combination device, and it mainly make up of construction, to hydraulic pump, low pressure oil box, high pressure oil tank, a floating machine frame, rotor hydraulic motor, electric generator, a distribution box, electrolytic tank. Automatic stepless speed regulating to the hydraulic motor is high efficient big power of using hydraulic pressure can switch is mechanical drive electric generator generate electricity, hydrogen electrolytic device for electrolytic water as hydrogen and oxygen fuel. The device can be large scale using wave power generation and electrolytic hydrogen, group is large and hydrogen fuel production line array and can move on at sea level.
NOVELTY - Lavender fertilization method comprises: (i) selecting a block, loosening soil, irrigating and administering 4-6 kg homemade organic fertilizer/ acre of land; (ii) planting seedling during May month, administering 16-20 kg Mushi urea and 12-15 kg diammonium fertilizer, planting at a distance of 8-9 cm with a depth of 10-12 cm; (iii) carrying out foliar fertilization for twice using 120 g urea and 100 g potassium dihydrogen phosphate for first time, and 160 g urea and 120 g potassium dihydrogen phosphate for second time after 12-15 days, then no-fertilizer after flowering period.    USE - The method is useful as Lavender fertilization method.    ADVANTAGE - The fertilizer satisfies different nutrient components required for the growth of Lavender, is non-toxic, odorless, safe and has long-lasting fertilizer efficiency.
NOVELTY - This utility new type relates to a synthesis ammonia production device one waste heat recovery system, including low variable furnace, low change to the water pre-heater, a gas pre-heater, a desalted water preheater, low change water-cooling device, a waste heat boiler, a desulphurization groove, natural gas heating furnace and oxygen removing groove, low change furnace, low change to the water pre-heater, a gas pre-heater, desalted water pre-heater and low change water cooling device in turn connecting, said low change to the outlet water pre-heater and a waste heat boiler connected with the natural gas inlet and outlet and a desulphurization groove, natural gas heating furnace of the gas pre-heater connected with the desalted water outlet and heater oxygen removing groove. This utility new type of synthesis ammonia production device waste heat recovery system, for natural gas in natural gas pipeline of a pre-increase the waste heat use efficiency and reduces the low variable water cooling device load, reduces the decarburization material pneuma air inlet temperature, increase the yield of decarburization section nitrogen pneuma and hydrogen.
NOVELTY - A one ammonia recovery vehicle draining system of ammonia in the pneuma, referring to the chemical technology field, use the original ammonia vehicle relaxation pneuma removing pipeline of the ice machine, the ammonia the relaxation of the pneuma ammonia into ammonia absorption tower bubbling section through the bottom and the upper part of the cover section two times and a desalted water absorption inner tower, absorbing the purge in 95% of ammonia, residual gas entering into absorption groove bottom, then one time and desalting water of wherein a bubble absorbed in tower makes the air containing ammonia is less than 0.5%, of a circulation ammonia water concentration to 11% urea analysis to a liquid ammonia for urea production with. This utility new type method is simple, a low investment cost, good economic benefit, not only a ammonia and does not pollute the environment, the good effect.
NOVELTY - Preparation of rebaudioside M involves performing substitution reaction of rebaudioside C and (2R,3R,4S,5S,6R)-5-(acetyloxy)-6-((acetyloxy)methyl)-3,4-bis((((2S,3R,4S,5R,6R)-3,4,5-tris(acetyloxy)-6-((acetyloxy)methyl)oxan-2-yl)oxy))oxan-2-yl 2,2,2-trifluoroacetate (I) in presence of silver carbonate to form an intermediate, and hydrolyzing the intermediate.    USE - Preparation of rebaudioside M (claimed).    ADVANTAGE - The method is environmentally-friendly, and enables efficient, economical and simple preparation of rebaudioside M with high yield and high quality.    DETAILED DESCRIPTION - Preparation of rebaudioside M involves performing substitution reaction of rebaudioside C and (2R,3R,4S,5S,6R)-5-(acetyloxy)-6-((acetyloxy)methyl)-3,4-bis((((2S,3R,4S,5R,6R)-3,4,5-tris(acetyloxy)-6-((acetyloxy)methyl)oxan-2-yl)oxy))oxan-2-yl 2,2,2-trifluoroacetate of formula (I) in presence of silver carbonate to form an intermediate, and hydrolyzing the intermediate.
NOVELTY - Reducing phosphorus activity in compost, involves (a) obtaining plant waste, performing pyrolytic carbonization of waste anaerobically at 400 degrees C for 4 hours to obtain carbon source as biomass and crushing biomass into powder, (b) mixing organic waste e.g. crop straw, and municipal waste or manure in a ratio of 3.3-5:1 and regulating carbon and nitrogen content in a ratio of 20-30:1, and making the mixture into a pile, and (c) adding crushed mixture obtained in step (a) into the pile and mixing mixture, composting mixture aerobically and crushing composted product.    USE - The method is useful for reducing phosphorus activity in compost (claimed).    ADVANTAGE - The method reduces pollution caused by above-mentioned waste, specifically water pollution and suppresses phosphorus loss.    DETAILED DESCRIPTION - Method for reducing phosphorus activity in compost, involves (a) obtaining plant waste, performing pyrolytic carbonization of waste anaerobically at 400 degrees C for 4 hours to obtain carbon source as biomass and crushing biomass into powder with particle size of 50 mesh, (b) mixing organic waste e.g. crop straw, and municipal waste or manure in a ratio of 3.3-5:1 and regulating carbon and nitrogen content in a ratio of 20-30:1, where the mixture has moisture content of 65-70%, and making the mixture into a pile, and (c) adding crushed mixture obtained in step (a) into the pile and mixing mixture, composting mixture aerobically under ventilation condition for 45 days and crushing composted product.
NOVELTY - An oxygen-increasing device for sludge aerobic compost fermentation comprises a distributing pipeline (1), the gas distribution pipeline is mounted with a multiaeration pipe (2), where the aeration pipe of the top close is set with a multi-hole upper side in the periphery side wall (3).    USE - As oxygen-increasing device for sludge aerobic compost fermentation (claimed).    ADVANTAGE - The device is simple and practical, and the use of special structure, solves the sludge aerobic uneven, easy to plug the difficult problem of maintaining the maximum extent possible to ensure aerobic sludge aeration process, making the sludge aerobic reaction fully, and because adequate oxygen also makes the sludge treatment process to eliminate odor.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of the oxygen-increasing device for sludge aerobic compost fermentation.    Distributing pipeline (1)    Multiaeration pipe (2)    Periphery side wall (3)
NOVELTY - Nutritional fertilizer comprises (in wt.%): sweet potato vine powder (4-6), pine tree leaves powder (2-4), radix achyranthis bidentatae powder (2-4), chicken manure powder (9-11), milk cow dung powder (6-8), pigeon dung powder (4-6), rapeseed straw powder (7-9), cotton seed hull powder (6-8), sorghum straw powder (7-9), rapeseed cake (6-8), peanut cake powder (2-6), corn leaves powder (11-13), plant ash powder (1-3), chip (2-4), pumpkin stem leaves powder (8-12), pine needle powder (4-6), dry tea powder (0.2-0.4), neem leaf powder (0.2-0.4), garlic powder (0.1-0.3) and ginger powder (0.1-0.3).    USE - Nutritional fertilizer used for growing ornamental sunflower (claimed) and preventing Fusarium wilt, root rot, nematodes infection and tumor in ornamental sunflower.    ADVANTAGE - The nutritional fertilizer is eco-friendly, and has sterilizing effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutritional fertilizer, which involves:    (A) mixing and crushing raw materials;    (B) fermenting mixture of raw material and effective microorganism for 36 hours at 55 degrees C; and    (C) molding fermented materials in presence of enzyme to obtain nutritional fertilizer.
NOVELTY - Organic fertilizer comprises 0.04-0.1 wt.% microbial composition, 0.04-0.1 wt.% molasses or brown sugar, 11-13 wt.% clean water and remainder duck manure.    USE - The organic fertilizer is useful for improving soil for agricultural and forestry application.    ADVANTAGE - The organic fertilizer is free from pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing microbial composition, molasses or brown sugar and clean water and uniformly sprinkling mixture on duck manure and stacking the mixture layer by layer and composting mixture, where the height of stack is 1.5 m, and turning stack for 2-3 times during composting process, where the stack is turned when it reaches 50 degrees C.
NOVELTY - Agent comprises 20-45 wt.% dry chicken manure, 3-5 wt.% calcium, 1-2 wt.% magnesium, 1-2 wt.% phosphorus, 20-45 wt.% organic matter, 5-15 wt.% ammonium phosphate, 3-10 wt.% protein, and 0.5-2 wt.% microbial composition, where the microbial composition includes 1.9-20 billion Bacillus subtilis per g, 3-4 million yeast per g, and 200-300 actinomycetes per g.    USE - The agent is useful for promoting growth of fish (claimed).    ADVANTAGE - The agent does not cause eutrophication.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the agent which involves mixing the above-mentioned raw materials except ammonium phosphate, stacking the mixture, fermenting the stacked mixture for 1-3 weeks, adding ammonium phosphate to the mixture, and allowing the mixture to stand for 1-3 hours.
NOVELTY - Producing a culture soil, comprises: mixing 35-45 wt.% of sawdust, 25-35 wt.% of leaves, 16-24 wt.% of food particles and 8-12 wt.% of quartz porphyry powder and molding the mixture to produce a leaf mold at room temperature; fermenting the mold for 1 month at 30-55 degrees C, and then spraying a culture fluid containing actinomycetes for 4-6 times a day for 1-20 days and for 1-3 times a day for 20-30 days to produce the culture soil; and packaging the culture soil in a container.    USE - The method is useful for producing a culture soil (claimed), which is useful improving the growth of plant. No biological data given.    ADVANTAGE - The method is capable of eco-friendly producing the culture soil with good moisturizing ability and permeability. The culture soil improves the plant yield.
NOVELTY - Producing ionized sericite powder comprises crushing sericite, applying an alternating current to the powder at a temperature of 400-1000 degrees C and a voltage of 10000-100000 V and then heating in a furnace for 4-8 hours.    USE - The method is useful for producing ionized sericite powder, which is useful in the cultivation of green vegetables (all claimed).    ADVANTAGE - The method is capable of producing the ionized sericite powder with high quality in an environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cultivating green vegetables comprising mixing the ionized sericite powder with water and then diluting, adding the diluted product to 4 kg/area soil, and making the soil to remain undisturbed for 7 days.
NOVELTY - Hydrolysis of lignocellulosic biomass involves: (a) pretreatment by an ionic liquid; and (b) treatment with acid reagents where the pretreatment step is a first step of dissolving the ionic liquid biomass, followed sequentially by precipitation with a polar solvent.    USE - The method is useful for hydrolysis of lignocellulosic biomass (claimed).    ADVANTAGE - The method for the hydrolysis of lignocellulosic biomass demonstrates that the speed of the hydrolysis increases by between 2 and 8 times depending on the temperature and the concentration of acid, as well as the type of acid used in the hydrolysis. It is rapid and efficient, and allows to easily prepare ionic liquid.
NOVELTY - Preparing a compost type nutritional supplement, comprises mixing 1000 pts. wt. starfish powder mixture and an apple extract such that the water content of the mixture is 60-80%, then adding 5-15 wt.% of glacial acetic acid and stirring at 40-60 degrees C for 12 hours to 3 days, adding 3-10 pts. wt. yeast culture fluid into the mixture, and then fermenting at 40-60 degrees C for 1-5 days such that the water content of fermentation product is of 30-40%.    USE - The method is useful for preparing a compost type nutritional supplement, which is useful for apple cultivation (claimed), promoting the growth of apple and preventing stress of the apple. No biological data given.    ADVANTAGE - The method is capable of economically preparing the compost type nutritional supplement in an eco-friendly manner. The nutritional supplement improves the quality of the apple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a compost type nutritional supplement.
NOVELTY - Manufacture of ceramic powder involves preparing a mixture by mixing manganese compound and copper compound with distilled water, preparing a sol by reacting the mixture with ethylene glycol and citric acid, forming a gel by heating the sol, heat-treating the formed gel, and again heat-treating the obtained gel.    USE - Manufacture of ceramic powder used for manufacturing metal separating plate protection film (claimed) for solid oxide fuel cell used as electrochemical energy converter.    ADVANTAGE - The method enables manufacture of nanoparticles capable of providing protection film with spinel structure having excellent interfacial resistance and electroconductivity. The solid oxide fuel cell consisting of the protection film has improved efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid oxide fuel cell metal separating plate protection film.
NOVELTY - Ginseng extract comprises more than 2.5 wt.% ginsenoside Rb2, more than 3 wt.% ginsenoside Rc, and more than 2 wt.% ginsenoside Rg1.    USE - The ginseng extract is useful in composition, preferably pharmaceutical composition, cosmetic composition, external preparation for skin or food composition for promoting hair sprouting and hair growth (all claimed). The external preparation for skin is in form including lotion, pack, cream and ointment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the ginseng extract, involves taking ginseng, adding solvent chosen from water, organic solvent and mixture of organic solvent or water, extracting, concentrating under reduced pressure, recovering solvent and obtaining product; and    (2) composition comprising the ginseng extract as an active ingredient.
NOVELTY - Preparing aqueous sugar solution from biomass containing fermentation-inhibitor, preferably coumaric acid involves using microbes that do not utilize glucose or xylose or with a crude enzyme product derived from the microbes, where the crude enzyme decomposes one or more types of compound chosen from coumaramide, ferulic acid, ferulic acid amide derivative, vanillin, vanillic acid, acetovanillon, furfural, and 3-(hydroxymethyl)furfural.    USE - The method is useful for preparing sugar solution, preferably saccharide solution (claimed) which is useful as fermentation feedstock for microorganisms, and as a raw material for various chemical products.    ADVANTAGE - The method prepares chemical substance which is highly stable, and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing a chemical substance which involves culturing the microbes in presence of a fermentation inhibitor, and converting the sugar solution into a chemical substance.
NOVELTY - Producing biomass comprises (a) culturing cells in heterotrophic or mixotrophic conditions in a continuous mode fermenter, and (b) continuously feeding and successively operating n-number of fermenters in semi-continuous mode by the cells produced in step (a), where n is greater than or equal to 2.    USE - The process is useful for producing biomass including an alcohol, an organic acid, a fatty acid, a polysaccharide, a terpene such as a botryococcene, a pigment such as a carotenoid, an amino acid, an enzyme, a vitamin, an antibiotic and/or pharmacologically active compound such as an exogenous or recombinant protein, preferably eicosapentaenoic acid, docosahexaenoic acid, arachidonic acid, fucoxanthin, canthaxanthin, astaxanthin, lutein or beta-carotene (all claimed), where the alcohol, organic acid, fatty acid, polysaccharide, terpene, pigment, amino acid, enzyme and vitamin are useful for food industries, the antibiotic and/or pharmacologically active compound is useful for pharmaceutical industries, and the pigments, organic compounds, polysaccharides and fatty acids are useful for cosmetic and petrochemical industries.    ADVANTAGE - The process is capable of producing the biomass with high yield in a cost effective manner.
NOVELTY - Sulphation of betulinic acid is carried out in 1,4-dioxane with a mixture of sulphamic acid and urea at 70-75 degrees C for 3.0-3.5 hours, and separation of the product is carried out by cooling the reaction mass, diluting with water, extracting with butyl or isoamyl alcohol, washing with water, treating the extract, concentrating the alcohol layer and separating the end product. Various versions of treating the alcohol extract are disclosed.    USE - Chemistry.    ADVANTAGE - Wider range of sulphating agents for sulphating betulinic acid, improved environmental friendliness of the method, wider range of sulphated betulinic acid derivatives.4 cl, 4 ex
NOVELTY - The fermenter (1) has vertically oriented charging opening (3) for filling and removing the biomass, in the closed state and liquid-tightly closing the closing device (5). A support device (6) is spaced behind the closing device in vertical state for underlying biomass. A percolate collection unit is arranged in the bottom of fermenter and in the plan view viewed from the support device.    USE - Fermenter for production of biogas from biomass such as corn in fresh form or silage.    ADVANTAGE - The clogging of covering grid of collecting channel with biomass is prevented, so that sufficient drainage to percolate into collecting channel is secured, while ensuring easy infiltration of percolate in the collector of the region immediately below the support apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an opened fermenter.    Fermenter (1)    Biogas removal opening (2)    Charging opening (3)    Closing device (5)    Support device (6)
NOVELTY - A buckwheat cultivating method involves selecting a field with fertile soil and weak alkaline content, sowing the seeds without any damage during last ten-day of april month after soaking the seeds in plant ash and liquor to obtain buckwheat rhizome. The field is weeded after the appearance of first secondary leaves and fertilized with human and animal excrement. The bees are placed in the field to obtain auxiliary pollination. The insecticides such as malathion, plant ash and water are sprayed into the field followed by setting gauze with the plant to collect fruit.    USE - Method for cultivating buckwheat.    ADVANTAGE - The method enables cultivating buckwheat with high survival rate, better quality and widely popularized.    DETAILED DESCRIPTION - A buckwheat cultivating method involves selecting a field with fertile soil and weak alkaline content, applying base fertilizer such as 120 kg/acre human excrement and 50kg/acre animal excrement into the field, sowing the seeds without any damage during last ten-day of april month after soaking the seeds in 6-8% plant ash and liquor for 30-35 minutes to obtain buckwheat rhizome. The field is weeded for 2-3 times after the appearance of first secondary leaves and fertilized with 25 kg/acre human excrement and 100 kg/acre animal excrement. The bees are placed in the field to obtain auxiliary pollination for 5-6 days. The insecticides such as 50% malathion, plant ash and water to ratio of 1: 4:1-2 are sprayed into the field for 2-3 times, followed by setting gauze with the plant to collect fruit.
NOVELTY - A Serratia HA1 strain deposited under CGMCC No: 7340, is new.    USE - The strain is useful in preparation of crude toxin for preventing weeds including Digitaria, Amaranthus retroflexus, barnyardgrass, green foxtail, Chloris virgata and other weeds (all claimed).    ADVANTAGE - The strain produces toxin which is safe as it is harmless, and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing crude toxin which involves (a) taking 5 g yeast extract, 10 g peptone, 10 g sodium chloride, and 1000 ml distilled water, and adjusting pH value of the medium to 7-7.5, taking 100 ml medium in a 250 ml flask, sterilizing the medium at 121 degrees C for 20 minutes in an autoclave, cooling the sterilized medium in a clean desk, streaking the Serratia HA1 strain under aseptic conditions on a plate at 80 degrees C, inoculating the strain for 36 hours in lysogeny broth, and culturing by shaking at a speed of 150 rotations per minute (rpm) at 37 degrees C for 24 hours to obtain seed liquid, (b) fermenting taking 5 g yeast extract, 10 g peptone, 10 g sodium chloride, and 1000 ml distilled water, sterilizing the medium at 120 degrees C for 30 minutes, cooling the fermented medium to 30 degrees C, inoculating 3% seed liquid, culturing the mixture at a temperature of 35 degrees C, and fermenting the culture for 96 hours to obtain fermented liquid, and (c) adding equal volume of ethyl acetate solution to the fermented liquid, extracting the liquid 3 times (each time for 24 hours), separating ethyl acetate phase by liquid separation, and evaporating the mixture to dryness to obtain brown crystalline paste.
NOVELTY - A petroleum hydrocarbon degradation carrier material preparing method involves cutting corn cob into pieces, rinsing with water, immersing in hydrochloric acid, taking out, rinsing with sterile water until neutral, drying, crushing, and sieving using 20 meshes sieve to obtain corn cob powder. Soybean straw is cut into pieces, rinsed with water, immersed in hydrochloric acid, removed out, rinsed with sterile water until neutral, dried, crushed through 20 meshes sieve to obtain soybean straw powder followed by mixing corn cob powder and soybean straw powder to obtain the finished product.    USE - Method for preparing petroleum hydrocarbon degradation carrier material for promoting contaminated soil remediation (claimed).    ADVANTAGE - The method enables preparing carrier material with increased efficiency.    DETAILED DESCRIPTION - A petroleum hydrocarbon degradation carrier material preparing method involves cutting corn cob into pieces, rinsing with water, immersing in aqueous solution of 10-12% hydrochloric acid for 12-16 hours, taking out, rinsing with sterile water until neutral, drying, crushing, and sieving using 20 meshes sieve to obtain corn cob powder. Soybean straw is taken and cut into pieces, rinsed with water, immersed in aqueous solution of 10-12% hydrochloric acid for 12-16 hours, removed out, rinsed with sterile water until neutral, dried, crushed through 20 meshes sieve to obtain soybean straw powder, followed by mixing corn cob powder and soybean straw powder at a mass ratio of 2:1 to obtain the finished product.
NOVELTY - The method involves establishing (S1) VBA data processing module. The VBA data processing module is invoked (S2) into a fuel cell test original data. The formatted VBA data processing module is invoked (S3) for importing data. The formatted VBA data processing module is invoked (S4) to draw an image. The formatted VBA data processing module is provided for rendering (S5) the images.    USE - Method for processing sub-area fuel cell based experiment data of fuel cell vehicle (FCV).    ADVANTAGE - The sub-area fuel cell based experiment data is rapidly and automatically processed. The data processing efficiency is increased. The error of user's operation is reduced, so that user data processing time and effort are saved. The Excel application is sued in the scientific research work, operation is simple and the convenient use is achieved. The data or images are rapidly and automatically formatted.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for processing sub-area fuel cell based experiment data.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the method for processing sub-area fuel cell based experiment data. (Drawing includes non-English language text)    Step for establishing VBA data processing module (S1)    Step for invoking VBA data processing module into a fuel cell test original data (S2)    Step for invoking formatted VBA data processing module for importing data (S3)    Step for invoking formatted VBA data processing module to draw an image (S4)    Step for rendering the images by formatted VBA data processing module (S5)
NOVELTY - Matrix comprises 20 pts. wt. normal farmland soil, 1 pt. wt. organic fertilizer, and 0.5 pt. wt. traditional Chinese medicinal composition. The organic fertilizer is a fermentation product of mixture comprising 20 wt.% crop straw powder, 70 wt.% animal excrement, and 10 wt.% bottom sludge. The traditional Chinese medicinal composition comprises 2 parts Asarum, 3 parts fortune Eupatorium herb, 3 parts Cassia nomame, 4 parts pyrethrum, 2 parts pepper, and 5 parts sawdust.    USE - The matrix is useful for planting radish and providing insecticidal effect for underground radish (claimed), and as insect repellent.    ADVANTAGE - The matrix is highly nutritious, improves yield and quality of radish, and avoids forked growth of radish.
NOVELTY - Microbial fertilizer comprises 55-65 wt.% weathered coal, 25-35 wt.% organic-humic acid, and 3-5 wt.% Trichoderma.    USE - The microbial fertilizer is useful for soil restoration (claimed) and controlling soil-borne diseases.    ADVANTAGE - The fertilizer reduces pesticide residues and soil salinization, adsorbs heavy metals e.g. calcium, copper and zinc, and improves soil fertility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the microbial fertilizer, which involves (a) crushing the weathered coal, and sieving obtained weathered coal powder using sieve having 40-60 mesh size to obtain fine powder, (b) uniformly mixing powder obtained in step (a) with the organic-humic acid and Trichoderma microbial inoculum, uniformly stirring obtained mixture using a stirrer at 80 revolutions/minute (rpm) in clockwise direction, and maintaining temperature of the mixture at 10-40 degrees C during stirring and mixing process, (c) adding mixture obtained in step (b) to dryer, drying the mixture at 50 degrees C for 30 minutes, and controlling moisture content of the mixture at 25%, where the mixture contains 0.5 million Trichoderma/g, and (d) placing dried product in a place without illumination, in absence of pressure and with moderate humidity, naturally fermenting the product at room temperature, and maintaining moisture content of the product at 20-25%.
NOVELTY - In this utility new type refers to a kind of one animal corpse biochemical treatment equipment, it is of biodegradable pour (1), hoisting machine (2), a heating device (3), a waste slag car (4), a condenser (5), supply oxygen humidifying device (6), a water filtering device (7), air filtering device (8), an exhaust port (9), water discharge device (10), the irrigation cover (11) composed of, wherein biodegradable pour (1) and hoisting machine (2), the irrigation cover (11) connect the upper end provided with supply oxygen humidifying device (6), a condenser (5), a biodegradable pour (1) provided with heating device (3), a condenser (5) and water filter (7), air filtering device (8) is connected, the air filtering device (8) is provided with an exhaust port (9), lower end set with water discharge device (11), biodegradable pour (1) has nine dead number, number six wall, irrigation cover (11) and hoisting machine (2) using interlocking and provided with limiting device. This new utility model comprises ring-friendly, no harmful gas, no smell, or the water after degradation can directly use recycling or directly discharge, can do fertilizer or common garbage treatment, sterilization completely, process is simple, can fit for large, middle, small animal cultivation site, slaughterhouse, food, equal related enterprise.
NOVELTY - This utility new type provide a one waste water microorganism culture device, by reactor, a top cover, a steel rod, the upper and lower water outlet, aeration pipe, pipeline, an aeration head, the pneuma hole, a temperature adjusting device, the reactor is a cylindrical steel rod, a top cover bottom are set with hanging filler with a number, a top cover is provided with a number of air hole, and set with water outlet on the reactor side, an aeration pipe 6. the reactor bottom aeration pipe through a pipeline switch to an external aerating pump. The utility model is new type device used for culture of culture and biochemical pool of pilot microorganism microorganism. This utility new type device a the laboratory and domestication of the microorganism cultivation rear reactor and then adding to the biochemical pool, strain capacity enhance survival, especially aiming at high salt waste water. This utility new type device design is reasonable, operation is simple, the practicability is strong.
NOVELTY - This utility new type claims a biomass fermentation using one of reaction device, comprising an outer tank body, a retainer and a inner tank body, the outer wall of said outer tank body ring set with several through a water pipe, a water pipe by one side outside the tank body and the inner tank body, a frame set with a fixed water pipe with a through hole, a water pipe by a one side at outside of outer tank body is coated with solar energy heat absorbing plate, said outer tank body close to the top position set with a water inlet pipe of one ring, a water inlet tube and the water tube between a first, with a first upper water pipe set with a first electromagnetic valve, said outer tank body close to the bottom position is set with a drain pipe, a drain pipe is connected with a water pipe and connecting with the second, a second upper water pipe set with a second electromagnetic valve, the device can be used for solar energy water heating process, increase the fermentation temperature of microorganism so that the microorganism fermentation to most fast of speed in a low temperature, increasing speed of garbage treatment.
NOVELTY - Extraction of capsaicin cyclodextrin comprises adding chili powder or chili essential oil in container, adding material liquid at ratio of 1:10-30 of 8-36 mg/mL beta -cyclodextrin or modified beta -cyclodextrin aqueous solution, at 25-70 degrees C, under 40 kHz, 400 W ultrasonic low effect and extracting for 5-30 minutes, filtering or standing, layering, filtering upper layer or repeating extraction, filtering or standing, layering, mixing capsaicin extract liquid, decompressing, and drying.    USE - Method of extraction of capsaicin cyclodextrin (claimed).    ADVANTAGE - The method has short time consumption, and is convenient to operate, mild condition, simple, green and pollution-free.
NOVELTY - Synthesis of 2-ethoxyethyl acrylate comprises adding ethyl acrylate, magnesium-aluminum solid catalyst and polymerization inhibitor compound into the reaction vessel, stirring, sealing, replacing inner kettle air with nitrogen, heating, introducing ethylene oxide, controlling temperature within the reactor until constant, packing, cooling and discharging.    USE - Method for synthesizing 2-ethoxyethyl acrylate (claimed).    ADVANTAGE - The method is simple, energy-saving and environment-friendly.
NOVELTY - The apparatus has a column including a gas dispersion part of the lower layer. An upper layer space is filled with earth and a sand part. The outside air of the center is filled with the sludge solidified soil or the general cover of a sterilized landfill molding layer. A greenhouse gas supply unit is connected to a gas dispersion part and serves to provide with the greenhouse gas. An external air supply part is connected to the upper layer space of the column and serves to supply the outside air. Methane, nitrogen and carbon dioxide are mixed at a ratio of 55 is to 45.    USE - Apparatus for decreasing greenhouse gases emitted from landfill using microorganisms.    ADVANTAGE - The greenhouse gas supply unit is connected to a gas dispersion part and serves to provide with the greenhouse gas, thus reduces cost, ensures carbon dioxide reduction and increases reduction efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for method for decreasing greenhouse gases emitted from landfill using microorganisms.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation of quantitative analysis of carbonate water.
NOVELTY - Apparatus (100) comprises a fermentation chamber (110) for loading waste, a mixer conveying unit (120) installed on top of the fermentation chamber to move back and forth, and a conveyor mixer fixed to an mixer conveying unit and for stirring the waste loaded in the fermentation chamber via a supporting frame. The conveyor mixer comprises a roller-type rotator fixed to the supporting frame, and first and second conveyor mixers (185, 186) installed on both sides of the roller-type rotator to rotate at predetermined angle.    USE - The apparatus is useful for fertilizing organic waste (claimed).    ADVANTAGE - The apparatus improves stirring efficiency of waste in the fermentation chamber, improves driving efficiency of device by selectively driving the conveyor mixer, and improves fermentation efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the apparatus for fertilizing organic waste installed with horizontally stretched conveyor stirrer in inclined state.    Apparatus (100)    Fermentation chamber (110)    Mixer conveying unit (120)    First conveyor mixer (185)    Second conveyor mixer (186)
NOVELTY - Garbage processing involves depositing garbage in cement walls. The deposited garbage is composted for six months under aerobic conditions.    USE - Method for processing garbage used for recycling floor material, particularly organic fertilizers, glass, batteries and scrap metal (all claimed).    ADVANTAGE - The method is simple and eco-friendly, and enables to recycle the product, which is used as fertilizer.
NOVELTY - Preparing sodium cefazedone anti-infection drug involves keeping cefazedone and sodium acetate in the anhydrous methanol and then dissolving the obtained material completely to obtain a salt at 10-30 degrees C. The obtained material is decolorized by adding the active carbon into the reaction liquid. The obtained material is stirred for decolorization and then the decolorized material filtered to remove activated carbon, at 10-30 degrees C. The obtained filter liquid is further filtered at filtering speed of 20 liter per hour and then adding dropwise ethanol to the filtered material for 0.5-1 hours.    USE - Method for preparing sodium cefazedone anti-infection drug (claimed).    ADVANTAGE - The method enables to prepare anti-infection drug in cost-effective, eco-friendly and simple manner, and with low impurity content and high product yield.    DETAILED DESCRIPTION - Preparing sodium cefazedone anti-infection drug involves keeping cefazedone and sodium acetate in the anhydrous methanol and then dissolving the obtained material completely to obtain a salt at 10-30 degrees C. The obtained material is decolorized by adding the active carbon into the reaction liquid. The obtained material is stirred for decolorization and then the decolorized material filtered to remove activated carbon, at 10-30 degrees C. The obtained filter liquid is further filtered at filtering speed of 20 liter per hour and then adding dropwise ethanol to the filtered material for 0.5-1 hours. The obtained material is added with a certain amount of acetone and then the obtained material is cooled to reduce the temperature to 5-15 degree Celsius per hour to 5 degree Celsius per hour. The cooled material is stirred at a speed of 80-120 revolutions per minute and then the stirred material is to crystallized for 1-3 hours. The crystallized material is dried and filtered and then the filtered material is washed and dried to obtain the desired product.
NOVELTY - Planted crop organic fertilizer prepared by (a) uniformly collecting waste edible mushroom, crushing, and (b) crushing in a fertilizer machine, air-drying or drying, where waste edible mushroom stem is taken as the main raw material of the organic fertilizer, is claimed.    USE - Used as planted crop organic fertilizer.    ADVANTAGE - The fertilizer: comprises easily available raw materials; is rich in nutrition; has long lasting fertilizer effect; can be completely absorbed by plants; and improves soil fertilization effect; and is produced with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer using waste edible fungus, comprising stirring 500 kg edible mushroom dry waste, 50 kg finely ground soil, 20 kg fertilizer and 16 kg aqueous ammonia, and fermenting for ten days.
NOVELTY - Fertilizer comprises nitrogen, phosphorus and potassium compound, loess, magnet ore powder, lees, rice straw pole, bamboo charcoal powder, wheat straw, citric acid, calcium superphosphate, potassium sulfate, naphthalene, polyethylene glycol, ammonium polyacrylate, boric acid, peanut leaves, Ginkgo, peony root, Alternanthera philoxeroides and effective microorganism.    USE - The fertilizer is useful for persimmon tree (claimed).    ADVANTAGE - The fertilizer can be simply and economically prepared with slow-release effect and fewer side effect, and increases yield and quality of the persimmon tree.    DETAILED DESCRIPTION - Fertilizer comprises 40-50 pts. wt. nitrogen, phosphorus and potassium compound, 23-25 pts. wt. loess, 20-25 pts. wt. magnet ore powder, 13-15 pts. wt. lees, 12-15 pts. wt. rice straw pole, 8-9 pts. wt. bamboo charcoal powder, 12-15 pts. wt. wheat straw, 2-4 pts. wt. citric acid, 2-3 pts. wt. calcium superphosphate, 1-2 pts. wt. potassium sulfate, 0.6-0.8 pts. wt. naphthalene, 0.5-0.7 pts. wt. polyethylene glycol, 0.1-0.3 pts. wt. ammonium polyacrylate, 0.8-1.2 pts. wt. boric acid, 7-9 pts. wt. peanut leaves, 3-5 pts. wt. Ginkgo, 2-4 pts. wt. peony root, 5-7 pts. wt. Alternanthera philoxeroides and 1-3 pts. wt. effective microorganism. An INDEPENDENT CLAIM is included for preparing fertilizer comprising drying wheat straw, cutting the dried wheat straw into small pieces, mixing wheat straw and potassium sulfate in a mass ratio of 1:3-4, and finally adding 10-15 wt.% of methyl methacrylate, stirring and heating the mixture at 60-70 degrees C for 30-40 minutes, weighing peanut leaves, peony root, and Alternanthera philoxeroides, crushing the weighed material, then adding effective microorganism and stacking to ferment at 35-40 degrees C for 8-10 days and each time for 2-3 days, weighing remaining raw materials and then mixing and fermenting.
NOVELTY - Extracting mogroside V from mangosteen involves (a) taking fresh mangosteen, washing fruit, and crushing washed fruit, (b) placing the crushed mangosteen in a high pressure tank, and adding purified water to tank to obtain pasty slurry, (c) carrying out carbon dioxide supercritical fluid extraction of slurry by adding ethanol to slurry, and (d) collecting extract, centrifuging extract, subjecting supernatant through HP-20SS resin column chromatography, eluting using ethanol solution, concentrating the extract, and spray drying concentrated extract.    USE - The method is useful for extracting mogroside V from mangosteen (claimed).    ADVANTAGE - The method is simple, cost-effective, and suitable for large-scale production of mogroside V. Environment-friendly.    DETAILED DESCRIPTION - Extracting mogroside V from mangosteen involves (a) taking fresh mangosteen, washing the fruit, and crushing the washed fruit, (b) placing the crushed mangosteen in a high pressure tank, adding equal amount of purified water to the tank, applying pressure of 4 kgf/cm2 for 10-15min, and restoring the tank back to its normal pressure to obtain pasty slurry, (c) carrying out carbon dioxide supercritical fluid extraction of the slurry by adding 50 Vol.% ethanol as entrainer to the slurry at a volume ratio of 1:4, or 1:2, where the extraction is done at a temperature of 50-60 degrees C, and pressure of 15-20 MPa for 15-20 hours, and (d) collecting the extract obtained after extraction, centrifuging the extract, subjecting the supernatant through HP-20SS resin column chromatography, eluting using 50-60% ethanol solution, concentrating the extract, and spray drying the concentrated extract.
NOVELTY - A system is formed by combining mash tower (GG) which distills fermented liquor (DD) produced in fermenter and hydrated ethanol vapor from tower top, modifier (JJ) which produces reformed gas, and solid oxide fuel cell (MM) operated using reformed gas as fuel. Portion of anode waste gas is refluxed to water-containing ethanol vapor line (6) leading from mash column to reformer at reflux ratio of 1-2. Using the reflux, the ethanol concentration of the water-containing ethanol vapor is adjusted to 25-35 wt.% by the moisture contained in anode waste gas of solid oxide fuel cell.    USE - Energy-saving method in combined system of bioethanol manufacturing apparatus and solid oxide fuel cell (claimed).    ADVANTAGE - The method effectively improves the power generation efficiency of solid oxide fuel cell, and reduces energy required for distilling fermented liquid.    DETAILED DESCRIPTION - A system is formed by combining mash tower which distills fermented liquor produced in fermenter of bioethanol manufacturing apparatus and hydrated ethanol vapor from tower top, modifier which produces reformed gas from hydrated ethanol vapor, and solid oxide fuel cell operated using reformed gas as fuel. Portion of anode waste gas is refluxed to water-containing ethanol vapor line leading from mash column to reformer at reflux ratio (reflux gas flow volume/(anode waste gas flow volume-reflux gas flow volume)) of 1-2. Using the reflux, the ethanol concentration of the water-containing ethanol vapor is adjusted to 25-35 wt.% by the moisture contained in the anode waste gas of the solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the energy-saving method in combination system of bioethanol manufacturing apparatus and solid oxide fuel cell. (Drawing includes non-English language text)    Water-containing ethanol vapor line (6)    Fermented liquor (DD)    Mash tower (GG)    Modifier (JJ)    Solid oxide fuel cell (MM)
NOVELTY - The light lanthanum phosphate catalyst (I), is new.    USE - Light lanthanum phosphate catalyst used in photocatalytic reduction of carbon dioxide and water system for methane and hydrogen (claimed).    ADVANTAGE - The light lanthanum phosphate catalyst cab be prepared in a simple and cost-effective manner without using expensive complex under moderate synthesis condition on large scale.    DETAILED DESCRIPTION - The light lanthanum phosphate catalyst has general formula LaPO4 (I), is new. An INDEPENDENT CLAIM is included for a method for preparing light lanthanum phosphate catalyst, which involves performing hydrothermal synthesis.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic x-ray diffraction pattern of the light lanthanum phosphate catalyst. (Drawing includes non-English language text).
NOVELTY - Preparing fertilizer involves fermenting molasses with Bacillus coagulans and alcohol waste, where pH and metal ion concentration of fermented product is measured. The metal complexing agent and sugar molasses alcohol are mixed with fermented product at 90-100 degrees C for 30-360 minutes. The pH regulator is added to mixture for maintaining pH to 7-8. The fermented product is kept in anaerobic condition for 12-48 hour. Organic and inorganic fertilizer are mixed with fermented product for 12-36 hour to obtain mixture that is granulated and mixed with biological flora to obtain product.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method enable to prepare fertilizer that ensures odor free high quality product in cost-effective manner.
NOVELTY - Preparing fertilizer involves mixing biogas residue, slag, phosphoric acid hydrogen, corn cob, oyster powder, urea, seaweed meal, naphthalene, potassium humate, potassium sulfate, wetting agent and water to obtain mixture. The mixture is crushed to obtain powder that is heated for 4 hours. The heated powder is fermented for 15-18 days. The fermented product is granulated to obtain fertilizer.    USE - Method for preparing fertilizer used for promoting root (claimed).    ADVANTAGE - The method enables to prepare fertilizer that is suitable for seedling.
NOVELTY - Selenium-enriched organic fertilizer comprises (in pts.wt.): dairy manure and pig manure mixture (400-500), spinach and spinach leaves in mass ratio of 2:3 (30-50), wooden meal mixed floating aquatic plants dry powder (80-120), fermented sawdust (50-80), clay powder with medical stone in mass ratio of 10:1 (40-60), golden cypress powder (10-30), dairy manure and pig manure in mass ratio of 2:5 (80-120).    USE - Selenium-enriched organic fertilizer used for selenium-poor land.    ADVANTAGE - The selenium-enriched organic fertilizer increases selenium content in poor land by 18-20% and crop absorption rate.
NOVELTY - Preparing organic fertilizer involves mixing sawdust, Lophatherum gracile, bean straw, dairy manure, pig manure, spinach, floating aquatic plant dry powder, wood, clay, medical stone powder, Phellodendron powder, henon leaves and water. The obtained mixture is fermented for 25-30 days. The fermented product is sealed for 10-12 days. Selenium, selenium additive and sodium selenite are added to fermented product to obtain another mixture that is dried for 3 days. The dried product is extruded and granulated to obtain organic fertilizer.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer that ensures high selenium content and increased crop absorption rate.
NOVELTY - Preparing herbaceous energy plant silage comprises (a) cutting herbaceous energy plants, crushing and mixing with microalgae mixed to obtain a mixture, where the microalgae accounts for 2-6 wt.% of herbaceous energy plants; (b) placing the mixture obtained in a sealed silage for 15 days at room temperature.    USE - The herbaceous energy plant silage is useful for producing biogas by anaerobic fermentation (claimed).    ADVANTAGE - The method increases the increase the silage raw material yield.
NOVELTY - This new type utility claims one fertilizer humic for a device, belonging to the garbage treatment device technology field. The device comprising a hemispherical tank body, a tank body set with inner humic in cavity, a tank body inclined arrangement with several vent pipe, lower end of the air pipe connecting the flow valve, the vent pipe of the upper end are a pneuma return tube, the return tube set with a stop valve, the humic in inner cavity of said upper air pipe set with several vent hole, the upper air return pipe set with one along the radius vertical extending of the tank body is set in tube, in the tube device end part of one connecting horizontal pipe, the horizontal pipe passes through the tank body, inner the humus by a cavity in the upper pipe is also set with several vent hole, between all the vent pipe and is set in pipe of angle are equal. This utility new type can be valid control ventilation quantity, corresponding to compost material uniform cloth air, accelerates the humic in progress of compost can be widely applied in garbage treatment.
NOVELTY - This new type utility claims one a compost fermenting device, belonging to the garbage treatment device technology field. The device comprising a vertical set of fermentation tank, fermentation tank comprising a coaxial set of inner tank body and outside the tank body, the tank body of inner cavity forming inside the fermentation chamber, the inner tank body and tank body outside a space forming gas buffer cavity, the inner tank body set with a plurality of connected gas buffer cavity and a vent hole of fermentation chamber, outside the tank body top part position set with a gas inlet, the tank body outside of the position set with drain wherein. This utility new type can be a fermentation tank inner different position uniform supply of needed to ensure any position of compost material can fully contact the air, satisfactory finishing ferment process, in a widely used in garbage treatment.
NOVELTY - This new type utility claims one a machinery stirring compost fermenting device, belonging to the garbage treatment device technology field. The fermentation device comprising a fermentation tank, the fermentation tank to rotate inner mounted with power device by driving a stir shaft, said inner set with temperature detecting a fermentation tank, a temperature detecting a connecting control unit, the bottom of the fermentation tank along the generatrix direction of the fermentation tank set with a multiple nozzle, each said nozzle of a spraying direction towards the stir shaft, said air nozzle are air storage tank through a pipeline, the storage tank connecting one air compressor, each said nozzle a in series one electric flow adjusting valve, a end of each a the electric flow rate regulating valve are connecting the control unit. This utility new type relative structure is simple, design is reasonable, compost in a fermentation process is not easy to leave dead angle, and a change of compost fermentation process according to a adjusting ventilation amount can be widely applied in garbage treatment.
NOVELTY - A tilmicosin microemulsion is prepared by mixing polyethylene glycol glyceride, OP-10 emulsifier and propylene glycol based on 7:4:9 mass ratio, placing in 37 degrees C water bath, stirring with magnetic stirrer at 100 revolutions/minute (rpm) to mix uniformly, adding tilmicosin powder into the mixture based on 1:5 mass ratio, and stirring with magnetic stirrer at 100 rpm under a water bath temperature of 37 degrees C to mix uniformly, dissolve completely and obtain tilmicosin microemulsion.    USE - Method for preparing tilmicosin microemulsion used as antibiotic in veterinary medicine for prevention and treatment of livestock diseases including cattle, sheep, pig and chicken diseases caused by germs and mycoplasma infection, such as pneumonia, mastitis, and chronic respiratory tract disease.    ADVANTAGE - The method is simple to operate, and can solve the problems associated with tilmicosin which has low solubility and bioavailability and which is easy to decompose when exposed to visible light. The obtained tilmicosin microemulsion has stable physical and chemical properties, small particle diameter, and centralized particle distribution. It has an average particle size of 5.59 nm as measured using laser particle size analyzer. It can be diluted with water without the occurrence of layering and emulsion breaking phenomenon. Further, it is environment-friendly, has low production cost, and can used conveniently with low treatment cost and high cure rate.
NOVELTY - Preparation of Euphorbia ebracteolata lactone A comprises grinding Euphorbia ebracteolata, ultrasonic extracting with ethanol, concentrating extract and drying; extracting extract with ethyl acetate, filtering, vacuum-concentrating filtrate to get concentrate; mixing concentrate with polyamide resin, volatilizing solvent, passing in polyamide resin column with dichloromethane-methanol, tracking monitoring with thin layer chromatography, collecting eluent; and concentrating eluate, performing high-speed countercurrent chromatography separation-purification and freeze-drying.    USE - Method for preparing Euphorbia ebracteolata lactone A used in preparing oral formulation for enhancing intestinal absorption of medium chain fatty acid salt, chenodeoxycholic acid and chitosan (all claimed).    ADVANTAGE - The method is simple, ensures high yield, small pollution and high purity. The lactone A has good antitumor effect and high degree of biological utilization.
NOVELTY - Synthesis and separation of phytosterol esters comprises mixing phytosterols, fatty acid and catalyst, performing esterification reaction to get crude product; and filtering crude product, mixing with crystallization solvent at mol ratio of 1-1:10, decoloring, and cooling to - 18-10 degrees C for 18-30 hours. The crystallization solvent is acid methyl ester, ethyl acetate or octanoic acid triglyceride. The catalyst contains copper nitrate as active component and nanohydroxyapatite as carrier.    USE - Method for synthesizing and separating phytosterol esters (claimed).    ADVANTAGE - The safe and simple method does not use organic solvent, and ensures environmental protection.
