NOVELTY - Manufacturing fermented material, involves collecting livestock excrement at one side of livestock barn, adding moisture controlling agent to the livestock excrements to control the moisture content of the livestock excrement, adding thermophiles to the livestock excrement, stirring the mixture, stacking the stirred livestock excrement on the bottom of the livestock barn, subjecting the stacked product to primary fermentation, subjecting the obtained product to secondary fermenting process, and performing final fermentation process.    USE - The method is useful for manufacturing fermented material.    ADVANTAGE - The method eliminates unpleasant odors emanating from the fermented material, and improves convenience of an excrement collecting process.    DETAILED DESCRIPTION - Manufacturing fermented material, involves collecting livestock excrement at one side of livestock barn, adding moisture controlling agent to the livestock excrements to control the moisture content of the livestock excrement to 50-70 wt.%, adding thermophiles to the livestock excrement, stirring the mixture