NOVELTY - Deodorizing system comprises regulating pool (1), former stage fermentation pool (2), microorganism culture device (3), microorganism (4), nutrition liquid tank (5), latter level fermenting pool (6), sedimentation pool (7), fermentation liquid storage tank (8), fermentation liquid spray deodorizing device (9), stirrer (10), charging device (11), mineral filler (12), microorganism reflux pipe (13) and fermentation liquid conveying pipe (14) for regulating pool.    USE - Deodorizing system used for processing municipal garbage (claimed).    ADVANTAGE - deodorizing system ensures processing of municipal garbage in cost-effective manner by requiring reduced energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of deodorizing system.    Regulating pool (1)    Former stage fermentation pool (2)    Microorganism culture device (3)    Microorganism (4)    Nutrition liquid tank (5)    Latter level fermenting pool (6)    Sedimentation pool (7)    Fermentation liquid storage tank (8)    Fermentation liquid spray deodorizing device (9)    Stirrer (10)    Charging device (11)    Mineral filler (12)    Microorganism reflux pipe (13)    Fermentation liquid conveying pipe (14)
NOVELTY - Turning device comprises turner roller (14) for driving turner wheel that rotates wheel drive equipment. The turners roller includes a rotating shaft (11) and turners rib frame (12), where rotary shaft and roller driving device are connected with connecting plate (13). Turners rib rack secured to rotary shaft. Turners device has a free end that is provided with turners teeth.    USE - Turning device used for fermenting biological fungus into humus (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of turning device.    Rotating shaft (11)    Turners rib frame (12)    Connecting plate (13)    Turner roller (14)
NOVELTY - Veterinary drug comprises motherwort, dandelion, Angelica, Epimedium, fried folium artemisiae argyi, fried large-headed Atractylodes rhizome, radix codonopsitis, Astragalus, hawthorn, seed of Chinese dodder, dyer's woad leaves, Ophiopogon root, immature bitter orange, peach kernel, Magnolia officinalis, safflower, honeysuckle, and radix glycyrrhizae.    USE - The veterinary drug is useful for treating postpartum endometritis in cows (claimed).    ADVANTAGE - The veterinary drug is prepared simply and rapidly and suitable to treat cows in large-scale, does not cause side effect, does not leave any medicinal residue, and has excellent oral absorbability.    DETAILED DESCRIPTION - Veterinary drug comprises 15-25 pts. wt. motherwort, 10-20 pts. wt. dandelion, 5-15 pts. wt. Angelica, 5-10 pts. wt. Epimedium, 5-9 pts. wt. fried folium artemisiae argyi, 5-7 pts. wt. fried large-headed Atractylodes rhizome, 4-8 pts. wt. radix codonopsitis, 4-8 pts. wt. Astragalus, 4-8 pts. wt. hawthorn, 4-7 pts. wt. seed of Chinese dodder, 3-8 pts. wt. dyer's woad leaves, 3-5 pts. wt. Ophiopogon root, 2-5 pts. wt. immature bitter orange, 2-4 pts. wt. peach kernel, 2-4 pts. wt. Magnolia officinalis, 2-3 pts. wt. safflower, 1-3 pts. wt. honeysuckle, and 1-2 pts. wt. radix glycyrrhizae. An INDEPENDENT CLAIM is included for method for preparing the above-mentioned drug, which involves (a) taking the motherwort, Epimedium, seed of Chinese dodder, Angelica, dandelion, safflower and peach kernel and crushing the mixture to mesh size of 80, (b) crushing the remaining traditional Chinese medicinal materials to mesh size of 80, (c) mixing the powders in step (b) for 15 minutes, and (d) blending the mixtures obtained in step (a) and step (c) for 20 minutes.
NOVELTY - Reducing dew point of maleic anhydride exhaust gas comprises mixing fresh air and n-butane, preheating the mixture and oxidizing, then cooling the oxidized product and entering into an absorption tower for separating maleic anhydride from maleic anhydride exhaust gas, entering the maleic anhydride exhaust gas into an exhaust gas separator divided into first part and second part of an air flow, then introducing the first part of the airflow into a combustion furnace and second part of the air flow into a washing tower.    USE - The method is useful for reducing dew point of maleic anhydride exhaust gas (claimed).    ADVANTAGE - The method is capable of reducing dew point of maleic anhydride exhaust gas with reduce product consumption and prevent corrosion to increase device efficiency.    DETAILED DESCRIPTION - Reducing dew point of maleic anhydride exhaust gas comprises mixing fresh air and n-butane, preheating the mixture and oxidizing, then cooling the oxidized product and introducing into an absorption tower for separating maleic anhydride from maleic anhydride exhaust gas, introducing maleic anhydride exhaust gas into an exhaust gas separator divided into first part and second part of an air flow, then introducing the first part of the airflow into a combustion furnace and second part of the air flow into a washing tower, washing the second part of the air flow with water and then with circulating air flow comprising gas mixture of fresh air and oxygen to form a oxygen enriched air mixture, feeding the oxygen enriched air mixture into n-butane and maintaining the consistency of oxygen content in the oxygen enriched air mixture.
NOVELTY - Producing biogas involves grinding food waste material, where ethanol and dry yeast powder is added to the crushed material. The obtained mixture is anaerobically fermented at 30 plus minus 1 degrees C in the presence of nitrogen gas for 12-72 hours to obtain desired product.    USE - Method for producing biogas by anaerobic fermentation (claimed).    ADVANTAGE - The method enables to produce biogas in a simple and economical manner.
NOVELTY - This new type utility claims a full automatic household garbage one organic fertilizer production line, comprising a fermentation system, pre-mixing system, a granule, sieving system, drying system, cooling system and system, wherein material feeding and pre-mixing system wherein a fermentation system of connected, wherein the discharge feed and wherein a granule of a pre-connected system, wherein the discharging material and sieving system wherein a granule of a connected, wherein a first material feeding system of screening and drying a wherein connected, wherein a second material feeding system of screening and wherein a pre-connected, wherein the discharge feed and wherein cooling system of a drying system connected, wherein the discharge feed and wherein system of a cooling system connected, the organic fertilizer granule a weighing and bagging. This utility new type of production efficiency high, without need to aritificial to carry, the cost is saved.
NOVELTY - This utility new type claims a sewage sludge one making a , vehicle comprising a vehicle body, a vehicle body set with a mix tank, a sludge pump and vacuum pump, the vacuum pump a pulse blowing device, wherein a pulse blowing device through a pipeline is further set with a rubbish in mix tank, tank wall of the mix tank, and fixing a rubbish in a sewage suction arm, the top part of the mix tank set with active carbon add material tank, a motor and a add material fermentation tank. Use mix the sludge collecting tank, match mix tank upper end of a add material fermentation tank and active carbon add material tank mix tank to add active carbon and stir in the fermentation of a, and stir, the sludge and active carbon and fermenting a mix uniform, then use pump to mix enough sludge of sludge through sludge nozzle can be directly green belt of a road, which avoids the frequently, a cause resource waste, at the same time supply sufficient nutrient a municipal garden.
NOVELTY - This utility new type relates to one with a gas ratio regulating function of hydrogen-oxygen mix gas happen device, this hydrogen-oxygen mix gas happen device comprising electrolytic groove main body, the electrolytic groove the inner set with one in supporting body, this upper part in mounted with air distributor, the air distributor upper surface is provided with multiple lower concentric ring groove, and the air distributor is further connected with one air pipeline, air pipeline downward passes through this in the bearing part and the bottom of the electrolytic groove main body, and set in the electrolytic groove main body external air of a connecting device. This utility new type air through a device, a separator of a plate inner electrolytic groove of the body a blowing bubble, it can accelerate a plate a produce of oxygen or hydrogen gas bubbles from a plate, a temperature further can relieve the electrolyte and electrode plate, at the same time the air oxygen in electrolytic and produce a gas mix, it can adjust a hydrogen-oxygen ratio in mix gas to increase content of oxygen so as to reduce the combustion produce a nitrogen oxide, and preventing a hydrogen electrode.
NOVELTY - Cultivating hemsley rockvine medicinal materials, comprises (a) washing the hemsley rockvine with water by a solar energy photovoltaic plate and then drying, (b) sewing dried hemsley rockvine to a special non-woven cloth having a height of 20-50 cm, and (c) mixing hemsley rockvine with 10-15 kg of special nutrition substrate and surface soil in a mass ratio of 1:10-40 in a culture medium, filling the hemsley rockvine by a cultivation bag and then sowing and seedling, and spraying a potash fertilizer on the hemsley rockvine materials for 2-5 times and then culturing for 3-5 years.    USE - The method is useful for cultivating hemsley rockvine medicinal materials (claimed).    ADVANTAGE - The method is capable of cultivating the hemsley rockvine medicinal materials with less energy consumption and improved yield in an eco-friendly manner.    DETAILED DESCRIPTION - Cultivating hemsley rockvine medicinal materials, comprises (a) washing the hemsley rockvine with water by a solar energy photovoltaic plate having an included angle of 15-75 degrees and height of 10-30 cm, where the plate is in a round, an ellipse, a square or a rectangular shape, (b) sewing dried hemsley rockvine to a special non-woven cloth having a height of 20-50 cm and rectangular shaped, where the non-woven cloth includes 20-90 mass% of polyester and 10-80 mass% of low melting point fiber, and (c) mixing hemsley rockvine with 10-15 kg of special nutrition substrate and surface soil in a mass ratio of 1:10-40 in a culture medium, where the nutrition substrate contains 40-70 pts. wt. fermented sheep manure, 18-30 pts. wt. fermented lees, 5-10 pts. wt. superphosphate, 5-10 pts. wt. potassium sulfate, 2-5 pts. wt. zeolite powder, and 2-5 pts. wt. limestone powder, filling the hemsley rockvine by a cultivation bag and then sowing and seedling, and spraying a potash fertilizer on the hemsley rockvine materials for 2-5 times in 7-10 days and then culturing for 3-5 years.
NOVELTY - Production of ammonia water includes collecting ammonia chloride wastewater in the ammonium chloride wastewater regulating tank, and microfiltering; carrying out microfiltration dialysis fluid high pressure reverse osmosis separation; allowing the high pressure reverse osmosis concentrate liquid to enter in bipolar film; and allowing the high pressure reverse osmosis dialysis liquid to penetrate a low pressure reverse osmosis separated liquid, and allowing the low pressure reverse osmosis concentrated liquid to enter into high pressure reverse osmosis in circulation treatment.    USE - Method for production of ammonia water (claimed).    ADVANTAGE - The method can achieve the wastewater zero discharge.    DETAILED DESCRIPTION - Production of ammonia water comprises:    (A) collecting ammonia chloride wastewater in the ammonium chloride wastewater regulating tank, microfiltering to obtain dialysis liquid and microfilter concentrate liquid, and returning the concentrate filtered liquid to adjust tank circulation treatment;    (B) carrying out microfiltration dialysis fluid high pressure reverse osmosis separation to obtain high pressure reverse permeable dialysis fluid and high pressure reverse osmosis concentrate;    (C) allowing the high pressure reverse osmosis concentrate liquid to enter in bipolar film; and    (D) allowing the high pressure reverse osmosis dialysis liquid to penetrate a low pressure reverse osmosis separated liquid to obtain low pressure reverse osmosis penetrating liquid and low pressure reverse osmosis concentrated liquid, and allowing the low pressure reverse osmosis concentrated liquid to enter into high pressure reverse osmosis in circulation treatment to produce low pressure reverse osmosis dialysis penetrated liquid.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic flow diagram of the method for production of ammonia water (Drawing includes non-English language text).
NOVELTY - The device has four input ports for introducing purge gas of propane (C3H8) in a sample port of gas. A zero demarcate gas port is matched with a span port. A valve island is provided with four electromagnetic valves. Zero demarcate gas is formed by 99.99% of high-pure nitrogen. Standard gas is formed by ethane, propane or carbon monoxide. The sample port is connected with a glass fiber filter and a stainless steel sintered filter. A generator main body is made of aluminum alloy material.    USE - Optical gas input device for a Raman spectrometer (claimed).    ADVANTAGE - The device is convenient to operate, and improves gas detection efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a Raman spectrometer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an optical gas input device.'(Drawing includes non-English language text)'
NOVELTY - Composition comprises (wt.%): water-soluble organic carbon (20-25), hydrolyzed animal protein (15-20), phosphorus (1-1.5), potassium (1-1.5), selenium (0.04-0.05), zinc (0.04-0.05), biogas slurry liquid (45-55) and fertile soil liquid extract (5-10).    USE - Composition used for providing selenium and zinc rich nutrients to plant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing composition, which involves:    (A) mixing water-soluble organic carbon, hydrolyzed animal protein, phosphorus, potassium, selenium, zinc, fertile soil liquid extract and biogas slurry liquid to obtain mixture;    (B) fermenting mixture at 35-45 degrees C for 10 days to obtain fermentation liquid; and    (C) filtering liquid to obtain the product.
NOVELTY - Producing alcohol from cellulose-containing biomass, by preprocessing cellulose-containing biomass, saccharifying preprocessed cellulose-containing biomass, eliminating saccharification residual solids, culturing alcohol fermentation microorganism with aqueous saccharide solution, eliminating alcohol fermentation microorganism from culture liquid, recovering alcohol by distillation of the alcohol fermentation liquid, filtering the distillation residue liquid through a reverse osmosis membrane and subjecting the retentate to wastewater treatment.    USE - The method is useful for producing alcohol from cellulose-containing biomass. The alcohol is methanol, ethanol, propanol, or butanol (all claimed).    DETAILED DESCRIPTION - Method for producing alcohol from cellulose-containing biomass, involves (a) preprocessing cellulose-containing biomass, (b) saccharifying the preprocessed cellulose-containing biomass using diastatic enzyme, (c) eliminating saccharification residual solids from the saccharified product, (d) culturing an alcohol fermentation microorganism with the aqueous saccharide solution obtained in step (d) as the starting material for fermentation, (e) eliminating the alcohol fermentation microorganism from the culture liquid containing the alcohol fermentation microorganism, (f) recovering alcohol by distillation of the alcohol fermentation liquid, (g) filtering the distillation residue liquid through a reverse osmosis membrane and (h) subjecting the retentate to wastewater treatment.
NOVELTY - Preparing bioethanol from lignocellulosic biomass, by minimizing impurity content of enzymatic saccharification raw material by extracting biomass using hot water, removing extractable substances, suppressing production of excessive degradation product of sugar, by pretreating the biomass, preparing fermentable sugar, without washing a pretreated solid obtained from subsequent solid-liquid separation, but by only concentrating a sugar solution obtained after enzymatic saccharification, and preparing bioethanol.    USE - The method is useful for preparing bioethanol from lignocellulosic biomass (claimed).    ADVANTAGE - The method enables cost-effective preparation of bioethanol with high yield.    DETAILED DESCRIPTION - Method for preparing bioethanol from lignocellulosic biomass, involves minimizing impurity content of an enzymatic saccharification raw material by extracting biomass using hot water, before pretreatment, removing extractable substances such as inorganic salts, suppressing, to the greatest extent, the production of an excessive degradation product of sugar, by pretreating the biomass, from which the hot water extractable substances have been removed, in a condition for maximizing xylan yield, preparing fermentable sugar, without washing a pretreated solid obtained from subsequent solid-liquid separation, but by only concentrating a sugar solution obtained after enzymatic saccharification, using a separation film and preparing bioethanol.
NOVELTY - A narcissus bulb stem ball storage method involves selecting plump bulb ball and stripping the outer piece of rotting bulbs and roots. A pharmaceutical agent solution is prepared. The plump bulb ball is soaked into the pharmaceutical agent solution in a basket. The entire bulb ball is immersed in the soaked solution. Mushroom type of waste and sewage sludge is mixed with the immersed bulb ball, water is added and stirred to obtain a paste material. The ball is placed under the sun and dried for 2-3 days. The dried bulb ball is placed in a warehouse and stored at room temperature.    USE - Method for storing narcissus bulb stem ball.    ADVANTAGE - The method enables storing narcissus bulb stem ball in an eco-friendly manner, avoiding the use of soil material to protect the ball resulting in huge loss caused by soil fertility decline, and avoiding a lot of insecticide spraying in the warehouse.    DETAILED DESCRIPTION - A narcissus bulb stem ball storage method involves selecting plump bulb ball and stripping the outer piece of rotting bulbs and roots. A pharmaceutical agent solution comprising 0.5-1.5% formalin solution, 0.05-0.15% triclosan, 0.1-0.3% thiophanate-methyl, 0.1-0.3% captan and remainder of water, is prepared, where the pharmaceutical agent solution temperature is 40-52 degrees C. The plump bulb ball is soaked into the pharmaceutical agent solution in a basket. The entire bulb ball is immersed in the soaked solution for 10-30 minutes. Mushroom type of waste and sewage sludge mass ratio of 1:2-4 is mixed with the immersed bulb ball, water is added and stirred to obtain a paste material. The ball is placed under the sun and dried for 2-3 days. The dried bulb ball is placed in a warehouse and stored at room temperature.
NOVELTY - Environmentally friendly water-based household insecticide aerosol comprises 0.3-0.61 wt.% complex plant source insecticide and pyrethroid insecticide preparation, 1-3 wt.% surfactant, 0.01-0.10 wt.% corrosion inhibitor, 0.1-22 wt.% osmotic agent, 6-16 wt.% solubilizer, complexing agent, wetting agent, defoaming (specific amount), purified water or deionized water excipient, and less than 0.026 wt.% essence. The aerosol further comprises dimethyl ether (DME) as propellant for filling.    USE - The insecticide aerosol or spray is useful for killing mosquitoes, flies, cockroaches, ants, termites, mites, ticks, bugs and fleas.    ADVANTAGE - The insecticide aerosol: can be stored for more than four years; is multifunctional (MIK) having repelling and long duration properties; and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the water-based household insecticide aerosol, comprising (i) taking the plant source pyrethroid insecticide and insecticide preparation, solubilizer and essence; (ii) adding water into the surfactant, corrosion inhibitor, osmotic agent, wetting agent and defoaming, and stirring to dissolve; and (iii) adding the components of the step (i) to the stirred mixture obtained in the step (ii), measuring the pH, then adding the complexing agent, uniformly stirring until a clear and transparent aqueous solution is obtained, allowing to stand, filtering, and then conveying into aerosol production line through a pipeline.
NOVELTY - Method for producing fiberboard, involves adding crop straw as main raw material into reaction vessel, mixing, adding hemicellulase and laccase, performing enzyme hydrolysis, maximizing the degree of hydrolysis, filtering hydrolyzed material using semipermeable membrane, remixing the enzyme treated crop straw fibers and enzymatic digestion solution, drying mixture, until the moisture content reaches 5-10%, adding rosin powder, mixing uniformly, molding mixture, and subjecting the molded material to vulcanizing machine to obtain waterproof fiberboard.    USE - The method is useful for producing fiberboard (claimed).    ADVANTAGE - The prepared fiberboard is simple, cost-effective, and environmentally-friendly and has excellent waterproof property.    DETAILED DESCRIPTION - Method for producing fiberboard, involves adding crop straw as main raw material into reaction vessel, mixing, adding hemicellulase and laccase, performing enzyme hydrolysis, applying pressure of 0.1-2 MPa, maximizing the degree of hydrolysis, filtering hydrolyzed material using semipermeable membrane, remixing the enzyme treated crop straw fibers and enzymatic digestion solution, drying mixture, until the moisture content reaches 5-10%, adding rosin powder, mixing uniformly, molding mixture, and subjecting the molded material to vulcanizing machine to obtain waterproof fiberboard.
NOVELTY - Antibacterial agent preparation involves mixing silver nitrate solution and copper nitrate solution in a molar ratio of 1:1-30:80. The obtained product is heated at a controlled temperature of 35-45 degrees C for 1 hour and then at 52-58 degrees C for half and hour with stirring condition to obtain composition. The obtained product is mixed with 0.5g of chitosan at 60-68 degrees C for 0.5 hour to obtain resultant product. The obtained product is cooled and filtered in a vacuum suction pump. The obtained filtered product is fried at 60 degrees C and then ground to obtain desired product.    USE - Method for preparing antibacterial agent (claimed).    ADVANTAGE - The method enables to produce eco-friendly antibacterial agent in economic way.
NOVELTY - A plant (P1) comprising an expression cassette which comprises an isolated nucleic acid segment encoding a cardiac glycoside reductase (CGR)2 and/or CGR3 enzyme, is new.    USE - The plant is useful for generating plant biomass and yielding fermentable sugars (claimed). The fermentable sugars are useful for generating biofuel e.g. ethanol.    ADVANTAGE - The method for yielding fermentable sugars is inexpensive and non-toxic and produces easily digestible biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) plant biomass from the plant (P1);    (2) seed from the plant (P1);    (3) method for yielding fermentable sugars involves digesting biomass from the plant (P1); and    (4) method for expressing CGR2 and/or CGR3 from an expression cassette at levels sufficient to increase a plant's biomass, where the expression cassette comprises at least one heterologous promoter and an isolated nucleic acid segment encoding CGR2 and/or CGR3 enzyme.
NOVELTY - An Enterococcus faecium strain having excellent growth rate and oligosaccharide removal rate from fermented soybean meal is isolated from soybean extract, is new.    USE - The strain is useful in preparation of fermented soybean meal, and lactic acid, organic acid and amino acid (all claimed) which is useful in agricultural, livestock and fishing industries.    ADVANTAGE - The fermented soybean meal has glucose concentration of 9-15%, protein concentration of 1-2%, excellent growth rate and oligosaccharide removal rate. The method is simple, environmentally-friendly and cost-effective, and produces nutritious fermented soybean meal effectively with optimized quality within a relatively short period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing Lactobacillus fermented soybean meal which involves extracting soybean using water at a temperature of 40-70 degrees C until the pH value of the extract reaches 4-5, culturing Lactobacillus strain in the extract, inoculating the cultivated Lactobacillus in soybean meal, fermenting the mixture at 30-35 degrees C until moisture content of the fermented mixture reaches 50-65%, to obtain fermented soybean meal.
NOVELTY - Method for controlling surface-inhabiting photosynthetic microorganism bloom in an aquatic system, involves producing buoyant composition comprising at least one photosynthetic microorganism inhibitor and floating agent, and applying the buoyant composition to the surface of the aquatic system under conditions which induce at least 50% reduction in the photosynthetic microorganism within a period of time in the aquatic system.    USE - The method is useful for controlling surface-inhabiting photosynthetic microorganism bloom in aquatic system, where the photosynthetic microorganism is chosen from Cyanobacteria, alga, plankton and their combinations, preferably Cyanobacteria (all claimed). The artificial system includes lakes, rivers, fountains, and ponds.    ADVANTAGE - The method controls 50-99% bloom, and reduces negative impact on environment and on health of humans and animals.    DETAILED DESCRIPTION - Method for controlling surface-inhabiting photosynthetic microorganism bloom in an aquatic system, involves producing buoyant composition comprising at least one photosynthetic microorganism inhibitor and floating agent, and applying the buoyant composition to the surface of the aquatic system under conditions which induce at least 50% reduction in the photosynthetic microorganism within a period of time in the aquatic system, where the at least one photosynthetic microorganism inhibitor is added at a concentration below drinking water allowable concentration in the aquatic system after the period of time, and is adapted to substantially disintegrate from the aquatic system such that it cannot be detected in its active form after the period of time. An INDEPENDENT CLAIM is included for diffusible buoyant composition which comprises photosynthetic microorganism inhibitor, and floating agent.
NOVELTY - A hydrogen storage composite electrode preparing method involves preparing a metal-organic framework composite electrode, dispersing nickel network, mixing porous material and conductive carbon material, adding absolute ethanol, adding PTFE to obtain paste, coating nickel with paste, and cooling to obtain the metal-organic framework composite electrode. The hydrogen storage process is subjected by taking aqueous solution followed by taking composite electrode and titanium oxide electrode, producing electrolytic hydrogen and stirring to obtain a finished product.    USE - Method for preparing a hydrogen storage composite electrode.    ADVANTAGE - The method enables preparing the hydrogen storage composite electrode with better charging and discharging capacity in an easy manner.    DETAILED DESCRIPTION - A hydrogen storage composite electrode preparing method involves preparing a metal-organic framework composite electrode by taking nitric acid and water at volume ratio of 1:3, dispersing 1x 8 cm nickel network in acetone for 20 minutes, washing using pickling solution, mixing metal-organic framework porous material and conductive carbon material in a container at mass ratio of 1:5-10:1, adding 1 ml absolute ethanol, dispersing ultrasonically for 30 minutes, adding 60% PTFE after heating and stirring, evaporating alcohol until the mixture to obtain paste, coating nickel network with the paste, mold pressing 1 mm sheet at 200 degrees C for 4 hours, and cooling to obtain the metal-organic framework composite electrode. The hydrogen storage process is subjected by taking 0.1-1 mol/l aqueous solution as conductive electrode followed by allowing nitrogen gas for 5-10 minutes, removing electrolyte air, taking metal-organic framework composite electrode as the cathode and titanium base oxide electrode as anode, producing electrolytic hydrogen and stirring continuously in the metal-organic framework composite electrode to obtain a finished product.
NOVELTY - This utility new type relates to a environment-friendly one stepping cotton pool, comprising circulation device and upper end opening of pool body, pool body set with a bearing plate, the pool body is divided into the upper part of layer and lower part of draining water layer, bearing plate set with connected upper layer and draining layer a penetrate hole water or penetrate water, circulation entrance device of a water draining layer, circulation device set with a located at one inner cotton layer or stepping pedal circulation exit of cotton layer. This utility new type of cotton pool process step the layer, and the excess of sewage through rear bearing plate entering into water draining layer circulation device is the lifting stepping cotton layer circulation use, which not only overcomes the loss and sewage culture material over-wet and so on, but also avoids the discharging and waste of water resource of sewage, and the sewage draining layer in a containing mushroom for growing of nutrition component, the circulation use a valid increase yield of straw mushroom. This utility new type also relates to one using a stepping cotton pool of the system. This utility new type application on a straw.
NOVELTY - This utility new type claims a one dragging belt aerobic sewage treatment device, including by the front water cabin and rear cabin is composed of, between said front water chamber and a rear water chamber set with baffle dam, a cabin body upper end is set with open type air entrance, a front water chamber upper end set with a towing gas transmission belt rotary wheel, said cabin body is further set with a drive used for towing gas transmission rotating wheel of belt motor, a motor connecting with a control system, a front water chamber through pipeline set with a water inlet and a rear water chamber set on the upper water port, a bottom set with cabin used for are set with active sludge and microorganism carrier inner connected a front water chamber and channel of said rear water cabin, a front water chamber and a rear water chamber. This utility new type provide a dragging belt aerobic sewage treatment device, small floor area, low investment cost and operation cost is low, biochemical process efficiency is high.
NOVELTY - Medicine comprises 21-24 pts. wt. Gentiana macrophylla, 23-26 pts. wt. radix angelicae pubescentis, 3-6 pts. wt. radix clematidis, 16-19 pts. wt. parasitic Loranthus, 14-17 pts. wt. Sambucus williamsii, 20-23 pts. wt. garden balsam stem, 17-20 pts. wt. giant knotweed, 15-18 pts. wt. Trachelospermum jasminoides, 26-29 pts. wt. caulis trachelospermi, 10-13 pts. wt. noded pit viper, 12-15 pts. wt. obscured homalomena rhizome and 5-8 pts. wt. Notopterygium root.    USE - The medicine is useful for dispelling rheumatism, promoting metabolism of human body, expelling wind and removing dampness, clearing away heat and removing toxins.    ADVANTAGE - The medicine is pure and environmentally-friendly, and causes no side effects.
NOVELTY - An aerobic granular sludge denitrification method involves utilizing completely mixing type continuous flow integrated sewage processing system, dividing into reaction area and deposition area at the valid volume ratio of (3-10):1, charging air by pump from the reactor reaction area under air flow quantity of 300-600 mL/min, from the water inlet above the reaction area, a precipitation zone and recycling sludge at ratio of 50-300 wt.%.    USE - Method for denitrification of aerobic granular sludge.
NOVELTY - An expression cassette having increased protein secretion ability in yeast compared to wild-type protein is new. The expression cassette comprises polynucleotide (P1) encoding translational fusion partner (TFP) and polynucleotide (P2) encoding proteins chosen from Trichoderma reesei xylanase II (TrXynII), TrBx1, T.reesei endoglucanase EG-II (TrEGL2), PaCEL1, PaCel2, TeCBH1, NfCBH1, Humicola grisea cellobiohydrolase I (HgCBH1), Chaetomium thermophilum CBH1 (CtCBH1), ClCBH2 and CfCex1.    USE - The expression cassette is useful in expression vector which is used in transformants for producing hemicellulase, endoglucanase or exoglucanase, and bioethanol. The hemicellulase, endoglucanase or exoglucanase is useful in cellulase cocktail which is used for saccharification of biomass (all claimed) for producing bioenergy or useful biochemical.    ADVANTAGE - The expression cassette has increased protein secretion ability in yeast as compared to wild-type. The cellulase cocktail simplifies saccharification process of the biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) expression vector comprising the above-mentioned expression cassette;    (2) transformant obtained by introducing the above-mentioned expression vector into host cell;    (3) production method of hemicellulase, endoglucanase or exoglucanase, involves culturing the above-mentioned transformants;    (4) production method of bioethanol, involves culturing the above-mentioned transformants, and collecting bioethanol from obtained culture or culture supernatant;    (5) mixed bacterial strain comprising one or more of the above-mentioned transformants;    (6) cellulase cocktail comprising endoglucanase, exoglucanase and beta -glucosidase, or hemicellulase produced by the above-mentioned method; and    (7) method for saccharification of biomass, involves using the above-mentioned cellulase cocktail.
NOVELTY - Catalyst comprises a catalytic element disposed on a substrate comprising cerium metal oxides (I).    USE - The catalyst is useful for: catalyzing a methanation reaction; and reducing the carbon monoxide content of a gas mixture including carbon monoxide and hydrogen (all claimed).    ADVANTAGE - The catalyst utilizes: the substrate to reduce poisoning of the catalytic element by a sulfur-containing gas or vapor (claimed); and the metallic elements which enhance the sulfur adsorption ability of the catalyst and/or increase the oxygen mobility in the substrate material.    DETAILED DESCRIPTION - Catalyst comprises a catalytic element disposed on a substrate comprising cerium metal oxides of formula (I).    x=0-0.3, optionally 0.01-0.3, preferably 0.1-0.2; and    M=metallic element other than Ce.    INDEPENDENT CLAIMS are also included for:    (1) methanation of a feedstock including carbon monoxide and hydrogen, comprising contacting the feedstock with the catalyst; and    (2) reducing poisoning of a catalytic element by a sulfur-containing gas or vapor, comprising depositing the catalytic element on the substrate.
NOVELTY - The present invention relates to a fast compost fermentation machine and method for manufacturing compost. Wherein the fast compost fermentation machine comprises one or more fermentation units that respectively contains a fermentor, a stirring unit, an heating unit and a driving unit. By the driving unit that drives the stirring unit to mix the materials to be fermented and the heating unit that maintains the fermentor space at specific temperature, the fast compost fermentation machine of the present invention remarkably reduces the time for manufacturing the organic compost, and provides the organic compost with large amount, high quality, low pollution and low cost.
NOVELTY - Covalent organic frameworks (COFs) contain porphyrin linked with hydroxyl aromatic compound by intramolecular O-H=NC bonding in which porphyrin is tetra(p-amino-phenyl)porphyrin (Tph), and hydroxyl aromatic compound is triformylphloroglucinol (Tp) or 2,5-dihydroxyterephthalaldehyde (Da/Dha).    USE - Covalent organic frameworks for gas storage, organic photovoltaic applications, and energy efficient water-alcohol separation to generate fuel-grade alcohol in biofuel industries.    ADVANTAGE - The COFs have good selectivity towards alcohol uptake at low pressure over water, are highly stable and porous, and have high crystallinity and surface area, along with hydrolytic and acid stability, excellent chemical stability, and porosity with moderate crystallinity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesis of COFs which involves mixing hydroxy aromatic compound and porphyrin at ratio of 2:1-1.8:1.2 in the presence of solvent to obtain reaction mixture, sonicating reaction mixture for 5-15 minutes to obtain homogenously dispersed reaction mixture, freezing reaction mixture at 70-80 K, preferably 77 K, degassing frozen mixture, heating at 110-130 degrees C for 3 days to obtain crude product, and purifying crude product to obtain 75-90% product.
NOVELTY - Rapid fertilization using bulk fertilizer comprises digging pits, filling with straw crop, adding bulk fertilizer, filling with farm crop, adding fertilizer, filling with grass or leguminous crop and adding fertilizer. Straw crop fertilizer comprises 80 pts. wt. potassium phosphate, 30 pts. wt. calcium superphosphate, 20 pts. wt. spirulina powder, 30 pts. wt. potassium sulfate, 20 pts. wt. animal fat and 10 pts. wt. aconite.    USE - Rapid fertilization using bulk fertilizer.    ADVANTAGE - The method is simple. The fertilizer is convenient and quick-effect.    DETAILED DESCRIPTION - Rapid fertilization using bulk fertilizer comprises digging pits, filling with straw crop, adding bulk fertilizer, filling with farm crop, adding fertilizer, filling with grass or leguminous crop and adding fertilizer. Straw crop fertilizer comprises 80 pts. wt. potassium phosphate, 30 pts. wt. calcium superphosphate, 20 pts. wt. spirulina powder, 30 pts. wt. potassium sulfate, 20 pts. wt. animal fat and 10 pts. wt. aconite. Farm crop fertilizer comprises 50 pts. wt. corn cob powder, 40 pts. wt. calcium superphosphate, 40 pts. wt. corn cob powder, 40 pts. wt. calcium superphosphate, 40 pts. wt. spirulina powder, 50 pts. wt. potassium sulfate, 40 pts. wt. animal fat and 30 pts. wt. aconite. Leguminous crop fertilizer comprises 45 pts. wt. fermented corn cob powder, 35 pts. wt. calcium superphosphate, 30 pts. wt. spirulina powder, 40 pts. wt. potassium sulfate, 30 pts. wt. animal fat and 20 pts. wt. aconite.
NOVELTY - Herbicide composition comprises propyrisulfuron and pyribenzoxim in a ratio of 1:10-128:5.    USE - The herbicide composition is useful for controlling weeds in paddy fields (claimed).    ADVANTAGE - The herbicide: can be used independently; increases the weeding effect; expands weeding spectrum; reduces generation of weed resistance; reduces the administration frequency; is economical; and has good environmental compatibility.
NOVELTY - Preparation of fertilizer comprises taking 3 fresh broken egg shell, 300 g crushed soybean, 750 g rice water, 500 g crushed animal bone and 1 kg plant ash, feeding into container, sealing, fermenting for 10-25 days, adding 5 kg rice water, fermenting for 5-8 days, filtering, recrystallizing to obtain 14-20 g crystals, packing, sealing and storing in dark room.    USE - Method for preparing fertilizer used for indoor flowering plant (claimed).    ADVANTAGE - The method can change allocation of raw materials based on soil pH to meet different kinds of flowers need.
NOVELTY - Indoor plant fertilizer comprises 2 g fresh egg shell, 40 kg soil fertilizer, 800 kg rice water, 100 g boiled vegetable water, 100 g fermented cow dung and 1 kg ash. It is prepared by mixing raw materials, fermenting for 10-25 days, removing air, fermenting for 5-8 days, removing waste, filtering, recrystallizing, packaging, sealing, adding 20-30 g charcoal, burying and sprinkling water.    USE - Indoor plant fertilizer.
NOVELTY - A fertilizer for indoor flower and plant comprises following raw material 4 kg fresh crushed egg shell, 0.6 kg farmyard manure, 750 g Tao Mishui, 500 g animal abdominal organs or animal corpse and 1 kg plant ash.    USE - As fertilizer for indoor flower and plant (claimed).    ADVANTAGE - According to the own property and growth need of plants, the present fertilizer can properly change the power of hydrogen of soil so as to meet the demands of different flowering plants.    DETAILED DESCRIPTION - A fertilizer for indoor flower and plant comprises following raw material 4 kg fresh crushed egg shell, 0.6 kg farmyard manure, 750 g Tao Mishui, 500 g animal abdominal organs or animal corpse and 1 kg plant ash; is prepared by taking the above the raw material into container according to given weight proportion, mixing uniformly, sealing the mouth of container by thin plastic film, fermenting for 10-25 days until the surface has no bubble, shifting it to the ventilated place and then injecting the container again 5 kg of Tao Mishui, sealing and continuing fermenting for 5-8 days, taking out the dregs, squeezing, filtering by using fine yarn cloth filter, and then recrystallization to obtain 15-20 g crystal followed by pouch packaging, sealing and storing; and is used by applying 3-5 g obtained crystal and 20-30 g charcoal slag mix on soil around plant in the pots, where the fertilizing layer thickness is 3-5 cm, placing it in sufficient sunlight for more than three days, and then watering by pool tank water, river water or rain water.
NOVELTY - Producing anti-caking agent, comprises deodorizing refined soybean oil by-products as raw materials, with diethanolamine to obtain soybean oil deodorizer distillate, where the mass ratio of refined soybean oil by-products and diethanolamine, is 5:1-6:1, and reacting fatty acid diethanolamine with soybean oil deodorizer distillate, in a mass ratio of 0.5:1-1:1, and obtaining fertilizer-based anti-caking agent with low condensing point.    USE - The fertilizer-based anti-caking is useful as nitro compound fertilizer, urea-based compound fertilizer, bulk blending (BB) fertilizer and various monomer-based fertilizers (claimed).    ADVANTAGE - The method converts waste into useful raw materials; is economical, and environmental friendly; has slight energy loss when compared to traditional anti-caking agent products, and good operation, and transportation procedures; and utilizes biodegradable raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of fertilizer anti-caking agent as nitro compound fertilizer, urea-based compound fertilizer, bulk blending (BB) fertilizer and various monomer-based fertilizers, where the anti-caking agent forms a brown-yellow suspension liquid at 25 degrees C.
NOVELTY - Organic fertilizer comprises (in wt.%): mushroom waste (30-70), sheep manure (20-60), soybean meal (5-30), hoof horn powder (0-5), cattle hairs powder (0-5), bone powder (3-10), microorganism group juice (0-0.5) and fermentation accelerant (0.1-1).    USE - Organic fertilizer used for preventing and treating pests in soil, preventing soilborne disease and heavy metal pollution.    ADVANTAGE - The organic fertilizer shows improved stress resistance of crop, improved crop yield and quality, improved soil fertilizing ability and soil organic matter content, and improved quantity of soil beneficial microorganism.
NOVELTY - A mesoporous aluminophosphate catalyst is prepared by mixing aluminum nitrate and phosphoric acid at molar ratio of 1:1 to obtain concentration of 0.3-0.6 mmol/g, adding ammonia at 70-90 degrees C to adjust pH to 4-6, stirring to obtain white precipitate aluminum phosphate, drying precipitate, placing in muffle furnace, calcining at 500-600 degrees C for 5-7 hours, and pulverizing to 20-40 mesh particles.    USE - Method for preparing mesoporous aluminophosphate catalyst (claimed).    ADVANTAGE - The method is simple, environment-friendly, and low-cost. The product is stable and has high lactic acid conversion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of mesoporous aluminophosphate catalyst comprising acetaldehyde decarbonylation.
NOVELTY - Synthesizing thymol involves adding raw material, carrier gas and the catalyst in the reaction vessel and then performing dehydrogenation, condensation and purification to obtain the finished product, where raw material is menthol, and catalyst is nickel-sodium silicate activated carbon supported catalyst.    USE - Method for synthesizing thymol (claimed).    ADVANTAGE - The method enables to synthesize thymol in a cost-effective and eco-friendly manner.
NOVELTY - Key intermediate 1-(3-methyl-1-phenyl-5-pyrazolyl) piperazine preparation involves adding N-Boc-N-acetoacetyl piperazine in Lawesson reagent and hydrazine in an organic solvent to form N-(tert.-butoxy)-4-(3-mrthyl-1-phenyl-1Hpyrazol-5-yl)piperazine. The formed N-(tert.-butoxy)-4-(3-mrthyl-1-phenyl-1Hpyrazol-5-yl)piperazine is treated with concentrated hydrochloric acid in an organic solvent for de-protection to get the finished key intermediate.    USE - Method for preparing key intermediate 1-(3-methyl-1-phenyl-5-pyrazolyl) piperazine (claimed).    ADVANTAGE - The method prepares key intermediate 1-(3-methyl-1-phenyl-5-pyrazolyl) piperazine in a simple, cost-effective and eco-friendly manner with high yield high on industrial scale.
NOVELTY - Enantioselective synthesis of dexlansoprazole comprises selective catalytic oxidation of 1.3-1.5 times of prochiral sulfide of lansoprazole compound excluding 1.5 times the mole equivalents of an oxidant in the presence of an asymmetric induction catalyst.    USE - The method is useful for enantioselectively synthesizing dexlansoprazole (claimed).    ADVANTAGE - The method is capable of enantioselectively synthesizing dexlansoprazole in an industrial, economical and eco-friendly manner with improved efficiency, high optical purity and chemical purity of the product.
NOVELTY - Extracting rutin from magnolia petals comprises (a) selecting fresh magnolia petals, adding 1-2 times of 50% ethanol to the petals and mashing; (b) adding 6-10 times of 50% acetic alcohol to the obtained slurry at 60 degrees C, extracting for 0.5-2 hours under microwave and filtering; (c) combining the extracts, removing ethanol and concentrating; (d) adding the concentrate into macroporous resin column and eluting; and (e) combining the eluates with 30% ethanol, concentrating, cooling, filtering the crystals, washing and vacuum drying the crystals at low temperature.    USE - The method is useful for extracting rutin from magnolia petals (claimed).    ADVANTAGE - The method is capable of extracting rutin with high purity and without using toxic organic solvent, hence the method is ecofriendly.    DETAILED DESCRIPTION - Extracting rutin from magnolia petals comprises (a) selecting fresh magnolia petals, adding 1-2 times of 50% ethanol to the petals at room temperature and mashing the petals to form magnolia pulp slurry; (b) adding 6-10 times of 50% acetic alcohol to the obtained slurry at 60 degrees C, extracting the slurry for 2-3 times for 0.5-2 hours under microwave and filtering the slurry to obtain an extract; (c) combining the extracts, removing ethanol using a rotary evaporator such that the extract is completely free of alcohol taste, and concentrating; (d) adding the concentrate into macroporous resin column, eluting the column first with distilled water and then with 30% ethanol; and (e) combining the eluates with 30% ethanol, concentrating the mixture, cooling, filtering the crystals, washing twice or thrice the crystals with a small amount of cold 95% ethanol and vacuum drying the washed product at low temperature.
NOVELTY - This utility new type relates to a one bulk solid organic substance fermentation using a device structure, especially relates to a bottom fermenting tower layer one blanking mechanism, comprising a bearing part, set with fixed in inner fermenting tower, with the at least one annular falling through a hole, scraping mechanism, a connecting bearing on the upper part, with the annular blanking through hole and a ring centre is overlapped set with a rotating center, and material of bearing and bearing clearance detector of blade moulding surface match a part, and an annular blanking through hole number of identical; time in scraper with scraping material mechanism, a material with the rotation of the scraper by the annular blanking through hole of falling. At the same time, the utility model is new type also relates to one with fermenting tower a blanking mechanism of this fermentation tower bottom layer. This utility new type using a technology plan, the whole structure is compact, few moving parts, the energy consumption is low, and it can bear more of multi-material, the whole structure is simple.
NOVELTY - This utility new type relates to a one fertilizer production device, specifically is a one controlled release fertilizer with a resin coating device. Comprising machine and resin fuser drum, said drum comprising a machine, set with a track ring, in a outside wall up and inserted in a cavity in a resin pipe, in the inner wall of a set up with a cavity between the arc plate, the arc plate and of a multi-ring distribute a set with a knocking block, a fuser comprising upper end enclosure is provided with a housing, a skirt mounted in housing, lower end of end enclosure is provided with outlet wherein, through pipeline to a resin groove in the outlet of the resin groove through pump and pipeline connecting to resin spraying pipe. This coating device a short period, a continuous production, realize the resin melt and coated continuous work, a greatly shortens the production period, reduces the loss and energy consumption of source material.
NOVELTY - Under one of a agricultural efficient multi-element selenium-enriched nutrition liquid of manufacturing device, multi-group a material A, material B and material C, mixing tank and material storehouse D E each one with a funnel and a pusher cavity electrically connecting is equipped with a pusher inner electric power in a pusher cavity, a material and a steelyard and multi-component proportioning bin and a feeder connecting power, wherein the discharging and conveying belt of a pusher cavity connecting electrically, the other end with transmission of the computer control positoin, a temperature, a pH automatic stir reaction kettle of a inlet, lower side outlet through pipeline and pump and storage tank inlet a, low in storage tank side outlet through pipeline and pump and a machine connecting. This utility new type computer capable of precise batching, the full-close device is not easy to pollute, rapid reaction, one can be finished for a flow.
NOVELTY - This utility new type relates to a one seal static aerobic biological fermentation device, comprising a one or multi-a, a multi-cabin by a multi-mutually independently of a cabin or compose a by a one or a vertical clapboard divides the one multi-a large cabin separating a mutually form a parallel multi-a, a chamber a of seal cabin, a cabin body set with inner containing space used for a fermentation material, the bottom of the cabin body set with cloth air pipeline, the cabin of cabin wall up a part and/or top of the chamber set with suction opening, a cloth air pipeline connecting with a blower, a suction opening with a fan or air channel and an air pipe is connected with a fan. This utility new type structure is simple, the floor space is small, scene mounting, operation and maintenance is convenient, and it is good for reducing the energy consumption and reducing the atmospheric pollution, the aerobic biological fermenting a each of a material.
NOVELTY - This utility new type claims a one collecting garden leaves produce organic fertilizer device, comprising box body, front end of the box body is opened with door, bottom end of the box body is set with organic fertilizer collecting box, the upper box body is further fixed with a leavening agent storage tank, a leavening agent storage box bottom end set with suction tube and organic fertilizer collecting box connected, the leavening agent storage roof set with one end a piston, used for organic fertilizer collecting box suction in fermentation liquid. This utility new type the garden leaves intensively stacking and fermenting process, produce organic fertilizer. Not only can the garden can be timely fallen leaves cleaning, but also avoids the environment pollution burning caused by a fallen leaves and unnecessary economic loss of, but also can produce good for plant growing of organic fertilizer.
NOVELTY - This utility new type claims a one micro-hydrogen-oxygen generator, comprising a cylindrical housing and a cylindrical housing is set on upper end of sealing cover, set with positive terminal and negative pole binding post outside in cylindrical housing, further set with oxygen supply wherein outside in a cylindrical housing, with one gas outlet, and set with a positive binding post and the cathode binding post is connected to electrolytic groove of inner component in the cylindrical housing, gas outlet connecting to air inlet pipe, a vehicle power source of engine and the anode binding post and the cathode binding post is connected with engine start time, an electrolytic groove module working electrolytic water produce hydrogen oxygen gas, wherein a oxygen for fuel of combustion-supporting, increase the combustion rate, and hydrogen is used for cylinder inner each part surface of removing carbon, carbon removing rear so that the fuel can burn fully, at the same time a different according to engine type regulating oxygen of the oxygen supply a wherein a oxygen amount, the hydrogen-oxygen mix gas in hydrogen-oxygen ratio is change, the engine of each type and a better match use.
NOVELTY - This new type utility claims one mower, comprising a mowing device and weed stir device, a mowing device including extension pole, two extension pole end of a hook and a cover, the front of the hook set with a handrail, a handrail set with a plate, a inner cover set with the first electric machine, the first electric machine a mowing, and the bottom of cover set with steel wire network. Through fan and cover the grass cutting and grass absorption to a crushing chamber under a fan room, a crushing room inner set with crushing bucket, chopping into rear inner crushing bucket by crushing knife crushing of at the same time, a raw material box a crushing bucket inner adding fermentation part, through stir mix to form a simple organic fertilizer, the organic fertilizer can be a inner buried in soil of garden, through fermentation in order to form so as to soil of a garden holding fertile, and past a set pouring weed, avoiding fertilizer loss, at the same time reduces the garden maintenance cost, but also green and environment-friendly.
NOVELTY - This utility new type claims a one economic type environmentally friendly warm-keeping pig, the pig house construction in a base, inner pigsty set with water heating device, pipeline device and a phase, wall of house by heat insulating material, the pipeline device comprising water inlet pipeline, latent pipeline, the water pipeline, transmission pipeline and circulation pipeline, a water inlet pipeline and circulation pipeline through connector and latent heat pipeline is connected with bottom fermentation pool set with latent heat pipeline, latent pipeline through connector and the water pipeline and delivery pipeline is connected with inlet of heat transferring pipeline and water-heating device, circulation pipeline and outlet of heating device is connected with each upper pipeline is set with a valve, inner fermentation pool is set with feeding groove, the utility model is new type use in fermentation process of fermentation pool heat of water flow of water-heating device for inner house a heating circulation, a piggery supply circulation heating, further a directly provide heating temperature water a pig farm, fully use the energy, at the same time, the device structure is simple, the practicability is strong.
NOVELTY - This utility new type relates to a one low temperature plasma waste gas treatment pipe, comprising stainless steel pipe and distributed with sharp teeth of wolf tooth rod, wolf tooth rod of two end are that there is a galvanized pipe, each of wolf tooth rod and the wolf tooth rod and stainless steel pipe set with a zinc-plated pipe in wolf tooth rod is suspended through a stainless steel tube of axis, wherein one part zinc-plated tube is exposed in a stainless steel tube outside a connecting anode and cathode of high voltage. And the existing technology, wolf tooth rod is stainless steel pipe and a connecting anode and cathode of high voltage, low in accelerate effect of electric field, the inner stainless steel tube produce high energy electronic, the time average energy exceeds a target treatment, a chemical key, a key broken, to eliminate a gaseous pollutant, the multi-stage process, it is easy to make a efficient pollutant decomposition, a low energy consumption and avoids the second pollution.
NOVELTY - This new type utility claims one a compost fermentation tower, comprising composting tower, spray tower and collecting pneuma tower, the tower top part set with compost with one sealing cover, a bottom set with a discharge port, a middle part cover with one set with a screw thread hole, and through this screw thread hole match with screw pole, screw pole lower end extending to compost inner tower, and to this end with one set with a pressure plate, the pressure plate and the composting tower inner wall clearance of 5 cm, a screw thread pole on one end cover top part set with one of a rotating handle, the side wall of said composting tower close to the top position set with a feeding port, the feeding port match with the first cover, the cover side wall position of the spray tower and the top part between a supply pneuma tube between the side wall and collecting pneuma tower of the spray tower is connecting with the first air supply pipe, this device can finish for compost, filter and gas of organic waste set the pneuma is high, at the same time a smaller area of the whole close, avoid damaging the surrounding environment.
NOVELTY - This new type utility claims one organic fertilizer filter a fermentation system. The system comprising at least one of a primary ferment pool, further comprising a level fermentation pool, filter the fermentation tank, a conveying channel and collector pool, a primary fermentation pool through transmission pipeline and second level fermenting pool is connected with the second level fermentation pool through transmission pipeline and filter the fermentation tank, a transmission pipeline set with the control valve, the bottom of the filter tank is set with liquid fermentation; the conveying channel is set below liquid-permeable, and collector pool and connected with the liquid pool circulation pump and a circulation pipeline, circulation pipeline outlet is set on the filter the fermentation tank. This utility new type is skilfully design the can be integrated strain culture, fermentation and repeated fermentation filter as a whole, without need to machinery or organic fertilizer fermenting system of aritificial. This utility new type has simple structure, simple operation, finish the continuous fermentation, saves the cost and increase the production efficiency.
NOVELTY - This utility new type claims a preparation compound fertilizer of one device, comprising sieving mixer and crusher, a crusher crushing of raw material through material guide plate to guide groove in the sieving separation of raw material through the first spiral conveying machine and conveying to storage in the collecting groove in raw material of inner tank body and then is sent to the mixing machine through a second spiral conveying machine a mix, a crushing, sieve and mix of a automatic, it can rapid mixing uniformly raw materials, it has low energy consumption is low and the cost is less than a.
NOVELTY - Number group swingably electromagnetic This utility new type relates to one with electric power saving device of a hydrogen-oxygen mix gas generator of electrolytic groove, comprising containing electrolyte of electrolytic groove, inner mounting in electrolysis groove and a connecting and a plate electrode, the electric power saving device comprising mounting in the electrolytic groove outside of a ultrasonic happen part number, and relative and set in the electrolytic groove outside of, the ultrasonic happen part, electromagnetic is swingably cross-shaped arrangement interval. This utility new type through ultrasonic happen part and swingably to weakening of electromagnetic force between the atom or molecule in electrolyte and for a negative ion, positive ion in electrolyte produce attraction, accelerate a separate, so as to activate and increase electrolytic efficiency and to save electric power of electrolytic effect.
NOVELTY - Manufacture of traditional Chinese medicinal healthcare pillow involves dispensing mixture comprising Rhodiola rosea, caulis polygoni multiflori, Flos Albiziae, notopterygium root, rush, lucid ganoderma, Angelica dahurica, erigeron breviscapus, storax, salvia, Tuckahoe, rehmanniae and black tea; making juice using water, heating to boiling juice; soaking and pea juice soaking; drying of pea into rear pillow inner set; sealing to make traditional Chinese medicine health care pillow.    USE - For manufacture of traditional Chinese medicinal healthcare pillow.    ADVANTAGE - The method prepares pillow without electricity. The process is environment-friendly and energy-saving, and the medicine use time is long. It can completely purify inner air quality. The pillow relieves fatigue and relieving pain in neck and heart, activates blood and provides good health care.    DETAILED DESCRIPTION - Manufacture of traditional Chinese medicinal healthcare pillow involves dispensing mixture comprising 10-20 pts. wt. Rhodiola rosea, 5-15 pts. wt. caulis polygoni multiflori, 10-30 pts. wt. Flos Albiziae, 3-7 pts. wt. notopterygium root, 2-6 pts. wt. rush, 2-6 pts. wt. lucid ganoderma, 1-2 pts. wt. Angelica dahurica, 2-4 pts. wt. erigeron breviscapus, 1-3 pts. wt. storax, 2-6 pts. wt. salvia, 1-2 pts. wt. Tuckahoe, 1-2 pts. wt. rehmanniae and 20-40 pts. wt. black tea; making juice using water, heating to boiling juice; soaking and pea juice soaking; drying of pea into rear pillow inner set; sealing to make traditional Chinese medicine health care pillow.
NOVELTY - Farmyard organic planting fertilizer comprises 20-25 pts. wt. tea plant, 12-18 pts. wt. mulberry, 23-30 pts. wt. straw, 18-24 pts. wt. plant ash, 5-8 pts. wt. oil cake meal, 7-12 pts. wt. human excreta, and 30-35 pts. wt. livestock manure.    USE - Used as farmyard organic planting fertilizer.    ADVANTAGE - The fertilizer utilizes raw materials of organic matter, thus reducing environmental pollution; can be prepared in a simple and easy manner; is rich in nutrition, and can be easily absorbed by plants, and has long lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing farmyard organic planting fertilizer, comprising: (a) taking tea plant, straw, plant ash, oil cake meal, human excreta, and livestock manure, allowing to stand, separately collecting tea leaves or tea tree branches, and collecting mulberry tree leaves and mulberry branches, cutting the straw and crushing into a powder, and crushing oil meal and livestock manure into granules; (b) drying the powder produced in step (a) up to a water content of 35-45%; (c) mixing the materials in uniform ratio; (d) fermenting and mixing the raw materials of step (c) at 0-25 degrees C for 35-50 days; (e) air drying the starting material to a moisture content of 30-35%; (f) pulverizing and sieving the product obtained in step (e) into powder of 80-100 mesh and granulating with a granulator to a particle size of 4-6 mm; and (g) storing the product in a plastic film packaging bags and placing in a storage warehouse, at 5-15 degrees C and relative humidity of 40-50%.
NOVELTY - Method for improving production yield of calcium chlortetracycline involves providing chlortetracycline fermentation solution, adjusting pH to 7.3 by adding sodium hydroxide solution, adjusting pH by adding calcium carbonate, stirring, filtering using plate and frame filter and drying filter cake.    USE - Method for improving production yield of calcium chlortetracycline (claimed).    ADVANTAGE - Calcium chlortetracycline having high quality is prepared with high yield by environmentally-friendly and economical process by reducing the chlortetracycline content in the discharged wastewater by 30%.
NOVELTY - Rapidly extracting high molecular weight fibroin protein, comprises (i) taking out silk gland from mature insect body, removing the outer layer of epithelial tissue, and collecting clear-transparent protein bands; (ii) soaking the protein bands in deionized water or washing with phosphate buffered saline (PBS); (iii) adding buffering solvent into silk fibroin protein, then placing on a shaking table, and shaking for 0.5-12 hours at 0-100 degrees C to obtain silk fibroin solution; and (iv) drying the silk fibroin solution to powder form or directly using in the preparation of other materials.    USE - The method is useful for rapidly extracting high molecular weight fibroin protein (claimed).    ADVANTAGE - The method has simple operation procedure, and mild preparation condition; shortens the extraction period; has simple and efficient extraction process, and thus it saves time; utilizes unused other toxic chemical agents during the extraction process; is economical; and does not produce other wastes while extracting, and thus it is environmental friendly.    DETAILED DESCRIPTION - Rapidly extracting high molecular weight fibroin protein, comprises (i) taking out silk gland from mature insect body, removing the outer layer of epithelial tissue, and collecting clear-transparent protein bands; (ii) soaking the protein bands in deionized water or washing sericin protein by using phosphate buffered saline (PBS), to obtain silk fibroin protein; (iii) collecting the silk fibroin protein by adding a buffering solvent, then placing on a shaking table, and shaking for 0.5-12 hours at 0-100 degrees C to obtain silk fibroin solution; and (iv) drying the silk fibroin solution to powder form or directly using in the preparation of other materials.
NOVELTY - Extraction and separation of high-purity resveratrol from peanut root involves grinding peanut roots into fine powder, extracting using ethanol, forming clear paste, cooling, providing resultant product into a macroporous adsorption resin column, eluting using water and 70% ethanol, collecting 95% eluted fractions, recovering ethanol, providing obtained product into a polyamide resin adsorption separation column, carrying out thin layer chromatography tracking and detection process, collecting resveratrol fractions, decoloring, evaporating, drying, and recrystallizing.    USE - Extraction and separation of high-purity resveratrol from peanut root (claimed).    ADVANTAGE - The method enables simple, reliable, economical and safe extraction and separation of high-purity resveratrol from peanut root using nontoxic solvent.    DETAILED DESCRIPTION - Extraction and separation of high-purity resveratrol from peanut root involves grinding peanut roots into fine powder, extracting using ethanol at 20-60 degrees C for 30-60 minutes, recovering ethanol from extracting liquid, concentrating to relative density of 1.18-1.22, forming clear paste, cooling, providing resultant product into a macroporous adsorption resin column, eluting using water and 70% ethanol, removing colorless liquid, eluting using 95% ethanol, collecting 95% eluted fractions, recovering ethanol, providing obtained product into a polyamide resin adsorption separation column using mixture of alcohol and acid as eluent, carrying out thin layer chromatography tracking and detection process, collecting resveratrol fractions, decoloring using activated carbon, filtering under protection of nitrogen at 50-70 degrees C, evaporating to relative density of 1.15-1.18, drying, recrystallizing using ethanol, and obtaining resveratrol with purity of more than 95%.
NOVELTY - Extracting amygdalin comprises taking loquat and then crushing into powder, adding bitter almond and supercritical carbon dioxide to the powder, uniformly mixing, extracting the mixture using anhydrous ethanol to obtain extraction liquid, and uniformly stirring.    USE - The method is useful for extracting amygdalin (claimed).    ADVANTAGE - The method is capable of efficiently, simply and easily extracting amygdalin with high yield of more than 2.68%, high purity and quality, improved solubility and reduced cost, and without harmful solvents.
NOVELTY - Gypenoside L and gypenoside LI (II) are new.    USE - (I) and (II) are useful for treating cancer, preferably human liver cancer (claimed).    DETAILED DESCRIPTION - Gypenoside L of formula and gypenoside LI of formula (II) are new. An INDEPENDENT CLAIM is also included for preparation of (I) and (II).
NOVELTY - Extracting DNA from plant leaves based on a simple rapid polymerase chain reaction (PCR) involves collecting fresh plant leaves, then shredding and directly placing in centrifugal tube filled with liquid (a1), soaking for at least 1 minute (preferably 30 minutes), adding liquid (b1) comprising 0.05M hydrochloric acid solution, mixing uniformly and extracting to obtain DNA template for PCR. The liquid (a1) is prepared by mixing 2 g sodium hydroxide, 0.7448 g ethylene diamine tetraacetic acid and 2.42 g trihydroxymethyl amino alkyl, then adding water to 1 l and sterilizing.    USE - For extracting DNA from plant leaves (claimed).    ADVANTAGE - Compared with the traditional technology, the present method utilizes simple reagent, is cost-effective, does not need large apparatus, avoids use of liquid nitrogen or ice for storing sample, avoids grinding, extraction, precipitation and dissolution steps, and is environment-friendly.
NOVELTY - Preparation of moxifloxacin hydrochloride intermediate compound (I) comprises carrying out reducing reaction of oxybenzene containing compound (A) in an organic inert solvent in zinc borohydride.    USE - Method for preparing moxifloxacin hydrochloride intermediate compound (I) (claimed).    ADVANTAGE - The method has reduced production cost, increased production safety, reduced industrial pollution, and high yield, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of moxifloxacin hydrochloride intermediate compound of formula (I) comprises carrying out reducing reaction of oxybenzene containing compound of formula (A) in an organic inert solvent in zinc borohydride.
NOVELTY - Fertilizer comprises (in pts.wt.): organic fertilizer (12-18), potassium sulfate (5-10), blood meal (4-8), phosphoric acid diamine (1-2), ammonium sulfate (2-3) and organic bentonite (20-30).    USE - Fertilizer used for increasing starch content in sweet potato (claimed).    ADVANTAGE - The fertilizer is green and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves mixing blood meal, organic fertilizer and organic bentonite, where obtained mixture is fermented for 5-8 days to obtain fermented base material, that is mixed with potassium sulfate, phosphoric acid diamine and ammonium sulfate to obtain product.
NOVELTY - Fertilizer comprises (wt.%): urea (20-22), ammonium salt (30-32), potassium salt (30-35), yeast powder (4-10) and inorganic adhesive material (4-10).    USE - Fertilizer.    ADVANTAGE - Fertilizer is eco-friendly.
NOVELTY - Organic culture medium comprises (in wt.%): chinaberry skin powder (0.2-0.8), chicken manure (6-6.5), sheep manure (15-15.5), plant ash (1.2-2), potassium sulfate compound fertilizer (1.0-1.5) and garden soil (74-76).    USE - Organic culture medium used for planting vegetable (claimed) and preventing plant diseases and insect pests.    ADVANTAGE - The organic culture medium increases fertility of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic culture medium, which involves:    (A) crushing chinaberry bark;    (B) drying garden soil;    (C) weighing potassium sulfate compound fertilizer;    (D) drying and mixing chicken manure, sheep manure and plant ash to obtain mixture;    (E) fermenting obtained mixture with effective microorganism at 45-50 degrees C for 7-15 days; and    (F) mixing fermented material with chinaberry bark powder, garden soil and potassium sulfate compound fertilizer to obtain organic culture soil.
NOVELTY - The impedance metric sensor assembly has one or more electrodes positioned on a substrate. Multiple electrospun nanofibers are positioned on the substrate. The impedance metric sensor assembly operates at a temperature of about 500 degrees Celsius or more and at a frequency of about 100 kilohertz or more to detect gas.    USE - Impedance metric sensor assembly for detecting reducing gas e.g. propane, carbon monoxide.    ADVANTAGE - Ensures real-time detection of reducing gas even at high temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an impedance metric sensor assembly fabricating method; and    (2) a nanofiber fabricating method.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory diagram of a sensor.
NOVELTY - The method involves laminating an insulator element (200) on cathode channel section for laminating cathode channel section which includes cathode channel element. An anode channel section (300) is laminated which includes anode channel element so that the fuel flows through fuel gas influx unit material (120a). The former laminated insulator element is ejected in upper side of a manifold unit through the fuel gas channel to the fuel gas discharge element (120b). The latter insulator element is ejected on the anode channel section through oxidant gas flow passage.    USE - Method for manufacturing solid oxide fuel cell.    ADVANTAGE - The method manufactures the solid oxide fuel cell in a simple manner with enhanced fuel cell efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic disassembled perspective view of the solid oxide fuel cell.    Lower manifold unit (100)    Influx unit material (120a)    Fuel gas discharge element (120b)    Insulator element (200)    Anode channel section (300)
NOVELTY - Catalyst is obtained by impregnation of glass fibre carrier (structured in form of material, woven from threads with 1 mm diameter) with film-generating solution, maturation of which is realised at temperature 20-22 degrees C for 4-5 days, and its further step-by-step thermal processing - at 60 degrees C for 30-40 minutes and at 700 degrees C for 1 hour, with the following ratio of initial solution components, wt %: titanium tetra-n-butoxide from 4.09 to 4.13, tetraethoxysilane from 0 to 1.49, cobalt(II) chloride tetrahydrate from 2.15 to 3.41, hydrochloric acid 0.27, distilled water from 0.56 to 1.04, n-butyl alcohol - the remaining part.    USE - Chemistry.    ADVANTAGE - Increased level of purification.1 tbl, 2 dwg, 3 ex
NOVELTY - Installation for bacterial leaching of metals from technogenic wastes includes apparatus for accumulation of microorganism mass in liquid medium with technogenic wastes, apparatus for leaching metals from technogenic wastes, unit for separation of metals from liquid medium with technogenic wastes in form of apparatus for ionic floatation and unit for regeneration of leaching solutions in form of reservoir with pneumatic system of aeration. Apparatus for accumulation of microorganism biomass is equipped with turbine mixer and external cooling circuit. As apparatus for metal leaching, used is multi-chambered floatation apparatus with devices of flow of liquid medium with technogenic wastes from chamber to chamber, made with possibility of changing conditions of aeration and intensity of mixing.    USE - Chemistry.    ADVANTAGE - Increased degree of metal leaching from technogenic wastes.5 cl, 5 dwg
NOVELTY - Preparing fertilizer involves soaking tulip seed in water for 10-15 minutes and then drying at 10-15 degrees C. The seed is crushed to obtain powder and then mixed with potassium permanganate, garlic, Bidens tripartita, honeysuckle, leek, sulfur powder, and bamboo charcoal ash to obtain the mixture. Sand is sterilized and then mixed with pig bone, urea, calcined oyster powder, ammonium chloride, perlite powder, prepared rhizome of Rehmannia, polysaccharide and water to obtain another mixture.    USE - Method for preparing fertilizer used for promoting growth of tulip (claimed).    DETAILED DESCRIPTION - Preparing fertilizer involves soaking tulip seed in water for 10-15 minutes and then drying at 10-15 degrees C. The seed is crushed to obtain powder and then mixed with potassium permanganate, garlic, Bidens tripartita, honeysuckle, leek, sulfur powder, and bamboo charcoal ash to obtain the mixture. Sand is sterilized and then mixed with pig bone, urea, calcined oyster powder, ammonium chloride, perlite powder, prepared rhizome of Rehmannia, polysaccharide and water to obtain another mixture. The mixture is heated at 40-50 degrees C and cooked rice and seaweed polysaccharide are added into mixture and then fermented to obtain fermented product. The fermented product is mixed mixture to obtain the product.
NOVELTY - Preparation of alginate oligosaccharide biological fertilizer comprises activating Flammeovirga pacifica (CCTCC No: M2012229) in culture medium flat plate to obtain seed culture medium, oscillating to obtain fermentation liquid, inoculating with sugar producing culture medium, continuously oscillating, centrifuging, collecting upper clear liquid, tubular film filtering, collecting filtrate and treating with protease.    USE - Method for preparing alginate oligosaccharide biological fertilizer used for crops (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application method of alginate oligosaccharide biological fertilizer comprising diluting alginate oligosaccharide biological fertilizer with water to final concentration of 25-500 mg/L and applying fertilizer once every 7-10 days at dosage of 50 mL/time for first four application times and 100 mL/time for next applications.
NOVELTY - A biological fertilizer with bactericidal effect comprises 4-6 pts. wt. zinc sulfate, 4-10 pts. wt. soybean powder, 1.1-2.05 pts. wt. Bacillus subtilis, 3.5-8 pts. wt. expansive soil, 0.3-0.6 pt. wt. metsulfuron-methyl, 4.2-7.6 pts. wt. potassium humate, 3.8-6.5 pts. wt. powdered rock phosphate, 5.5-9 pts. wt. plant ash, 3.1-6.4 pts. wt. potassium nitrate, 2.3-4.8 pts. wt. thunder god vine, 3-5 pts. wt. diammonium phosphate, 1.2-3.4 pts. wt. calcium chloride, 1.3-3.4 pts. wt. tobacco leaves residue powder, 1.5-4.2 pts. wt. flax waste, and 0.6-1.4 pts. wt. grass peat.    USE - Biological fertilizer with bactericidal effect (claimed).    ADVANTAGE - The fertilizer satisfies plant growth, effectively kills bacteria in soil, reduces risk of plant disease, and improves crop yield.
NOVELTY - Organic type sow thistle special fertilizer comprises 30-50 pts. wt. dry excrement, 30-45 pts. wt. bean cake, 20-35 pts. wt. cassava residue, 10-20 pts. wt. straw, 5-10 pts. wt. plant ash, 1-5 pts. wt. water retention agent and 1-2 pts. wt. soil loosening agent.    USE - As organic type sow thistle special fertilizer.    ADVANTAGE - The fertilizer supplies nutrients to sow thistle, increases effectiveness of soil nutrients, phosphorus content, permeability of soil and water retention capacity of soil, and improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing the raw materials, stirring the mixture for 70-80 minutes, crushing the mixture into 8-15 mesh, adding mixture into fermenting tank, stacking mixture, covering mixture with plastic cloth, hermetically fermenting mixture for 68-78 hours, pelleting, packaging and storing product in storehouse.
NOVELTY - Biological organic fertilizer comprises 3-7 pts. wt. Lactobacillus acidophilus, 2.5-6 pts. wt. Bacillus subtilis, 3.5-8 pts. wt. diammonium phosphate, 1.5-4.6 pts. wt. sodium humate, 2.2-4.9 pts. wt. glutamic acid, 0.8-1.7 pts. wt. ferrous sulfate, 3.6-7.5 pts. wt. potassium nitrate, 4-8 pts. wt. sheep manure, 2.4-5.7 pts. wt. animal bone powder, 1.2-3.4 pts. wt. egg shell powder, 1.5-4.3 pts. wt. borax decahydrate, 3.2-6.8 pts. wt. ammonium formate and 0.6-1.4 pts. wt. growth regulator.    USE - As biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer improves soil structure, is suitable for land with damaged soil, can perform soil repair function for long period of time, and loosens soil.
NOVELTY - Special fertilizer for corn comprises 6-11 pts. wt. carbamide, 3-8 pts. wt. potassium dihydrogen phosphate, 2-6 pts. wt. calcium biphosphate, 2-3.6 pts. wt. manganese sulfate, 1.2-2.6 pts. wt. diatomaceous earth, 2-4 pts. wt. Bacillus licheniformis, 1.6-2.7 pts. wt. methionine, 1.3-2.8 pts. wt. mushroom residue, 0.7-1.6 pts. wt. rhizobia, 0.2-0.5 pts. wt. ferric oxide, 0.3-0.7 pts. wt. surfactant, 0.6-1.2 pts. wt. rice bran, 1.5-2.4 pts. wt. potassium fulvate, 2.5-6 pts. wt. cow dung and 2.2-4.6 pts. wt. ammonium sulfate.    USE - The special fertilizer for corn is useful for inducing formation of well-developed root system capable of effective absorption of nutrients.    ADVANTAGE - The special fertilizer enhances disease resistance ability and ensures plant health.
NOVELTY - A container nursery substrate for growing orange seedling comprises sludge, and river sand, where the sludge contains sludge water, industrial waste water and life sewage sludge. The sewage sludge comprises 30-60 vol.% river sand, and 40-70 vol.% raw material. The life sewage sludge comprises sewage sludge, waste and garden greening bag having volume ratio of 2:1:1.    USE - As a container nursery substrate for growing orange seedling (claimed).    ADVANTAGE - The container nursery substrate uses low cost raw materials; provides high survival rate of orange seedling; reduces the releasing speed of nutrient; reduces nutrient loss, so that it realizes slow release long-acting effect; and reduces the cost of the operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the container nursery substrates involving mixing sludge contains sludge water, industrial waste water and life sewage sludge in turners, stacking at 50-70 degrees C, for 3-5 days to obtain sewage sludge compost; removing impurities; filtering; preparing life sewage sludge by mixing sewage sludge, waste and garden greening bag; removing impurities; filtering; and packing.
NOVELTY - Fertilizer comprises 4-8 pts. wt. chicken manure, 3-7 pts. wt. calcium dihydrogen phosphate, 2.5-6 pts. wt. straw powder, 3.5-7 pts. wt. vermiculite, 2.3-5 pts. wt. potassium sulfate, 2.2-4.8 pts. wt. borax, 3.4-8 pts. wt. radix sophorae flavescentis, 4.1-7.6 pts. wt. coating agent, 3.5-8 pts. wt. Lactobacillus acidophilus, 4.5-9 pts. wt. Artemisia rupestris, 1.2-4 pts. wt. hop, 3-7 pts. wt. limestone, 3.6-7.4 pts. wt. plant ash and 3-7 pts. wt. rice bran.    USE - The fertilizer is useful for improving soil acidity (claimed).    ADVANTAGE - The fertilizer enhances absorption ability and disease resistance ability of plant, and hence ensures fully nutritious plant.
NOVELTY - A long-acting biological organic fertilizer comprises: 3-7 pts. wt. castor bean, 4-9 pts. wt. semen armeniacae amarae, 3.2-4.8 pts. wt. radix sophorae flavescentis, 10-20 pts. wt. pig manure and human excrement, 1.5-6 pts. wt. plant ash, 3.5-8 pts. wt. clover, 2.2-4.6 pts. wt. carrot, 2.4-5.9 pts. wt. potato, 3-3.8 pts. wt. honey, 0.6-1.5 pts. wt. sodium tetraborate, 0.4-9 pts. wt. zinc sulfate, 0.6-1.3 pts. wt. soluble potassium salt, 0.6-1.1 pts. wt. large intestine, 0.4-9 pts. wt. Bacillus subtilis, and 0.5-0.7 pts. wt. Trichoderma.    USE - As a long-acting biological organic fertilizer (claimed), used in agricultural products, for soil and crop.    ADVANTAGE - The fertilizer enhances ability to resist disease of crop; improves soil structure; reduces environmental pollution; provides environment safety; is non-toxic; and is environment-friendly fertilizer.
NOVELTY - Sophie Bouvet intermediate compound is prepared by performing dynamic kinetic resolution of anhydrous aprotic solvents under action of organic base and/or inorganic base at 10-30 degrees C for 5-10 hours to obtain propionic acid isopropyl ester derivative.    USE - Preparation of Sophie Bouvet intermediate compound (claimed).    ADVANTAGE - The preparation process can perform selectively phosphatidyl center epimerization without destroying L-alanine isopropyl chiral, and has high reaction conversion rate and product purity, low cost, and is environment-friendly.    DETAILED DESCRIPTION - Sophie Bouvet intermediate compound of formula (II) is prepared by performing dynamic kinetic resolution of anhydrous aprotic solvents, such as propionic acid isopropyl ester derivative of formula (II) under action of organic base and/or inorganic base at 10-30 degrees C for 5-10 hours to obtain propionic acid isopropyl ester derivative of formula (I). The aprotic solvent is ester solvent, ketone solvent, and/or ether solvent. Organic base and/or quality of inorganic base is represented by compound (II) with 0.1-10 mass%. Compound (II) is composed of mixture of compound (I) and propionic acid isopropyl ester derivative of formula (III), with mass content ratio of 1:1-1:9. Wavy bond represents S configuration or R configuration. Substituted C5-C10 aryl group is electron withdrawing substituents.    R=substituted 5-10C aryl group.
NOVELTY - A rutin is extracted by taking rutin extract, placing in separation medium, adsorbing, eluting with alcohol at volume ratio of 1:1-8, collecting eluate, concentrating, filtering, drying, and purifying.    USE - Method for extracting rutin (claimed).    ADVANTAGE - The method is non-toxic, safe, short, environmental-friendly, simple, easy and suitable for industrial production; it has high yield. The product has good purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of rutin extract comprising crushing material containing rutin, sieving, adding distilled water, adjusting pH value to 0-6.0, adding complex enzymes, hydrolyzing at 40-60 degrees C for 1-6 hours, filtering, adding alcohol at weight to volume ratio of 1:5-20, stirring, extracting, and filtering.
NOVELTY - Self-cleaning environment-friendly chicken, comprising chicken cage and fermenting bed, mounting inner in chicken coop, per a hencoop bottom plate a right of fecal leakage plate network, network fecal leakage plate mounting the inclined manure guide plate, the upper guide plate is further mounted the excrement flushing pipe, flush mounted in transverse coop side wall inner side of the fermentation bed. in henhouse, manure guide plate through a wall to wall outside and the fermentation bed. The beneficial effect is fecal leakage plate is convenient for network of urine and manure, manure guide plate rear real time clean cultivation chicken size convenient for real time into fermenting bed, urine and excrement flushing can be flushing rear retention of urine and excrement, urine and excrement in network fecal leakage plate or guide plate a manure into a fermenting bed, a fermenting bed set in chicken house outside, so the chicken cage inner without pollution and inner machine and has no pollution, the real of the chicken field living environment is a vapor phase.
NOVELTY - Preparing borneol comprises adding camphene mixture having camphene content of more than 95%, solvent and water into a distilling kettle, heating for distilling at azeotropic temperature, condensing tower top product of the distillation kettle to form distillate, passing the distillate into the distillation kettle through a fixed catalyst bed to react at 50-80 degrees C for 8 hours to obtain a reactant, performing sampling analysis of the reactant in the distillation kettle, stop heating when the camphene content in the reactant is less than 3%, and cooling to 40 degrees C to discharge.    USE - The method is useful for preparing borneol (claimed).    ADVANTAGE - The method is capable of efficiently preparing borneol without pollution in a cost-effective manner.    DETAILED DESCRIPTION - Preparing borneol comprises adding camphene mixture having camphene content of more than 95%, solvent and water according to a weight ratio of 1:2-5:0.36-0.72 into a distilling kettle, heating for distilling at azeotropic temperature of 60-80 degrees C, condensing tower top product of the distillation kettle to form distillate, passing the distillate into the distillation kettle through a fixed catalyst bed to react at 50-80 degrees C for 8 hours to obtain a reactant, performing sampling analysis of the reactant in the distillation kettle, stop heating when the camphene content in the reactant is less than 3%, cooling to 40 degrees C to discharge. The solvent is isopropyl alcohol. The fixed catalyst bed is provided with a solid acid catalyst.
NOVELTY - Microorganism decomposing processor comprises fermentation tank (1), a feeder (2), a feeder pump (3), oil water separating tank (4), a draught fan (5), a box (6) and a shell, where the fermentation tank is semi-cylindrical groove shaped thin wall stainless steel. The inner cavity of lower part of fermentation tank is rotated left and right. Cylindrical spiral edge of strip-shaped stirrer (11) is connected with front side groove wall part of the fermentation tank through rectangular hole (12). The rectangular hole is connected with a feeding door with opening and closing properties.    USE - Microorganism decomposing processor for kitchen food residue (claimed).    ADVANTAGE - The microorganism decomposing processor is used conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows an internal structure of a microorganism decomposing processor.    Fermentation tank (1)    A feeder (2)    Feeder pump (3)    Oil water separating tank (4)    Draught fan (5)    Box (6)    Strip-shaped stirrer (11)    Rectangular hole (12)
NOVELTY - Biological organic matter returning soil improving fertilizer comprises 30-60 pts. wt. tea bar, 10-50 pts. wt. edible fungi, 5-30 pts. wt. plant oilseed cake, 3-35 pts. wt. amino acids, 0.3-2 pts. wt. sugar powder, 1-10 pts. wt. lime powder, 3-20 pts. wt. Polygonum whole plant, and 2-30 pts. wt. Sophora whole plant.    USE - Used as biological organic matter returning soil improving fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing biological organic matter returning soil improving fertilizer comprising: (a) taking waste tea bar and edible fungi, crushing into fine powder of 30-300 meshes, crushing plant oilseed cake into fine powder of 50-300 meshes, and adding sugar powder and lime powder, and mixing; (b) uniformly stirring the obtained powder and storing in a closed fermentation tank (1), at room temperature for 6-15 days for fermenting; and (c) after the completion of fermentation, adding Polygonum whole plant and Sophora whole plant, grinding into micron-sized powder as a preservative pesticide.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the internal structure of the fermentation tank.    Closed fermentation tank (1)    Side plates (1-1)    Cover plate (1-2)    Discharge port (2)    Diatom mud layer (4)
NOVELTY - This utility new type relates to a one a dejection to degrade a temperature pigsty, belonging to the cultivation technology field. Pigsty is a semi-opened structure, solar energy device set with a hot water pipeline and the cold water pipeline of water storage pool on the house roof, solar energy device through bi-directional gate at a, bi-directional gate a cold hot water entering into a radiating tube, a tube with the water pool water inlet pipe form a circulation, lower the piggery ground set with cross transverse and vertical hole channel and lower cross horizontal and vertical pit channel a the upper tunnel and the lower tunnel, cement pig bed set with radiating network, water pipe, a reverse film, one end heat insulating film and cross horizontal and vertical type tunnel, water pipe of a cold and hot water inlet pipe, and the other end connecting the water pipe, the water pipe uniform on the cross hole channel is set up. This utility new type can provide a piggery temperature can, at the same time, a excrement degradation of pigsty, which pig breeding industry in very important and great increase of the benefit of pig, promotes the development of industry, reduces the pig cultivation of a cost.
NOVELTY - Organic fertilizer comprises (wt.%): manure (20-40), silkworm dropping (20-40), vegetable cake (15-25), humic acid (5-15), microelements (0.01-0.02) and perlite (5-10).    USE - Organic fertilizer used for promoting growth of dendrobe (claimed).    ADVANTAGE - Organic fertilizer enhances the drought resistance and pest resistance capabilities of dendrobe.
NOVELTY - Preparation of m-fluorophenol involves adding potassium hydroxide, dimethyl sulfoxide and water to reactor, heating to 120-140 degrees C, dripping difluorobenzene, heating to 140-150 degrees C for 4-6 hours, cooling to 26-34 degrees C, evaporating solvent under reduced pressure of 3-6 KPa, adding steam, heating to 140-160 degrees C, adding resultant reaction mixture to ice water, adjusting pH to 3-5, extracting using ether and distilling solvent.    USE - Preparation of m-fluorophenol (claimed).    ADVANTAGE - The method enables preparation of m-fluorophenol with high yield by economical, safe and environmentally-friendly process in short period of time.
NOVELTY - The biogas pool has a container that is attached with a tank housing (1). The tank housing is provided with a support frame (3), and a heating water pipe (2) is wound at an outer side of the tank housing. An end portion of the tank housing is provided with a feeding port (4). The tank housing is provided with a discharging port (7) and a stirring shaft (5) whose end portion is connected with a motor. The stirring shaft is comprised of a hollow shaft and a blade.    USE - Container type biogas pool.    ADVANTAGE - The biogas pool is featured with convenient use, quick mounting, reduced cost and shortened construction period, convenient transportation and reduced carbon accumulation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic internal structural view of the container type biogas pool.    Tank housing (1)    Heating water pipe (2)    Support frame (3)    Feeding port (4)    Stirring shaft (5)    Discharging port (7)
NOVELTY - A Streptomyces sp. strain preserved in the China microorganism strain preservation management committee normal microorganism centre with CGMCC No. 7094, is new.    USE - Streptomyces sp. strain for preventing and treating sludge bulking (claimed).    ADVANTAGE - The strain has reduced production cost, reduced pollution, and is simple to use.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following: (1) a method for cultivating Streptomyces sp. strain, which involves pretreating sweet potato starch wastewater, using aqueous sodium hydroxide or lime to adjust pH of the wastewater to 6.8-8.0, sterilizing at 105-126 degrees C for 10-35 minutes, preparing liquid seed, equipping flask with a good sweet potato starch wastewater pretreatment of Streptomyces inoculated slant, shaking at 25-37 degrees C for 120-200 rpm for 24-36 hours to obtain liquid seed, performing cascade amplification in liquid culture, transferring 50 l the sweet potato starch wastewater to fermenter and inoculating 2-15% liquid seeds at 25-37 degrees C for 15-36 hours under sterile air, inoculating broth into a sweet potato starch wastewater pretreatment equipped with 500 l fermentation tank at 25-37 degrees C for 15-36 hours through sterile air, inoculating the broth equipped pretreated sweet potato starch wastewater in the fermenter at 25-37 degrees C for 15-36 hours through sterile air to obtain broth of Streptomyces, (2) a method for utilizing Streptomyces sp. strain for preventing and treating sludge bulking, which involves adding 5-6% culture broth of Streptomyces with activated sludge wastewater in an aerobic treatment system aeration tank, and mixing, followed by depositing sludge in secondary settling tank for 2-3 days, adding more than 80% sludge to aerobic pool.
NOVELTY - Process for garbage and sewage treatment, involves (a) performing an operation at mesophilic temperatures by reducing withstanding temperature to upper mesophiles to provide pre-acclimating methanogenic organism culture to the reactor conditions, (b) introducing a methanogenic organism culture to the reactor, (c) using specific enzymes at low doses in a given mixture of feedstocks, and (d) using fermentable forms or their oligomers in higher concentrations for stimulating microbial growth and promoting enzyme release, and increasing gas production per feedstock.    USE - The process is useful for garbage and sewage treatment (claimed).    ADVANTAGE - The process requires less time for garbage degradation, is cost-effective to perform, and consumes less power.    DETAILED DESCRIPTION - Process for garbage and sewage treatment through a method able to accelerate the anaerobic digestion output and resulting product, and further allowing use of various feedstock, involves (a) performing an operation at mesophilic temperatures that are also be carried out in a thermophilic system by reducing the withstanding temperature to upper mesophiles to provide the pre-acclimating methanogenic organism culture to the reactor conditions, (b) introducing a methanogenic organism culture to the reactor being possible to increase both the output and the operational speed, (c) using specific enzymes at low doses in a given mixture of feedstocks, where such enzymes are intended to reduce such mixture to similar molecular forms that act as a homogeneous feed source for mutagenesis and other organisms as well when associated products e.g. single sugars, oligosaccharides, fatty acids and their derivatives, and (d) using fermentable forms or their oligomers in higher concentrations for stimulating microbial growth and promoting enzyme release, and increasing gas production per feedstock where the increase is higher than 60% over a non-treated anaerobic digestion.
NOVELTY - This utility new type relates to egg chicken production technology field, one end one, especially a environment-friendly chicken house excrement storage groove, comprising a rectangular excrement storage groove body, the groove body is chicken manure, manure storage groove body and placed above the egg of chicken cage, the excrement groove body set with outlet of manure, manure outlet is set with valve device, bottom surface of middle part wherein the bottom of the excrement storage groove body is arched structure, said arched structure protruding upwards, the arched structure along the excrement storage groove body of long edge direction, is provided with two edge filter ditch, the ditch circle of mutually connected a filter are of a certain width of a the bottom surrounding edge of four sides of the excrement groove body arched structure, seal cover plate on the wall of filter ditch, the utility model is new type not only saves a use of scraper machine egg chicken manure in production, reduces the production cost, but also through the chicken manure groove in natural fermenting, the water content of chicken manure, realize the chicken manure as biological organic fertilizer of the utilizing the water again, so as to reach the aim of energy saving and emission reduction and environment protection.
NOVELTY - This utility new type claims a plant nutrition liquid of one preparation device, the comprising: used for rice, vegetable washing pool, and lower water pipe of vegetable washing pool of washing and sink the lower part of the fermentation tank, used for collecting and storing from the lower water pipe of sewage into the inner, so to form the plant nutrition liquid; and a fermentation tank connected with the bottom of liquid storage tank, for storage by the fermentation tank into a plant nutrition liquid inner thereof; wherein, said fermentation tank entrance set with water inlet pipe, and the water inlet pipe through a tee joint and a lower water pipe and the drain pipe of building, wherein, said water inlet tube set used for regulating water inlet valve of the water amount. This utility new type of preparation device, simple structure, natural ferment for a plant nutrition liquid, preparation cost is low, a valid the municipal sewage disposal quantity and save family plant planting irrigation with water and fertilizing cost.
NOVELTY - Preparation of 7-methoxy-6-(3-morpholin-4-yl-propoxy) quinazolin-4-(3H)-one includes performing cyanation of vanillin, performing nitration and reduction, dissolving in formic acid, adding formate and hydroxylamine hydrochloride, reacting to obtain 3-hydroxy-4-methoxy carbonitrile, dissolving in solvent, adding aqueous potassium nitrate and fuming nitric acid to obtain 5-hydroxy-4-methoxy-2-nitrobenzene nitrile, dissolving in solvent, adding reducing agent, and adding acid and cyclization reagent to obtain 6-hydroxy-7-methoxy-3H-quinazolin-4-one.    USE - Method for preparation of 7-methoxy-6-(3-morpholin-4-yl-propoxy) quinazolin-4-(3H)-one (claimed).    ADVANTAGE - The method is safe, convenient, environmental-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparation of 7-methoxy-6-(3-morpholin-4-yl-propoxy) quinazolin-4-(3H)-one involves performing cyanation of vanillin, performing nitration and reduction, dissolving in formic acid, adding formate and hydroxylamine hydrochloride, reacting to obtain 3-hydroxy-4-methoxy carbonitrile, dissolving in solvent, adding aqueous potassium nitrate and fuming nitric acid to obtain 5-hydroxy-4-methoxy-2-nitrobenzene nitrile, dissolving in solvent, adding reducing agent, adding acid and cyclization reagent to obtain 6-hydroxy-7-methoxy-3H-quinazolin-4-one, dissolving in solvent, adding base and N-(3-chlorophyl)morpholine to obtain 6-hydroxy-7-methoxy-3H- quinazolin-4-one.
NOVELTY - Improving sulfasalazine purification and production efficiency comprises cooling the dispersed sulfasalazine in a crystallization pot to 5-10 degrees C, then filtering the solution via dissolution filter, pressing the material dry using nitrogen gas, removing the material which is not dry, purifying by aqueous acetic acid, passing via dissolution filter, mixing the solid material, directly passing the solid-liquid mixture into purification pot, discharging and transferring.    USE - The method is useful for improving sulfasalazine purification and production efficiency (claimed).    ADVANTAGE - The method is carried out in a closed system; shortens operation time and reduces labor intensity; satisfies GMP requirements; and reduces environment pollution by avoiding prolonged exposure to contaminated material.
NOVELTY - The method involves performing fermentation of biomass in fermenter (12) according to dry fermentation principle. Waste and contamination is passed to percolate tank (18), and portion of contaminated percolate is recycled from percolate tank. The recycled portion of contaminated percolate is directed into hygienization tank (26). The contaminated percolate is sanitized by thermophilic fermentation in hygienization tank at specific temperature for specific days. The sanitized and decontaminated percolate is derived as liquid fertilizer from hygienization tank.    USE - Method for producing liquid fertilizer.    ADVANTAGE - The process control in the percolate tank is thermophilic so that the percolate is sanitized effectively in percolate tank. The percolate tank and hygienization tank used in the process is enabled to effectively and independently perform the sanitizing of percolate in improved manner. The circulation of percolate between the fermenter and percolate tank is enabled to transfer the excess percolate to sanitizing tank whenever excess percolate accumulates. Thus, the surplus percolate that accumulates also sanitized even while biogas is produced in fermenter. The separation between percolate tank and hygienization tank prevents recontamination of sanitized percolate so that the sanitizing of percolate is performed only once.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas facility for performing the process for producing liquid fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biogas facility for performing the process for producing liquid fertilizer.    Fermenter (12)    Percolate tank (18)    Hygienization tank (26)    Storage tank (30)    Valve (32)
NOVELTY - The generator has series of electrode plate (1,2,6) in which each face sides being in parallel. A gap between each of the electrode plates comprises a containment chamber (7) of electrolyte solution. An electrical connection is provided on the electrode plates in the series. The edges of the electrode plates are sealed from contact with the electrolyte solution. The electrical connections on the electrode plates are sealed from contact with the electrolyte solution. A combination of two electrode plates on either side of an electrolyte solution chamber makes one electrolysis cell.    USE - Hydrogen and oxygen (HHO) generator of dry cell type, for internal combustion engines. Uses include but are not limited to motor vehicle, boat, airplane and electrical power generator.    ADVANTAGE - Since the chamber containing electrolyte solution and an electrode plate are added, the cell shares an electrode plate with the next cell in series, or with the next cell and the preceding cell. The electrolysis cell chamber has a lower exit aperture through the sealed side in order to enable electrolyte replenishment flow.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of the HHO generator.    Electrode plates (1,2,6)    Electrolyte solution entry aperture (3)    Oxygen gas exit aperture (5)    Containment chamber (7)    Electrolysis cell (8-10)
NOVELTY - The separation tank (1) has a round cylinder tank that is provided for holding electrolyte solution. An oval cylinder stainless steel tank is large enough to hold the round tank and the space between the tanks is for the circulation of cooling liquid. A valve (11) drains the used solution and liquid out. A permanent magnet (13) creates an electromagnetic field while direct current is passing through the solution. A Z shaped stainless steel plate (15) helps to increase the flow speed of solution thus increases the reaction to produce hydrogen gas when current passes through the solution.    USE - Hydrogen separation tank with liquid cooling system used in electrical engineering and physics field.    ADVANTAGE - The harmful emission is reduced from the engine, by combining hydrogen system to petroleum engines. The electrolysis process for electromagnetic field required constant temperature control to continuously produce hydrogen. The temperature inside the hydrogen separation tank is constantly monitored and the cooling system start once the temperature reaches a given point.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen separation tank inside the cooling tank with the lid connecting to both tanks.    Hydrogen separation tank (1)    Cathode shaft (9)    Valve (11)    Permanent tank (13)    Z shaped stainless steel plate (15)
NOVELTY - Method for processing biomass involves using methane fermentation system containing high concentration of recalcitrant glycoprotein, and adding metal salt containing stable metal ion components in ionic state than iron group metal ion component of bivalent within the system.    USE - The method and apparatus are useful for processing biomass, e.g. coffee powder (all claimed).    ADVANTAGE - The method is simple and convenient to perform and enables to convert waste material into methane gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus, which comprises solubilizing tank comprising processing liquid and coffee powder, where the solubilizing tank solubilize coffee powder using processing liquid under anaerobic condition, methane fermentation tank comprising methane for fermenting solubilized coffee powder and metal salt addition portion.
NOVELTY - Cultivating selenium-enriched mushroom material involves taking 69-78 pts. wt. sawdust, 15-16 pts. wt. wheat bran, 4-8 pts. wt. corn powder, 1-2 pts. wt. gypsum powder, 0.1-3 pts. wt. garlic powder, 0.05-0.5 pts. wt. egg, and 0.1-0.5 pts. wt. Chinese gooseberry, mixing uniformly, adding 55-60 wt.% water, and stirring uniformly, packaging, sterilizing, inoculating and growing.    USE - For cultivating selenium-enriched mushroom material (claimed).    ADVANTAGE - The method greatly enhances antioxidant activity of the mushroom.
NOVELTY - Manufacture of hydrogen molecule-dissolved water involves interacting stabilizer containing saccharide and/or polyphenol, with electrolytically reduced water containing hydrogen molecule. The concentration of hydrogen molecules is 0.8 ppm or more.    USE - Manufacture of hydrogen molecule-dissolved water (claimed).    ADVANTAGE - The concentration of dissolved hydrogen molecule in water is maintained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolytic cell for manufacturing hydrogen molecule-dissolved water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic cell. (Drawing includes non-English language text)    Dissolved hydrogen molecule stabilizer solution chamber (1)    Dissolved hydrogen molecule stabilizer solution inlet port (2)    Dissolved hydrogen molecule stabilizer solution exit (3)    Cathode chamber (4)    Cathode chamber inlet port (5)
NOVELTY - Fertilizer comprises (in wt.%): fly ash from combustion of biomass (40-60), secondary sludge from paper industry (10-30) and gypsum (10-50). The secondary sludge provides lignin, which acts as a chelating agent.    USE - Fertilizer used for improving degraded soil (claimed).    DETAILED DESCRIPTION - (A) performing sludge stabilization by aerobic fermentation sludge bins and stabilizing in a semi-closed place for 15-45 days and periodically turning to maintain humidity 60%;    (B) mixing all components with the stabilized sludge feed uniformly by using a mixer for 1-2 hours to obtain a homogeneous mixture; and    (C) pelletizing the homogeneous mixture by feeding into a pelletizer to obtain final product.
NOVELTY - Manufacture of nitrobenzene compound (I) involves reacting aniline compound (II) in presence of metal salt of nitrous acid and acid, and reacting the resultant product in presence of metal salt of nitrous acid and copper compound. The total usage amount of water during reaction of aniline compound is 1.2-2.2 L with respect to 1 mole aniline compound (II).    USE - Manufacture of nitrobenzene compound used as intermediate for manufacturing organic compound, pharmaceuticals and agrochemicals.    ADVANTAGE - The method is environmentally-friendly, and enables efficient and economically manufacture of nitrobenzene compound with high purity, high yield and reduced generation of waste material, by simple method without using a special reaction apparatus and hydrogen peroxide.    DETAILED DESCRIPTION - Manufacture of nitrobenzene compound of formula (I) involves reacting aniline compound of formula (II) in presence of metal salt of nitrous acid and acid, and reacting the resultant product in presence of metal salt of nitrous acid and copper compound. The total usage amount of water during reaction of aniline compound is 1.2-2.2 L with respect to 1 mole aniline compound (II).    R1=halo;    R2-R4=H, halo or alkyl;and    R5=halo or alkoxycarbonyl.
NOVELTY - Processing paper mill waste water involves separating solid components from the waste water, where the separated gravel ash, plastic metal, and solid waste present in waste water. The obtained waste water devoid of solid particles are then poured directly to the paper mill waste water tank. The garbage that is composed of organic matter is then decomposed aerobically to obtain dung as fertilizer is then placed inside the septic tank. The dung is mixed with acidic solution, and then heated at 800 degrees C for 16 hours to produce biogas.    USE - Method for processing paper mill waste water used for decomposing dioxins found in sewage waste water and for generating marsh gas (claimed) that is utilized in power generation.    ADVANTAGE - The method enables to process paper mill waste water that effectively reduces pollution of environment.
NOVELTY - Preparing a Gossypium hirsutum seed extract, comprises collecting Gossypium hirsutum seed, and naturally drying after washing with water, separating Gossypium hirsutum seed from its pericarp, extracting the pericarp separated seed by a hot bath method and an ethanol dipping method, and freezing and drying the extracted extract.    USE - The method is useful for preparing a Gossypium hirsutum seed extract, which is useful for preparing Gossypium hirsutum seed oil used in a cosmetic composition and a cleaning composition (all claimed). The cosmetic composition is useful for preventing or treating skin aging and moisturizing the skin. Test details are described but no results given.    ADVANTAGE - The Gossypium hirsutum seed oil has antioxidation ability and skin improvement effect, is safe to use, does not cause irritation to human skin, and can be eco-friendly prepared.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparing Gossypium hirsutum seed oil, comprising collecting Gossypium hirsutum seed, and naturally drying after washing with water, separating Gossypium hirsutum seed from its pericarp, and supercritically extracting the treated seed using sulfuric acid at 50-70 degrees C and a pressure of 200-400 bar; (2) Gossypium hirsutum seed extract prepared by the above method; (3) the Gossypium hirsutum seed oil prepared by the above method; and (4) a cosmetic composition or cleaning composition comprising 1-3 wt.% Gossypium hirsutum seed oil of the extract.
NOVELTY - Method (M1) for producing polyhydroxyalkanoate (PHA), involves culturing one or more bacterial strains that are capable of accumulating PHA from pyrolyzed wax in a culture medium comprising pyrolyzed wax obtained from the pyrolysis of polyethylene and optionally a rhamnolipid, and recovering the PHA from the culture medium.    USE - The methods (M1) and (M2) are useful for producing PHA (all claimed).    ADVANTAGE - The methods enable to produce biodegradable PHA from non-biodegradable polyethylene by effective utilization of the pyrolyzed wax produced as by-product during conversion of the PE to biodiesel, as culture substrate for the bacterial accumulation of PHA.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for producing PHA from polyethylene (PE), which involves subjecting the polyethylene to pyrolysis under suitable conditions for producing a liquid diesel fraction and pyrolyzed fraction, and producing PHA from the pyrolyzed fraction by performing the above-mentioned method (M1).
NOVELTY - Preparing amides of N-(1-(S)-(ethoxycarbonyl)-3-phenylpropyl)-L-alanine (A), comprises: (a) reacting N-(-(S)-(ethoxycarbonyl)-3-phenylpropyl)-L-alanine (I) in the presence of an acid with N,N-dimethyl-chloromethyl-iminium chloride, in a suitable organic solvent; and (b) reacting the product obtained in step (a) with amine comprising compounds (B) in the presence of a base in a mixed solvent system of water and a water immiscible solvent.    USE - The process is useful for preparing amides of N-(1-(s)-(ethoxycarbonyl)-3-phenylpropyl)-L-alanine which are useful to produce ramipril, enalapril, quinapril, trandolapril, delapril, or moexipril (all claimed) that are useful to treat hypertension and heart failure. No biological data given.    ADVANTAGE - The process provides higher yields of highly pure compounds (A), in a highly selective, simple, safe, rapid, environmental friendly and cost effective manner.    DETAILED DESCRIPTION - Preparing amides of N-(1-(s)-(ethoxycarbonyl)-3-phenylpropyl)-L-alanine (A) of formulae (IIIa), (IIIb), (IIIc), (IIId), (IIIe) or (IIIf), comprises: (a) reacting N-(-(S)-(ethoxycarbonyl)-3-phenylpropyl)-L-alanine of formula (I) in the presence of an acid with N,N-dimethyl-chloromethyl-iminium chloride, in a suitable organic solvent; and (b) reacting the product obtained in step (a) with amine comprising compounds (B) of formulae (IIa), (IIb), (IIc), (IId), (IIe) or (IIf) in the presence of a base in a mixed solvent system of water and a water immiscible solvent.    R = protecting group.
NOVELTY - Foam aerosol cosmetic composition in a form of water in oil emulsion, comprises: an aqueous phase; a fatty phase; and a fatty acid ester having 12-16C chain as an acid moiety, and hydrophilic-lipophilic balance value of 7.5-10.    USE - The foam aerosol cosmetic composition is useful: as a makeup product including a face makeup product, preferably a foundation, a makeup base or an eyeshadow; and making up keratinous materials including skin of face (all claimed).    ADVANTAGE - The composition: exhibits improved wear property, wash-up property and stability; provides improved emollient and watery feeling due to the high level of aqueous phase; can be prepared in an easier manner; reduces sticky and oily feeling; and forms a fine and stable foam when sprayed from an aerosol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a cosmetic aerosol device for discharging the foam aerosol cosmetic composition in form of water in oil emulsion from an equipment through its outlet, comprising: a base composition comprising the aqueous phase, the fatty phase and the fatty acid ester; and a propellant to expand the base composition, where the base composition and the propellant being conditioned in a same recipient or distinct recipients connected between each other.
NOVELTY - Method includes the application of complex compost, consisting of manure and wastes of agricultural crops, for increase of number and activation of activity of earthworm. Meanwhile the complex compost is brought into the soil to the depth of the top layer. Complex compost in addition includes a waste of chemical industry - phosphogypsum. Wastes of agricultural crops - vegetative residue of sunflower (caps), sugar beet, corn, wastes of grain cleaning, spew of vegetables and fruit, straw of barley, wastes of fodder for of animals, are taken in equal proportions, at the following interrelation of components, %: wastes of agricultural crops - 2-3, phosphogypsum - 5-6, manure of the black cattle - the rest.    USE - Agriculture.    ADVANTAGE - Method allows to improve the soil fertility with simultaneous improvement of physical, chemical and biological properties of soil.1 tbl, 1 ex
NOVELTY - The electrolyzer has a working electrode provided with partitions. The partitions are arranged in a jacket of the working electrode. A set of plate-like anodes is provided with a set of plate-like cathodes.    USE - Electrolyzer for producing hydrogen.
NOVELTY - This utility new type provide one of a high purity moxa extract device, comprising distiller, , a centrifuge, and rectifier, front cooling bucket, pot, rear cooling bucket, filter, a distiller, , a centrifuge, and rectifier, front cooling bucket, pot, rear cooling bucket, filter pipeline connecting in turn, and through DCS control system. This utility new type: set a whole integrated operation, which avoids the middle process of pollution caused by a greatly avoids the raw material saves energy in a loss in operation process, a single control system a whole control, which avoids the conflict in each aspect time, low energy consumption, labour consumption of between a multi-control system, a large, reduces the enterprise cost, operation greatly simplify of, 1 to 3 can ensure normal operation of whole set device, reduces the enterprise manpower resource in aspect of cost.
NOVELTY - This new utility model belongs to solid fermentation area, specifically relates to a kind of one aerobic compost reactor. The reactor main body is a tank body, the tank body top is set with reactor upper cover, is set with stirring shaft in the tank body and central, upper end of stirring shaft through belt pulley and output shaft of stirring motor connected, lower terminal of stirring shaft mounted stirring paddle, stirring shaft top end is set with connected air inlet of main tank body internal of the stirring electric machine and control cabinet connected with the side wall of tank body is set with multiple individual data monitoring port, and covers can open type insulating layer, of reactor upper cover is set with a feeding port, the tank body bottom set with air inlet for future use, extracting port, a discharge port, said main air inlet and air inlet port are connected and for future use. This new utility model can make material uniformly, improving ventilation, material ferment starting, no existing local hypoxia or agglomeration, feedstock is simple, material before treatment to low requirement, the fan can manually control, can online monitor all data and invoke analysis at any time.
NOVELTY - This utility new type claims a one shed groove static organic fertilizer fermentation device, including compost fermentation groove and greenhouse plastic tent, this compost fermenting groove comprise groove bottom, side wall and pipeline, main pipe arranged outside in one side wall, in one end of a timing air blower pipe to a oxygen, this pipe and uniform cloth inner buried in concrete floor of multi-air pipeline, the uniform multi-branch pipe set up in each air pipeline, a branch pipe is set air outlet groove to form air channel, one forming a static aeration system, greenhouse plastic tent bracket fixed in the fermentation groove side wall a, the top of the two end wall and greenhouse side using a transparent plastic film cover, two end wall above a free a coil film, end wall mounted exhaust fan. This organic fertilizer shed groove type static fermentation device investment, fermenting, sterilizing and deodorizing operation completely, without a second pollution, for proliferation and harmless degree high, product quality, production efficiency is high and easy popularization of.
NOVELTY - This utility new type provide the one a kitchen food residue waste degradation, comprising fermentation tank (1), a feeder (2), a feeder (3), oil water separating tank (4), a draught fan (5), a box (6), a shell (7). The practical new using set with stirrer, a discharge wherein the interlayer groove, an air inlet window and pumping hole in fermentation tank, inner interlayer groove is provided with heat conducting oil and electric heat tube, a screw feeder set with oil water output pipe, feeder set with crusher, inner oil water separating tank is set with oil water layer; working time, food garbage crusher crushing, then separating by the oil water mix liquid feeder and a residue, residue is pushed into a fermentation tank, oil water mix liquid entering into oil water separating tank, a residue is stir and mix the fermentation strain in a fermentation tank, inner constant temperature for standing a humic fertilizer, oil water mix liquid after depositing, standing layering inner oil water separating box in a dirty oil and sewage through pipeline of each of a technology solution, the food waste disposer having the deep processing function of degradation.
NOVELTY - Traditional Chinese medicinal composition comprises 4-8 pts. wt. Astragalus, 2-5 pts. wt. motherwort, 2-5 pts. wt. Epimedium, 2-5 pts. wt. Cistanche salsa, 1-2 pts. wt. Angelica, and 1-2 pts. wt. radix glycyrrhizae.    USE - The traditional Chinese medicine composition is useful for increasing chicken egg production and egg quality (claimed), enhancing immunity of chicken, and promoting blood circulation.    ADVANTAGE - The traditional Chinese medicine composition has reduced toxic side effects, does not produce harmful residues in meat and other characteristics of chicken, and can directly provide nutrients for the growth and development of chicken thus increasing egg production and egg quality of the chicken.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the traditional Chinese medicine composition comprising weighing the above raw materials, adding water for impregnation, heating for 2 times, filtering, combining two filtrate, concentrating at 50-60 degrees C to obtain a traditional Chinese medicine liquid under a relative density of 1.1-1.2, adding 90-95% of ethanol to the traditional Chinese medicine liquid, uniformly mixing and then standing overnight, recycling ethanol, repeating the addition of ethanol, recovering the liquid, filtering, refrigerating the filtrate, concentrating the filtrate at 80 degrees C under relative density of 1.35-1.38 to obtain clear paste, adding sugar and dextrin to the clear paste, where a mass ratio of paste, sugar and dextrin is (1-1.5):(3-3.5):(1-2), mixing, granulating, and drying.
NOVELTY - Polymeric film, is claimed. The polymeric film is prepared by cross-linking the polymer with antifouling agent or two-dimensional nano-material, and then freeze-drying.    USE - The polymeric film is useful as a biological antifouling film in biomedical material or ocean engineering material interface (claimed).    ADVANTAGE - The method is simple, economical, environmentally-friendly and does not generate harmful agents.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing polymeric film by freeze-drying method.
NOVELTY - Organic basal fertilizer comprises 25 wt.% sugarcane leaves, 15 wt.% bagasse, 5 wt.% peanut shell powder, 7 wt.% cow dung, 5 wt.% horse dung, 5 wt.% plant ash, 3 wt.% mushroom residue, 3 wt.% soybean meal, 5 wt.% protein sludge, 3 wt.% lees, 3 wt.% vinegar, 10 wt.% biogas pool liquid, 3 wt.% river silt, 7 wt.% water, 0.8 wt.% rice bran and 0.2 wt.% organic fertilizer fermenting powder.    USE - The fertilizer is useful for improving the soil structure, increasing the permeability of soil, and promoting plant growth development.    ADVANTAGE - The method utilizes large amount of raw material sources, is economical, and has production yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the fertilizer, comprising (i) adding sugar cane leaves of 3 cm long into a crusher; (ii) uniformly mixing all the above mentioned raw materials except rice bran and organic fertilizer fermenting powder; (iii) preparing fermenting powder by uniformly mixing the rice bran and organic fertilizer fermenting powder; (iv) paving a layer of mixed material of the step (ii) to a thickness of 20 cm, and spraying the fermenting powder, and paving a layer of fermenting powder of the step (iii) to a thickness of 10 cm, spraying the fermenting powder again, and carrying out staggered stacking to a height of 2.5 m, and adding sugarcane leaves to tightly cover the mixture for 25 days to obtain semi-decomposed substance; and (v) overturning the semi-decomposed substance, and simultaneously crushing large pieces of materials, spraying 9 wt.% water along the edges, regulating humidity, and stacking for 15 days, and packaging, to obtain the final product.
NOVELTY - Device comprises a machine frame (1), a reaction kettle, a motor (3), a gear transmission device (4), a speed reducer (5), and temperature control cabinet (10), where reaction kettle is provided with hammer head paddle type stirrer. The reaction kettle outer wall is provided with electric heating unit. The reaction kettle is provided with top cover, which is set with observation window glass. The reaction kettle is provided with water separator is connected with bottom end of the reaction kettle. The reaction kettle is provided with reaction kettle jacket.    USE - Device used for treating organic waste.    ADVANTAGE - The device reduces the energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device.    Machine frame (1)    Motor (3)    Gear transmission device (4)    Speed reducer (5)    Temperature control cabinet (10)
NOVELTY - A stevia blade rebaudioside A (RA) and stevioside (STV) are extracted by adding stevia blade powder into 48-52% ethanol at volume ratio of 1:18-22, oscillating at room temperature overnight, ultrasonically extracting at 38-42 degrees C for 55-65 minutes, centrifuging at 9000-10000 rpm for 8-12 minutes to obtain supernatant, and filtering in 0.45 mu m organic microporous filter film.    USE - Extraction of stevia blade rebaudioside A and stevioside (claimed).    ADVANTAGE - Extraction process has high efficiency and low pollution and is simple.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the effect of ethanol concentration on extraction efficiency of rebaudioside and stevioside.
NOVELTY - A cervical suppository has hollow double-layer design in which hollow suppository and double-layer suppository characteristics are combined and cotton core bolt design is used.    USE - A cervical suppository (claimed).    ADVANTAGE - Product shortens treatment period, provides good physiological environment, promotes wound healing, maintains clean vagina environment, has no peculiar smell and side effect and simple structure, and is low-cost and stable, and preparation process does not produce pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cervical suppository which involves converting curcuma zedoary and borneol into fine powder of 100 meshes, taking 20 g of semi-mix fatty acid glyceride cut into small blocks with easy melting characteristic, heating in water bath at 70 degrees C until melted to obtain substrate, maintaining temperature at 50 degrees C, uniformly mixing 1 g each of borneol and curcuma zedoary through 100 meshes sieve, adding into mold, placing into unsolidified mold before inserting the same volume, removing after 1 s, naturally cooling to obtain outer layer, taking 20 g mixture of glycerol, glutin, and distilled water at ratio of 60:30:10, heating in water bath at 75 degrees C until melted to mix uniformly, adding 1 g of rhizoma zedoariae, uniformly mixing and adding into mold, cooling to 40 degrees C, adding basic fibroblast growth factor (bFGF), natural cooling to obtain middle layer, rolling medical absorbent into cylindrical shape, pulling wire system, performing hollow double-layer bolt mold extrusion molding, processing drug containing substrate and sequentially injecting into hollow double-layer mold, inserting cotton plug core, and cooling.
NOVELTY - Treatment of alcohol waste mash from sugar refinery comprises taking alcohol waste mash, keeping at 18-45 degrees C, performing aerobic aeration, performing hydrolysis acidification, entering pre-inoculation and biological oxidation pool, adding 3-5 wt.% photosynthetic bacteria and dodecylmaltoside mixture at mass ratio of 1:0.3-0.6, fermenting for 40-48 hours and precipitating to obtain composite fertilizer.    USE - Method for treating alcohol waste mash from sugar refinery (claimed).    ADVANTAGE - The method with low operating cost has biochemical oxygen demand and chemical oxygen demand reduction rate of 60-70% and sulfate and sulfide reduction rate of 70-80%.
NOVELTY - Special fertilizer comprises 10-20 pts. wt. soybean meal, 3-7 pts. wt. potassium humate, 2.3-6 pts. wt. Lactobacillus, 3.1-5.8 pts. wt. ferrous sulfate, 4-8 pts. wt. potassium chloride, 3.2-6.7 pts. wt. EDTA chelated zinc, 3.5-6.9 pts. wt. rape straw charcoal, 3-7 pts. wt. polyvinyl alcohol, 3.2-4.8 pts. wt. sodium selenite, 3.2-4.8 pts. wt. manganese sulfate, 1.2-2.5 pts. wt. inorganic salt, 1.4-5.3 pts. wt. gypsum powder and 0.6-2.8 pts. wt. bagasse.    USE - The special fertilizer is useful for tea (claimed) and improving soil.    ADVANTAGE - The fertilizer increases quality of tea.
NOVELTY - This utility new type claims a one quick composting of manure fermentation device. C design is beautiful and practical, hollow cylinder body, including fermentation, monitoring, ventilation, water collecting and heat preservation filter 5 a, a process temperature and humidity, and gas pressure sense measure, sampling a combine, manure fermentation supply in time of a complete, full-closeness. heat preservation, controllable temperature and pressure, the highest fermentation temperature 55 to 60 degrees C, pressure is 0.02 to 0.03Mpa; according to the sampling, discharging and cleaning, and a sampling tube and discharge scraping harrow and so on auxiliary tool and prevent the material from the fermentation room falls into the design of cloth pneuma room, through a temperature and pressure and so on, with device for livestock excrement, the quick-acting nutrient, bacteria, Escherichia coli and fermentation period to compare, and the effect is better than a temperature and pressure device and fermentation, a temperature and pressure control for normal plastic bucket with the same volume of 12 to 15 days, a temperature and pressure needs 18 days, control for 42 days.
NOVELTY - Extracting aucubin monomer from Eucommia fruit, involves drying the bark of fruit shell to obtain kernel, crushing, degreasing using petroleum ether and extracting the degreased material using alcohol, filtering the extract, concentrating the extract, crystallizing the concentrate, adding acetone, cooling, crystallizing, subjecting the aucubin crude crystal to silicone glue column chromatography, adding ethyl acetate saturated solution and methanol, collecting the eluate, drying the liquid, and freeze-drying to obtain the product.    USE - The method is useful for extracting aucubin monomer from Eucommia fruit (claimed).    ADVANTAGE - The method enables to mass produce aucubin monomer with high purity and less toxicity, consumes less energy, and is highly stable.    DETAILED DESCRIPTION - Method of extracting aucubin monomer from Eucommia fruit, involves drying the bark of fruit shell to obtain kernel, crushing, degreasing using petroleum ether and extracting the degreased material using alcohol, filtering the extract, combining the extracting liquid, concentrating the extract at 40-60 degrees C, crystallizing the concentrate, adding acetone, cooling, crystallizing, subjecting the aucubin crude crystal to silicone glue column chromatography, adding ethyl acetate saturated solution and methanol, collecting the eluate, drying the liquid at 40-60 degrees C, and freeze-drying to obtain the product.
NOVELTY - A gefitinib crystal, is new. The crystal exhibits X-ray diffraction analysis pattern with peaks using Cu-K alpha radiation given in the patent specification.    USE - The gefitinib crystal is used as anticancer agent.    ADVANTAGE - The crystal is prepared by environmentally-friendly and cost-effective method and stable even in form of a solvent-free storage, and has high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the gefitinib crystal.
NOVELTY - Method for performing combustion process in furnace assembly involves combusting fuel mixture of fossil fuel, preferably methane or methanol in a combustion zone of furnace assembly, removing carbon dioxide-containing exhaust gas discharged from combustion process, carrying out methanation process, obtaining methane or methanol, introducing methane or methanol into a storage reservoir, supplying carbonaceous fuel e.g. fossil fuel and waste oil and/or bone meal to the combustion zone, feeding methane or methanol from the reservoir, supplying hydrogen and oxygen and reacting.    USE - Method for performing combustion process in furnace assembly of industrial plant e.g. carbon dioxide-emitting plant (claimed).    ADVANTAGE - The combustion process is carried out by economical process.    DETAILED DESCRIPTION - Method for performing combustion process in furnace assembly involves combusting a fuel mixture of fossil fuel, preferably methane or methanol in a combustion zone of the furnace assembly, removing 60 vol.% or more, preferably 80 vol.% or more, most preferably more than 90 vol.% from carbon dioxide-containing exhaust gas discharged from combustion process of fuel, carrying out methanation process under supply of oxygen and carbon dioxide in a reactor, obtaining methane or methanol, introducing the obtained methane or methanol into a methane or methanol storage reservoir, supplying carbonaceous fuel e.g. fossil fuel and waste oil and/or bone meal to the combustion zone of the furnace assembly, feeding methane or methanol as fuel of combustion zone of furnace assembly from the methane or methanol storage reservoir, supplying hydrogen from a hydrogen storage reservoir and oxygen from an storage oxygen reservoir and reacting. An INDEPENDENT CLAIM is included for industrial plant.
NOVELTY - This utility new type claims a one structure is simple, operation is convenient, work efficiency of high fermenting steam exploded wood fibre straw stack turning machine, comprising a machine body, a bracket, a motor, wherein a bracket and a connecting body, the electric machine set on the lower end machine body, electric machine and the control panel is connected with the main body of inner set with tooth conveying belt, the conveyer belt is obliquely placed, the top end connecting with lower hopper.
NOVELTY - This utility new type claims a one of organic fertilizer raw material pre-processing and fermentation device, a axial line of tube, comprising tube of the column is set with a main shaft, a main shaft set with blade, and a horizontal tube with an acute angle, right end of tube higher than the left end, left end set with discharging tube wherein the tube inner side wall set with liquid spray pipe, liquid pipe set with a spray nozzle, inner tube cooling air channel set with a vertical set, lower end of inner tube side wall set with a heating piece, outside side of tube set with heat preservation layer, a main shaft, a liquid spraying pipe and cooling wind channel and a connecting tube of a seal connecting the inner tube set with aeration device. This utility new type can be for organic fertilizer raw material pre-processing process and fermenting for a raw material pre-processing can be valid decomposition is not easy to fermentation decomposition of nutrition component, valid control ferment temperature and oxygen concentration to ensure a good fermentation condition, increase use rate and fertility of a organic fertilizer raw material.
NOVELTY - A multi-one green energy and emission reduction machine, the a integrated structure, comprising electrolytic groove, 1-8 a plate electrode, a water inlet, a micro-computer, hydrogen oxygen outlet, wherein a plate and a micro-computer is connected with each electrode plate by a 2-18 piece a piece compose. This utility new type provide one of a multi-green energy and emission reduction machine, which not only electrolytic efficiency is high, the power consumption amount, hydrogen oxygen reduction rate low, but also according to power requirement of internal combustion engine adjusting a plate number so as to satisfy a corresponding hydrogen oxygen.
NOVELTY - Antioxidant facial mask comprises (in pts.wt.): vinegar (15-25), traditionalChinese medicinal ingredients (10-20), far Infrared powder (5-15), humectant (3-7), and deionized water (20-30). The traditional Chinese medicinal ingredients comprise (in pts.wt.): jasmine flower (5-10), Astragalus membranaceus (3-5), gingko leaves (5-8), ginseng (1-3), Cassia seed (2-6), kudzu root (5-9), giant knotweed (2-7), and Erigeron breviscapus (3-7).    USE - Antioxidant facial mask.    ADVANTAGE - The antioxidant facial mask prepared effectively protects the skin from ultraviolet radiation that ultimately causes skin aging in an eco-friendly manner.
NOVELTY - Treatment of aquaculture wastewater involves mixing 10 pts. wt. Bacillus pumilus, 2 pts. wt. Sphingomonas and 1 pt. wt. Rhodococcus to obtain bacteria mixture, adding sawdust, low-temperature drying to obtain microbial inoculum, taking aquaculture wastewater, standing, adjusting pH value to 7-8, dosing 10 g microbial inoculum, transferring to plate and frame filter press, discharging liquid, collecting fermentation products, taking dried corn stalks, grinding, adding humic acid and water, stirring, adding fermentation product and granulating to obtain fertilizer.    USE - Method for treating aquaculture wastewater (claimed).    ADVANTAGE - The method is environment-friendly.    DETAILED DESCRIPTION - Treatment of aquaculture wastewater comprises mixing 10 pts. wt. Bacillus pumilus, 8 pts. wt. Thiobacillus denitrificans, 6 pts. wt. Alcaligenes faecalis, 5 pts. wt. Pseudomonas aeruginosa, 2 pts. wt. Bacillus cereus, 2 pts. wt. Sphingomonas and 1 pt. wt. Rhodococcus to obtain bacteria mixture, mixing bacteria mixture and sawdust at mass ratio of 1:1 and low-temperature drying at 4 degrees C until moisture content is 8% to obtain microbial inoculum; taking aquaculture wastewater, passing through grille and mud-water separator, removing solids, transferring to sedimentation tank, standing for 6 hours, transferring to purifying tank, adjusting pH value to 7-8, dosing microbial inoculum at 10 g/m3 wastewater for 3 days, transferring to plate and frame filter press, discharging liquid and collecting microorganisms and fermentation products; and taking dried corn stalks, grinding, feeding to fermenter, adding humic acid, peat, zeolite powder and water, stirring at 1000 revolutions/minute for 15 minutes, standing for 7 days, adding 1/10 times fermentation product, low-temperature drying and granulating to obtain fertilizer.
NOVELTY - A garbage fertilizer-making device comprises and rotating shaft equipped with blade, stirring tank body, pressurizing tank body, and crushing tank body, where tank bodies have valves (3,4, 5, 6). The stirring tank body is connected with feeding opening (2). The crushing tank body is connected with discharging opening.    USE - Garbage fertilizer-making device.    ADVANTAGE - The device quickly ferments organic garbage, particularly human and animal feces. It has simple structure and convenient usage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of garbage fertilizer-making device.    Feeding opening (2)    Valves (3,4, 5, 6)    Belt wheel (10)    Stirring shaft (11)    Transmission chain (12)
NOVELTY - A garbage aerobic fermentation system comprises a fermentation tank (1), a vent pipe, and a cover film (3). The system further comprises a control device which controls the microbial activity at predetermined level according to the oxygen concentration and temperature control air flow of the fermentation tank and ventilation time of the vent pipe.    USE - Garbage aerobic fermentation system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for household garbage processing method comprising:    (A) primarily sorting of garbage, and crushing;    (B) conveying organic and inorganic compounds in a semi-wet disintegrator, and crushing to obtain the organic compound;    (C) adding the mushroom residue, chicken manure, straw, activated carbon and bentonite into the organic compound, and mixing; and    (D) carrying out garbage aerobic fermentation of the nutrition soil.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the garbage aerobic fermentation system.    Fermentation tank (1)    Cover film (3)    Liquid (4)    Pressure sensors (5, 6)
NOVELTY - An organic fertilizer reaction device comprises a reaction tank (9) set with stir shaft (17) having stir blade (10). A sidewall of the lower part of the tank is set with a through opening. A top outside side plate of the reaction tank is set with a vent hole (5). The middle upper part of the reaction tank is set with a conveying pipeline having an inner auger (3) and a feeding port (8). A lower part bottom surface of conveying pipeline (2) is set with a water outlet. An upper part of conveying pipeline is set with a blank tank.    USE - Organic fertilizer reaction device.    ADVANTAGE - The device shortens the reaction time of organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the organic fertilizer reaction device.    Conveying pipeline (2)    Inner auger (3)    Vent hole (5)    Feeding port (8)    Reaction tank (9)    Stir blade (10)    Stir shaft (17)
NOVELTY - Preparing aspirin eugenol ester comprises adding aspirin, thionyl chloride and N,N-dimethylformamide in flask, heating flask, adding sodium hydroxide and acid gas to mixture and then reacting, distilling off unreacted thionyl chloride, diluting acid chloride in organic solvent, adding eugenol, tetrabutylammonium bromide and sodium hydroxide solution in flask, adding diluted acid chloride in flask, adding aqueous sodium hydroxide solution to mixture, filtering solution to obtain white solid, and crystallizing using methanol to obtain white crystalline solid of aspirin eugenol ester.    USE - The method is useful for preparing aspirin eugenol ester (claimed).    ADVANTAGE - The method is capable of easily preparing the aspirin eugenol ester with improved pharmacological effects and yield, and reduced side effects in an eco-friendly manner.    DETAILED DESCRIPTION - Preparing aspirin eugenol ester comprises adding aspirin, thionyl chloride and N,N-dimethylformamide in a round bottom flask equipped with an electromagnetic stirrer, heating the flask at 70 degrees C for 2 hours, adding aqueous sodium hydroxide and acid gas to the mixture and then reacting under reduced pressure of -0.08 MPa, distilling off the unreacted thionyl chloride, diluting acid chloride in an organic solvent including tetrahydrofuran, adding eugenol, and 5% of phase transfer catalyst including tetrabutylammonium bromide and sodium hydroxide solution in the flask, dropwisely adding the above diluted acid chloride in the flask and then stirring, adding aqueous sodium hydroxide solution to the mixture, maintaining pH value of the mixture to 10 to obtain a basic solution, filtering the solution to obtain a white solid, washing the white solid with distilled water and an aqueous solution of sodium hydroxide, and crystallizing the obtained product using methanol to obtain a white crystalline solid of aspirin eugenol ester.
NOVELTY - Rapid decomposing of rice-wheat straw comprises cutting rice-wheat straw, mixing with rice bran, fermenting and gradually decaying naturally.    USE - Method for rapid decomposing of rice-wheat straw (claimed).    ADVANTAGE - The ecological and environment-friendly method uses rice bran which has low cost and is easy to obtain in rural area. It does not add additives, and has convenient operation.
NOVELTY - A microorganism microbial inoculum comprises Ensifer adhaerens, Acinetobacter calcoaceticus and Flavobacterium chungangense.    USE - Microorganism microbial inoculum used for preparing composite fertilizer (claimed) of cucumber.    ADVANTAGE - The fertilizer has rich nutrition to improve quality of cucumber. It increases and yield to 10-60% and soluble sugar to 10-20%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) composite fertilizer comprising microorganism microbial inoculum, humic acid and inorganic fertilizer; and    (2) preparation of composite fertilizer comprising absorbing microorganism microbial inoculum into humic acid and adding inorganic fertilizer.
NOVELTY - Preparing the domestic traditional Chinese fertilizer paste comprises weighing 5-15 pts. wt. turtle shells, 20-30 pts. wt. seaweed ash, 10-15 pts. wt. radix aconiti agrestis, 15-20 pts. wt. radix bupleuri, 10-15 pts. wt. dried ginger, and 4-11 pts. wt. Gentiana, mixing the raw materials and then grinding to prepare powder, adding 80-100 pts. wt. bean dregs and 40-60 pts. wt. glycerol monostearate in a stirrer, then adding the powder to the mixture and then heating until the powder is completely dissolved, and then fermenting for 10-15 days.    USE - The method is useful for preparing domestic traditional Chinese fertilizer paste (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the domestic traditional Chinese fertilizer paste prepared by the above method.
NOVELTY - A special fertilizer comprises 6-10 pts. wt. potassium chloride, 5-9 pts. wt. urea, 1.5-6.8 pts. wt. magnesium sulfate, 3.5-8 pts. wt. humic acid, 1.3-4.2 pts. wt. borax, 2.2-3.6 pts. wt. nano carbon, 7-12 pts. wt. organic fertilizer, 1.5-4 pts. wt. slow release agent, 1.1-2.06 pts. wt. zinc sulfate, 1.2-2.3 pts. wt. biological microbial inoculum, and 1-3 pts. wt. potassium nitrate.    USE - Special fertilizer used for corn (claimed).    ADVANTAGE - The fertilizer prolongs fertilizer effect, improves soil, and increases disease resistance.
NOVELTY - Fertilizer capable of improving soil comprises 6-14 pts. wt. chicken manure and pig manure, 5-9 pts. wt. clover, 3-6 pts. wt. silt, 1.5-4 pts. wt. lees, 3-8 pts. wt. soybean, 2.2-5 pts. wt. diammonium phosphate, 3-5 pts. wt. Bacillus mucilaginosus, 3.2-6.8 pts. wt. straw carbon powder, 0.3-0.8 pts. wt. borax, 2.5-6 pts. wt. ammonium molybdate, 3.5-6 pts. wt. fruit residue, 1-3 pts. wt. saw dust.    USE - As fertilizer (claimed).    ADVANTAGE - The fertilizer is repairs damage to the soil, improves soil quality, prevent long-term use of pesticides, improves fertilizer and soil compaction caused by fertility decline, and has no soil pollution.    DETAILED DESCRIPTION - Fertilizer capable of improving soil comprises 6-14 pts. wt., preferably 10 pts. wt. chicken manure and pig manure, 5-9 pts. wt., preferably 7 pts. wt. clover, 3-6 pts. wt., preferably 4.5 pts. wt. silt, 1.5-4 pts. wt., preferably 2.9 pts. wt. lees, 3-8 pts. wt., preferably 6 pts. wt. soybean, 2.2-5 pts. wt., preferably 3.8 pts. wt. diammonium phosphate, 3-5 pts. wt., preferably 4 pts. wt. Bacillus mucilaginosus, 3.2-6.8 pts. wt., preferably 5.1 pts. wt. straw carbon powder, 0.3-0.8 pts. wt., preferably 0.6 pts. wt. borax, 2.5-6 pts. wt., preferably 4.3 pts. wt. ammonium molybdate, 3.5-6 pts., preferably 4.8 pts. wt. wt. fruit residue, 1-3 pts. wt., preferably 2 pts. wt. saw dust.
NOVELTY - Soybean bio-fertilizer comprises 3-7 pts. wt. potassium chloride, 0.6-1.3 pts. wt. manganese sulfate, 1.5-3.4 pts. wt. chicken manure, 0.5-0.8 pts. wt. Bacillus mucilaginosus, 4-8 pts. wt. nitrogen fertilizer, 2.5-7 pts. wt. phosphate fertilizer, 3.4-6.9 pts. wt. pig manure, 4.5-9.2 pts. wt. medical stone, 2.4-6.5 pts. wt. yellow mealworm powder, 0.6-1.7 pts. wt. microelements, 1.3-3.5 pts. wt. citric acid, 2.2-3.6 pts. wt. carboxymethyl cellulose, 3.1-5.6 pts. wt. potassium sulfate, and 0.2-0.6 pts. wt. effective microorganisms (EM) inoculum.    USE - Used as soybean bio-fertilizer.    ADVANTAGE - The bio-fertilizer: does not pollute the environment and destroy the soil structure; promotes plant nutrient absorption; and is pollution-free.
NOVELTY - Multi-effect biological fertilizer comprises 6-11 pts. wt. potassium chloride, 4-9 pts. wt. diammonium phosphate, 1-3 pts. wt. copper sulfate, 2.5-6 pts. wt. celestite powder, 3.5 pts. wt. earthworm manure handicraft, 1.2-3 pts. wt. potato straw, 2.3-4.8 pts. wt. gypsum powder, 3.5-8 pts. wt. pig manure, 1.3-3.2 pts. wt. wheat bran, 0.6-1.3 pts. wt. egg shell powder, 1.3-2.8 pts. wt. ferrous sulfate, 1.5-4 pts. wt. EM microbial inoculum, 1.1-2.04 pts. wt. zinc oxide or 1.5-3.4 pts. wt. lactobacillus.    USE - As multi-effect biological fertilizer (claimed).    ADVANTAGE - The multi-effect biological fertilizer provide crop nutrition, can improve soil, soil for a repair, does not pollute soil and water.    DETAILED DESCRIPTION - Multi-effect biological fertilizer comprises 6-11 pts. wt., preferably 9 pts. wt. potassium chloride, 4-9 pts. wt., preferably 7 pts. wt. diammonium phosphate, 1-3 pts. wt., preferably 2 pts. wt. copper sulfate, 2.5-6 pts. wt., preferably 4.2 pts. wt. celestite powder, 3.5 pts. wt., preferably 4 pts. wt. earthworm manure handicraft, 1.2-3 pts. wt., preferably 2.1 pts. wt. potato straw, 2.3-4.8 pts. wt., preferably 3.6 pts. wt. gypsum powder, 3.5-8 pts. wt., preferably 5.4 pts. wt. pig manure, 1.3-3.2 pts. wt., preferably 2.7 pts. wt. wheat bran, 0.6-1.3 pts. wt., preferably 0.9 pts. wt. egg shell powder, 1.3-2.8 pts. wt., preferably 2 pts. wt. ferrous sulfate, 1.5-4 pts. wt., preferably 3.1 pts. wt. EM microbial inoculum, 1.1-2.04 pts. wt., preferably 1.7 pts. wt. zinc oxide or 1.5-3.4 pts. wt., preferably 2.8 pts. wt. lactobacillus.
NOVELTY - High-efficient fertilizer comprises 3-8 pts. powdered rock phosphate, 3.5-6 pts. corn straw, 3.4-7.5 pts. boric acid, 3.5-7.4 pts. amino acid, 3.5-7.2 pts. royal jelly, 3.2-6.8 pts. balsam pear root, 4.2-7.6 pts. ammonium dihydrogen phosphate, 1.2-2.3 pts. Bacillus subtilis microbial inoculum, 1.3-3.7 pts. Phellodendron, 6-10 pts. peat, 2-4 pts. humic acid, and 8-13 pts. urea.    USE - Used as a high-efficient fertilizer.    ADVANTAGE - The fertilizer increases soil absorption rate, prevents soil compaction, loosens the soil and increases soil fertility.
NOVELTY - An aspirin in crystal form is new. The aspirin in crystal form exhibits an X-Ray powder diffraction pattern with peaks given in the specification.    USE - Aspirin in crystal form used as antipyretic, analgesic, and antiinflammatory drug and for treating cardiovascular and cerebrovascular diseases (claimed).    ADVANTAGE - The aspirin in crystal form takes effect after 1-2 hours and has 1-4 hours efficacy rate. The method is simple, environment-friendly, and easy. The aspirin has fast in vitro dissolution test, quick effect, high efficacy, and long-lasting effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of aspirin in crystal form.
NOVELTY - Improved method for producing 3-(2,2,2-trimethylhydrazinium)propionate methylsulfate (A), comprises (i) using intermediates 3-(2,2-dimethylhydrazino)propionate and methylating agent (dimethyl sulfate), separating and purifying the reaction medium using a solvent or a solution of sodium hydroxide or potassium hydroxide in ethanol, dimethylformamide, potassium carbonate solution, methylene chloride, acetone, potassium carbonate solution, glycerol, ethylene glycol, toluene, potassium hydroxide solution, carbon tetrachloride-sodium ethoxide solution and ethylene glycol-sodium solution.    USE - (A) is useful as meldonium intermediate for cardiac protection.    ADVANTAGE - (A): is easy to absorb. The method: is carried out in a rapid, simple, and environmental friendly manner for producing high yield and high stability product; does not require recrystallization, centrifugal separation and complex process steps of drying, and thus it is carried out in a cost efficient manner.    DETAILED DESCRIPTION - Improved method for producing 3-(2,2,2-trimethylhydrazinium)propionate methylsulfate, comprises (i) using intermediates 3-(2,2-dimethylhydrazino)propionate and methylating agent (dimethyl sulfate), separating and purifying the reaction medium using a solvent or a solution of sodium hydroxide or potassium hydroxide in ethanol, dimethylformamide, potassium carbonate solution, methylene chloride, acetone, potassium carbonate solution, glycerol, ethylene glycol, toluene, potassium hydroxide solution, carbon tetrachloride-sodium ethoxide solution, and ethylene glycol-sodium solution. The molar ratio of excess methyl acrylate and 1,1-dimethyl-hydrazine is 1-50%. The molar ratio of 3-(2,2-dimethylhydrazino)propionate, dimethyl sulfate and alkaline solution or solvent is 1:1.2:1-3. The mixing ratio of the organic solvent to alkali solution is 1-3:0-2. The alkali concentration is 1-35%.
NOVELTY - Preparation of diazidoglyoxime involves dissolving glyoxime in organic solvent at room temperature, cooling obtained glyoxime solution to 10 degrees C or less, adding N-halogenated succinimide, reacting at room temperature, reducing temperature to less than 10 degrees C, then adding azide reagent, reacting, adding reaction mixture to water, leaving still, filtering and naturally drying. The molar ratio of reaction product and azide reagent is 1:2-3:1.5-3.    USE - Preparation of diazidoglyoxime (claimed).    ADVANTAGE - The method enables simple and economical preparation of diazidoglyoxime with yield of 80-90% by safe and environmentally-friendly process.
NOVELTY - An allicin is extracted by soaking garlic into water for 30 minutes, peeling, removing foreign matters and rotten garlic, ultrasonically washing for 5-10 minutes, grinding washed garlic into paste, baking into oven at controlled temperature of 60-65 degrees C for 6-8 hours, pulverizing into powder using crusher, screening into 80-100 meshes sieve, adding 10-20 g cellulase and 100-200 g sodium fatty acid, hydrolyzing, adding 25-35 mass% petroleum ether solution, soaking for 10-12 hours, extracting for 3-6 hours, separating upper layer of extracting liquid in other Soxhlet extractor, and concentrating.    USE - Extraction of allicin (claimed).    ADVANTAGE - Process is simple and saves energy consumption.
NOVELTY - Preparing huperzine A intermediate, comprises substituting 3-bromo-6-methoxy-2-methylpyridine with N- bromosuccinimide to obtain a substituted product, and reacting the substituted product with methyl acetoacetate and cuprous iodide for ring closure to obtain 2-methoxy-6-hydroxy-7,8-dihydro-5-quinoline carboxylate.    USE - The method is useful for preparing huperzine A intermediate.    ADVANTAGE - The method: is carried out in a cost efficient and environmental friendly manner for producing good quality and high yield reaction product; is carried out under mild reaction conditions to ensure the safety of the operator; and comprises simple refining process.
NOVELTY - Converting configuration of voriconazole, is claimed.    USE - The method is useful for converting configuration of voriconazole (claimed).    ADVANTAGE - The method is capable of converting configuration of voriconazole with high yield of 35% and reduced cost and environmental pollution.
NOVELTY - Synthesizing huperzine A intermediate comprises adding N,N-dimethylformamide, alpha -dimethyl acetal and substituted carbonyl group to 1,4-hexanedione as a raw material, uniformly mixing, performing substitution reaction to obtain a mixed product, adding methyl cyanoacetate to the mixed product, carrying out ring closure reaction, performing cyclization reaction, and carrying out decarboxylation reaction.    USE - The method is useful for synthesizing huperzine A intermediate (claimed).    ADVANTAGE - The method is capable of simply and conveniently synthesizing huperzine A intermediate with high quality and yield under mild reaction conditions, and reduced cost and environmental pollution.
NOVELTY - High purity triisopropylsilyl acrylate is prepared by mixing triisopropylsilyloxyphenyl alcohol, solvent, and acid binding agent, according to mole ratio of 1 mol:350-450 ml:1.1-1.4 mol, adding phenothiazine or copper acetate, in which mass of phenothiazine or copper acetate in triisopropylsilyloxyphenyl alcohol is 0.02-0.04 mass%, adding dropwise alkenyl acid chloride at 10-80 degrees C, in which ratio of acryloyl chloride with triisopropyl silanol is 1 mol:1-1.2 mol, completing dropwise addition, filtering, reacting for 2 hours after filtration, and distilling liquid phase.    USE - Preparation of high purity triisopropylsilyl acrylate (claimed) used in antifouling paints for ship industry.    ADVANTAGE - The preparation process is simple and safe, and has high yield. The high purity triisopropylsilyl silicon acrylate has low toxicity, low pollution, has slowly replaced toxic tin-containing antifouling paints, has good strength and excellent toughness.
NOVELTY - Preparation of 3-carbonyl-4-aza-5-androstene-17( beta ) derivative (I) involves suspending 3-((3aS,6R)-3a,6-dimethyl-7-oxo-dodecahydro-cyclopenta(a)naphthalen-6-yl)-propionic acid-type compound (II) in an aqueous solution of ammonium acetate, carrying out ring closure reaction, cooling, adjusting pH using ammonia, filtering, drying the filter cake and washing.    USE - Preparation of 3-carbonyl-4-aza-5-androstene-17( beta ) derivative (claimed).    ADVANTAGE - The method efficiently and economically provides 3-carbonyl-4-aza-5-androstene-17( beta ) derivative having high purity of more than 99%, with high yield without affecting the environment, under mild reaction condition without using organic solvent and special equipment.    DETAILED DESCRIPTION - Preparation of 3-carbonyl-4-aza-5-androstene-17( beta ) derivative of formula (I) involves suspending 3-((3aS,6R)-3a,6-dimethyl-7-oxo-dodecahydro-cyclopenta(a)naphthalen-6-yl)-propionic acid-type compound of formula (II) in an aqueous solution of ammonium acetate, carrying out ring closure reaction, cooling, adjusting pH using aqueous ammonia, filtering, drying the filter cake and washing.    R=carbonyl, carboxylic acid group, carboxylate, amido, acetyl, hydroxy, hydrocarbyl, ether group or chloro.
NOVELTY - Chicken manure degradation involves taking fresh chicken manure. The chicken manure is added with distilled water. The mixture is stirred. The obtained manure liquid is kept in a bottle. The obtained bottle is shaked with a rotating speed of 40-60 rotations per minute. The obtained product is sterilized and then cultured at 28-32 degrees C for 65-75 hours using heterotrophic microalgae. The product is inoculated for 180-220 hours to obtain desired product.    USE - Method for degrading chicken manure (claimed).    ADVANTAGE - The method enables to degrade chicken manure with cost-effective and efficient manner.
NOVELTY - Marsh gas fermenting initiator comprises pond sludge, wheat straw, animal excrement, ammonium bicarbonate, and succinic acid producing strain including Bacteroides, Butyrivibrio fibrisolvens, Bacillus subtilis, microzyme and Sarcina.    USE - Marsh gas fermenting initiator.    ADVANTAGE - The marsh gas fermenting initiator can greatly shorten starting time and increase gas production and gas production speed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the marsh gas fermenting initiator comprising taking wheat straw and then crushing, adding pond sludge and animal excrement to the crushed wheat straw, uniformly mixing, adding succinic acid producing strain to the mixture, fermenting the mixture for 36 hours, adding ammonium bicarbonate to the fermented mixture, and stirring.
NOVELTY - Preparing microemulsion involves utilizing (in wt.%): bromoxynil (7-9), dimethyl formamide (10-12), 2-methyl-4-chlorophenoxyacetic acid (5-7), diethyl ether (10-12), fatty alcohol sodium sulfate (6) and balanced amount of water. Dimethyl formamide and bromoxynil are stirred in a tank at normal temperature for 0.2-0.4 hours. Diethyl ether, 2-methyl-4-chlorophenoxyacetic acid, fatty alcohol sodium sulfate and water are added into reaction tank. The obtained reaction mixture is stirred for 1-2 hours to obtain microemulsion.    USE - Method for preparing microemulsion (claimed) used for controlling broad-leaf weeds such as Polygonum, quinoa, amaranth, Silene, Solanum nigrum, cocklebur, Lithospermum arvense, Salsola, bindweed and wild buckwheat.    ADVANTAGE - The method enables to prepare high dispersible microemulsion in simple and eco-friendly manner by requiring mild reaction conditions.
NOVELTY - Regenerating paracetamol from pharmaceutical waste comprises adding raw material comprising activated carbon to the pharmaceutical waste to remove impurities, microwave heating the pharmaceutical waste at 145-175 degrees C and a power of 0-10 kW for 8-10 minutes, and drying the hot product at 105-115 degrees C for 24-48 hours and then cooling.    USE - The method is useful for regenerating paracetamol from pharmaceutical waste (claimed).    ADVANTAGE - The method is capable of easily regenerating the paracetamol from pharmaceutical waste with a pore volume of 0.95-1.10 ml/g, yield of 90%, and polar surface area of 1000 m2/g in an energy-efficient and environmentally-friendly manner.
NOVELTY - This utility new type relates to a one device, especially relates to a rural domestic waste compost device one. Wherein the valve and a condensing tower, condensing tower and an exhaust fan, the exhaust fan and the pneuma pipeline is connected with a gas inlet pipeline with an air inlet, a household garbage pool with a garbage inlet, air window, ventilation hole, compost outlet, one end domestic garbage pool and garbage percolate pipeline of the other end pipeline of landfill leachate into in deposition pool, deposition pool in a filter screen, one end and the condensing tower and a pipeline, and the other end extends in deposition pool. Because using said technology scheme, this utility new type has the advantages and positive effects of is a fermentation period short, low investment, operation and management of, structure is simple, economical and practical.
NOVELTY - This utility new type provide the a one in-situ repairing groundwater nitrate pollution of microorganism fuel cell, comprising an anode room, a cathode room, cathode room located on two side of anion exchange film and outside a system, a anode room set with water inlet pipe, water outlet pipe and discharge pipe, in the anode room set with biological anode, a anode attached biological anaerobic power generating microorganism, an anode room is filled with the anode liquid, and the anode room a efficient anaerobic digestion sludge, a cathode room set with discharge pipe, in the cathode room set with biological cathode, a cathode attached electroactive biological denitrifying microorganism, a cathode room is filled with cathode liquid and the cathode room a denitrifying sludge, outside a system including a outside, lead and electric signal collecting a record. This utility new type at the same time with an organic waste water treatment, biological power generating and groundwater nitrate pollution in-situ repairing triple function to avoid in restoring heavy saline land in situ for groundwater cause organic matter, microorganism such as a secondary pollution problem, and this device structure is compact, operation cost is low, economical and efficient.
NOVELTY - Preparation of environmental-friendly plant matrix involves collecting branches and leaves, crushing to 0.6-0.8 cm, adding 4-5 kg chicken manure and/or dry dairy manure, and 40-50 kg calcium superphosphate, adding composite strain, stirring, adding 50-60 wt.% water, performing primary fermentation at 60 degrees C, performing secondary fermentation, adjusting carbon/nitrogen ratio to 20-25, adding water, drying and packaging.    USE - Method for preparing environmental-friendly plant matrix (claimed).    ADVANTAGE - The method is suitable for flower, vegetable or nursery stock and ecological restoration.
NOVELTY - Ecological environmentally friendly biological organic fertilizer industrial production line comprises a plant crushing device, an automated screening feeding device, at least one set of feeding device, raw material premixing device, strain auxiliary material feeding device, a fertilizer manufacturing device, an online conveying device, at least one fermentation reaction tank, a pipeline type online drying device and online fertilizer homogenization device.    USE - Used as an ecological environmentally friendly biological organic fertilizer industrial production line.    ADVANTAGE - The production line produces the organic fertilizer in sealed condition without noise, smell, matter discharge, sewage, emissions, vibration and heat.    DETAILED DESCRIPTION - Ecological environmentally friendly biological organic fertilizer industrial production line comprises a plant crushing device, an automated screening feeding device, at least one set of feeding device, raw material premixing device, strain auxiliary material feeding device, a fertilizer manufacturing device, an online conveying device, at least one fermentation reaction tank, a pipeline type online drying device and online fertilizer homogenization device. The plant crushing device, automated screening feeding device, at least one set of feeding device, premixing device, fertilizer manufacturing device, online conveying device, at least one fermentation reaction tank, pipeline type online drying device and online fertilizer homogenization device are sequentially connected. The strain auxiliary material feeding device is connected to the fertilizer manufacturing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the ecological environmentally friendly biological organic fertilizer industrial production line.
NOVELTY - This utility new type claims a straw compost spiral stir one type CO2 a device, vertical cylinder set with a reaction container, power output device, rotating drive mechanism and the fan. A reaction container comprising an upper cover plate, cylinder wall and the porous lower bottom plate, upper part of reaction container set with feeding port with the pneuma hole, the lower reaction container set with a discharging port, a porous lower bottom plate of upper plate surface set with multi-used for ventilation and a drop of water through hole, a porous lower bottom plate is further set with a water collecting container. Use time, the straw and a corresponding corrosion agent into a reaction container a stir and ferment, to get carbon dioxide gas or a conversion is a peripheral gas of carbon dioxide, safe and reliable, a. the inner outer agricultural greenhouse or shed, provide sufficient photosynthesis of crops CO2 nutrient, promote plant growing. Inner reaction container through a differential gear and so on, the stir device of revolution at the same time rotating, turning, and valid counteracts the straw compost produce at a time of starting torque.
NOVELTY - This utility new type claims a new-type one in rural marsh gas pool with biogas residue liquid extractor, mainly by a cap opening, and inner screw thread, connecting steel wire and sealing plug, filter, an overflow pipe, a fixing plate, a observation window, detention room, a pressing block, a check valve, a feeding pipe, soft pipe and drawing pipe of the said upper cap through inner screw thread of the upper part set with a detention room; the sealing plug through a steel wire set on the overflow pipe of the left side of the filter set on upper part of feeding pipe, a fixed plate set with a stay room of; said observation window set on the front face of a retention room, the pressure block set on the upper surface of the check valve, a soft pipe set with a upper part of the drawing. Through filter set and transverse observation window, which is good for increase filter efficiency to prevent the feeding pipe blocking, increase real time observation property and use life.
NOVELTY - Carrot special fertilizer comprises 54.5-68% organic fertilizer, 0.8-2% organic fungus, 1-1.5% tea, 0.2-2% brown sugar, 17-24% phosphate fertilizer, and 13-16% bagasse.    USE - As carrot special fertilizer (claimed).    ADVANTAGE - The carrot special fertilizer increases a carrot growing rate, pest, increases yield carrot, and fertilizer manufacturing method is simple, and it is convenient to popularize.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing Carrot special fertilizer involving putting brown sugar at 100 kg in water, then orderly putting tea cake, phosphate fertilizer, bagasse and organic strain, and stir uniform, activated strain culture: stir uniform rear, putting into a steam-cured pump, taking activated strain of culture for 24 hours, obtain a water activity, and according to each ton of organic fertilizer, adding water ratio, uniform spraying, stirring, turning fermentation: after 48 hours, time temperature reaches 60-68 degrees C, and turning process.
NOVELTY - Organic fertilizer comprises 40-70 wt.% of blue-green algae powder, 10-25 wt.% of nitrogen, 5-20 wt.% of phosphorus pentoxide and 5-15 wt.% of potassium oxide.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer can be simply prepared without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the organic fertilizer, comprising (a) collecting blue-green algae with 8-10% of water and then filtering to obtain algae slurry and then concentrating, and drying the algae mud and then crushing into 150-200 meshes powder, uniformly mixing the algae powder with nitrogen, phosphorus pentoxide and potassium oxide and then stirring and granulating.
NOVELTY - A vegetable seedling matrix comprises 15-20 wt.% vermiculite, 15-20 wt.% slag ash, 10-15 wt.% mushroom residue, 25-35 wt.% fermented cow dung, 20-25 wt.% fermented chicken manure, and 0.1-0.3 wt.% nitrogen-phosphorus-potassium composite fertilizer.    USE - Vegetable seedling matrix.    ADVANTAGE - The method is rich in nutrients, has low cost, and reduces cow dung and chicken manure pollution to the environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) production of fermented cow dung comprising piling fresh cow dung, fermenting at 50 degrees C, turning at 50-65 degrees C for 15-20 days, interphase turning for 8-10 times, cooling to 30-40 degrees C until water content of 20-40%, and screening; and    (2) production of fermented chicken manure comprising digging 50-70 mm ground pit, pouring fresh chicken manure, covering on top with soil, decomposting at room temperature for 15-20 days, turning for 8-10 times until water content of 30-50%, and grinding into powder.
NOVELTY - Manufacture of hydrogen by decomposing water, involves reacting water with alkali complex oxide compound to form sulfur dioxide gas, sodium hydroxide and hydrogen gas, and reacting sodium hydroxide and hydrogen gas to form alkali complex oxide compound.    USE - Manufacture of hydrogen used for fuel cell (claimed) for car and power plant.    ADVANTAGE - The method enables manufacture of hydrogen with energy consumption reduced by 90% or more.    DETAILED DESCRIPTION - Manufacture of hydrogen by decomposing water, involves reacting water with alkali complex oxide compound of formula: Na'xS'2O4 to form sulfur dioxide gas, sodium hydroxide and hydrogen gas, and reacting sodium hydroxide and hydrogen gas to form alkali complex oxide compound, where x is 2-4, S' is sulfur, carbon or nitrogen, and Na' is sodium, potassium or lithium. An INDEPENDENT CLAIM is included for manufacture of hydrogen fuel cell.
NOVELTY - This new type utility claims one a composting device including compost tower, a compost tower top part set with a feeding port, the bottom is set with a discharging port, a feeding port is set with the first cover, a discharge port set with a second cover, said first cover middle part set with air supply pipe, a first cover top is welded with a bracket, and set with one support a air blower through the bracket, the output end of said air blower and the air pipe between the set set with PVC soft pipe, a compost tower inner wall close to the top position set with a heating device, a compost tower outside close to the top position is set with an air outlet, a compost tower outside close to the bottom position is set with a drain valve, the device can be a piling and fermenting the organic material provide a certain constant temperature to promote the growth of microorganism, accelerate fermentation of organic material, at the same time, this device using closed design, which avoids odour leakage, and using a tower structure, reduces floor area, fit and use.
NOVELTY - Preparing bio-organic fertilizer involves crushing pineapple buds, stem or leaves to obtain powder. The powder is mixed uniformly with microbial inoculum in weight ratio of 90-110:1 and then water (60-70%) is added to carry out fermentation 4-5 times at 60-65 degrees C to obtain a fermented product. The fermented product is stacked and wrapped thin film around it and cooled to 25-35 degrees C to obtain final product.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-organic fertilizer that increases soil fertility and soil permeability.
NOVELTY - Preparing iodine substituted aryl compound (I) comprises reacting bromine substituted aryl compound (II) with iodine source in the presence of catalyst, ligand and organic solvent, and separating reaction product by silica gel column. (II) is bromobenzene compound, naphthalene compound or heterocyclic ring compound. The catalyst is cuprous bromide, cuprous chloride, cuprous oxide, copper acetate, copper chloride, copper bromide or copper oxide. The ligand is 4-(2-(diphenylphosphino)phenyl)morpholine, L-proline, 1,6-hexamethylenediamine, or ethylenediamine.    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The method is capable of preparing (I) in an eco-friendly manner with good compatibility under a mild reaction condition.    DETAILED DESCRIPTION - Preparing iodine substituted aryl compound of formula (I) comprises reacting bromine substituted aryl compound of formula (II) with iodine source in the presence of a catalyst, a ligand and an organic solvent at 50-200 degrees C for 12-36 hours, and separating the obtained reaction product by silica gel column. (II) is bromobenzene compound, naphthalene compound or heterocyclic ring compound. The catalyst is cuprous bromide, cuprous chloride, cuprous oxide, copper acetate, copper chloride, copper bromide or copper oxide. The ligand is 4-(2-(diphenylphosphino)phenyl)morpholine, ethylenediamine, L-proline, 1,6-hexamethylenediamine, or ethylenediamine. The mole ratio of (II) and iodine source is 1 :1-1:20. The mol ratio of (II) and catalyst is 1:0.01-1:1. The mole ratio of ligand and catalyst is 1:0.01-1:1. The iodine source is ammonium iodide, tetramethylammonium iodide, tetra-n-butylammonium iodide or potassium iodide.    R = H, halo, alkyl, amino, CN, acyl, carboxyl, aldehyde, ester, OH or nitro.
NOVELTY - A organic-inorganic complex fertilizer comprises: 6-11 parts acrylamide, 3-7 parts ammonium nitrate, 4-8 parts boric acid, 8-15 parts component A (sic), 5-10 parts pig manure, 2-4 parts calcium biphosphate, 1-3 parts base shell spore powder, 4-7 parts furfural residue, 2-6 parts chicken meat slaughter waste, 6-8 parts peanut cake, 3-7 parts corn straw, 0.5-1.5 parts microorganism fertilizer, 2-4 parts bentonite, and 6-10 parts amino acid.    USE - As organic-inorganic complex fertilizer for crop (claimed).    ADVANTAGE - The organic-inorganic complex fertilizer can increase the utilization rate of fertilizer; can increase soil fertility; and has good social value and economic value.
NOVELTY - Biological fertilizer comprises 8-15 pts. wt. urea, 4-7 pts. wt. potassium dihydrogen phosphate, 3-6 pts. wt. monopotassium phosphate, 2-6 pts. wt. chicken manure, 3-6 pts. wt. ferrous sulfate, 2-4 pts. wt. potassium chloride, 2-5 pts. wt. waste straw fermentation agent, 4-9 pts. wt. plant straw, 1-4 pts. wt. lactic acid bacteria, 0.6-2 pts. wt. yeast, 5-8 pts. wt. cattle, sheep and pig manure, 1-5 pts. wt. plant ash, 0.5-1 pts. wt. amino acid, and 1-3 pts. wt. Bacillus subtilis.    USE - The biological fertilizer is useful for enhancing disease resistance and drought resistance of vegetable.    ADVANTAGE - The biological fertilizer can increase the nitrogen source in the soil and increase the quality of the crop, and is cost effective.
NOVELTY - Organic fertilizer comprises (in pts.wt.): straw (10-20), amino acid (5-8), balsam pear root (3.5-7), clay (2.5-6), biogas slurry (0.5-4.9), calcium nitrate (3.5-9.5), animal bone powder (4-8), gypsum powder (2.3-4.8), pig manure (2.6-5.7), straw ash (6-10), potassium fulvate (8-14), bean cake (3.2-5.6), Bacillus subtilis (4-9), zinc sulfate (5-7) and manganous sulfate (1-3).    USE - Organic fertilizer used for soil.    ADVANTAGE - The organic fertilizer is cost-effective, and has long effect, air and water pollutions are small.
NOVELTY - Preparing fertilizer, comprises (i) drying an organic fertilizer, and crushing to a particle size of less than 80 meshes; (ii) mixing bacterial manure with the organic fertilizer in a ratio of 1:500-1.5:500, wetting by covering with water, composting for 3-5 days, and turning once from middle; and (iii) packaging the fertilizer according to standard of 100-250 g fertilizer/bag, and adding 1-3 g sodium polyacrylate high water-absorbing resin into each bag.    USE - The method is useful for preparing fertilizer (claimed).    ADVANTAGE - The method produces product with good water retention capacity (claimed), and moisture retention capacity in soil; and has simple, and easy preparation procedures; and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for fertilizer prepared as mentioned above.
NOVELTY - Preparing nitrogen containing heteroaryl substituted 3-amino-4-phenyl-but-2-en-1-one compounds (I) comprises reacting nitrogen containing heteroaryl substituted (S)-3-amino-4-phenyl-butan-1-one compounds (II) with halogenating reagent to obtain nitrogen containing heteroaryl substituted (S)-3-(haloamino)-4-phenyl-butan-1-one compounds (III), and subjecting (III) to elimination reaction. The halogenating agent is e.g. sodium dichloroisocyanurate, dibromo isocyanuric acid, sodium dibromoisocyanurate, potassium dichloroisocyanurate, trichloroisocyanuric acid or chlorobromoisocyanuric acid.    USE - The method is useful for preparing nitrogen containing heteroaryl substituted 3-amino-4-phenyl-but-2-en-1-one compounds (claimed).    ADVANTAGE - The method recycles waste drug isomers, and is economical and suitable for industrial production.    DETAILED DESCRIPTION - Preparing nitrogen containing heteroaryl substituted 3-amino-4-phenyl-but-2-en-1-one compounds of formula (I) comprises reacting nitrogen containing heteroaryl substituted (S)-3-amino-4-phenyl-butan-1-one compounds of formula (II) with halogenating reagent to obtain nitrogen containing heteroaryl substituted (S)-3-(haloamino)-4-phenyl-butan-1-one compounds of formula (III), and subjecting (III) to elimination reaction. The halogenating agent is sodium dichloroisocyanurate, dibromo isocyanuric acid, sodium dibromoisocyanurate, potassium dichloroisocyanurate, trichloroisocyanuric acid, chlorobromoisocyanuric acid, 1,3-dibromo-5,5-dimethyl hydantoin or 3-bromo-1-chloro-5,5-dimethylhydantoin or its hydrate.    A = phenyl (optionally substituted with 1-5 halo or CF3);    X = N or CR2;    R2 = H, straight or branched 1-6C alkyl (optionally substituted with 1-5 F) or phenyl (optionally substituted 1-3 F, OCH3 or OCF3);    R1 = H or 1-6C alkyl (optionally substituted with 1-5 F or phenyl); and    X1 = Cl or Br.
NOVELTY - Preparing tadalafil comprises adding compound B with water, adding 1-10% of tetrabutylammonium bromide and 2-5 ml/g of aqueous methylamine to the obtained solution and then reacting by heating at 60-90 degrees C for 6-10 hours, cooling the reaction solution at 20-25 degrees C for 3-6 hours, crystallizing the solution, filtering the solution to obtain a filter cake, and washing the filter cake and then drying. The compound B is 1-(benzo(d)(1,3)dioxol-5-yl)-2-(2-chloroacetyl)-2,3,4,9-tetrahydro-1H-pyrido(3,4-b)indole-3-carboxylate.    USE - The method is useful for preparing tadalafil (claimed).    ADVANTAGE - The method is capable of simply, economically preparing the tadalafil with high purity of 99.90% and yield in an environmentally-friendly manner.
NOVELTY - Methanol gasoline prepared using coal based light oil comprises 35.7-40.2% distilled oil, 11.96-30.4% methanol, 1.04-1.6% cosolvent, 17-17.4% national standard no. 90 gasoline, 14.28-14.62% aromatic hydrocarbon and 1.02-2.78% additive. The distilled oil is obtained after distilling coal based light oil, and taking less than 120 degrees C fraction. The cosolvent comprises isobutanol, isopropanol and pentanol in a weight ratio of 3:1:2. The additive is tetrahydrofuran, methyl tert-butyl ether (MTBE) and toluene in a weight ratio of 1:1:1.    USE - Used as methanol gasoline prepared using coal based light oil.    ADVANTAGE - The method: utilizes easily available raw materials; is economical and environmentally friendly; consumes less energy; and has strong dynamic performance.
NOVELTY - Preparing engineered bacteria comprises taking wheat soil bacteria as bacterial source, culturing under UV illumination condition in a benzene containing culture medium and collecting bacterial colonies, inoculating bacterial colonies into benzene-containing (of concentration 50-500 mg/l) agricultural wastewater, irradiating under 280 nm UVB and culturing for 3-5 days to obtain bacteria, inoculating the bacteria into benzene-containing (of concentration 50-1000 mg/l) agricultural wastewater, irradiating under 280 nm UVB and culturing for 6-8 days to obtain engineered bacteria.    USE - The engineered bacteria is useful for removing benzene from wastewater (claimed).    ADVANTAGE - The engineered bacteria has benzene removing rate of more than 90%.    DETAILED DESCRIPTION - Preparing engineered bacteria comprises (i) taking wheat soil bacteria as bacterial source, culturing at 25-29 degrees C for 18-22 hours (pH of 8.6-9.2) under UV illumination condition in a benzene containing culture medium, and collecting bacterial colonies, and (ii) inoculating bacterial colonies into benzene-containing (of concentration 50-500 mg/l) agricultural wastewater, irradiating under 280 nm UVB and culturing for 3-5 days to obtain bacteria, (iii) inoculating the bacteria obtained in the step (ii) into benzene-containing (of concentration 50-1000 mg/l) agricultural wastewater, irradiating under 280 nm UVB and culturing for 6-8 days, and (iv) adding agricultural wastewater into 10 times high concentration benzene culture medium and culturing at 22-28 degrees C (pH 8.8-9.2) for 3-4 days under low illumination condition to obtain engineered bacteria.
NOVELTY - This utility new type relates to a one in production of organic fertilizer fermentation device, specifically is a one organic fertilizer fermenting turning device. Undercarriage comprising two side set with walking wheel and a turn stack, stack machine turn mounting a drive motor fixed on the upper disk, driving motor and a transmission including a drive motor and a transmission of fixed connecting a rotating shaft and the rotating shaft of double-spiral plate group, a double-spiral plate group including two pieces of spiral strip to the rotating shaft is set with a centre, two pieces of spiral strip of spiral direction opposite, one end of two spiral strip through a driving end connecting pole fixed connect to a rotating shaft, and the other end of two spiral strip through a driven connecting pole connect to a driven shaft, a driven shaft through a bearing on the bracket a, a bracket fixed on the lower end of the connecting disk. The turning device firm structure, design is reasonable, use life is long, the material turned completely, which is good for increase fermentation quality of organic fertilizer product.
NOVELTY - This new type utility claims one and a pig farm dung material efficient process by system, belonging to the aquaculture waste treatment field, the device the device comprising primary settling annular sedimentation pool, a precipitating pool, regulating pool fertilizer, solid fermentation tank, material pump, water pump, pH monitoring device, pH neutralizing device and medicine-adding device, using the primary-secondary pool and efficient annular sedimentation pool for a manure of efficient solid-liquid separate processing, a process taking a biological fermentation and absorbing self-purification filter for dung and pig waste liquid, the prepared biological organic fertilizer, dung and pig of the high concentration waste liquid proceed fast purification is discharged, and also organic fertilizer, at the same time, the process is simple, the cost is low, a valid to solve the problem of environment and scale pig farm dung fertilizer.
NOVELTY - This new type utility claims one a microorganism treatment device, a transverse rotating shaft set with inner mixer stir bucket comprising, a rotating shaft, a rolling blade rod, a motor and a gear, a mixer stir bucket, the lower part set with rolling blade rod, a mixer stir bucket has a blade set with a flow exit, a mixer stir bucket side set with valve, valve connecting interval upper shaft of hydraulic cylinder, hydraulic driving valve of opening and closing, the outer opening set with filter screen. A microorganism one. The utility model is a new type of using the residual substance of vegetable and fruit putting them into the mixer stir above a device entrance bucket, and the microorganism ferment, motor and gear drive by the rotating shaft to rotate, so as to make the blade rod rolling produce stirring, and the vegetable and fruit of inner bucket stir a stir, and through the friction temperature rising, to accelerate the decomposition speed, quick decomposition and conversion is liquid organic fertilizer, this utility new type healthy and environment-friendly, it has a good economic benefit.
NOVELTY - This utility new type belongs to waste processing device technology field, especially relates to a one organic garbage processing device, comprising bracket and crushing device, a conveying device and mix ferment device, a fermentation device is inclined to a mounting bracket a, a fermentation device comprising fermenting and heat preserving cylinder, a gear rolling device is set on the said outer wall of a fermenting and heat preserving of and a motor with a gear rolling device of a, fermenting and heat preserving cylinder is set with a temperature sensor, a humidity sensor, a sampling port, a water inlet pipe and the pneuma pipe, said water inlet pipe and one end of inlet pipe extends into the inner a pneuma fermenting and heat preserving cylinder, a water inlet pipe one end extends into a fermenting and heat preserving inner cylinder set with a spray head, the inner wall of said fermenting and heat preserving cylinder is set with multi-inner strip. The organic garbage processing device structure is simple, the component cost is low, a valid processing vegetable waste, kitchen garbage and organic waste, and the treatment effect is good.
NOVELTY - The bottom of the tower of this utility new type relates to one based on a light liquid layer evaporator of biological fuel continuous rectification system, mainly comprising constituent and a finished product tower, dehydration and finished product are set with light liquid layer evaporator, light phase inlet and liquid phase inlet of the dehydration tank is connected, the top of a dehydration with a condenser II, the bottom of dehydration through discharging pump II and a finished product tower liquid phase inlet connected. This utility new type of beneficial effect is: this utility new type double-tower is easier to apply a light component and heavy component, obtaining target product biological fuel of high quality and reduce the heating tray liquid layer thickness, reduces the heating medium temperature, increase heating vaporization amount to the largest extent eliminate the residence time is too long a cause of high temperature thermal decomposition, and coking, increase distillation yield and quality of biological fuel oil and reduce the energy consumption.
NOVELTY - This utility new type claims a one biomass gasification furnace pressure control system, comprising gasification furnace, gas pipeline of said gasification furnace in turn connect with the first valve, the first expansion joint, high temperature draught fan and the first frequency conversion module, a first high temperature draught fan output end of connecting in turn with a first expansion joint and the first output. This utility new type through frequency conversion module for a high temperature draught fan of a regulating, it can avoid gasification furnace inner pressure change is too big, the inner explosion and so on, the gasification furnace operation safety, which greatly increase safety coefficient. And two table high temperature draught fan connecting with an interlocking control, safety and a button switch, a time switch and convenient repairing. This utility new type a wide application in the gasification furnace and in the field.
NOVELTY - This new type utility claims biological diesel oil extraction tank device, comprising a tank body, wherein said tank body the same side connected with one return pipe, a reflux pipe set with one reflux pump, set with raw oil inlet of the tank body, a steam entrance methanol and methanol steam exit, set with one control valve up the methanol steam exit, a tank body set with inner layer number catalyst layer, the catalyst layer by fixing one fixing frame, fixing frame is clamped in the tank body set with one constant-temperature heater at the bottom of the tank body, a valve and a constant temperature heater is connected with one control station a. This utility new type has simple structure and purifying efficiency, reduces the production cost of biological diesel oil.
NOVELTY - This new type utility claims one a rotating gasifier for furnace, comprising the ash cone body, the outer surface of said dust cone body from lower to upper with multiple layer air hole set on the same one layer of inner air hole along the circumference of the distribute, each said air hole are a mounting with a nozzle, said nozzle is exposed 25 to 35, the inner diameter of the air nozzle is 16 to 19, the said ash taper body of taper is 35 to 40 degrees. This utility new type has following advantages, ash falling slope of taper body, the ash is easier, nozzle exit is small and the multi-number, the exit air quantity at the same time of satisfying the air outlet pressure high is not easy to plug the problem of the exposed air nozzle for the carbon ash layer also has as a stir, is more beneficial for ash discharging. This utility new type has compact structure, the manufacturing technique is simple, the technology is reliable, stable operation, wide application range, good economical efficiency and strong practicability, rotating furnace row is widely application to a biomass gasification furnace in a, and the market prospect is good.
NOVELTY - This utility new type claims a one biomass gasification furnace ignition device, comprising the set with a combustion port in a side wall of the gasification furnace, further comprising and burning torch burner mounting with a fixed inner tube base, fixed base through bolt mounting tube with a flange cover, a flange cover is welded with an oil connecting short tube and a short ignition, rear connecting short pipe and ignition connecting short pipe passes through the fixing base extends into the gasification furnace inner tube, a short tube and a short screw mounting with ignition, injection end of through a short internal oil into gasification furnace, the ignition end of ignition through the ignition connecting short pipe extends into the gasification furnace. For there is no pressure of air in this utility new type, simple structure, burning torch and of both is a detachable mounting of, solves the problem that the long-term burning by high temperature burning damage of.
NOVELTY - This utility new type claims a one biomass gasification furnace dry slag discharging device, a slag at the bottom of gasification furnace lower part comprising gasification furnace and the gasification furnace form a funnel-shaped ash discharging mechanism comprising discharging pipe, sleeve is set on the side of the outer discharging pipe, a spiral shaft inner discharging pipe and power mechanism driving spiral shaft a, front end of upper pipe and set with a cinder inlet connection, discharging pipe end lower side set with a discharging port, the discharging pipe and sleeve pipe form circulation water cavity, the front end and the tail end of a sleeve and set with the first circulation water cavity water outlet connection of the first and the water. This utility new type structure is compact, a long-term use, strong reliability, convenient operation, time cooling ash does not directly contact with the water so as to avoid the impact phenomenon, the ash with water produce peculiar smell and a secondary, use life is long, the slag and convenient for loading and unloading. Biomass gasification furnace of dry-type deslagging system gives one strip of ideal design idea.
NOVELTY - Refining of moclobemide comprises adding purified water to crude moclobemide, pulping at room temperature, adding acetic acid, stirring to clarify, heating at 65-75 degrees C, adding activated carbon, decoloring, filtering, cooling to 25 degrees C, dropping ammonia water, regulating pH at 8-9, cooling to 5 degrees C, centrifuging, washing with cold water at 4-6 degrees C until pH is 6.5-7.5, and vacuum-drying to constant weight.    USE - Method for refining moclobemide (claimed).    ADVANTAGE - The environmental and economical method recovers organic solvent, improves product quality, and increases product yield from 85% to 96%.
NOVELTY - Purifying epigallocatechin gallate (EGCG) comprises (i) placing dry silica gel in a glass column; (ii) soaking low level EGCG polyphenol in 70% ethanol, than adding into silica gel column, and carrying out chromatography; (iii) eluting; (iv) collecting the eluate, where the segment liquid is EGCG eluate segment liquid; (v) concentrating the collected EGCG, to obtain EGCG extract; (vi) placing the EGCG extract in a conical flask, adding 75% ethanol, dissolving for 1 hour, crystallizing, filtering, and collecting the crystals; and (vii) vacuum drying the crystals at 70 degrees C.    USE - The composition including EGCG is useful for treating senile dementia (claimed).    ADVANTAGE - The method has simple operation, consumes less energy, is economical, environmentally-friendly, and produces EGCG with purity of not less than 99%, and the yield of not less than 90%. The composition delays the occurrence of senile dementia, shows remarkable treatment effect, enhance memory recovery capacity of the patient, and has no side effect.    DETAILED DESCRIPTION - Purifying epigallocatechin gallate (EGCG) comprises (i) placing dry silica gel in a glass column having diameter of 5 cm and height of 80 cm; (ii) soaking low level EGCG polyphenol in 70% ethanol, than adding into silica gel column, and carrying out chromatography; (iii) adding eluent and carrying out elution; (iv) collecting the eluate by thin-layer chromatography, where the segment liquid is EGCG eluate segment liquid; (v) concentrating the collected EGCG, to obtain EGCG extract; (vi) placing the EGCG extract in a conical flask, adding 75% ethanol, then placing in 65 degrees C water bath, stirring while heating, dissolving for 1 hour, crystallizing by allowing to stand overnight, then filtering, and collecting the crystals; and (vii) vacuum drying the crystals at 70 degrees C. An INDEPENDENT CLAIM is also included for medicine composition, comprising EGCG and tetrandrine.
NOVELTY - A one molasses alcohol fermentation liquid comprehensive utilization production device, is a using molasses alcohol fermentation liquid and solid fertilizer production raw material of compound fertilizer, comprising molasses alcohol fermentation liquid storage tank, solid fertilizer raw material storage device, a conveying device, a feeding device, granulating device, drying device, cooling device, coating device and packaging equipment of food weighing device, the molasses alcohol fermentation liquid storage tank exit through the conveying pump and pipeline connected to the granulating device of nozzle, a solid fertilizer raw material storage device through a conveying device to a feeding device, then a granulating device of molasses alcohol fermentation liquid from the nozzle spray solid fertilizer raw material up to a pelleting, pelleting device exit orderly is connected with drying device, cooling device, coating device and packaging equipment of food weighing device, into a fertilizer product. This utility new type a a molasses alcohol fermentation liquid fertilizer resource utilization, solves the valid molasses alcohol production process end discharge of organic waste water;
NOVELTY - This utility new type category anaerobic biological treatment technology field, specific relates to a chain one penicillin a residue of a device, the device comprising chain penicillin a slag storage pool, alkali liquid tank, a reaction pool, regulating pool, tank, fermenting steam exploded wood fibre straw ASBR anaerobic reactor, slag collecting pool, a PLC automatic control system, an online water quality monitoring system and so on. The utility model is new type by computer PLC automatic control system is a finish of the first chain penicillin a slag and alkali into a reaction pool, heating a rear hot alkali preprocessing, a pre-mix liquid placed in a regulating pool, by making use of straw fermentation liquid regulating C/N ratio and pH rear ASBR into the anaerobic reactor, carrying out anaerobic digestion rear, biogas generated by using as a clean fuel, waste residue identified as harmless in the biogas residue collecting pool as a raw material for producing organic fertilizer. This utility new type device improves the chain penicillin a residue organic matter of the efficiency, at the same time, a chain penicillin a slag harmless and reclamation.
NOVELTY - One is suitable for a multi-temperature a long-term acclimating sludge and device storing anti-leaching ore bacteria of arsenic, relating to one suitable for a different temperature of anti-arsenic leaching ore bacteria of acclimating sludge and continuous long-term storage of a simple device. This utility new type is simple, energy consumption is low, operation for scientific instrument loss is small, by constant temperature culture box, an air inflation pump, gas-guide tube, the culture tank. Wherein it is prepared by means of the sulphide ore containing arsenic as a growing the bioleaching of energy substance, the constant-temperature culture box a domestication culture temperature, air inflation pump through a leaching ore bacteria domestication culture tank in air, air to a mineral powder and stirring, a anti-arsenic leaching ore bacteria of long-term domestication culture, and the leaching ore bacteria obtain. Constant temperature culture box temperature change, long-term domestication culture and can be stored for different temperature of continuous anti-arsenic leaching ore.
NOVELTY - Extracting resveratrol, comprises (i) crushing giant knotweed rhizome to obtain raw material powder, (ii) extracting the raw material powder with 85-95% ethanol thrice, filtering the extracts and mixing filtered liquid, (iii) concentrating the obtained filtered liquid at 80-85 degrees C under vacuum pressure until absence of alcohol taste, (iv) adding acid and stabilizer into concentrated liquid, stirring, and hydrolyzing, and (v) cooling the hydrolyzed liquid at room temperature, adding alkali to adjust pH value to neutral, incubating for crystallizing, filtering and vacuum drying.    USE - The composition is useful for treating Alzheimer's disease (claimed).    ADVANTAGE - The method reduces amount of solvent, shortens extraction time, and increases productivity, is simple, economical and suitable for industrial production, and has process stability and strong feasibility. The medicinal composition improves cognitive ability and life-span of patient.    DETAILED DESCRIPTION - Extracting resveratrol, comprises (i) crushing giant knotweed rhizome to obtain raw material powder, (ii) extracting the raw material powder with 85-95% ethanol thrice, each time for 3-4 hours, 2-3 hours and 1-2 hours at 80-85 degrees C by adding solid-liquid ratio of 6-8 g/ml, 4-6 g/ml, and 3-4 g/ml of ethanol, filtering the extracts and mixing filtered liquids, (iii) concentrating the obtained filtered liquid at 80-85 degrees C under vacuum pressure until the absence of alcohol taste, (iv) adding acid and stabilizer into concentrated liquid at 65-70 degrees C, stirring, and hydrolyzing for 3-4 hours, and (v) cooling the hydrolyzed liquid at room temperature, adding alkali to adjust pH value to neutral, incubating for crystallizing, filtering and vacuum drying. INDEPENDENT CLAIMS are also included for:    (1) resveratrol extracted by the above method; and    (2) medicinal composition comprising resveratrol and tetrandrine.
NOVELTY - The method involves performing an artificial sorting process and a magnetic sorting process to collect domestic waste rubbish. Harmful rubbish is separated from the domestic waste rubbish. A stabilization process is performed in the harmful rubbish. Organic waste is separated by an anaerobic fermentation process. A high molecular material, a catalytic splitting reaction material and a high active material are separated from a residue material. A black metal centralization transportation process is performed by a metal cleaning drying device.    USE - Municipal domestic rubbish recovery method.    ADVANTAGE - The method enables performing domestic rubbish recovery in wide application.
NOVELTY - Synthesizing cetirizine hydrochloride comprises (a) taking hydroxyzine as a raw material, using (2,2,6,6-tetramethylpiperidin-1-yl)oxy (TEMPO)/sodium hypochlorite or pyridine sulfur trioxide compound (PST)/dimethyl sulfoxide (DMSO) as an oxidation system, where first hydroxyzine is oxidized to aldehyde intermediate, (b) adding organic solvent and a buffer solution into the aldehyde intermediate, oxidizing by an oxidation reagent, post-processing to form cetirizine hydrochloride reaction system.    USE - The method is useful for synthesizing cetirizine hydrochloride (claimed).    ADVANTAGE - The method has total yield of more than 80%; is simple, short and economical; has low energy consumption; reduces three wastes; and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - Synthesizing cetirizine hydrochloride comprises (a) taking hydroxyzine as a raw material, using (2,2,6,6-tetramethylpiperidin-1-yl)oxy (TEMPO)/sodium hypochlorite or pyridine sulfur trioxide compound (PST)/dimethyl sulfoxide (DMSO) as an oxidation system, where first hydroxyzine is oxidized to aldehyde intermediate, (b) adding organic solvent and a buffer solution into the aldehyde intermediate, oxidizing by an oxidation reagent, post-processing to form cetirizine hydrochloride reaction system, or (c) taking hydroxyzine as a raw material, using one pot boiling method, carrying out two-stage oxidation reaction simultaneously in the same reaction system.
NOVELTY - Reducing (M1) recalcitrance in cellulosic or lignocellulosic materials, comprises: contacting, in a mixture, a first cellulosic or lignocellulosic material having a first level of recalcitrance with at least one compound comprising at least one naturally-occurring, non-radioactive group 5, 6, 7, 8, 9, 10 or 11 elements, to produce a second cellulosic or lignocellulosic material having a second level of recalcitrance lower than the first level of recalcitrance.    USE - The method is useful for reducing recalcitrance in cellulosic or lignocellulosic materials (claimed) and producing ethanol and/or butanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a composition comprising a cellulosic or lignocellulosic material, at least one compound comprising at least one naturally-occurring, non-radioactive group 5, 6, 7, 8, 9, 10 or 11 elements, and, optionally, oxidants capable of increasing an oxidation state of at least some of the elements; and    (2) reducing recalcitrance in cellulosic or lignocellulosic materials, comprising contacting a first lignocellulosic material having a first level of recalcitrance with at least one ligninase and/or at least one biomass-destroying organism, to produce a second lignocellulosic material having a second level of recalcitrance lower than the first level of recalcitrance and contacting the second lignocellulosic material with an enzyme and/or microorganism.
NOVELTY - Composition comprises lentinan and chitosan.    USE - The composition is useful in preparation for selectively repairing heavy metals in soil and promoting plant growth and quality in the soil. The plant is tea plant. The heavy metals are cadmium and/or chromium. The soil is not rich in zinc and lead (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation, which comprises the above-mentioned composition and excipient chosen from pH regulating agent, filler, solvent, cosolvent, emulsifier, dispersing agent, anti-freezing agent, defoaming agent, thickener, stabilizer, and binder, preferably pH regulating agents and/or filler, the preparation is a solid preparation, preferably powder.
NOVELTY - This new type utility especially claims a one biodegradable planting greenhouse. The biodegradable planting greenhouse, include soil culture medium and cover body set on a soil culture medium, said culture medium comprise is connected with a soil layer, the bottom of a layer is paved with one, set with a water system and a water collecting system on the upper part of inner layer and a lower part, the area of water system and a water collecting system are less than anti-seepage layer of area. This utility new type biodegradable planting greenhouse of the following beneficial effects: low cost, a simple process, reduces the environment pollution and absorbing nutrient to crop growth of at the same time, obtain the organic waste water purification process, through the growth of crops absorbing nutrient organic waste water purification and harvesting crops, organic waste water into waste is changed into treasure, growth of crop without fertilizing, thrived, realize the organic waste water of ecological circulation and organic waste water of purification of standard-reaching exhaust and degradation purification effect is obvious.
NOVELTY - This utility new type relates to compost technology field, specific relates to a one seepage filtered liquid return, include: used for collecting leachate of collecting liquid nozzle through a pipeline and a collecting tank, water pump, set up in a pipeline. This utility new type the percolate for compost process in the condition that the water content of the material discomfort of a low return, to increase water content of material to reach the most optimal material fermentation water; on the other hand, but also reduces the discharge of leachate, using the processing device of a filter liquid, saves the compost.
NOVELTY - The method involves combining agave bagasse, water and enzyme to form a hydrolysis mixture comprising water-soluble sugar. The water-soluble sugar is separated from the hydrolysis mixture. The water-soluble sugar is combined with fermentable sugar i.e. glucose, derived from agave pina and yeast to prepare fermentation mixture. The fermentation mixture is fermented to prepare wort comprising ethanol. The wort is distilled twice to prepare tequila, where the steam treated agave bagasse is cooled before combining the agave bagasse, the water and the enzyme.    USE - Method for producing potable ethanol from potable agave bagasse/agave leaves of agave tequilana for distilled beverage e.g. biofuel such as tequila/mezcal. Can also be used in an animal feed and paper production.    ADVANTAGE - The method enables subjecting the agave bagasse from tequila operation to enzyme hydrolysis to increase yield of fermentable sugar obtainable from the agave pina. The method enables optional acid hydrolysis and steam treatment to be effective to disrupt and separate fibrous strands in the agave bagasse, thus making fiber more available to enzymes in subsequent enzymatic hydrolysis to make acidic conditions to hydrolyze a portion of celluloses, hemicelluloses, inulins and lignins into lower molecular weight polymer. The method enables pretreatment of the bagasse to enhance enzyme accessibility to cellulose and to sterilize the fiber to minimize risk of bacterial contamination in a subsequent enzymatic hydrolysis step. The method enables acidic and high temperature conditions in steam treatment to break down lignin-hemicellulose complexes.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing potable ethanol from agave.
NOVELTY - Production of biomass involves introducing nutrient component comprising carbon, nitrogen and phosphorus, and water into aerobic reaction zone containing sewage sludge, and maintaining food-to-microorganism ratio as 0.25-2 kg chemical oxygen demand (COD) (mg oxygen/l of liquid in aerobic reaction zone)/kg mixed liquor suspended solid (MLSS) (mg solid in aerobic reaction zone/l of liquid in the aerobic reaction zone).day in aerobic reaction zone under aerobic conditions for period of time to produce biomass.    USE - Production of biomass used for treatment of Fischer-Tropsch reaction water (all claimed). The treated water is used for environmental release, irrigation and reuse in process cooling.    ADVANTAGE - The Fischer-Tropsch reaction water is efficiently treated using the biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treatment of FT reaction water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the plant for production of biomass.    Plant (10)    Reactor (11)    Anoxic zone (14)    Primary aerobic reaction zone (16)    Secondary aerobic reaction zone (18)
NOVELTY - Method (M1) for producing sugar solution form cellulose-containing biomass, involves (a) hydrolyzing the cellulose-containing biomass with filamentous fungus-derived cellulase, (b) subjecting hydrolyzate to solid-liquid separation, (c) washing saccharification residue with an aqueous solution containing lignin blocking agent, and (d) filtering wash solution to collect an unpenetrated solution containing the filamentous fungus-derived cellulase.    USE - The method (M1) is useful for producing sugar solution form cellulose-containing biomass. The method (M2) is useful for producing chemical substance (all claimed). The chemical substance is alcohol e.g. ethanol, propanol, and butanol, organic acid e.g. acetic acid, lactic acid and pyruvic acid, or nucleosides e.g. inosinic acid.    ADVANTAGE - The method is cost-effective and enables to reducing usage amount of cellulase.    DETAILED DESCRIPTION - Method (M1) for producing sugar solution form cellulose-containing biomass, involves (a) hydrolyzing the cellulose-containing biomass with filamentous fungus-derived cellulase to produce a hydrolyzate, (b) subjecting the hydrolyzate to solid/liquid separation to produce sugar solution and saccharification residue, (c) washing the saccharification residue with an aqueous solution containing lignin blocking agent to produce wash solution containing the filamentous fungus-derived cellulase contained in the saccharification residue, and (d) filtering the wash solution to collect an unpenetrated solution containing the filamentous fungus-derived cellulase. An INDEPENDENT CLAIM is included for method (M2) for producing chemical substance, which involves culturing microorganisms having capability to produce chemical substance by making the sugar solution as fermentation medium.
NOVELTY - The system has a waste gas heat exchanger (2) with which the waste gas from fuel cell (21) or hydrogen generator and the hot/cold water from a hot water storage tank (3) are heat-exchanged. The temperature of hot/cold water which flows through a path (5a) between an exit side of a heat radiator (8) in a hot water storage water circulation path (5) and an entrance side of waste gas heat exchanger is more than predetermined temperature, such that a circulation pump (4) makes the flow volume of hot/cold water which circulates through hot water storage water circulation path increase.    USE - Fuel cell system such as solid oxide-type solid fuel cell system and high polymer-type fuel cell system for generating electrical energy by direct reaction of hydrogen and oxygen, used for home-use and business-use.    ADVANTAGE - Since the circulation pump makes the flow volume of hot/cold water which circulates through hot water storage water circulation path increase, the water required for the electric power generation from the condensed water of the waste gas in waste gas heat exchanger stably is recovered and ensured effectively. Thus, the excellent in water autonomous is reliable, and the enlargement of the fuel cell system is suppressed. The structure of the fuel cell system is simple with reduction in cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system. (Drawing includes non-English language text)    Waste gas heat exchanger (2)    Hot water storage tank (3)    Circulation pump (4)    Hot water storage water circulation path (5)    Path (5a)    Heat radiator (8)    Fuel cell (21)
NOVELTY - The method involves integrally molding an anode side gas diffusion layer (21) with a reinforcing material (12) and a sealing material, to manufacture the anode side gas diffusion layer integrated seal (17). Two or more unit cells provided with the gas diffusion layer are stacked with a membrane/electrode joining structure and a separator to manufacture a cell stack. The reinforcing material is removed from the gas diffusion layer by supplying liquid fuel to the cell stack and the reinforcing material is dissolved.    USE - Method for manufacturing fuel cell.    ADVANTAGE - By integrally molding an anode side gas diffusion layer with a reinforcing material and a sealing material to manufacture the anode side gas diffusion layer integrated seal, the generation of wrinkles in the gas diffusion layer is suppressed and the reinforcing material is removed easily. The electric power generation performance of the fuel cell is improved reliably and simply.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic views of the anode side gas diffusion layer during manufacturing process. (Drawing includes non-English language text)    Reinforcing material (12)    Anode side gas diffusion layer (13,21)    Seal (17)    Seal portion (22)
NOVELTY - This new utility model claims of one of gas heat pump energy comprehensively using device, comprising compressor, evaporator, throttle valve, heating pipe, the auxiliary condenser, arrange heat condenser, cooling processing medium outlet of compressor respectively connected with auxiliary control valve and arrange and heat control valve, control valve and auxiliary condenser entrance connected with auxiliary heating, heat control valve and arrange arrange heat entrance connected with the condenser and auxiliary condenser outlet and arrange heat condenser and throttle valve entrance connected with exit, a throttle valve and an evaporator outlet entrance connected, an evaporator outlet and connected compressor, heating pipe is set with biogas ferment device in internal, cool water entrance and exit the condenser and the auxiliary heating pipe mutually connected, outlet of heating pipe and water pump connect rear and cooling water entrance and auxiliary condenser connected with. Using refrigeratory air as cold source and heat pump unit, circulation medium through processing unit after heat exchange, and again biogas ferment device in material, system operation efficiency is high, the gas generating amount large and stable, whole work energy use rate high.
NOVELTY - The device has a rectangular inner fixing gas cover (2) that is provided on a reinforcing steel bar track (4). A charging basket (5) is moved sequentially in the inner tank (1) such that the raw material in the basket is moved with a certain time in peak period and declining period, after the initial period of time so as to improve the utilization rate of raw material.    USE - Device for moving raw material for producing biogas.    ADVANTAGE - The raw material is moved in the tank reliably. The time and labor force are saved. The cost of producing biogas is reduced. The high efficiency of production of biogas is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for moving raw material for producing biogas.    Inner tank (1)    Rectangular inner fixing gas cover (2)    Air hole (3)    Reinforcing steel bar track (4)    Charging basket (5)
NOVELTY - The electrolyzer comprises water electrolysis tub, ion exchange membrane (10), oxygen flux ball (12,22,32), and hydrogen flow ball (13,23,33,51d). The oxygen flux ball, and the hydrogen flow ball are arranged on both sides of the ion exchange membrane. An electrode (20) pair is installed inside water electrolysis tub and provided with electrolyte inlet hole, which is connected with oxygen flux ball. A groove is installed one surface of oxygen flux ball and provided with a gasket (50), which is placed on corresponding side of electrode.    USE - Electrolyzer.    ADVANTAGE - The electrolyzer comprises water electrolysis tub, ion exchange membrane, oxygen flux ball, and hydrogen flow ball, and thus improves electric decomposition efficiency and prevents ion exchange membrane from damage.    DETAILED DESCRIPTION - The electrolyzer comprises water electrolysis tub, ion exchange membrane, oxygen flux ball, and hydrogen flow ball. The oxygen flux ball, and the hydrogen flow ball are arranged on both sides of the ion exchange membrane. An electrode pair is installed inside water electrolysis tub and provided with electrolyte inlet hole, which is connected with oxygen flux ball. A groove is installed one surface of oxygen flux ball and provided with a gasket, which is placed on corresponding side of electrode. An outer cover is interposed on the inner surface of electrodes provided with an ion substitution film.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an electrolyzer.    Ion exchange membrane (10)    Oxygen flux balls (12,22,32)    Hydrogen flow balls (13,23,33,51d)    Electrode (20)    Outer cover (40)    Gasket (50)
NOVELTY - The electrolyte manufacturing apparatus (1) has a vibrating unit that is installed at one side of an electrolyte premixing tub. A discharging unit ejects a mixed electrolyte within the electrolyte premixing tub to an electrolyte mixed tide (30). A redirect unit alternately supplies the raw material electrolyte to each electrolyte premixing unit. An electrolyte supply unit (20) is provided with the raw material electrolyte of high concentration. A distilled water supply unit (10) discharges the distilled water to the electrolyte mixed tide.    USE - Apparatus for manufacturing electrolyte.    ADVANTAGE - The failure rate of the hydrogen fuel cell which obtains the hydrogen of the high purity through the water electrolysis tub is reduced. Since the electrolyte of the pre-set concentration is consecutively supplied to the electrolyte mixed tide, the productivity of the manufacturing apparatus is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolyte manufacturing apparatus.    Electrolyte manufacturing apparatus (1)    Distilled water supply unit (10)    Electrolyte supply unit (20)    Electrolyte mixed tide (30)    Electrolyte exhaust pump (34)
NOVELTY - A crosslinked thermally rearranged poly(benzoxazole-co-imide) having a repeating unit (I), is new.    USE - New crosslinked thermally rearranged poly(benzoxazole-co-imide) is used in preparation of gas separation membrane (all claimed) used for carbon dioxide/methane separation.    ADVANTAGE - The crosslinked thermally rearranged poly(benzoxazole-co-imide) has excellent sensitivity and permeability.    DETAILED DESCRIPTION - A crosslinked thermally rearranged poly(benzoxazole-co-imide) having a repeating unit of formula (I), is new.    Ar'=aryl chosen from tetravalent 6-24C arylene and tetravalent 4-24C heterocyclyl (both optionally substituted);    Q=single bond, O, S, CO, SO2, Si(CH3)2, (CH2)p, (CF2)q, C(CH3)2, C(CF3)2, CO-NH, C(CH3)(CF3), or optionally substituted phenylene;    p,q=1-10;    x=0.8-0.95;    y=0.05-0.2;and    or x+y=1.    Two or more of aryl form condensed ring together and are linked to each other through O, S, CO, SO2, Si(CH3)2, (CH2)p,(CF2)q, C(CH3)2, C(CF3)2 or CO-NH. INDEPENDENT CLAIMS are included for the following:    (1) preparation of crosslinked thermally rearranged poly(benzoxazole-co-imide);    (2) gas separation membrane (excluding flue gas separation membrane), which comprises the crosslinked thermally rearranged poly(benzoxazole-co-imide); and    (3) preparation of gas separation membrane, which involves obtaining monoesterified o-hydroxypolyimide copolymer, casting a polymer solution containing the monoesterified o-hydroxypolyimide copolymer dissolved in an organic solvent, subjecting the obtained membrane to transesterification crosslinking, and carrying out thermal rearrangement of the crosslinked o-hydroxypolyimide copolymer membrane.
NOVELTY - The system (10) has a controller (70) that operates a second electrochemical cell (40) or a cell stack (20) when hydrogen demand signal is greater than zero and first gas is not available at first electrochemical cell or cell stack inlet. The first cell and cell stack is operated as primary hydrogen source and to operate second cell or cell stack as a secondary hydrogen source to hydrogen demand signal and hydrogen output of first electrochemical cell or cell stack when demand signal is greater than zero and first gas is available at first electrochemical cell or cell stack inlet.    USE - System for providing hydrogen.    ADVANTAGE - The power consumption and operation of the first electrochemical cell is relatively self-regulating. The first electrochemical cell or stack can effectively operate with lower power requirements and/or higher efficiency than the second electrochemical cell or stack.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of providing hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for providing hydrogen.    System for providing hydrogen (10)    Cell stack (20)    Second electrochemical cell (40)    First gas inlet (60)    Controller (70)
NOVELTY - Transmitted film (30) comprises multiple hemisphere type projecting parts which are formed among surface at one side or both sides.    USE - Transmitted film used for manufacturing portable electronic instrument and developing fuel for generating electricity in capacitor (claimed).    ADVANTAGE - The transmitted film improves bonding force between transmitted film and transmitted electrode, and decreases breaking down property of the transmitted film.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of transmitted film.    Transmitted film (30)    Cathode (200a)    Anode (200b)    Anode catalyst layer (203)    Cathode catalyst layer (205)
NOVELTY - The method involves applying ceramic adhesive to joint portions of constituent element so that flow path carrying fuel or oxidant gas inside a fuel cell module (2) are formed in an airtight manner. The applied ceramic adhesive is dried in which drying and hardening process includes hardening process for hardening applied ceramic adhesive. The solvent remaining within ceramic adhesive are eliminated and hardened from ceramic adhesive which was hardened in all workable hardening process, and are dried to a state capable of withstanding temperature rise in a startup procedure.    USE - Method for manufacturing solid oxide fuel cell apparatus for generating electricity (claimed).    ADVANTAGE - The airtightness in the adhered parts is lost when the fuel cell apparatus is first operated and exposed to high temperatures. Thus cracking prone to create airtightness failures is reliably avoided while working efficiency is increased. Since the cracking occurs in ceramic adhesive layers, or airtightness is insufficient, no degradation of fuel cells or extraordinary reduction in performance is triggered, and time required for manufacturing can be reduced, while avoiding major problems. The ceramic adhesive hardening process on the cell joint portions with the particular requirement to secure airtightness can be performed multiple times while efficiently executing the assembly of the fuel cell module, and the two goals of efficient assembly and sufficient airtightness can both be achieved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an apparatus for manufacturing a solid oxide fuel cell apparatus for generating electricity; and    (2) a solid oxide fuel cell apparatus for generating electricity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid oxide fuel cell.    Fuel cell module (2)    Thermal insulation (7)    Entire generating chamber (10)    Exhaust collection chamber (18)    Heat exchanger (34)
NOVELTY - Determination of level of deep gas in near surface formation involves measuring carbon dioxide, oxygen, methane and nitrogen levels from near surface geological samples, adding water vapor content to the measured carbon dioxide, oxygen, methane and nitrogen levels, normalizing the mixture and determining the ratios of oxygen and carbon dioxide to distinguish in-situ vadose zone carbon dioxide from exogenous deep leakage carbon dioxide and carbon dioxide and nitrogen or carbon dioxide and nitrogen/oxygen to determine the degree of oxygen influx and/or consumption.    USE - Determination of level of deep gas in near surface formation (claimed).    ADVANTAGE - The method enables determination of level of deep gas in near surface formation by simple process without requiring the background monitoring.    DETAILED DESCRIPTION - Determination of level of deep gas in near surface formation involves measuring (in vol.%) carbon dioxide, oxygen, methane and nitrogen levels from one or more surface or near surface geological samples, adding water vapor content to the measured carbon dioxide, oxygen, methane and nitrogen levels, normalizing the gas mixture to 100 vol.% or 1 atmospheric total pressure and determining the ratios of oxygen and carbon dioxide to distinguish in-situ vadose zone carbon dioxide from exogenous deep leakage carbon dioxide and carbon dioxide and nitrogen to distinguish whether carbon dioxide is removed from the near surface formation or carbon dioxide is added from exogenous deep leakage input or carbon dioxide and nitrogen/oxygen to determine the degree of oxygen influx and/or consumption. The ratios are indicative of natural in situ carbon dioxide or carbon dioxide from the exogenous deep leakage input.
NOVELTY - The biological gas plant facility has fermenter space (4) which is spaced from a post-fermentation chamber (5) and carrying-in device which are provided for discharging biogas and for heating process. The post-fermentation chamber and carrying-in device are combined together in all the spaces in the form of a horizontal parallelepiped structure whose ratio of length to height is 1: 4. The walls, floor and ceiling are internally coated against a corrosion steel container (15). The corrosion steel container is mounted with a steep slope portion.    USE - Biological gas plant facility.    ADVANTAGE - The fermenter space is spaced from the post-fermentation chamber and carrying-in device which are provided for discharging biogas and for heating process, such that Cost effect is reduced reliably. The flexible structure is realized. The fermenter space is protected. The heat transfer is reduced. The pollution is reduced in short time.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological gas plant facility.    Fermenter space (4)    Post-fermentation chamber (5)    Wide vertical connecting tube (6)    Corrosion steel container (15)    Pipe connection (18)
NOVELTY - The device (300) has a mixing plate (102) formed with a perforation and movably fixed within the liquid (101). A drive mechanism (302) is coupled to move the plate in the liquid to accomplish turbulence in the liquid for maintaining a component in a suspended state.    USE - Mixing device e.g. agitator for photosynthetic organism culturing apparatus, for mixing components e.g. nutrients, solid organic/inorganic chemicals, waste, recyclable materials and biomass in liquid such as manmade/natural liquid (claimed) like pilot/laboratory scale liquid and reservoir/pond for fish rearing and wastewater treatment.    ADVANTAGE - The mixing device helps to keep the solid mass in suspended state, thus improving the efficiency of the process. The volume of mixing is increased by increasing the running length of the mixing device without increasing the motor power. The perforation in the mixing plate consumes less energy due to less resistance for the flow of components through the mixing plate, which in turn improves the mixing quality.    DESCRIPTION OF DRAWING(S) - The drawings show the schematic views of the mixing device.    Liquid (101)    Mixing plate (102)    Mixing device (300)    Guide rail (301)    Drive mechanism (302)
NOVELTY - The cell has a first insertion element (31) which is inserted in cathode gas supply manifold (35), and second insertion element (32) inserted in cathode gas discharge manifold (36). First insertion element is changed, such that first order differential of cross-sectional area becomes negative and second order differential becomes positive as first insertion element progresses from inflow port. Second insertion element is changed, such that first order differential of cross-sectional area becomes negative as second insertion element progresses from discharge port.    USE - Fuel cell for generating power.    ADVANTAGE - Since the first order differential of cross-sectional area becomes negative and second order differential becomes positive as first insertion element progresses from inflow port, and first order differential of cross-sectional area becomes negative as second insertion element progresses from discharge port, distribution property is improved effectively to uniformly distribute the fluid flowed in from the outside to each fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view, top view, and sectional view of the fuel cell.    First insertion element (31)    Second insertion element (32)    Cathode gas supply manifold (35)    Cathode gas discharge manifold (36)    Anode gas supply manifold (37)
NOVELTY - A clean liquid fuel contains 50-75 wt.% methanol, 10-15 wt.% waste alcohol, 13-35 wt.% water, 0.5-1 wt.% toluene, 0.05-0.1 wt.% n-hexane, 0.05-0.1 wt.% ammonium nitrate, 0.5-1.5 wt.% glycerin, 0.1-0.5 wt.% nitric acid, and 0.5-1.5 wt.% acetone.    USE - Clean liquid fuel (claimed).    ADVANTAGE - The fuel has high heat value and flame temperature, no toxic gas and combustion smell, easy to obtain raw materials and clean, and low cost, changes waste to valuable material, and prevents environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of clean liquid fuel which involves adding ammonium nitrate in water, stirring to dissolve, adding glycerin, stirring to dissolve, adding nitric acid to obtain 1st solution, standing for 10-25 minutes, sequentially adding toluene, methanol, and n-hexane in acetone, stirring to obtain 2nd solution, weighing waste alcohol as 3rd solution, and stirring 1st, 2nd, and 3rd solutions.
NOVELTY - Producing butanol involves preparing a seed culture medium, which is inoculated with desired bacterial species, and then incubated at certain conditions to obtain a seed culture broth. A certain amount of inoculum is pipetted out, and then inoculated into a fermentation medium to obtain a fermentation broth. The obtained fermentation broth is then placed into a microbial fuel cell system, where hydrogen as electron donor is generated by the reduction of volatile free acids to obtain butanol as by--product.    USE - Method for producing butanol using volatile fatty acid by anaerobic fermentation.    ADVANTAGE - The method enables to produce butanol in high yield by effectively shortening the fermenting time in an economical manner.
NOVELTY - Pre-processing straw, comprises crushing the straw using a ball mill, and carrying out ozone pre-treatment of the crushed straw.    USE - The method is useful for pre-processing straw including corn straw, rice straw or wheat straw (all claimed).    ADVANTAGE - The method is capable of economically pre-processing the straw with increased enzymolysis efficiency and less energy consumption, and increases the saccharification rate of the straw.
NOVELTY - Preparation of adenosylmethionine by yeast fermentation involves carrying out aerobic fermentation of high-expression adenosylmethionine in yeast fermentation medium, culturing, continuously adding L-methionine precursor, obtaining high-level adenosylmethionine fermentation broth, breaking cell by mixing resultant broth and acid solution, sedimenting and obtaining adenosylmethionine crude extract, mixing crude extract and picric acid solution, obtaining precipitate, stratifying, obtaining adenosylmethionine precipitate, purifying, extracting adenosylmethionine and decolorizing.    USE - Preparation of adenosylmethionine (claimed).    ADVANTAGE - The method enables simple, easy, economical and environmentally-friendly preparation of adenosylmethionine having high and stable quality, and purity of more than 98%.    DETAILED DESCRIPTION - Preparation of adenosylmethionine by yeast fermentation involves carrying out aerobic fermentation of high-expression adenosylmethionine in yeast fermentation medium, culturing by adding 40-45 g/L sucrose for 9-11 hours, culturing at a rate of 1.5 g/hour for 23-25 hours, continuously adding L-methionine precursor until the fermentation is complete, obtaining high-level adenosylmethionine fermentation broth, breaking cell by mixing resultant broth and 15-30 %mass acid solution in volume ratio of 0.8-1:1, maintaining at 3-4 degrees C for 2-3 hours, stratifying supernatant, sedimenting and obtaining adenosylmethionine crude extract, mixing adenosylmethionine crude extract and picric acid solution, adjusting pH value to 2.8-2.9, obtaining precipitate, stratifying, obtaining adenosylmethionine precipitate, purifying resultant precipitate, extracting adenosylmethionine, and decolorizing.
NOVELTY - This utility new type relates to a one fermentation garbage bucket, by upper cover, an outer bucket, inner bucket, container filled with the seal ring, the cover and slide, wherein the annular upper cover is buckled on the outer bucket, inner bucket is set in the outer bucket set of fixed card up. Slide bar installed liquid container corresponding to the inner bucket bottom sliding connect the outer end of a bucket, a feeding cover and a middle cover the inlet screw thread connect, this utility new type convenient to clean, upper cover and the outer bucket is buckled sealing property, but also set with smaller diameter of the feeding port, to open feeding and cover, has a fertilizer leaking in the process of reaction.
NOVELTY - This utility new type claims a one microwave liquid phase plasma alcohol hydrogen device, belonging to the non-discharging alcohol hydrogen. Comprising microwave generator, said inner reactor used for containing reaction object set with a space, a reactor upper part connecting with said composite vacuum meter, a liquid phase discharge electrode is located at the bottom of a space and is welded on said reactor upper, up a liquid phase discharge electrode connecting with said waveguide coaxial cable, a waveguide coaxial cable upper connecting with said microwave generator, a reactor side wall of a part with a discharge tube, a discharge tube in turn connect with a close valve and dry-type vacuum pump, a dry-type vacuum pump connecting with said air discharging valve and gas collecting valve, upper part of said reactor connecting with a feeding pipe, the bottom of said reactor with a material pipe. This utility new type with hydrogen preparing speed is fast, discharge device miniaturization design, can be a simple and convenient of preparing hydrogen.
NOVELTY - This utility new type provide the one used for a surge raw positoin purification of river structure, wherein including along the bank wall of building and set with a platform, and the river bed platform above a forming isolating body, said isolating body in form, isolating body with the river and the river bed form pollutant purification cavity; a pollutant purification chamber and the sewage pipeline connected, and pollutant purification chamber and the connected channel. The building structure engineering is simple, the cost is low, effectively in a river purification, at the same time solves the filling of a river bed mud stacking.
NOVELTY - This utility new type claims a one process aritificial wetland of nitrogen and phosphorus in sewage, comprising a bed body (1), the bed body (1) set with cloth water pipe of one end (2) and the bed body (1) set with water collecting pipe of the other end (3), the bed body (1) inner of cloth water pipe (2) end and (3) end from outside a inner in turn are fill with gravel (4), in the gravel (5) and fine gravel (6), the bed body (1) of middle part from the upper to the lower in turn fill sand (8) and (7), purification is planted with a plant on the sand (8) (9). This utility new type can be valid to prevent filler layer and cloth water pipe and water collecting pipe in area to be blocked, water flow of aritificial wetland in high load, the nitrogen-phosphorus removing effect..
NOVELTY - This utility new type belongs to a technology field of environment-friendly pig raising industry, provide a one pigsty excrement sewage processing device. The main machine frame is set up with the dung dirt pipeline, spiral feeder, heating drying chamber, biogas slurry conveyer pipe, an anaerobic fermentation pool, microorganism inoculating chamber, AO reaction unit, a storage silo, a dung dirt pipeline is inclined set, connected upper end of pigsty excrement discharging groove, spiral material transporting machine is inclined set, upper end and upper end of heating drying chamber connected, lower end connected said biogas slurry conveyer pipe, lower end of biogas slurry conveyer pipe connecting anaerobic fermentation pool, lower end of the dung dirt pipeline connecting a spiral feeder of rear section, microorganism a chamber set on the lower part of heating drying chamber, AO reaction unit set at the bottom of a chamber, microorganism and microorganism and a chamber through pipeline phase with discharging valve of connected. With the existing technology phase compare, the new type one a pigsty excrement sewage processing device has a simple structure, a high efficiency, saves labour resource of.
NOVELTY - One a composting device, comprising a dehydrator, a dehydrator and mix stirrer is connected, mix stirrer with the compost bin, compost chamber and a secondary fermentation chamber is connected, through a solid rear dehydrator dehydrating organic compost according to the a, a water content proportion, mix and auxiliary inner mix in the stirrer, stir the mix of material to compost chamber rear stir process, aerobic process in turn heating, high temperature and cooling the compost temperature 55-60 degrees C degrees centigrade sterilizing for 8-12 days, is sent to a secondary fermentation chamber of the fermentation material rear aerobic, futher process for decomposition of organic substance is not easy to decompose, after 13-16 days, a secondary fermentation, fermenting a clinker with simple structure of environment-friendly.
NOVELTY - This utility new type relates to a composite biological fertilizer of one production device, comprising in turn a crushing mix device of the fermentation device, crushing device, mix device, granulating device, the first screening device and packaging device, fermenting device comprising the first fermentation device and second fermentation device, a crushing device set with dryer, a mix device connect with deliver device, the deliver device a first weighing device, the top end of granulating device set with liquid feed port, a liquid inlet through the fermentation device and water washing machine, set with second weighing device between the first screening device and packaging device, the first screening device a connect with a re-processing device, a processing device and a a second screening device, screening device and the second a second weighing device connect. The whole production process is smooth processing of the production device is simple, environment-friendly, increase the working efficiency, shortens the working time, in a process dust, clean, and it has important application value of.
NOVELTY - This utility new type claims a vegetable waste one of quick composting fermentation device. The device is beautiful and practical, which is a hollow cylinder body, comprising fermenting, sterilizing, monitoring, ventilation, collecting filtered liquid, heat preservation, deodorizing and tool 8 a, a temperature and humidity, and gas pressure sense measure, combine sampling analysis, is provide in a comprehensive data; a steam sterilizing and a temperature and pressure, the highest fermentation temperature 45 degrees C, pressure 0.02 to 0.03MPa; according to the sampling, discharging and cleaning, and a sampling tube and discharge target and prevent the material from the fermentation room falls into the design of cloth pneuma room; device a temperature and pressure fermenting waste increase the rotten degree and bacteria and reduce bacteria and shortening a period, and the effect is better than a temperature and pressure and control normal plastic bucket with the same volume of fermentation, a temperature and pressure for 10 to 12 days, a temperature and pressure for 19 days, control for 37 days, c a withered cucumber wilt a is not detected, and control each of 2 asterisk 103 a.
NOVELTY - This utility new type relates to a one of organic fertilizer production device, comprising a a crushing in turn mix device, the fermentation device, crushing device, mix device, granulating device, the first screening device, second weighing device and packaging device, a screening device comprising the first sieving device and collecting device, collecting device comprising the first weight processing box, and the second processing tank, a second tank weighing device, a first weight processing box and the processing box connecting a second re-processing device, a a processing device and a a second filtering device, a second filtering device comprising box, oscillator, a sliding groove, a storage box and a collecting box, the collecting box and the second weighing device connect. The whole production process is smooth processing of the production device is simple, environment-friendly, increase the working efficiency, shortens the working time, in a process dust, clean, and the first sieving device and simple design of second sieving device is reasonable and practical.
NOVELTY - This utility new type relates to a one bromine chlorine hydantoin production device of piece, orderly comprising the first weighing device, mixer, tabletting device, second weighing device, and a machine outer packing machine mixer set with feeding port, inner port set with spring cover, inner mixing machine is also set with the clean device and stir device, clean device comprising a cleaning device and dust collecting device, a stir device comprising a main shaft, a blade and a bottom leaves, the blade comprising blade and vertical to inclined blade, bottom leaves set at the bottom end of main shaft, the pressing machine connecting device, the pressing device and the second weighing device connect, second weighing device through the outer machine connecting machine. The whole production process is smooth processing of the production device is simple, environment-friendly, increase the working efficiency, shortens the working time, a stir device inner mixing machine has reasonable design, and inner mixing machine set with clean device, the weight of each component of a tablet in a certain and can be valid to avoid the cross pollution and so on.
NOVELTY - This utility model new supply of one of organic material dry distillation cracking gasification furnace, comprising: cracking gasification furnace body, the gasification furnace body equipped with feedstock cracking port and air outlet, multiple of distillation, the multi-number and place in the dry distillation cracking gasification furnace in the adjacent gap and turn on two of dry distillation chamber between, each of the dry distillation chamber bottom are provided with material port arrange, and electric heating bar, electric heating rod vertical of the setting as to the material in the multiple dry distillation chamber for isolating the whole dry distillation in the multi-air of indoor dry distillation, to produce solid carbon material and carbonization. According to organic material dry distillation cracking gasification furnace of this utility model can be updated without pollute extent of use such as the material of low-rank coal, oil page rock foam equal, for maximum use of the organic material.
NOVELTY - A one plant waste preparing biological carbon and bio-oil, a gas device, tube by leg support, a tube top plate is provided with a chamber hole, upper part of a feeding tube, a feeding cylinder is feeding cover. Inner tube with air inlet cover, inner cylinder, in the cylinder, a cover with pneuma hole and air hole are distributed on the cylinder wall of upper cover and the top plate. A pyrolysis chamber is inner cylinder form a cavity, pneuma room is cavity cylinder and the inner cylinder formed in a chamber cavity tube is in the form of cylinder. The air inlet pipe passes through the tube bottom plate of air inlet cover connected with the air pipe, the carbon tube passes through the tube and, in cylinder, pneuma room, inner cylinder and the pyrolysis room connected, the oil tube, an exhaust tube passes through the tube and, in pneuma room connected with the cylinder, the water pipe, the water inlet pipe passes through the water room connected tube.
NOVELTY - This utility new type of target is feeding system provides a safe one of a fixed bed gasification furnace of. This utility new type of a fixed bed gasification furnace feeding system comprising a gasification furnace and the gasification furnace upper part set with a bracket, a upper mounting bracket with a trolley bracket along the moving of the trolley through a motor and a lifting rope on the electrical machine shaft is hung a lifting hopper of; a of a top part set with a open and close of the feeding door, a discharging port of the bottom set with a discharging door, one end a discharge door through a side wall of the rotating shaft and a connecting, directly or through connecting piece and a lifting rope connecting, said gasification furnace top feeding port and set with sliding door, the shape size of said discharge hole is connected with the feeding port are identical, two said side feeding port set with a horizontal guide rail, a sliding door is set on the horizontal guide rail up activity, and moving along the horizontal guide rail below the drive of cylinder, to open or close; a feeding port is further set with insulating water seal structure.
NOVELTY - This utility new type claims a rice hull gasification furnace of one locking device, comprising the storage hopper, a close air inlet of the, locking device and lower inflation airlock, a airlock of said feeding port and the material exit is connected with a feeding port of the inflation of a close air inlet of the locking device is connected with a lower discharge hole of feeding port is connected with lock inflation of airlock, airlock below a discharge hole is material exit, said inflation locking device is provided with an air inlet, a one end a supply system of the inert gas source, and the other end is connected with the air inlet of inflation lock is connected with airlock entering into such a storage bin by a blast of inert gas into the inner inflation lock part, a part of the material lower airlock of exit is discharged into the atmosphere, so as to prevent material a gas exchange with the external environment, at the same time, make the material a dry row material, collecting the material to a, compared with the existing technology, the air lock device a valid row material collection cost is reduced, and use safe and reliable.
NOVELTY - This utility new type belongs to the carbonizing rice hull processing device, relates to a one for slag dry cooling of a moving bed gasification rice shell vertical to a spray cooling device, comprising air injection system and cooling water supplied system, a pipeline and a water supply pipeline of cooling water system of a system meeting air injection nozzle, using aerosol combine a method for fire bed ash slag dry cooling process, the temperature for a very sensitive, cooling of high reliability.
NOVELTY - This utility new type claims a one wood biomass granule fuel production device, comprising in turn a sawdust of crusher, a drier and extrusion molding, ton material room set with a dryer and between the extrusion molding, for transfer wooden meal raw material and a moisture content of wood raw material. The wooden meal as raw material to prepare wood biomass granule fuel, the production method has simple process, fit the industrialization production, preparation of wooden biomass granule fuel, the combustion rate and heat efficiency is high.
NOVELTY - This utility new type claims a one for a waste of device, said device comprising a and a connecting a power source with a crusher, the first belt conveyor, sieving device, second belt conveyor, the first separator, a winnowing machine, the third belt conveyor and fine crusher, a crusher, the first belt conveyor, sieving device, second belt conveyor, the first separator, a winnowing machine, belt conveyor and third crusher in turn or a set. After domestic garbage into a coarse roughing, after the first belt conveyor to a sieving, sieving the second rear conveyor belt to the first separator, a rear magnetic separation by a winnowing machine, and then conveying to a fine crusher through the third belt conveyor, wherein the rear of fine manufacturing domestic garbage derived fuel to finish the process and for use of domestic garbage, the domestic garbage for solves the problem of bad affect of human life.
NOVELTY - This utility new type claims a one high acid value grease continuous prepare biology diesel oil of c, category oil chemical industry technology field. The device comprising raw material mixer, a metering pump, a sieve fill reactor I, a sieve fill reactor II, a heater, a separator, a distilling tower, a cooler, a three-way valve I and triple valve II, the three-way valve III, the three-way valve IV, three-way valve V, as water of esterification product one is removed in time, esterification reaction completely so that a direction of a biological diesel oil process, increase the conversion rate of biological diesel oil, use only two molecule sieve fill esterification reactor connected in parallel, only one work, the other one can proceed regeneration processing, mutually and alternately, to ensure a continuous operation, realize the continuous preparation of biological diesel oil, the technology is simple, operation is convenient, high efficiency, no pollution, low energy consumption and a clean process, continuous production of.
NOVELTY - This utility new type claims a alcohol mash liquid generate one of a marsh gas power generation, alcohol mash liquid pool (1) by a pipeline to anaerobic generator (2), an anaerobic generator and marsh gas desulfurization purifier (3), gas filter (4), gas mixer (5), a drying gas with turbocharger (6), fire arrestor (7), an electromagnetic valve (8), a constant (9), an air storage tank (10), a methane generator set (11) connect in turn. This utility new type has the advantages of alcohol enterprise uses for this technology is a valid one in one a bottomless and inexhaustible of a renewable energy resource, alcohol waste mash a marsh gas generating is efficient use of clean, low discharge, economic property is good and use much attention, not only a clean supply of electric energy, but also can solve the problem of environment pollution, changes waste into valuable, realize resource comprehensive utilization and reduce emission of greenhouse gas.
NOVELTY - Two side this utility new type claims a one hydrogen oxygen gas generating device and a vehicle thereof, device comprising electrolytic groove and is a positive pole, negative pole, clapboard, anode pole and cathode pole a inner electrolysis groove of the clapboard, further comprising water supplying tank, a solvent tank, replenishing pneuma water separator, a pressurizing pump, a one-way valve, a gas storage room, one-way valve, water supply tank and solvent supply tank through pipeline with electrolytic groove is connected with a electrolytic groove at one side is connected with third pole, a electrolytic groove nagetive pole located at one side connected with the first pneuma channel, and through the first channel with the gas storage room, the pneuma pneuma water separator, a pressurizing pump, a one-way check valve in turn is set on the first channel a pneuma according to electrolytic groove to storage a room, a storage room is connected with a second air passage, a one-way valve is set on the second channel a pneuma. Vehicle, comprising the vehicle frame and engine, further comprising the the hydrogen oxygen gas generating device. The vehicle is not needed with fuel oil or gas, solves the problem of energy shortage problem, there is no tail pneuma.
NOVELTY - This utility new type claims a one-type drying machine and comprising a biomass granule fuel wood production device, a dryer of the type comprising heating device, feeding device, drying device and dust-removing device, the heating device comprising calcining furnace, hopper, a hopper through conveyer belt and the extrusion molding machine discharging port a, used for input the biomass wood fuel product as a fuel part is set on air blower of a calcining furnace and is set on the bottom of the calcining furnace. The conditions, local materials, it does not need additional heat source; in addition, the calcining furnace burning biomass granule fuel wood product to detect the combustion heat value, combustion rate and heat efficiency so as to quality of real time monitoring of biomass granule fuel finished product and the wooden meal.
NOVELTY - The device has a hydrogen fuel cylinder fixed on an inner part of a seal cavity. A bottom part of the hydrogen fuel cylinder is provided with a liquid inlet. A liquid phase is formed with an entrance part of the seal cavity and connected with the liquid inlet. An entrance part of the liquid phase is fixed with a seal valve that is provided with a cutting off pipeline, where the liquid phase is a water or alcohol-containing liquid phase. A vacuum system is formed with the seal cavity. Liquid phase material is added in the alcohol-containing liquid phase.    USE - Self-interrupt hydrogen making device.    ADVANTAGE - The device is portable to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic block diagram of a self-interrupt hydrogen making device.
NOVELTY - Insect attractant comprises an allelochemical obtained from Mikania micrantha, where myrcene is dissolved in dichloromethane to control the concentration of the attractant to 10-4 g/ml.    USE - The insect attractant is useful for attracting bugs (claimed) such as male and female adult bugs.    ADVANTAGE - The insect attractant can be prepared in an environment-friendly, economical and simple manner, and has strong attracting effect.
NOVELTY - Composite multifunctional biological foliar fertilizer comprises Rhizopus stolonifer fermentation liquid and Trichoderma viride fermentation liquid.    USE - The composite multifunctional biological foliar fertilizer is useful for preventing aphid, Trialeurodes vaporariorum, cabbage butterfly, red spider, other pests, and its eggs.    ADVANTAGE - The composite multifunctional biological foliar fertilizer is eco-friendly and a high efficient organic fertilizer, and reduces pesticide use and degrades pesticide residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing composite multifunctional biological foliar fertilizer comprising uniformly mixing 30-45 pts. wt. Rhizopus stolonifer fermentation liquid, 30-45 pts. wt. Trichoderma viride fermentation liquid, 1-3 pts. wt. sodium borate, 0.5-1.5 pts. wt. water-soluble chitin, 1-2 pts. wt. potassium fulvate and 5-13 pts. wt. composite amino acid powder.
NOVELTY - Producing nutritive soil involves stirring phosphogypsum in stirrer to obtain nutritive soil sheet that is dried in microwave at 60-100 degrees C for 30-120 minutes. Dried nutritive soil sheets are sterilized, cooled and packed. Nutritive soil comprises (in wt.%): dehydrated phosphogypsum (15-35), acidified waste matter (25-55), high-viscosity attapulgite clay (2-15), porcelain granule (2-15), pulverized peat (2-15), biogas residue (2-15), plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and super absorbent resin (0.1-5).    USE - Methods for producing nutritive soil (claimed) used for reducing pathogenic bacteria and pest i.e. harmful for plant.    ADVANTAGE - The method enables to produce nutritive soil that ensures normal growth and development of plant by providing nutritional elements.
NOVELTY - Organic fertilizer comprises (in pts.wt.): grass (30-45), Sorghum (24-36), gourd vine (6-8), fulvic acid (6-8), monoammonium phosphate (5-6), potassium (4-5), zinc sulfate (4-5), manganese sulfate (3-4), aluminum silicate (3-5), pine needle (3-5), microbial inoculum (4-5), ferrous sulfate (4-5), sulfur (3-4), celestite powder (3-4), ethylene diamine tetraacetate chelated zinc (2-4), flint clay powder (2-3), soil conditioning agent (9-11) and balanced amount of water. Soil conditioning agent (in pts.wt.): kaolin (40-50), medical stone (20-30), sludge (12-18) and zinc sulfate (12-16).    USE - Organic fertilizer used for growing blueberry (claimed).    ADVANTAGE - The organic fertilizer is economic.    DETAILED DESCRIPTION - Organic fertilizer comprises (in pts.wt.): grass (30-45), Sorghum (24-36), gourd vine (6-8), fulvic acid (6-8), monoammonium phosphate (5-6), potassium (4-5), zinc sulfate (4-5), manganese sulfate (3-4), aluminum silicate (3-5), pine needle (3-5), microbial inoculum (4-5), ferrous sulfate (4-5), sulfur (3-4), celestite powder (3-4), ethylene diamine tetraacetate chelated zinc (2-4), flint clay powder (2-3), soil conditioning agent (9-11) and balanced amount of water. Soil conditioning agent (in pts.wt.): kaolin (40-50), medical stone (20-30), sludge (12-18), zinc sulfate (12-16), pumpkin (10-12), apple (8-10), dickite (6-8), diammonium phosphate (6-8), clamshell (5-8), borax (5-6), sulfuric acid (5-6), ivory mussel powder (4-5), apple shell powder (3-4) and feather meal (2-3).
NOVELTY - This utility new type claims a one acid collecting device, comprising a self-return tank the bottom of product flow pipe, isobutyric collecting device further comprising a product collecting tank and a product tank, outflow tube with reflux pump, return pipe of a connecting end with a forced return pipe and a product collecting tube, product collecting pipe end of a second output pipe is provided with a product collecting tank of the first output pipe and a tank connecting of the product, a product a tank connecting with a product output pipe, a product collecting tank is equipped with the sampling pipe, a forced reflowing pipe, collecting pipe, a first pipe and a second output pipe is equipped with a valve. This utility new type high-efficiency, energy-saving and capable of realize the acid collecting process, the purity of the product and process advantages can be of a time in real time.
NOVELTY - A vertical one aerobic fermentation storehouse, belonging to the garbage processing device, comprising a tank body, a tank body inner set with distributing device, a ventilation device, a tank body comprising tank top and tank bottom, a side wall, a bottom set with a discharging port, a tank top set with a feeding port, the inner tank body is also set with stir, turning device, stir, turning device comprising centre shaft, fixing a spiral, drive motor and transmission device to the centre axis a. This utility new type vertical aerobic fermentation storehouse, can make the material loose, avoiding plate, enhance aerobic fermentation effect.
NOVELTY - The reaction device has an oxygen carrier rotor fixed with a gas channel (822) that is formed with a honeycomb hole (821). A gas output device (10) is parallelly connected with a middle shaft of a gas seal plate. A pneumatic room is provided with a fan-shaped unit, a pyrolysis rear pneumatic room, a hydrogen gas output room and a gas exhaust pneumatic room. A gas inlet room and the hydrogen gas output room are connected with the gas exhaust pneumatic room. A position of a pyrolysis pneumatic output channel (6) is connected with a pyrolysis pneumatic inlet room.    USE - Bio-mass pyrolysis and chemical chain made hydrogen continuous reaction device.    ADVANTAGE - The device is environment-friendly and convenient to use, and has wide range of applications, and improves hydrogen purity and avoids tar.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bio-mass pyrolysis and chemical chain made hydrogen continuous reaction device manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a bio-mass pyrolysis and chemical chain made hydrogen continuous reaction device.    Feed inlet (1)    Pyrolysis pneumatic output channel (6)    Gas output device (10)    Honeycomb hole (821)    Gas channel (822)
NOVELTY - Manufacturing fiber sheet involves crushing garden waste process to obtain garden waste particle (1-20 mm), where garden waste is selected from tree limbs, branches or leaves by clippings and pruning methods. The garden waste particle is softened in a mold by adding water (80-90%) and microorganism (1-3%) and pH value is adjusted to 7.5-8.0. Fermentation is carried out in the mold at 60-65 degrees C for 48-90 hours to obtain a softening material, from which solid and liquid materials are separated and then concentrated to obtain concentrated liquid.    USE - Method for manufacturing fiber sheet (claimed).    ADVANTAGE - The method enables to manufacture fiber sheet, where liquid is enriched in nitrogen, potassium, organic matter and nutritional component.    DETAILED DESCRIPTION - Manufacturing fiber sheet involves crushing garden waste process to obtain garden waste particle (1-20 mm), where garden waste is selected from tree limbs, branches or leaves by clippings and pruning methods. The garden waste particle is softened in a mold by adding water (80-90%) and microorganism (1-3%) and pH value is adjusted to 7.5-8.0. Fermentation is carried out in the mold at 60-65 degrees C for 48-90 hours to obtain a softening material, from which solid and liquid materials are separated and then concentrated to obtain concentrated liquid. The concentrated liquid is sterilized at high temperature by using spray granulation method to obtain an organic fertilizer. The organic fertilizer is subjected to solid grinding process by using a disk mill at 100-110 degrees C for 1-5 minutes to obtain a slurry. The slurry is concentrated to obtain pulpy material, which is dried to obtain the fiber sheet.
NOVELTY - Fertilizer comprises (wt.%): crop straw (92.7), wheat bran (4), brown sugar (0.6), corn starch (0.7) and composite microorganism strain (2).    USE - Fertilizer used for improving soil fertility and improving growth of crop.    ADVANTAGE - The fertilizer increases crop yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer which involves:    (A) mixing raw materials; and    (B) heating materials at 50-55 degrees C for 10 hours and then turning the materials for 6-8 times to obtain the product.
NOVELTY - Manufacturing fertilizer involves fermenting tea oil by using fresh rice bran (0.1 wt.%), hametz and diluting agent to obtain a tea cake. Rice bran (5 kg) is required for 1 kilogram fertilizer, where water regulating agent is added in the tea cake and then crushed to obtain granules. The granules are stirred uniformly and subjected to aerobic fermentation, where air is passed at normal temperature for 48 hours, and then temperatue is increased at 50-60 degrees C.    USE - Method for manufacturing fertilizer (claimed).    ADVANTAGE - The method enables to manufacture fertilizer in a cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Manufacturing fertilizer involves fermenting tea oil by using fresh rice bran (0.1 wt.%), hametz and diluting agent to obtain a tea cake. Rice bran (5 kg) is required for 1 kilogram fertilizer, where water regulating agent is added in the tea cake and then crushed to obtain granules. The granules are stirred uniformly and subjected to aerobic fermentation, where air is passed at normal temperature for 48 hours, and then temperatue is increased at 50-60 degrees C. Third day temperatue is maintained at 70 degrees C and decreased to 55-65 degrees C and then oxygen is supplied for 6-8 days in a container at normal temperature.
NOVELTY - Preparing organic fertilizer involves mixing raw materials and then regulating water content to 50-70%. The raw materials are stacked and then fermented at 45 degrees C to obtain fermented materials. The stacked materials are mixed and then water content is regulated to 45%. The stacked are again fermented at 45 degrees C for 20 days to obtain the product.    USE - Method for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prevent the loss of nitrogen content during fermentation.
NOVELTY - Preparing bio-organic fertilizer involves drying and crushing fertilizer according to appropriate nutrient content, where obtained fertilizer powder is granulated using disk granulator at 50 degrees C or below to obtain bio-organic fertilizer.    USE - Method for preparing bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-organic fertilizer in simple and cost-effective manner.
NOVELTY - Fertilizer comprises (in wt.%): rotten manure (10-30), humic acid (10-30), urea (10-20), calcium magnesium phosphate fertilizer (20-40), potassium chloride (10-15), borax (0.5-2), zinc sulfate (0.5-2), ammonium molybdate (0.01-0.05), sodium nitrophenolate (0.005-0.02), alpha-sodium naphthylacetate (0.001-0.01), hymexazol (0.01-0.05) and diazinon (0.01-0.05).    USE - Fertilizer used for reducing peanut continuous cropping obstacles (claimed).    ADVANTAGE - The fertilizer increase peanut yield in simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) fermenting rotten manure and humic acid;    (B) crushing mixture into particles;    (C) mixing urea, calcium-magnesia phosphate fertilizer, potassium chloride, borax, zinc sulfate, ammonium molybdate, sodium nitrophenolate and alpha-sodium naphthylacetate to obtain mixture;    (D) granulating obtained mixture;    (E) adding diazine and hymexazol with granule to obtain product; and    (F) packing and storing obtained product.
NOVELTY - Fertilizer comprises (in pts.wt.): plant ash (40-45), manure (10-12), urea (20-23), boron (3-5), potassium dihydrogen phosphate (8-10) and bark (30-35).    USE - Fertilizer used for promoting growth of wheat (claimed).    ADVANTAGE - The fertilizer increases disease resistance and taste of wheat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) weighing raw materials and then crushing to obtain powder;    (B) mixing powder and then fermenting at 45-65 degrees C for 10 days to obtain fermentation product; and    (C) granulating fermentation product and then packing to obtain the finished product.
NOVELTY - Fertilizer comprises (in pts.wt.): poultry manure (52-65), plant ash (22-28), potassium dihydrogen phosphate (11-15), rapeseed cake (10-16), Chinese herbal medicine (5-8) and manure fermentation agent (1-3).    USE - Fertilizer used for promoting growth of Litsea cubeba (claimed).    ADVANTAGE - The fertilizer increases yield and disease resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) crushing poultry manure, plant ash, potassium dihydrogen phosphate, rapeseed cake and Chinese herbal medicinal to obtain and then mixing to obtain mixture; and    (B) adding manure fermentation agent into mixture and then fermenting at 50-70 degrees C for 30-35 days to obtain the product.
NOVELTY - Biological fertilizer comprises (in pts.wt.): seaweed (5-50), sodium nitrophenolate (5-20), urea (150-450), triple superphosphate (200-500), potassium sulfate (100-350), calcium superphosphate, calcium-magnesium phosphate fertilizer (20-200), EDTA chelated trace elements (0-20) and microbial agents (10-40). The raw material is extracted with alkali, filtered, concentrated, and then nitrogen-containing urea is added to the product.    USE - Biological fertilizer.    ADVANTAGE - The biological fertilizer ensures balanced nutrient, increases the utilization ratio of fertilizer and soil improvement, and improves the quality of the crop.    DETAILED DESCRIPTION - Biological fertilizer comprises (in pts.wt.): seaweed (5-50), sodium nitrophenolate (5-20), urea (150-450), triple superphosphate (200-500), potassium sulfate (100-350), calcium superphosphate, calcium-magnesium phosphate fertilizer (20-200), EDTA chelated trace elements (0-20) and microbial agents (10-40). The raw material is extracted with alkali, filtered, concentrated, and then nitrogen-containing urea is added to the product. Potassium sulfate, calcium-magnesium phosphate fertilizer and EDTA chelated trace elements are also added to the product, and then processed to obtain the desired product. An INDEPENDENT CLAIM is included for a method for preparing biological fertilizer, which involves:    (A) mixing seaweed powder, sodium nitrophenolate, urea, triple superphosphate, potassium sulfate, calcium-magnesium phosphate fertilizer and EDTA chelated trace elements in a groove;    (B) crushing the mixture in a crusher;    (C) granulating the crushed material at 40-50 degrees C; and    (D) drying the material at 65-75 degrees C to obtain the finished product.
NOVELTY - Fertilizer comprises (in pts.wt.): urea (200-500), superphosphate (200-500), potassium sulfate (150-350), Chrysanthemum powder (20-60), humic acid (5-30), Bacillus thuringiensis powder (20-50), Serratia (20-50), polyaspartic acid (10-50) and EDTA (1-30).    USE - Fertilizer used as insect repellent (claimed), for promoting growth of crop and killing nematode.    ADVANTAGE - Fertilizer improves the quality of crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing urea, superphosphate, potassium sulfate, Chrysanthemum powder, humic acid, polyaspartic acid and EDTA to obtain mixture;    (B) spraying mixture to obtain granules;    (C) drying granules at 60-75 degrees C and then cooling; and    (D) sieving the granules and then packing to obtain the finished prodcut.
NOVELTY - Biological organic fertilizer comprises Bacillus subtilis with earthworm manure. The obtained mixture is stirred uniformly.    USE - Biological organic fertilizer used for planting and cropping watermelon (claimed) and used as base fertilizer.    ADVANTAGE - The biological organic fertilizer has improved nitrogen content (0.95-2.5%), phosphorus content (1.1-2.9%), potassium content (0.96-2.2%), organic matter (25-38%), humic substance (21-40%), beneficial bacterium number (5000-5000 million per gram), mineral trace element and amino acid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for fermenting Bacillus subtilis, which involves:    (A) utilizing solid fermentation culture medium, which comprises bran (19.5 g), chaff (0.5 g) and soybean meal (1.0-22 ml);    (B) adding tap water (20-22 ml) to the obtained culture medium;    (C) stirring the obtained culture medium uniformly;    (D) adding the obtained culture medium in a triangular bottle (250 ml);    (E) heating the obtained culture medium at 121 degrees C for 30 minutes;    (F) cooling the obtained culture medium;    (G) inoculating Bacillus subtilis inoculation liquid (0.9 ml) to the obtained culture medium;    (H) placing the obtained mixture at 37 degrees C in a culture box for 48 hours;    (I) drying the fermented product at 60 degrees C; and    (J) crushing the dried product to obtain the desired product.
NOVELTY - Synthesis of pyrazole derivative (I) involves reacting dicarbonyl compound (Ia) and phenylhydrazine hydrochloride (Ib) in presence of bis-sulfonic acid ionic liquid (Ic) as catalyst under microwave irradiation.    USE - Synthesis of pyrazole derivative (claimed).    ADVANTAGE - The pyrazole derivative is synthesized by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Synthesis of pyrazole derivative of formula (I) involves reacting dicarbonyl compound of formula (Ia) and phenylhydrazine hydrochloride of formula (Ib) in presence of bis-sulfonic acid ionic liquid of formula (Ic) as catalyst under microwave irradiation.    R1=H or ethyl;    R2=methyl or ethoxy;and    R3=phenyl, p-chlorophenyl or 2,4-dimethylphenyl.
NOVELTY - Hexamethylenetetramine and ethanol as solvent are added to N-(2-benzoyl-4-chlorophenyl)-2-chloroacetamide (III) which is obtained using 2-benzoyl-4-chloroaniline (II), stirred, heated at 50-60 degrees C. Ammonium bicarbonate is added to the reaction mixture, and reacted at 40-80 degrees C for 4-6 hours to obtain 7-chloro-5-phenyl-2,3-dihydro-1H-1,4-benzodiazepin-2-one (IV). Phosphorus pentasulfide is added to the obtained product (IV), stirred, reacted at 75-85 degrees C for 4-8 hours, cooled, dried and filtered, to obtain crude product of 7-chloro-5-phenyl-2,3-dihydro-1H-1,4-benzodiazepine-2-thione (V).    USE - Preparation of 7-chloro-5-phenyl-2,3-dihydro-1H-1,4-benzodiazepine-2-thione used as intermediate for manufacturing alprazolam.    ADVANTAGE - The method enables preparation of 7-chloro-5-phenyl-2,3-dihydro-1H-1,4-benzodiazepine-2-thione with high productivity under mild condition by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Hexamethylenetetramine and ethanol as solvent are added to N-(2-benzoyl-4-chlorophenyl)-2-chloroacetamide of formula (III) which is obtained using 2-benzoyl-4-chloroaniline of formula (II), stirred, heated at 50-60 degrees C. Ammonium bicarbonate is added to the reaction mixture, and reacted at 40-80 degrees C for 4-6 hours to obtain 7-chloro-5-phenyl-2,3-dihydro-1H-1,4-benzodiazepin-2-one of formula (IV). Phosphorus pentasulfide is added to the obtained product (IV), stirred, reacted at 75-85 degrees C for 4-8 hours, cooled, dried and filtered, to obtain crude product of 7-chloro-5-phenyl-2,3-dihydro-1H-1,4-benzodiazepine-2-thione (V).
NOVELTY - Cyclic reaction of caffeine intermediate, comprises carrying out catalytic reaction by using a catalyst system comprising ethylamine, adding water, and carrying out cyclic reaction of 1,3-dimethyl-4-amino-5-carboxamido semicarbazide hydrochloride with 1,3-dimethyl 2'-deoxy-2'-fluoro- beta -D-arabinouridine (FAU), to obtain the product, where the weight ratio of 1,3-dimethyl FAU, water and catalyst system, is 1:4-8:0.5-2.    USE - The method is useful in cyclic reaction of caffeine intermediate (claimed).    ADVANTAGE - The method increases the yield of theophylline; is environmental friendly; has low processing pressure, and low production cost; produces high quality product; and easily controllable, and operating procedures.
NOVELTY - Preparing nitrogen containing heteroaryl substituted 3-amino-4-phenyl-butan-1-one compounds (I) comprises performing conversion reaction of heteroaryl substituted (S)-3-amino-4-phenyl-butan-1-one compounds (II) with a thiol in presence of radical initiator.    USE - The method is useful for nitrogen containing heteroaryl substituted 3-amino-4-phenyl-butan-1-one compounds (claimed).    ADVANTAGE - The method recycles the waste, reduces the production cost and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing nitrogen containing heteroaryl substituted 3-amino-4-phenyl-butan-1-one compounds of formula (I) comprises performing conversion reaction of heteroaryl substituted (S)-3-amino-4-phenyl-butan-1-one compounds of formula (II) with a thiol in presence of radical initiator.    A = phenyl (optionally substituted with 1-5 halo or CF3);    X = N or CR2;    R2 = H, 1-6C alkyl (optionally substituted with 1-5 F) or phenyl(optionally substituted 1-3 F, OCH3 or OCF3); and    R1 = H or 1-6C alkyl (optionally substituted with 1-5 fluoro or phenyl).
NOVELTY - Utilization of glyphosate mother liquor resource involves: removing solid insoluble impurities in raw mother glyphosate liquid, separating triethylamine from raw glyphosate mother liquid by preprocessing, subjecting the obtained mother liquid to first stage membrane treatment, acidifying, entering it into second stage treatment, acidifying, then entering it into three-exchange membrane electrodialysis desalting treatment, combing the three stage treatment liquid to form fourth level treatment liquid, diluted it and then passing it into first stage membrane treatment.    USE - For utilization of glyphosate mother liquor resource to prepare glyphosate (claimed) which used as pesticide.    ADVANTAGE - The process provides simple operation; and is environment friendly.
NOVELTY - Preparation of 25-hydroxycholesterol involves taking desmosterol derivative, adding hydroxyl group-containing reagent in an organic solvent in presence of a catalyst at a low temperature of -40 degrees C to 150 degrees C for 1-40 hours, completing reaction by alkaline hydrolysis, and subjecting the reaction solution to further separation treatment to obtain 25-hydroxycholesterol.    USE - For the preparation of 25-hydroxycholesterol (claimed) used as vitamin D3 active metabolite for promoting bone development in poultry animal, for promoting bone density, for reducing chick death rate, for reducing osteoporosis and fatigue in cage egg chicken, for improving eggshell quality, for increasing egg hatchability and for prolonging egg laying period.    ADVANTAGE - The method uses easily available raw materials, causes reduced environmental pollution, has easy operation, is convenient to carry out, has mild reaction condition, has simple operation, has good selectivity, exhibits high efficiency, and provides product in high yield. The method has simple processing, allows easy separation of product, and is easy to be industrialized. The method is highly efficient, environment friendly, allows industrial scale synthesis of the compound, and provides high economic and social benefits.    DETAILED DESCRIPTION - Preparation of 25-hydroxycholesterol of formula (I) involves taking desmosterol derivative of formula (II), adding hydroxyl group-containing reagent of formula R2-OH (III) in an organic solvent in presence of a catalyst at a low temperature of -40 degrees C to 150 degrees C for 1-40 hours, completing reaction by alkaline hydrolysis, and subjecting the reaction solution to further separation treatment to obtain 25-hydroxycholesterol (I).    R1 and R2=H or 1-12C acyl.
NOVELTY - A water-biomass catalytic pyrolysis method involves utilizing biomass feedstock for the dehydration process. Water content of less than 30% is utilized in biomass feedstock at atmospheric pressure, at 550-800 degrees C into lower middle calorific value of the gas and the solid residue. The solid residue is separated from the lower phase of the calorific value of gas out of the reaction system, followed by producing gas at low calorific value after pyrolysis, eliminating tars and reducing the content of methane and other hydrocarbons, increasing the gas content and circulating water to be cool down.    USE - Water-biomass catalytic pyrolysis method.    ADVANTAGE - The method enables producing low biomass ash, zero pollution, low carbon, anthracite dust, high combustion rate, in simple and cost effective manner.    DETAILED DESCRIPTION - A water-biomass catalytic pyrolysis method involves utilizing biomass feedstock for the dehydration process, so that the total water content of less than 30% of the biomass feedstock, including firewood, timber, biogas, rice husk, corn stalks, rice straw, wheat straw and organic waste. Water content of less than 30% is utilized in biomass feedstock at atmospheric pressure, at 550-800 degrees C into lower middle calorific value of the gas and the solid residue. The solid residue is separated from the lower phase of the calorific value of the gas out of the reaction system, the combustion of solid phase residue again provide energy, followed by producing gas at low calorific value after pyrolysis at 1000-1500 degrees C under cracking conditions, eliminating tars and reducing the content of methane and other hydrocarbons, increasing the gas content and yield of the product hydrogen to form a high calorific value gas, and circulating water to be cool down.
NOVELTY - This utility new type inner claims a defective one urea recovery processing system, wherein comprising dissolution groove (1), sedimentation groove (2), a pump (3) and collecting groove (4), a dissolution groove (1), groove (2), a pump (3) and collecting groove (4) through pipeline in turn in series, said dissolution groove (1) is set with rough (5); the dissolution groove (1) of liquid inlet pipe connect said rough (5), a sedimentation groove (2) is set with inner (6), the sedimentation groove (2) liquid inlet pipe of said access (6). This utility new type one a defective urea recovery processing system, which not only solves the problem that the waste material to a pressure treatment, which reduces the environmental pollution and reaches the energy-saving and consumption-reducing, changes waste into valuable, and reduces a production cost of urea product, at the same time, the implementation of space technology, low investment and operation is simple and easy to operate.
NOVELTY - Porphyrin derivates (I) are new.    USE - (I) are useful for application of research and development of anti-oxidation medicine.    ADVANTAGE - (I) are environmentally friendly, simple to prepare and easy to use, and have good bioavailability.    DETAILED DESCRIPTION - Porphyrin derivates of formula (I), are new.    M = Zn, Ni, Mn, La, Ce, Lu, Tm, Pr, Nd, Sm, Yb, Cu, Fe, Zr, Eu, Cd, Ru, Mg, Co, or H;    R1 = -OH, -OCH3, -OCH2CH3, -OCH2CH2OH, -NH2, -NHCH3, -NH(CH3)2, -NHCH2CH3, -N(CH2CH3)2; and    R2 = (2,3-dihydroxyphenyl), (2,5-dihydroxyphenyl), (2,6-dihydroxyphenyl), (2-hydroxyphenyl), (2-aminophenyl), (2,3-diaminophenyl), (2,6-diaminophenyl), (2,3,4-trihydroxyphenyl), (2,3,6-trihydroxyphenyl), (2,4,6-trihydroxyphenyl), (2,5-diaminophenyl), (2-hydroxy-3-methoxy-phenyl), (2-hydroxy-3-methyl-phenyl), (2-hydroxy-5-methyl-phenyl), (2-hydroxy-6-methyl-phenyl), (2,3,4-triaminophenyl), (2,3,6-triaminophenyl), (2,4,6-triaminophenyl), (2-amino-3-hydroxy-phenyl), (2-hydroxy-5-methoxy-phenyl), (2-hydroxy-6-methoxy-phenyl), (2-amino-5-hydroxy-phenyl), (2-amino-6-hydroxy-phenyl), (1-hydroxy-2-naphthyl), (2-hydroxy-1-naphthyl), 1H-indol-3-yl, 1H-pyrrol-2-yl, (3-carboxy-2-hydroxy-phenyl), 2-furyl, 2-carboxy-4,5,6-hydroxyphenyl or 2-thienyl.    An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - A peanut fertilizer comprises 12-33 wt.% organic substrates; 5-9 wt.% inorganic substrate; and 62-79 wt.% nitrogen fertilizer, potassium fertilizer, and active calcium phosphate fertilizer. The active calcium phosphate fertilizer is prepared by adding 30-40 pts. mass mud carbon, 5-10 pts. mass sawdust, 5-10 pts. mass bran, and 40-60 pts. mass calcium superphosphate or calcium-magnesia phosphate fertilizer; crushing; adding with 3-4 pts. mass ammonium hydrogen carbonate and 0.2-0.3 pts. mass straw pole; fermenting at 60 degrees C for 35-42 days; and drying until the water content is 30-40 wt.%.    USE - Peanut fertilizer.    ADVANTAGE - The fertilizer has high content of humic acid and active calcium, has long-term effect, is simple to prepare, and is environment-friendly.    DETAILED DESCRIPTION - Peanut fertilizer comprises 12-33 wt.% organic substrates; 5-9 wt.% inorganic substrate; and 62-79 wt.% nitrogen fertilizer, potassium fertilizer, and active calcium phosphate fertilizer. A mass ratio of nitrogenous fertilizer, potash fertilizer and active calcium phosphate fertilizer (N:P205:K2O:CaO) is 9-13:4-5:11-15:5-7. The active calcium phosphate fertilizer is prepared by adding 30-40 pts. mass mud carbon, 5-10 pts. mass sawdust, 5-10 pts. mass bran, and 40-60 pts. mass calcium superphosphate or calcium-magnesia phosphate fertilizer; crushing to granule whose diameter is 0.1-0.3 mm; adding with 3-4 pts. mass ammonium hydrogen carbonate and 0.2-0.3 pts. mass straw pole; fermenting at 60 degrees C for 35-42 days; and drying until the water content is 30-40 wt.%. An INDEPENDENT CLAIM is included for preparing the peanut fertilizer comprising crushing organic substrate, inorganic substrate, nitrogen fertilizer, active calcium phosphate fertilizer and slow release fertilizer into granule; taking into disc granulator for pelleting at 50-60 degrees C; and drying until the water content is less than 12 wt.%.
NOVELTY - Flint clay tailings production involves placing flint tailings ingredients in a blender. The obtained mixture is stirred, and then compressed in a compression machine, where the thickness of flint flakes is 5-30 millimeters. The obtained material is dried in a microwave, and then sterilized at 60-100 degrees C for 30-120 minutes, where the water content of the flint flakes is 15%. The obtained material is processed for thermal sterilization, and then cooled to obtain the desired product, where the flint clay tailings comprises (wt.%): (15-35), acidic mud (25-55) and attapulgite clay (2-15).    USE - Method for producing flint clay tailings used for preparing composition for acidifying soil and providing nutrient (claimed) for plant growth and reducing pathogenic bacteria and pest in plant.    ADVANTAGE - The method is simple, eco-friendly, and enables to produce the product that has high nitrogen, phosphorus, potassium and organic matter content.    DETAILED DESCRIPTION - Flint clay tailings production involves placing flint tailings ingredients in a blender. The obtained mixture is stirred, and then compressed in a compression machine, where the thickness of flint flakes is 5-30 millimeters. The obtained material is dried in a microwave, and then sterilized at 60-100 degrees C for 30-120 minutes, where the water content of the flint flakes is 15%. The obtained material is processed for thermal sterilization, and then cooled to obtain the desired product, where the flint clay tailings comprises (wt.%): flint clay (15-35), acidic mud (25-55), attapulgite clay (2-15), gravel attapulgite flower-shaped ceramic slurry (2-15), mud (2-15), slag (2-15), plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and high water-absorbing resin (0.1-5).
NOVELTY - Nutrition soil preparation involves selecting raw material (nutrition earth sheet). The selected material is placed in a mixer, and then stirred uniformly, where the thickness of nutrition earth sheet is 5-30 millimeters. The mixed material is placed in a microwave belt type drying machine under low temperature, and then dried at 60-100 degrees C for 30-120 minutes, where the water content of nutrition earth sheet is less than 15%. The obtained material is sterilized in a heat-insulating sterilized, and then cooled. The obtained material is packed to obtain the finished product.    USE - Method for producing flint clay tailings used for preparing composition for acidifying soil and providing nutrient (claimed) for stimulating plant growth and reducing pathogenic bacteria and pest in plant.    ADVANTAGE - The method is simple, eco-friendly, and enables to produce the product that has high nitrogen, phosphorus, potassium and organic matter content.    DETAILED DESCRIPTION - Nutrition soil preparation involves selecting raw material (nutrition earth sheet). The selected material is placed in a mixer, and then stirred uniformly, where the thickness of nutrition earth sheet is 5-30 millimeters. The mixed material is placed in a microwave belt type drying machine under low temperature, and then dried at 60-100 degrees C for 30-120 minutes, where the water content of nutrition earth sheet is less than 15%. The obtained material is sterilized in a heat-insulating sterilized, and then cooled. The obtained material is packed to obtain the finished product, where the nutrition soil comprises (in wt.%): acidified shale (15-35), acidic mud (25-55), attapulgite clay (2-15), gravel attapulgite flower-shaped ceramic slurry (2-15), pulverized peat, (2-15), biogas (2-15), plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and high water-absorbing resin (0.1-5).
NOVELTY - Producing bentonite mine tailings comprises introducing mine tailing soil ingredients into mixer and then stirring, compressing tailings using compressor to obtain flakes, introducing flakes to sterilizing machine using conveyor belt, drying to reduce moisture content of the product, and cooling flakes and then packaging. The mine tailing soil ingredients comprise acidified bentonite tailings, acidified sludge, high-viscosity attapulgite, flower-shaped ceramic granule, pulverized peat, charcoal, pulverized plant fiber, vermiculite, perlite and superabsorbent resin.    USE - The method is useful for producing bentonite mine tailing (claimed), which is useful as a fertilizer for promoting growth of plants.    ADVANTAGE - The method is capable of easily producing the bentonite mine tailings with high nutrition content in an eco-friendly manner. The bentonite mine tailings reduces pathogenic bacteria and pest in plants.    DETAILED DESCRIPTION - Producing bentonite mine tailings comprises introducing mine tailing soil ingredients into a mixer and then stirring, compressing the tailings using a compressor to obtain flakes having a thickness of 5-30 mm, introducing the flakes to a sterilizing machine using a conveyor belt and then sterilizing, drying at 60-100 degrees C for 30-120 minutes to reduce moisture content of the product to less than 15%, and cooling the flakes and then packaging. The mine tailing soil ingredients comprise 15-35 wt.% of acidified bentonite tailings, 25-55 wt.% of acidified sludge, 2-15 wt.% of high-viscosity attapulgite, 2-15 wt.% of flower-shaped ceramic granule, 2-15 wt.% of pulverized peat, 2-15 wt.% of charcoal, 1-10 wt.% of pulverized plant fiber, 0.5-5 wt.% of vermiculite, 0.5-5 wt.% of perlite and 0.1-5 wt.% of superabsorbent resin.
NOVELTY - Nutrition soil preparation involves stirring phosphate containing mine tailings in a stirrer, where the thickness of phosphate containing mine tailings is 5-30. The obtained mine tailings is placed in a microwave belt type drying machine, and then sterilized in a device at 60-100 degrees C for 30-120 minutes, where the water content of obtained sheet is less than 15%. The obtained sheet is cooled, and then packed to obtain the desired product. Mine tailings comprises (in wt.%): sepiolite acidified tailings (15-35), acidified sludge (25-55) and attapulgite clay (2-15).    USE - Method for preparing nutrition soil (claimed) used for promoting plant growth, and reducing pathogenic bacteria and pest.    ADVANTAGE - The method enables to produce the nutrition soil that has nitrogen, phosphorus, potassium and organic matter that has improved plant growth and eco-friendly.    DETAILED DESCRIPTION - Nutrition soil preparation involves stirring phosphate containing mine tailings in a stirrer, where the thickness of phosphate containing mine tailings is 5-30. The obtained mine tailings is placed in a microwave belt type drying machine, and then sterilized in a device at 60-100 degrees C for 30-120 minutes, where the water content of obtained sheet is less than 15%. The obtained sheet is cooled, and then packed to obtain the desired product. Mine tailings comprises (in wt.%): sepiolite acidified tailings (15-35), acidified sludge (25-55), attapulgite clay (2-15) and stone shaped attapulgite ceramic flower leaching liquid (2-15), peat (2-15), biogas (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and water-absorbing resin (0.1-5).
NOVELTY - One vertical to flow a two level anaerobic reactor, belonging to the waste water processing technology field. Comprise sealed tank body, a first-stage packed bed, screen cover, tube, a level packed bed, pneuma liquid separate, return tube, a heat accumulator, circulation pump, a gas-liquid mixer, rotate material and discharging tube, two packed bed level b. first-stage stuffing bed liquid rising flowing speed high, reduces the high organic load of impact for the anaerobic environment, a level filling bed flow rate is low, which is good for a pollutant intercepting and depth anaerobic biochemical reaction, good water quality, sludge yield; sewage anaerobic reaction produce of a methane heat energy recovery, and the reactor in a temperature environment temperature constant, realize the benign circulation of anaerobic reaction. This utility new type has simple operation, high concentration organic waste water treatment efficiency, stable and reliable operation, small floor area, low investment and operation cost is low, at the same time has the load impact resistance, salt resistance, toxicity ability, water power staying time short and so on.
NOVELTY - An impurities removing method involves contacting the biodiesel with a sorbent composition, where the sorbent composition comprises sawdust and molecular sieve, where weight ratio of the sawdust and molecular sieve is 1:0.04-6.    USE - Method for removing impurities from biodiesel oil.    ADVANTAGE - The method enables removing impurities from biodiesel oil in an effective manner.
NOVELTY - This utility new type of name is the one with a aeration stir pole and using pressurized aeration of compost, the compost c by a compost reactor main body part, a power part, an air supplied, preprocessing and pressurizing part, gas absorption and compost processing part. Compost reactor main body part by feeding port, a heat preservation layer, the stir pole, stir shaft, a discharge port, a compost cabin. Multi-strip stir pole as centre to centre of a stir shaft a different direction of compost bin, a compost reaction to ensure a uniform stir time of material, through a pressurized air aeration stir pole up to the each a compost chamber of part, to achieve the purpose of uniform aeration at the same time to avoid hole blockage of aeration. The device can realize organic waste composting process time, uniform stir material, sufficient uniform aeration, the stack body exist of anaerobic. the lowest horizontal, a composting reaction process of greatly reducing the acceleration a of a bad smell.
NOVELTY - This utility new type relates to a new organic fertilizer and one, solution is as follows: comprise support machine frame and the transverse guide wheel device of running machine frame to support a rack, support rack is set with lengthways guide wheel, a walking machine frame rotating with a rotating bracket, a rotating bracket mounting the free end connecting with a vertical turn of polishing bracket, the bracket bottom end set with turn twisting roller polishing, polishing turn twisting roller by the third drive is installed on the rotating bracket of a driving device, a rotating bracket middle part position between the walking machine frame and a hydraulic cylinder, the hydraulic station driving hydraulic cylinder, a turn throwing glue rear roller set with lengthways upper part of spraying tube is uniformly distributed with a multi-spray head, spray tube through the water valve is set in the upper part of a water tank spray tube a, a turn throwing glue roller front the upper part set with microbial inoculum applied to device, the utility model is new type can conveniently adjust turn throwing height of twisting roller, spraying device and set with microbial inoculum applied to device, increase the fermentation and turn polishing efficiency of fertilizer, saving the labour force and automatic degree high, the fermentation effect is good.
NOVELTY - This utility new type claims a one for a household garbage clean energy device, comprise the heating room, heating room used for the subsequent device supply heat energy, heating room and gas converter is connected, the converter gas with a gas tower, cracking reactor is connected the gas tower gas purification tower connected with the gas purification tower and the gas storage tank, gas storage tank for a rear purification of a combustion gas. A harmless process completely in the domestic garbage for a heat treatment process, is large, strong adaptability, low energy consumption, energy conversion utilization rate high, environmental and economic benefit of purpose, this utility new type garbage can completely replace of the landfill, incineration, pyrolysis process, and the garbage of organic matter in conversion is clean fuel gas, used for heat supply or power generation, environmental protection, using natural gas as the heat supply or power generation, without second pollution.
NOVELTY - Production of hydroxyapatite tailings compressed nutritional soil comprises adding hydroxyapatite tailings and nutritional soil into stirring machine, uniformly stirring, conveying into microwave drying sterilizing machine through belt conveyor for sterilizing and drying, controlling the moisture content, conveying to heat-insulating sterilizing library, continuously sterilizing and drying, cooling and packaging to obtain the product including acidified hydroxyapatite tailings, acidified sludge, high-viscosity attapulgite clay and broken stone-shaped attapulgite flower ceramic.    USE - Production of hydroxyapatite tailings compressed nutritional soil (claimed) used for reducing pathogenic bacteria and pests harmful for plant and protecting the ecological environment.    ADVANTAGE - The hydroxyapatite tailings compressed nutritional soil contains nitrogen, phosphorus, potassium, organic matter and multiple elements for plant growth, and enables normal growth and development of plant.    DETAILED DESCRIPTION - Production of hydroxyapatite tailings compressed nutritional soil comprises adding hydroxyapatite tailings and nutritional soil into stirring machine, uniformly stirring, conveying into microwave drying sterilizing machine through belt conveyor for sterilizing and drying at 60-100 degrees C for 30-120 minutes, controlling the moisture content at less than or equal to 15%, conveying to heat-insulating sterilizing library, continuously sterilizing and drying, cooling and packaging to obtain the product comprising 15-35 wt.% acidified hydroxyapatite tailings, 25-55 wt.% acidified sludge, 2-15 wt.% high-viscosity attapulgite clay, 2-15 wt.% broken stone-shaped attapulgite flower ceramic, 2-15 wt.% crushed peat, 2-15 wt.% slag, 1-10 wt.% crushed plant fiber, 0.5-5 wt.% expanded vermiculite, 0.5-5 wt.% expanded perlite, and 0.1-5 wt.% high water absorbing resin.
NOVELTY - Processing kaolin involves stirring acidified kaolin, where obtained kaolin is dried in microwave at 60-100 degrees C for sterilization. The dried kaolin cooled and then packed. Kaolin comprises (in wt.%): acidified kaolin (15-35), acidified residue (25-55), attapulgite clay (2-15), leaching liquid (2-15), biogas (2-15), plant fiber (1-10), vermiculite (0.5-5), perlite (0.5-5) and super absorbent resin (0.1-5).    USE - Method for processing kaolin (claimed) used for providing nutrition to plants and reducing pathogenic bacteria and harmful pest.    ADVANTAGE - The method enables to process kaolin in simple and eco-friendly manner.
NOVELTY - Producing water-quenched slag involves putting water quenched slag ingredients into a compressed machine and then stirred uniformly to obtain a water quenched slag compressed sheet and placed into a microwave belt type sterilizing machine to sterilize at 60-100 degrees C under low temperature. The obtained water quenched slag compressed sheet is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material, and then dried, cooled and packaged to obtain the final product.    USE - Method for producing water-quenched slag used for providing nutrition to soil (claimed) and growth and development of plant.    ADVANTAGE - The method is eco-friendly, enables to produce water-quenched slag that provides nutrition of nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Producing water-quenched slag involves putting water quenched slag ingredients into a compressed machine and then stirred uniformly to obtain a water quenched slag compressed sheet and placed into a microwave belt type sterilizing machine to sterilize at 60-100 degrees C under low temperature. The obtained water quenched slag compressed sheet is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material, and then dried, cooled and packaged to obtain the final product. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and high water absorbing resin (0.5-5).
NOVELTY - Processing stone tailing involves stirring acidified stone tailing, where obtained stone tailing is dried in microwave at 60-100 degrees C for sterilization. The dried stone tailing is cooled and then packed. Stone tailing comprises (in wt.%): acidified stone tailing (15-35), acidified mud (25-55), high viscosity attapulgite clay (2-15), leached ceramic (2-15), peat (2-15), biogas (2-15), plant fiber (1-10), vermiculite (0.5-5), perlite (0.5-5) and super absorbent resin (0.1-5).    USE - Method for processing stone tailing (claimed) used for providing nutrition to plant and reducing pathogenic bacteria and harmful pest.    ADVANTAGE - The method enables to process stone tailing in simple and eco-friendly manner.
NOVELTY - Processing bauxite tailing involves stirring acidified bauxite tailing, where obtained bauxite tailing is dried in microwave at 60-100 degrees C for sterilization. The dried bauxite tailing cooled and then packed. Bauxite tailing comprises (in wt.%): acidified bauxite tailing (15-35), acidified mud (25-55), attapulgite clay (2-15), leaching liquid (2-15), peat (2-15), biogas (2-15), plant fiber (1-10), vermiculite (0.5-5), perlite (0.5-5) and super absorbent resin (0.1-5).    USE - Method for processing bauxite tailing (claimed) used for providing nutrition to plant and reducing pathogenic bacteria and harmful pest.    ADVANTAGE - The method enables to process bauxite tailing in simple and eco-friendly manner.
NOVELTY - Nutrition soil production involves preparing volcanic ash by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10) and expanded vermiculite (0.5-5).    USE - Method for producing nutrition soil by using volcanic ash (claimed) for growth and development of plant.    ADVANTAGE - The method enables to produce nutrition soil in eco-friendly manner that provides nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Nutrition soil production involves preparing volcanic ash by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5), and high water absorbing resin (0.5-5).
NOVELTY - Producing calcium carbide slag involves putting calcium carbide into mixture machine and then stirred and placed into a microwave belt type sterilizing machine to sterilize calcium carbide at 60-100 degrees C under low temperature. The obtained kaolin is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15) and crushed plant fiber (1-10).    USE - Method for producing calcium carbide slag used for providing nutrition to soil (claimed) and growth and development of plant.    ADVANTAGE - The method is ecofriendly, enables to produce calcium carbide slag that provides nutrition of nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Producing calcium carbide slag involves putting calcium carbide into mixture machine and then stirred and placed into a microwave belt type sterilizing machine to sterilize calcium carbide at 60-100 degrees C under low temperature. The obtained kaolin is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and high water absorbing resin (0.5-5).
NOVELTY - Producing clay tailing involves putting lime into a machine and then stirred uniformly and placed into a microwave belt type sterilizing machine to sterilize clay at 60-100 degrees C under low temperature. The obtained clay is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material, and then dried, cooled and packaged to obtain the final product. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55) and leaching liquid (2-15).    USE - Method for producing clay tailing used for providing nutrition to soil (claimed) and growth and development of plant.    ADVANTAGE - The method is ecofriendly, enables to produce clay tailing that provides nutrition of nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Producing clay tailing involves putting lime into a machine and then stirred uniformly and placed into a microwave belt type sterilizing machine to sterilize clay at 60-100 degrees C under low temperature. The obtained clay is treated in water at 30-120 degrees C to obtain a product. The product is mixed with material, and then dried, cooled and packaged to obtain the final product. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5) and high water absorbing resin (0.5-5).
NOVELTY - Nutrition soil production involves preparing illite by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10) and expanded vermiculite (0.5-5).    USE - Method for producing nutrition soil by using illite (claimed) for growth and development of plant.    ADVANTAGE - The method enables to produce nutrition soil in eco-friendly manner that provides nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Nutrition soil production involves preparing illite by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5), and high water absorbing resin (0.5-5).
NOVELTY - Processing gypsum tailing involves stirring acidified gypsum tailing, where obtained gypsum tailing is dried in microwave at 60-100 degrees C for sterilization. The dried gypsum tailing cooled and then packed. Gypsum tailing comprises (in wt.%): gypsum tailing (15-35), acidified mud (25-55), attapulgite clay (2-15), leaching liquid (2-15), peat (2-15), biogas (2-15), plant fiber (1-10), vermiculite (0.5-5), perlite (0.5-5) and super absorbent resin (0.1-5).    USE - Method for processing gypsum tailing (claimed) used for growing plant and reducing pathogenic bacteria and harmful pest.    ADVANTAGE - The method enables to process gypsum tailing in simple and eco-friendly manner.
NOVELTY - Processing serpentine tailing involves stirring serpentine tailing, where obtained serpentine tailing is dried in microwave at 60-100 degrees C for sterilization. The dried serpentine tailing cooled and then packed. Serpentine tailing comprises (in wt.%): acidified serpentine tailing (15-35), acidified mud (25-55), attapulgite clay (2-15), leaching liquid (2-15), peat (2-15), biogas (2-15), plant fiber (1-10), vermiculite (0.5-5), perlite (0.5-5) and super absorbent resin (0.1-5).    USE - Method for processing serpentine tailing (claimed) used for growing plant and reducing pathogenic bacteria and harmful pest.    ADVANTAGE - The method enables to process serpentine tailing in simple and eco-friendly manner.
NOVELTY - Producing talc mine tailings comprises introducing mine tailing soil ingredients into mixer, compressing tailings to obtain flakes, introducing flakes to sterilizing machine using conveyor belt and then sterilizing, drying to reduce moisture content of dried product, and cooling flakes and then packaging. The mine tailing soil ingredients comprise acidified talc tailings, acidified sludge, high-viscosity attapulgite, flower-shaped ceramic granule, pulverized peat, charcoal, pulverized plant fiber, vermiculite, perlite and super absorbent resin.    USE - The method is useful for producing talc mine tailing (claimed), which is useful as a fertilizer for promoting growth of plants.    ADVANTAGE - The method is capable of easily producing the talc mine tailings with high nutrition content in eco-friendly manner. The talc mine tailings as a fertilizer reduce pathogenic bacteria and pest in plants.    DETAILED DESCRIPTION - Producing talc mine tailings comprises introducing mine tailing soil ingredients into a mixer and then stirring, compressing the tailings using a compressor to obtain flakes having a thickness of 5-30 mm, introducing the flakes to a sterilizing machine using a conveyor belt and then sterilizing, drying at 60-100 degrees C for 30-120 minutes to reduce moisture content of the dried product to less than 15%, and cooling the flakes and then packaging. The mine tailing soil ingredients comprise 15-35 wt.% of acidified talc tailings, 25-55 wt.% of acidified sludge, 2-15 wt.% of high-viscosity attapulgite, 2-15 wt.% of flower-shaped ceramic granule, 2-15 wt.% of pulverized peat, 2-15 wt.% of charcoal, 1-10 wt.% of pulverized plant fiber, 0.5-5 wt.% of vermiculite, 0.5-5 wt.% of perlite and 0.1-5 wt.% of super absorbent resin.
NOVELTY - Bioactive compound fertilizer comprises 55-60 wt.% of nitrogen fertilizer, phosphate fertilizer and potassium fertilizer in a weight ratio of 12-14:10-11:4-7, 36-41 wt.% of active matrix, and 4-5 wt.% of inorganic matrix. The active matrix is prepared by mixing 40-60 pts. wt. coal, 20-30 pts. wt. furfural residue, 20-30 pts. wt. xylose residue having a particle diameter of 0.1-0.3 mm, 3-4 pts. wt. ammonium bicarbonate, and 0.2-0.3 pts. wt. decomposition agent, heating mixture at 60 degrees C in a reactor, fermenting hot mixture for 35 days, and drying to reduce moisture content of mixture to 30-40%.    USE - The bioactive compound fertilizer is useful for Bohai grains (claimed).    ADVANTAGE - The eco-friendly bioactive compound fertilizer can be easily and economically prepared with high nutrition content and storage stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing bioactive compound fertilizer comprising crushing active matrix, inorganic matrix, nitrogen fertilizer, phosphate fertilizer and potassium fertilizer to a particle size of 0.1-0.3 mm and then uniformly mixing to obtain a mixture, passing the mixture to a disc granulator for granulating, and drying the granulated product at 40-50 degrees C to reduce moisture content to less than 12%.
NOVELTY - Nutrition soil production involves preparing lake sludge by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15) and slag (2-15).    USE - Method for producing nutrition soil by using lake sludge (claimed) for growth and development of plant.    ADVANTAGE - The method enables to produce nutrition soil in eco-friendly manner that provides nitrogen, phosphorus, potassium, organic matter and multi-element to soil, and reduces pathogenic bacteria and pest which are harmful to plant.    DETAILED DESCRIPTION - Nutrition soil production involves preparing lake sludge by putting them into machine and then stirred and transferred into a microwave belt type sterilizing machine to sterilize them at 60 degrees C under low temperature. The obtained material is treated with water at 30-120 degrees C to obtain a product. The product is mixed with material and then packaged. Material comprises (in wt.%): acid sludge (15-35), high-viscosity attapulgite clay (25-55), leaching liquid (2-15), attapulgite floral ceramic (2-15), peat (2-15), slag (2-15), crushed plant fiber (1-10), expanded vermiculite (0.5-5), expanded perlite (0.5-5), ferrous sulfate (0.1-5) and superabsorbent (0.5-5).
NOVELTY - The system has a gas-liquid separator (5) connected with a draught fan (7). A conveyor (1) is connected with a dust remover (3) that is fixed with a carbonizing furnace (2). The dust remover is fixed with the gas-liquid separator that is fixed with a tar separator (4). The draught fan is equipped with a wax liquid separator (6). The carbonizing furnace is connected with an inner wall of a shell. A middle part of the carbonizing furnace is connected with an air channel. A center part of a cooling layer is fixed with a discharge cone shaped part.    USE - Crop straw carbon production and tar, wood wax liquid recovery system.    ADVANTAGE - The system increases straw carbon conversion efficiency, thus reducing energy consumption. The system has low labor intensity, user-friendly environment, better environment protection without pollution problem, high product quality, high stability and high production efficiency.    DETAILED DESCRIPTION - The air channel is a dry distillation layer that is material layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a crop straw carbon production and tar, wood wax liquid recovery system.    Conveyor (1)    Carbonizing furnace (2)    Dust remover (3)    Tar separator (4)    Gas-liquid separator (5)    Wax liquid separator (6)    Draught fan (7)
NOVELTY - The port has a square-shaped bucket made of metal material. A mouth cover ignition hole is formed on an ignition mouth edge that is formed with a square seal groove. An ignition port cover is arranged close to a lighting unit. Length and width of an ignition port body are 0.2mm and 0.12mm. The ignition port body and the ignition port cover are provided with a hinge.    USE - Wood tar extracting cabinet door ignition port for a plant pesticide pyroligneous liquor product.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of a wood tar extracting cabinet door ignition port.
NOVELTY - Preparing plant acid comprises filling agricultural and forestry production waste into a horizontal spiral furnace, carrying out low temperature carbonization at 170-370 degrees C, recovering carbonization produced flue gas and cooling into liquid, allowing to stand to stratify to obtain transparent substance having yellowish-brown layer in the middle layer.    USE - The plant acid is useful in water-soluble fertilizer (claimed).    ADVANTAGE - The method: uses horizontal spiral furnace, which replaces conventional vertical furnace; carries out optimized carbonization and filling process, which greatly increase the yield of plant acid; ensures plant acid and activated carbon yield ratio to be 1:1, in comparison with conventional vertical furnace can only can reach 0.2:1.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for water-soluble fertilizer prepared by the aforementioned method.
NOVELTY - An environmentally-friendly fuel comprises 10-40 parts mass coal oil, 20-40 parts mass vegetable fats and oils, 3-6 parts mass vegetable oil acid or ethanolamine and 10-25 parts mass methanol.    USE - Environmentally-friendly fuel (claimed).    ADVANTAGE - The environmentally-friendly, nontoxic, smokeless and odorless low-volatile fuel has high calorific value and excellent stability, and saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environmentally-friendly fuel, which involves mixing coal oil and vegetable fats and oils, adding vegetable oil acid or ethanolamine and methanol, and mixing.
NOVELTY - A one absorbing, environment-friendly and multifunctional fermentation tank, fermentation include box body, a fermenting box body by side plate and cover plate form a seal space, a fermentation box body set with a discharge port, a cover plate connecting with a gas guide tube, fermenting the top of the box body from the upper to the lower in turn distribute firstly coated with carbon layer, diatom ooze layer and wood crushing layer, a cover plate is of upward convex arc-shaped structure and the carbon layer and set with air of the inner cavity. A gas each new type of fermentation tank of this utility model is reasonable design, fully absorbing the fermentation material (poultry to) in a out to prevent the harmful gas polluted air and nutrition substance waste, and make safety device, structure is simple, it is convenient and a multi-times, manufacturing cost is low.
NOVELTY - This utility new type claims a one marsh gas, dehydrating and dust-removing device, comprise one shell, upper part of the shell body set with one lifting lug, the lower part set with a water outlet, a shell set with an air inlet, an air outlet, an air inlet and an air outlet at the same height of a shell, in the shell from the upper to the lower in turn set with a baffle plate, a guide plate and a lower baffle plate. The device structure is simple, production cost is low, the mounting is convenient, energy-saving, dehydrating and dust-removing efficiency is high, it can reduce the engineering investment, shorten the construction period, saves space resource and energy, and efficient in a marsh gas, dehydrating and dust-removing process, protecting transportation pipeline.
NOVELTY - Method of preparing microemulsion, involves adding cyclohexanone into stirring tank and stirring at low temperature and 30-40 rotations/minute (rpm), adding methane, cyhalofop-butyl and carbendazim, stirring the mixture for 0.8-1 hour, then adding water and stirring at 50-60 rpm, adding sodium lauryl polyoxyethylene ether sulfate, completely dissolving the materials by stirring at 210-220 rpm and reacting for at 1-1.2 hours to obtain the finished product.    USE - The method is useful for preparing microemulsion used for killing weeds (claimed).    ADVANTAGE - The composition can be prepared simply, is environmentally-friendly, and has good quality and synergistic effect.    DETAILED DESCRIPTION - Method of preparing microemulsion, involves obtaining 7-8 wt.% cyhalofop-butyl, 3-4 wt.% carbendazim, 8-9 wt.% cyclohexanone, 15-16 wt.% methane, 6-7 wt.% sodium lauryl polyoxyethylene ether sulfate and water (remainder), adding cyclohexanone into stirring tank and stirring at low temperature and 30-40 rotations/minute (rpm), adding methane, cyhalofop-butyl and carbendazim, stirring the mixture for 0.8-1 hour, then adding water and stirring at 50-60 rpm, adding sodium lauryl polyoxyethylene ether sulfate, completely dissolving the materials by stirring at 210-220 rpm and reacting for at 1-1.2 hours to obtain the finished product.
NOVELTY - This new type utility claims a multifunctional one solid waste treatment device, comprise the shell, inner shell set with a heating room, a part with the carbonization reaction kettle of heating room, lower part and anoxic reaction chamber is connected with gas catalytic reaction kettle is connected with the front end of carbonization reaction kettle and the upper part of gas catalytic reaction kettle is connected, front end lower part and anoxic reaction chamber of a gas catalytic reaction kettle, gas catalytic reaction kettle set with gas exit end, rear end of the anoxic reaction chamber and the carbon slag chamber is connected, carbonizing rear end of the reaction kettle is set with leading-in seal type feeding mechanism used for a solid waste. Strong adaptability, harmless treatment completely of; a processing domestic garbage, agricultural waste, medical waste, animal corpse, poultry body and so on, a waste process heat decomposition is low in the absence of oxygen and anoxic condition, there is no dioxin produce condition, would for the environment is not a secondary pollution.
NOVELTY - Catalyst comprises 0.1-1 wt.% platinum metal component, 2-5 wt.% chlorine and balance of gamma -alumina carrier.    USE - The catalyst is useful for isomerization reaction of 4-9C n-alkane (claimed).    ADVANTAGE - The catalyst has high isomerization rate, reaction activity, and good stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing the catalyst, comprising (i) impregnating 80-120 pts. wt. gamma -alumina carrier in 20-30 pts. wt. chloroplatinic acid, drying the impregnated product at 100-120 degrees C for 2-5 hours, then oxidizing at 500-700 degrees C for 2-5 hours, (ii) reducing the resulting product, at 200-500 degrees C for 2-5 hours, at pressure of 1-3 MPa, (iii) subjecting the resultant product to inorganic chlorination using 15-50 wt.% inorganic chlorinating agent aluminum chloride, at 400-500 degrees C for 2-8 hours, (iv) subjecting the resultant product to organic chlorination using organic chlorinating agent at 100-400 degrees C for 0.5-2 hours, and cooling, where the organic chlorinating agent is carbon tetrachloride or chloro(dimethyl)aluminum, and accounts for 30-50 wt.%;    (2) use of catalyst for isomerization reaction of n4-9C alkane; and    (3) isomerization reaction, comprising carrying out reaction at 120-180 degrees C, under hydrogen partial pressure of 1-3 MPa, where n-alkane and hydrogen gas volume ratio is 0.1-1, and volume of airspeed is 1-2/hour.
NOVELTY - Capsaicin is extracted from chili powder or chili essential oil, and macroporous resin enrichment is carried out to obtain chili powder total alkaloid. Chili powder total alkaloid is separated by countercurrent chromatography using solvent system. Solvent system is added to separating funnel, and layers are separated. The upper phase is taken as stationary phase, and lower phase as mobile phase. The chromatography column is filled with stationary phase, sample is injected, eluted and detected to obtain colorless crystals of capsaicin monomer, and dihydrocapsaicin.    USE - Preparation of high-purity capsaicin monomer (claimed).    ADVANTAGE - The method provides high-purity capsaicin monomer with high yield by simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - Capsaicin is extracted from chili powder or chili essential oil using alcohol, and macroporous resin enrichment is carried out to obtain chili powder total alkaloid. Chili powder total alkaloid is separated by high-speed countercurrent chromatography using solvent system comprising hydrocarbon, ester, alcohol, and water, or alkane, ester, alcohol, water, or acid and/or base. Acid or base-mediated solvent is added to resulting mixture, pH is adjusted to 1-14, and the solvent system is added to separating funnel, shaken well, and layers are separated. The upper phase is taken as stationary phase, and lower phase as mobile phase. The countercurrent chromatography column is filled with stationary phase, when the system temperature is 5-65 degrees C, and mobile phase is pumped into the column. Sample is injected from the injection valve, eluted and detected using spectra to obtain colorless crystals of capsaicin monomer having purity of 98% or more, and dihydrocapsaicin. The volume ratio of alkane, ester, alcohol, water, or acid and/or base is 1-6:1-6:1-6:1-6.
NOVELTY - Antibiotic compound is purified by placing cefazedone and sodium isooctoate solvent in anhydrous methanol, performing salt-forming reaction at 15-35 degrees C to dissolve cefazedone, adding activated carbon, decoloring, filtering to remove activated carbon, maintaining filtrate temperature at 10-30 degrees C, filtering, adding 1st acetone and 1st ethyl acetate to filtrate, crystallizing at 15-20 degrees C for 1-2 hours, adding 2nd acetone and 2nd ethyl acetate, stirring and crystallizing at 15-25 degrees C and 80-120 rpm for 2-4 hours, filtering, washing filter cake, and drying to obtain sodium cefazedone fine product.    USE - Purification of antibiotic compound (claimed).    ADVANTAGE - Antibiotic compound has low moisture and impurity content and high stability, and preparation is low-cost, simple, and environment-friendly and has high yield.
NOVELTY - This utility new type belongs to the field of organic fertilizer production technology field, especially relates to a one for organic fertilizer production of biomass a material molding device. Comprise a shell, a horizontal feeding port, the shell set with one feeding roller for the inner horizontal feeding port, the feeding roller for include the driving roller and the driven roller, the inner shell, a rear feeding roller set with side cutting roller, cutting roller along the circumference a mounting surface with a multi-cutter, the lower part of the cutting roller set with filter plate, two side said filter screen plate and movably connected with the inner wall of inner box body is hinged with the lower surface of a filter screen fixed mounting with a vibrator, filter plate under the storage hopper, storage hopper inner set with horizontal spiral discharging device, one side of storage hopper set with a discharging port, further comprise transmission and power mechanism. A biomass material molding. This utility new type used for organic fertilizer production of structure is simple, it can increase production efficiency and reduce the production cost, reduce the energy consumption, saving resource, convenient use and suitable for popularization.
NOVELTY - Use of fermented grass liquid for improving denitrification capacity in sewage treatment is claimed.    USE - Fermented grass liquid for improving denitrification capacity in sewage treatment.    ADVANTAGE - The fermented grass liquid improves denitrification capacity in sewage treatment in a simple manner and with better effect, contains cheap and easily obtainable raw materials, and has important social, economical and ecological benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the above-mentioned fermented grass liquid, which involves collecting and crushing grass, adding crushed grass to a fermentation tank, controlling active sludge in the mixture, adding water to the mixture, and filtering the mixture at constant temperature to remove Potamogeton crispus grass residue to obtain the fermented grass liquid.
NOVELTY - The method involves arranging a gravel layer on a water inlet pipe that is connected with a water branch tube. A water inlet tube is mounted with a liquid valve and a liquid flow meter. An aeration branch tube is provided with an aeration device. An aerobic microbe layer and the gravel layer are arranged on a steel wire net. A water outlet unit is formed with a water hole and a water collecting groove. An artificial marsh tank is connected with a water inlet tube. An inner side wall of a tank body is arranged on a barrier layer.    USE - Sewage water processing method.    ADVANTAGE - The method enables combining immobilized microorganism, microorganism aerobics and anaerobics with artificial wetland organics so as to enhance artificial microorganism.    DETAILED DESCRIPTION - The aeration branch tube is a PVC tube.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a sewage water processing method.
NOVELTY - Use of fermented grass liquid for removing nitrogen in artificial wetland is claimed.    USE - Fermented grass liquid for removing nitrogen in artificial wetland.    ADVANTAGE - The fermented grass liquid removes nitrogen in artificial wetland in a simple manner and with better effect, contains cheap and easily obtainable raw materials, and has important social, economical and ecological benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the above-mentioned fermented grass liquid, which involves collecting and crushing grass, adding crushed grass to a fermentation tank, controlling active sludge in the mixture, adding water to the mixture, and filtering the mixture at constant temperature to remove Potamogeton crispus grass residue to obtain the fermented grass liquid.
NOVELTY - A micro-ecological preparation comprises Streptococcus faecalis, photosynthetic bacteria and denitrifying bacteria.    USE - Micro-ecological preparation for use in water cultivation field application for reducing ammonia nitrogen and nitrite in a water-containing quantity (all claimed).    ADVANTAGE - The micro-ecological preparation has increased shelf life, rapid effect of reducing ammonia nitrogen and nitrite in toxic and harmful substances such as water, optimizing cultivation environment and promoting water ecological environment benign circulation effect, and reduces consumption of oxygen in for cultivation water.
NOVELTY - Organic fertilizer is prepared by (a) mixing the reed stem tip portion and rice straw and crushing the mixture, (b) mixing water, 90-95% cyanobacteria and livestock manure and subjecting the mixture to wet fermentation, (c) mixing the crushed mixture and biogas residue produced by fermentation in a mass ratio 2-2.5:1 in mixing device, (d) performing anaerobic digestion by stirring and subjecting the mixture to anaerobic fermentation, (e) subjecting the obtained mixture aerobic fermentation, and (f) granulating the obtained biogas residue and drying the granules.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is environmentally-friendly.    DETAILED DESCRIPTION - Organic fertilizer is prepared by (a) mixing the reed stem tip portion and rice straw in a mass ratio of 1:(1-3) and crushing the mixture, (b) mixing water, 90-95% cyanobacteria and livestock manure in a mass ratio of 5:(1-2) and subjecting the mixture to wet fermentation, (c) mixing the crushed mixture and biogas residue produced by fermentation in a mass ratio 2-2.5:1 in mixing device, (d) performing anaerobic digestion by stirring and subjecting the mixture to anaerobic fermentation at 25-55 degrees C, (e) subjecting the obtained mixture aerobic fermentation at 45-50 degrees C, and (f) granulating the obtained biogas residue and drying the granules.
NOVELTY - Discharging device comprises a feeding roller (1), where the feeding roller has a shifting function. A feeding roller is set in front of the discharging device. A material shifting device is mounted on the discharge end of a material handling equipment. A hydraulic system is installed in the internal device, and below a belt conveyor. Discharging device comprises a feed belt (2), a belt supporting cylinder (3), a pump motor (6) and a collector (7).    USE - Discharging device used for compost.    ADVANTAGE - The discharging device is simple, discharges material continuously, and has improved efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a compost discharging device.    Feeding roller (1)    Feed belt (2)    Belt supporting cylinder (3)    Pump motor (6)    Collector (7)
NOVELTY - Fertilizer composition comprises 22 wt.% organic compost, 15 wt.% nitrogen, 5 wt.% phosphorus pentoxide, 10 wt.% potassium oxide, 2 wt.% calcium, 0.5 wt.% magnesium, and 0.5 wt.% zinc.    USE - As fertilizer composition for cherry and tomato (claimed).    ADVANTAGE - The composition is environmentally-friendly, completely utilizes raw materials, and reduces pollution caused by manure in pig farm.    DETAILED DESCRIPTION - Fertilizer composition comprises 22 wt.% organic compost, 15 wt.% nitrogen, 5 wt.% phosphorus pentoxide, 10 wt.% potassium oxide, 2 wt.% calcium, 0.5 wt.% magnesium, and 0.5 wt.% zinc. The fertilizer is prepared by (a) mixing fresh manure and rice husk in a ratio of 3-4:1, adding 2-3 pts. wt. microbial fermentation agent (effective microorganism) to mixture, uniformly mixing added material, and fermenting obtained mixture, (b) maintaining carbon-nitrogen ratio of the mixture at 25:1 and pH of the mixture at 7, (c) stacking fermented product to obtain heap having height of 1.2-1.5 m, composting at 55-60 degrees C for 5-7 days, and continuing composting up to 12 days to obtain organic compost, (d) drying and crushing organic compost to obtain semi-finished product, and (e) mixing the semi-finished product with fertilizer component chosen from calcium superphosphate, potassium chloride and calcium chloride.
NOVELTY - Organic fertilizer composition preparation involves crushing raw materials (in wt.%): lees (33-35), vegetable oil straw (17), monosodium glutamate (5), castor seed (8), peanut shell (10), sawdust (3), starch (5), mildew feed (5), dried pig manure (10-12), organic fertilizer fermenting agent (1) into powder, and then fermenting them for 20-22 days. Deodorizer (1%) is added to the obtained fermented material, and then the obtained material is dried. The obtained material is granulated, and the obtained granules are dried 65-68 degrees C to obtain the finished product.    USE - Method for preparing organic fertilizer composition used for improving plants growth in drought, cold and stress condition, and treating yellow leaves.    ADVANTAGE - The method enables to prepare organic fertilizer composition, which shows improved soil fertility.
NOVELTY - Mushroom cultivation waste recycling involves utilizing mushroom waste and earthworms.    USE - Method for recycling mushroom cultivation waste used as poultry feed, particularly chickens and ducks (claimed).    ADVANTAGE - The method is simple and eco-friendly.
NOVELTY - Culturing Pleurotus cystidiosus involves utilizing lychee branch and cereal grains.    USE - Method for culturing Pleurotus cystidiosus (claimed).    ADVANTAGE - The method cost-effective and ecofriendly manner, enables to culture Pleurotus cystidiosus having high yield value, ensures short duration to culture Pleurotus cystidiosus that has wide industrial applicability.
NOVELTY - Producing biological substrate, involves crushing wheat straw, corn silk and pumice, adding water and peat to crushed product, mixing materials, placing mixture on base material, composting mixture, adjusting pH of mixture regularly, maintaining moisture of the substrate, introducing earthworms into compost, aging the compost, removing earthworms from the compost, inspecting quality of the compost, using unqualified material as raw material for fermentation, drying and pulverizing qualified compost, mixing fertilizer with compost, and packing mixture.    USE - The method is useful for producing biological substrate (claimed).    ADVANTAGE - The method utilizes raw material that is abundant, cost-effectively produces substrate, and is environmentally-friendly and simple. The substrate can be decomposed completely, and has high fertilizing effect.    DETAILED DESCRIPTION - Method for producing biological substrate, involves (a) using 30-35 wt.% wheat straw, 20-30 wt.% corn silk, 10 wt.% pumice, 10-15 wt.% peat and 20-35 wt.% base material, (b) crushing wheat straw, corn silk and pumice, (c) adding water and peat to crushed product, mixing materials, and placing mixture on base material, (d) composting mixture from February to March, adjusting pH of mixture regularly by adding lime (required amount), and maintaining moisture of the substrate at 30-35%, (e) introducing earthworms into compost, aging the compost for a period of two weeks, and removing earthworms from the compost, (f) inspecting quality of the compost, using unqualified material as raw material for fermentation, drying and pulverizing qualified compost, and mixing 5-10 kg fertilizer with respect to one ton compost, and (g) packing and storing mixture.
NOVELTY - Biological medicinal fertilizer comprises (in pts.wt.): chicken manure (35-45), acid hydrolyzed residue (19-25), straw (8-15), egg shell powder (8-15), Bacillus subtilis (0.1-0.2), weeds (30-35), Aspergillus oryzae (0.1-0.2), Saccharomyces cerevisiae yeast (0.1-0.2), Celastrus (5-7), neem (3-4), radix aconite (4-6), rhizoma coptidis (3-5), copper sulfate (2-4), potassium sulfate (12-14), ammonium hydrogen carbonate (9-12), calcium superphosphate (8-13) and urea (11-14).    USE - Biological medicinal fertilizer used for culturing fish, improving water quality, regulating microenvironment for fish polyculture and increasing fish immunity.    ADVANTAGE - The biological medicinal fertilizer has insecticidal property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biological medicinal fertilizer, which involves:    (A) extracting Celastrus, neem, radix aconiti and rhizoma coptidis with water to obtain extract that is filtered and then filtrate is concentrated;    (B) mixing obtained concentrate, weeds, chicken manure, acid hydrolyzed residue, straw, egg shell powder and grass;    (C) adding Bacillus subtilis, Aspergillus oryzae and Saccharomyces cerevisiae yeast in obtained mixture at pH of 3.5-5.5;    (D) fermentating mixture for 2 days;    (E) adding calcium superphosphate and urea in fermenting mixture;    (F) fermenting obtained mixture at optimum temperature;    (G) mixing leavening agent, sulfuric acid copper, potassium sulfate and ammonium hydrogen carbonate and fermented materials;    (H) granulating obtained mixture; and    (I) filling obtained granules in paraffin envelope.
NOVELTY - Special organic fertilizer for rice, comprises 40-60 pts. wt. duck manure, 30-45 pts. wt. silkworm excrement, 2-5 pts. wt. microbial fermentation agents and 1-8 pts. wt. quicklime.    USE - The special organic fertilizer is useful for rice (claimed).    ADVANTAGE - The fertilizer is environmentally-friendly, rich in nutrition, prepared simply, cost-effective and suitable for large-scale production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the special fertilizer, which involves adding 3-10 times water to microbial fermentation agents, diluting mixture at normal temperature for 5-10 hours to obtain liquid, mixing duck manure, silkworm excrement and quicklime, crushing mixture into 100-200 mesh sieve, adding the liquid, uniformly stirring mixture, fermenting mixture at 30-42 degrees C for 25-30 days, drying fermented material until the water content reaches 10-18%, pelleting dried material, and packaging product.
NOVELTY - Preparing ceftriaxone sodium in a vertical logistics system, comprises: (a) adding crude ceftriaxone sodium into acetone solution, completely dissolving at 20-25 degrees C, reducing the temperature to 15 degrees C, adding crystal seed, stirring to separate out large amount of crystal, and (b) performing solid-liquid separation after drying the crystal, the resulting solid was separated from the transfer device to the drying device, where a separation device is located on the upper end, drying device on lower end, a separate device and drying device are connected through a vertical channel.    USE - The method is useful for preparing ceftriaxone sodium (claimed).    ADVANTAGE - The method: prevents emission of lead thus is environmental friendly; produces highly sterile drug substance; utilizes logistics system which has gravity as the main driving force, has high transport efficiency, and is economical.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of vertical logistics system.    Solvent tank (1)    Carbon filter (2)    Filter (3)    Sterile filter (4)    Crystallization tank (6)
NOVELTY - Salt-tolerant Escherichia coli mutant strain (I) having a preservation number of CGMCC No. 9288, is new.    USE - (I) is useful for the production of chiral aspartic acid, preferably L-aspartic acid (all claimed).    ADVANTAGE - (I) is capable of economically recycling the wastewater during the production of chiral aspartic acid in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing chiral aspartic acid, preferably L-aspartic acid comprising (a) reacting maleic acid with sodium bromide in the presence of ammonium persulfate and ammonia to obtain sodium fumarate as precipitate, (b) mixing obtained product and (I) to culture and carrying out enzymatic reaction with L-aspartic acid, and (c) regulating the pH value to acidity.
NOVELTY - Obtaining marsh gas involves mixing bacterial strain and straw in a molar ratio of 1:1, and then adding balanced amount of water to the obtained fermentation mixture to obtain desired product.    USE - Method for obtaining marsh gas (claimed).    ADVANTAGE - The method enables to obtain marsh gas, where the strain involved effectively decomposes the straw to obtain biogas in a simple, convenient and cost-effective manner.
NOVELTY - A vehicle fuel comprises 10-45 wt.% alcohol, 1-3 wt.% emulsifier, 15-45 wt.% heavy aromatic compound, 15-35 wt.% solvent oil, and 8-30 wt.% polyoxymethylene dimethyl ether. The alcohol is methanol, t-butanol or cyclohexanol. The emulsifier is mixture of oleic acid, diethyl ether, methyl benzoate and acetone. The heavy aromatic compound is xylene. The aromatic solvent oil is 180#-type aromatic solvent oil and/or 220#-type aromatic solvent oil.    USE - Vehicle fuel (claimed).    ADVANTAGE - The vehicle fuel has flash point of 55-60 degrees C, cetane number of 60-80, storage period of 1 year or more and copper corrosion level of 1a, and reduced generation of smoke.
NOVELTY - A biomass fuel comprises 4-5 pts. wt. raw straw, 2-3 pts. wt. dry leaves and 2-3 pts. wt. straw/weed.    USE - Biomass fuel (claimed).    ADVANTAGE - The biomass fuel has high combustion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass fuel, which involves mixing and pulverizing raw material components using a pulverizer to particle size of 30-50 mesh, drying until the moisture content in material is less than 15%, and compressing into blocks.
NOVELTY - A hydrostatic mechanical power split transmission working fluid composition comprises base oil containing natural gas liquid and trimethylolpropane ester compound, and composite additive comprising 4-7 %mass anti-wear agent, 1-2 %mass rust inhibitor, 0.5-1.5 %mass antioxidant, 0.001-0.005 %mass anti-foam agent, 0.2-1 %mass demulsifying agent, 0.5-1.5 %mass metal deactivator, 0.2-1 %mass reinforcing agent, 2-5 %mass oiliness agent, 0.5-2 %mass friction modifier and 1-3 %mass dispersant.    USE - Hydrostatic mechanical power split transmission working fluid composition (claimed).    ADVANTAGE - The hydrostatic mechanical power split transmission working fluid composition has excellent viscosity-temperature characteristics, low-temperature fluidity, shear stability, corrosion resistance, air release properties, anti-foaming effect, thermal oxidation stability, hydrolytic stability and wear resistance.
NOVELTY - Substituted N,N-diethyl-N-methylethanaminium 2-phenoxyacetate compounds (I), are new.    USE - (I) are useful in herbicidal composition (claimed).    ADVANTAGE - The method: produces environment-friendly (I) with low volatility and less odor; is simple; and has good solubilizing property, high herbicidal stability and low production and transportation costs.    DETAILED DESCRIPTION - Substituted N,N-diethyl-N-methylethanaminium 2-phenoxyacetate compounds of formula (I), are new.    X1, X2 = Cl, Br, I or H; and    R1 = 1-10C alkyl or H.    INDEPENDENT CLAIMS are also included for:    (1) preparation of (I); and    (2) herbicidal composition, comprising (I) and auxiliary agent.
NOVELTY - Decoloring and purifying azoxystrobin, comprises: (a) completely dissolving azoxystrobin crude product in ethyl acetate at normal temperature, adding activated carbon, stirring for 1-2 hours, and filtering to obtain filtered liquid, and (d) adding the obtained filter liquid in normal hexane, stirring at 0-5 degrees C for 1.5 hours to crystallize, filtering, and drying to obtain purified azoxystrobin.    USE - The method is useful for decoloring and purifying azoxystrobin (claimed).    ADVANTAGE - The method has low energy consumption, easy operation, high yield of more than 80%, and produces white azoxystrobin finished product with excellent quality and increased content of more than 99%.
NOVELTY - A synthetic rubber accelerator CBS plasma oxidation (2-N-cyclohexyl benzothiazole sulfonamide) preparation method comprises mixing 2-mercaptobenzothiazole and deionized water, stirring, adding non-ionic surfactant and amine water solution, stirring for 1 hour, mixing, heating at 35-45 degrees C, putting into ozone plasma generator, carrying out oxidation reaction for 1-4 hours, precipitating, filtering, water washing, and drying.    USE - Synthetic rubber accelerator CBS plasma oxidation (2-N-cyclohexyl benzothiazole sulfonamide) preparation method (claimed).    ADVANTAGE - The method is simple, low-cost, environment-friendly and energy efficient. It has high product yield and suitable for industrialization. The synthetic rubber is suitable for tires, rubber shoes, hose, tape and cable.
NOVELTY - Preparing aztreonam medicinal raw materials based on vertical stream comprises using solvent for crystallization, carrying out solid-liquid separation of liquid material after curing, crystallizing and drying, then after separating solid, transferring solid using gravitation effect.    USE - The method is useful for preparing aztreonam medicinal raw materials based on vertical stream (claimed).    ADVANTAGE - The method avoids environmental pollution problems caused by exposure of aztreonam material during transfer process, uses high level sterile raw material, and uses gravity as the main driving force. The material has high transport efficiency and is economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of vertical stream production of aztreonam medicinal raw materials.
NOVELTY - Producing cefalotin sodium injection, comprises dissolving cefalotin sodium powder in a solvent in vertical logistics system, where the powder is transferred to the system by gravity from an airtight container.    USE - The process is useful for producing cefalotin sodium injection (claimed).    ADVANTAGE - The process is capable of efficiently producing cefalotin sodium injection under sterile environment conditions in a cost effective and eco-friendly manner.
NOVELTY - The method involves combing solvent distribution device (1), a filtering device (2), solid-liquid separate device (3), a drying device (4), a crushing device (5), a storage device (6) and charging device (7). The solution distribution to packaging is finished in a vertical to the stream of system. The crushing device is set with storage device.    USE - Method for preparing clindamycin hydrochloride in vertical to logistics system.    ADVANTAGE - The transfer material avoids the expose caused by environment pollution. The sterile level of the preparation of raw material medicine of sterile level is high with high transport efficiency and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the logistics system.    Solvent distribution device (1)    Filtering device (2)    Solid-liquid separate device (3)    Drying device (4)    Crushing device (5)    Storage device (6)    Charging device (7)
NOVELTY - A clindamycin hydrochloride in vertical logistics system is prepared by using vertical logistics system which consists of solvent distribution device (1), filtering device (2), solid-liquid separation device (3), drying device (4), crushing device (5), storage device (6), and charging device (7), using clindamycin hydrochloride as solvent for crystallization principle, and finishing solution distribution to packaging.    USE - Preparation of clindamycin hydrochloride in vertical logistics system (claimed).    ADVANTAGE - Preparation process avoids environmental pollution, has high transport efficiency, and is low-cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of vertical logistics system.    Solvent distribution device (1)    Filtering device (2)    Solid-liquid separation device (3)    Drying device (4)    Crushing device (5)    Storage device (6)    Charging device (7)
NOVELTY - Preparing 17 alpha -hydroxy progesterone involves reacting 17 beta -cyano-3,3-dioxolanyl-5-androstene-17-ol with dimethylzinc or methyl zinc chloride reagent in presence of lithium/copper chloride catalyst in an organic solvent.    USE - For preparing 17alpha-hydroxy progesterone (claimed), which is a steroid hormone drug which is further used as intermediate for other steroidal hormones.    ADVANTAGE - The method provides 17alpha-hydroxy progesterone in a purity of more than 99.5% (by HPLC detection) and total yield of 83-87%. Compared to prior art methods, it reduces production cost; uses single solvent; simplifies the refining technology, is economical and environment-friendly; and is very suitable for industrial production.    DETAILED DESCRIPTION - Preparing 17alpha-hydroxy progesterone involves: dissolving 17 beta -cyano-3,3-dioxolanyl-5-androstene-17-ol in organic solvent, adding lithium chloride as catalyst, stirring at 40-80 degrees C, dropping 2M of dimethyl zinc or toluene solution of methyl zinc chloride, after completion of reaction, adding 25% ammonium chloride solution, extracting, combining organic layer, then adding low-carbon alcohol, mixing, heating at 40-60 degrees C, adding acid solution, carrying out acid hydrolysis reaction, after completion of acid hydrolysis, adding weak base to adjust the pH, adding water, continuing evaporating solvent, adding tap water, cooling and then crystallizing to obtain crude product of 17alpha-hydroxy progesterone. Reagents as hydrochloric acid or sulphuric acid or phosphoric acid, or organic acid such as acetic acid or p-toluenesulfonic acid.
NOVELTY - Method of preparing controlled-release fertilizer using super absorbent polymer involves (a) preparing aqueous sodium hydroxide solution, (b) adding into acrylic acid, subjecting to neutralization reaction, adding urea and potassium, and cooling mixture, (c) subjecting to copolymerization reaction by adding methylenebisacrylamide, (d) drying the obtained mixture, and (e) crushing the dried mixture to obtain granules.    USE - The method is useful for preparing controlled-release fertilizer in form of granules using super absorbent polymer (all claimed).    ADVANTAGE - The method ensures to prepare stable, environmentally-friendly and cost-effective fertilizer having excellent water absorption rate.    DETAILED DESCRIPTION - Method of preparing controlled-release fertilizer using super absorbent polymer involves (a) weighing 1070 g sodium hydroxide and preparing 32.5% aqueous sodium hydroxide solution, (b) adding the prepared aqueous sodium hydroxide solution drop wise into 2000 g acrylic acid having purity of 99.5% or more, subjecting the resulting mixture to neutralization reaction for 20 minutes, adding 1200 g urea having nitrogen content of greater than or equal to 46%, and 1180 g greater than or equal to 50% potassium sulfate and potassium hydroxide to the obtained neutralized mixture, and cooling the resulting mixture to 56-65 degrees C, (c) subjecting the mixture obtained in the step (b) to copolymerization reaction by adding 5 g cross-linking agent, preferably methylenebisacrylamide, stirring the resulting mixture at 65-70 degrees C and 90-100 revolutions per minute (rpm) for 10 minutes, adding 15 g potassium persulfate to the stirred mixture and reacting the resulting mixture at 110-115 degrees C for 15 minutes, (d) drying the obtained mixture for 10-20 minutes, and (e) crushing the dried mixture to obtain granules.
NOVELTY - Preparation of high-molecular water-absorbing resin potassium-phosphate fertilizer involves preparing sodium hydroxide aqueous solution, dripping resultant product in acrylic acid, carrying out neutralization reaction, adding phosphoric acid and potassium, cooling resultant product, adding polyethylene glycol and crosslinking agent, stirring the resultant product, adding potassium persulfate initiator, carrying out copolymerization reaction, heating resultant product, providing the resultant product into polymerization reactor, drying the resultant product and crushing.    USE - The method is useful for preparing high-molecular water-absorbing resin potassium-phosphate fertilizer (claimed).    ADVANTAGE - The method is cost-effective, and environmentally-friendly, produces high-quality fertilizer with excellent stability, and reduces usage amount of fertilizer. The fertilizer has improved water-retention property.    DETAILED DESCRIPTION - Preparation of high-molecular water-absorbing resin potassium-phosphate fertilizer involves preparing 1560 g 32.5% sodium hydroxide aqueous solution, dripping the resultant product in 3000 g acrylic acid having purity of more than 99.5%, carrying out neutralization reaction for 20 minutes, adding 1500 g phosphoric acid and 2100 g potassium, cooling the resultant product to 56-65 degrees C, adding 80 g polyethylene glycol and crosslinking agent, stirring the resultant product for 10 minutes under 90-100 rpm, adding 15 g potassium persulfate initiator, carrying out copolymerization reaction at 65-70 degrees C, heating the resultant product to 110-115 degrees C for 15 minutes, providing the resultant product into polymerization reactor for 10-20 minutes to obtain solid product, naturally drying the resultant product and crushing.
NOVELTY - The device has a bracket fixed with a heating furnace i.e. biomass semi-gasification furnace. An outer heat preservation cylinder is fixed with an upper part of the heating furnace. The outer heat preservation cylinder and an inner heat preservation cylinder are formed with a hot air cavity. The outer heat preservation cylinder and an upper end of the inner heat preservation cylinder are fixed with a cover body. The cover body is formed with a distillation pyrolysis chamber. A center part of the inner heat preservation cylinder is fixed with a heating tube in a uniform manner.    USE - Biomass pyrolysis temperature balanced outer heating device.    ADVANTAGE - The device is simple in structure and convenient to operate and maintain. The device balances biomass pyrolysis temperature, increase balanced biomass pyrolysis speed and ensures better controllable biomass pyrolysis process safety. The device has high biomass pyrolysis temperature balancing reliability.    DESCRIPTION OF DRAWING(S) - The drawing shows a partial sectional view of a biomass paralysis balanced outer heating device.
NOVELTY - The device has a storage hopper (3) connected with a fermentation chamber (7), a granulator (1) and a conveyor (4). The fermentation chamber is connected with a burning furnace (6) that is connected with a cracking furnace (9) through a gas pipeline (10). A steam pipeline is connected with a bottom part of an air supply pipeline. A heat exchanger is connected with a gas storage tank (16) through another gas pipeline. A tube channel is connected with a pressurizing fan (15). A hopper (8) is connected with a top end of the fermentation chamber.    USE - Bio-mass material conversion biological energy device.    ADVANTAGE - The device improves energy conversion and economic efficiency and avoids biological energy loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bio-mass material conversion biological energy device.    Granulator (1)    Storage hopper (3)    Conveyor (4)    Burning furnace (6)    Fermentation chamber (7)    Hopper (8)    Cracking furnace (9)    Gas pipeline (10)    Pressurizing fan (15)    Gas storage tank (16)
NOVELTY - The furnace has a dual-tapered structure shaped furnace body provided with a furnace cover, an air entrance, a steam inlet, an electric ignition device, a jacket water entrance, a gas exit, a water exit and a heat preservation layer. The furnace body is arranged with a drying layer, a solution layer, a silicon oxide layer and a reducing layer. A side wall of the furnace body is connected with an air nozzle. The furnace body is arranged on a lower part of an oxidation area to produce carbon dioxide.    USE - Reverse combustion-type dual-medium domestic rubbish gasification furnace for an automatic household rubbish processing system (claimed).    ADVANTAGE - The furnace achieves harmless solid waste disposal facilities and reduces resource requirements.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a reverse combustion-type dual-medium domestic rubbish gasification furnace.
NOVELTY - The method involves connecting a biomass gasification furnace with a tube type gas-liquid heat exchanger. A gas storage device is fixed with the biomass gasification furnace. Direct-combustion fuel is generated with direct drive energy. Biomass gasification smoke is transmitted to a water gas direct combustion machine. A temperature sensor is fixed on the tube type gas-liquid heat exchanger. A temperature control system is fixed with a fan and a spiral blade, where heating temperature of direct-combustion fuel is 200 degree Celsius.    USE - Small-scale biomass gasifier combined cold-heat power supplying method.    ADVANTAGE - The method enables increasing material motor rotating speed and biomass gasification precision, providing reasonable configurations, reducing temperature waste and improving energy utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a small-scale biomass gasifier combined cold-heat power supplying system.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic block diagram of a small-scale biomass gasifier combined cold-heat power supplying system. '(Drawing includes non-English language text)'
NOVELTY - Synthetic fuel comprises (in wt.%): methanol (40-75), acetone (5-30), water (5-30), displacing agent (1-10), and dust removing agent (1). The displacing agent is selected from petroleum ether, n-heptane, toluene, n-pentane or eicosapentaenoic acid. Molar ratio of mixing methanol, acetone, water, displacing agent, and dust removing agent is 1:2:2:1:2.    USE - Synthetic fuel.    ADVANTAGE - The synthetic fuel is eco-friendly in application.
NOVELTY - A vehicle fuel comprises 25-65 wt.% alcohol, 3-5 wt.% emulsifier, 20-45 wt.% aromatic hydrocarbon and 15-35 wt.% solvent oil. The alcohol is methanol, t-butanol or cyclohexanol. The emulsifier is ether, isopropanol, acetone and/or butanol. The aromatic hydrocarbon is benzene, toluene and xylene.    USE - Vehicle fuel (claimed).    ADVANTAGE - The vehicle fuel has octane number of 110-118, and excellent combustion property and storage property. The component using the fuel has excellent corrosion resistance and suppressed deterioration.
NOVELTY - Biomass fuel comprises (in pts.wt.): wood powder (1-3), peanut shell powder (2-4) and straw powder (4-6).    USE - Biomass fuel.    ADVANTAGE - The biomass fuel is eco-friendly and cost-effective, and solves agricultural and forestry waste disposal problems and alleviates the current shortage of fuel energy problems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass fuel, which involves:    (A) crushing wood dust, peanut shell and straw in a crusher to obtain 30 to 50 meshes wood powder, peanut shell powder and straw powder;    (B) mixing wood powder, peanut shell powder and straw powder and then drying the mixed material to reduce the water content to 25%; and    (C) pressing the dried mixture into blocks to obtain finished product.
NOVELTY - A small Aeromonas i.e. Micromonospora aurantiaca strains, Accession No. CGMCC No.8215, is new.    USE - Aeromonas i.e. Micromonospora aurantiaca strains for degradation terpenes such as alpha-pinene, or terpene based compound such as benzene compound, which are synthesized from chemical industry waste water treatment process (all claimed).    ADVANTAGE - The strains have good treatment effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of small Aeromonas i.e. Micromonospora aurantiaca strains for degradation of terpenes by collecting cells by centrifugation, washing growth phase of the small number of strains of Aeromonas, with sterile water, after resuspension in sterile water adjusted OD to 1.5, to give fresh broth, inoculating into fresh broth containing alpha - alpha-pinene as the sole carbon source and inorganic salt in liquid medium and shaking flask culture.
NOVELTY - Producing biogas by dry-type anaerobic fermentation of cyanobacteria, reed and rice straw comprises (i) crushing reed shoot tip section and rice straw into small pieces, and mixing the crushed reed and rice straw; (ii) mixing cyanobacteria with animal manure, and carrying out wet fermentation; (iii) adding the crushed material of step (i) during wet fermentation process to produce biogas, then mixing the obtained biogas in the mixing device; (ii) carrying out dry anaerobic fermentation at 25-55 degrees C; and (v) purifying the collected biogas, and storing in the gas tank.    USE - The method is useful for producing biogas by dry-type anaerobic fermentation of cyanobacteria, reed and rice straw (claimed).    ADVANTAGE - The method does not produce secondary pollution.    DETAILED DESCRIPTION - Producing biogas by dry-type anaerobic fermentation of cyanobacteria, reed and rice straw comprises (i) crushing reed shoot tip section and rice straw into small pieces, and mixing the crushed reed and rice straw in the mass ratio of 1:(1-3); (ii) mixing cyanobacteria having water content of 90-95% with animal manure in the mass ratio of 5:(1-2), and carrying out wet fermentation; (iii) adding the crushed material of step (i) during wet fermentation process to produce biogas, then mixing the obtained biogas in the mixing device, where the mass ratio of biogas to crushed material is 2-2.5:1; (ii) carrying out dry anaerobic fermentation at 25-55 degrees C; and (v) purifying the collected biogas, and storing in the gas tank.
NOVELTY - Fermentative production of ethanol from plant straw, comprises adding the plant straw with sugar and then hydrolyzing on a fermentation substrate, and adding manganese ion and yeast in a fermentation medium and then fermenting.    USE - The method is useful for fermentative production of ethanol from plant straw (claimed).    ADVANTAGE - The method is capable of fermentatively producing the ethanol from plant straw with improved yield.
NOVELTY - Increasing yield of ethanol by plant straw fermentation, comprises taking plant straw hydrolyzed sugar as fermentation substrate, adding lecithin into a fermentation culture medium, and producing ethanol through yeast fermentation.    USE - The method is useful for increasing yield of ethanol by plant straw fermentation. The culture medium is useful in fermentative production of ethanol (all claimed).    ADVANTAGE - The method increases the yield of ethanol; ensures development and utilization of plant stalks, reduction in environmental pollution, and food security.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a culture medium for fermentation production of ethanol, comprising 16-30% (wt./vol.) reducing sugar of plant straw hydrolyzed sugar, 0.4-0.7% (wt./vol.) yeast extract, 0.2-0.5% (wt./vol.) peptone, 0.01-0.1% (wt./vol.) urea, and 30-100 mg/l lecithin, where the pH is 3.5-6.5 and temperature is 30-32 degrees C.
NOVELTY - A photoelectric catalytic membrane comprises halogen bismuth oxide based cathode chamber and anode chamber, diaphragm, and electrolytic solution, where the metals and its oxides are utilized as anode, hydrogen storage materials as cathode, xenon lamp as light source, under applied voltage of 1-8 V of photoelectrocatalytic decomposition of water into hydrogen generated at the on-line storage of the cathode hydrogen storage material, where the film thickness is 100. 05 mu m.    USE - Photoelectric catalytic membrane for water synergistic catalytic decomposition of hydrogen in on-line electrochemical hydrogen storage.    ADVANTAGE - The membrane provides hydrogen high quantum efficiency of 90-96%, and high purity of hydrogen of 99-99.9%.
NOVELTY - The device has a device body provided with a U-shaped shell that is fixed with a middle ring (7). The middle ring and side parts of the U-shaped shell are connected with a circular-shaped thin film sheet (6) that is formed with a pneuma hole. A hydrogen entrance part (1) and a gas exit (4) are formed with a hydrogen cavity. An oxygen entrance part (12) and an oxygen exit are formed with an oxygen cavity. The thin film sheet is fixed with an inner part of a circular-shaped moving film (8). A side part of the middle ring is formed with the pneuma hole. The oxygen cavity is formed on a lug boss.    USE - Water electrolysis hydrogen double-film gas balance device.    ADVANTAGE - The device avoids thin film sheet damage, gas leakage by using the middle ring and safety hidden trouble.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a water electrolysis hydrogen double-film gas balance device.    Hydrogen entrance part (1)    Gas exit (4)    Thin film sheet (6)    Middle ring (7)    Moving film (8)    Oxygen entrance part (12)
NOVELTY - This new type utility claims one a multifunctional water ecological restoration device, include culture room, the culture room is provided with a water outlet, the bottom is provided with inlet and outlet, the culture room through connecting piece connecting with outside floater, inlet and outlet connecting with a water device, and the water outlet with a nozzle, a culture room inner is provided with ecological, ecological restoration device mounting a control with a device with a water inlet distribution box, the water inlet a device with waterproof function, a water inlet device sleeved with a filter grid, said connecting piece is a fixed connecting rod, a floater is floating between the water outlet and the spray head mounting a monitoring instrument, a monitoring instrument monitoring culture water of room temperature, the flow amount and pressure, the utility model is new type of beneficial effects: practical, production cost is low, the use is convenient, promoting microorganism breeding, improving water environment and increase water dissolve oxygen content, increase quality of water, recovering, as ornament can be put on a use.
NOVELTY - The utility model claims a new sewage purification processing technique area, especially claims using microorganism to process purification treatment and sewage microorganism sewage purification device, comprising mutually connected with the supporting device and microorganism fixing device, also comprising device and floating aeration device, the aeration device and holding device and the fixing device respectively connected with microorganism, the floating device and the supporting device mutually connected. And the existing technology, this utility new type has simple designing optimizing, using suitable operation, make sewage purification treatment and to obtain greatly increase efficiency, solving of sludge problem, notable reducing of operating cost low, prolonging of using life, can avoid generating the full second time pollute, and, mounting and dismounting maintain is simple and fast, shows full of purification treatment effect and green environmental protection and is suitable for the river and lake at equal treatment sewage purification processing area and application.
NOVELTY - This new type utility also claims a one cassava alcohol waste water depth processing system of, in turn comprise of a fluidized bed, anaerobic film biological reactor, middle pool and device. This new type utility also claims a one cassava alcohol waste water depth processing process of, cassava ethanol after multi-stage anaerobic biogas pneuma produce a waste water, sequence entering into the anoxic fluidized bed, a membrane biological reactor, middle tank and a nanofiltration device, filter water outlet;
NOVELTY - This new type utility claims chicken manure turn polishing machine, wherein the turner comprise beam, motor, turning component and walking mechanism, electric machine fixed on the beam two end, an electric machine and a speed reducer, a walking mechanism comprise transverse shaft and fixed on the walking wheel of two end cross shaft, a cross shaft of walking wheel upper fixed with a belt wheel, a belt wheel is connected with reducer through connecting end, lower beam end through a column and the polishing component turn connecting. Usually uses a static compost chicken manure, chicken manure accumulation on the inner cover in advance a good , the walking wheel of the walking mechanism is placed on the two side, a walking, at the same time, the component in the process of machine in operation, using the blade and shovel continuously crushing effervescent chicken manure, chicken manure so that inner of bacterial oxygen supply is enough, the anaerobic fermentation and reduces environment pollution.
NOVELTY - This utility new type claims a one pneuma with smoke waste heat utilization function of bamboo wood carbonization kiln furnace, comprise several refractory brick stacked by multiple chamber is formed of several said chamber upper end is a opening of sealing cover, a multiple chamber comprise combustion room, preheating room and drying room, a combustion chamber, a pre-heating room and the drying room through smoke pneuma channel in turn, said inner combustion room is used for placing set with a firewood combustion chamber. This utility new type a the pneuma with smoke waste heat utilization function of bamboo wood carbonization kiln furnace can make full use of the flue gas waste heat of kiln furnace, increase energy utilization rate, but also greatly shortens the whole bamboo charcoal production period, increase bamboo charcoal.
NOVELTY - This utility new type claims a one produce biogas by making use of straw of two-way backflow anaerobic reaction system and reactor, refluxing the anaerobic reactor comprise a tank body, the upper set with stir device, stir device comprise inner set in a tank body of multi-liquid tube and multi-root of marsh gas tube, a liquid tube passes through a rear tank body a slurry return pipe, and the other end a liquid return pipe connecting to a side wall of a tank body of a biogas slurry with a tank body inner connected, a biogas reflux pipeline set with a pressurizing pump, a rear tube passes through a marsh gas tank connect the marsh gas return pipe, a biogas reflux pipeline used for connecting to marsh gas tank. This utility new type, using biogas slurry reflow pipeline and return pipeline form gas path, the material of inner tank form lengthways flow, increase stir strength, increase the fermentation efficiency, increase the production rate. And the main power device located on stir reactor, a convenient maintenance.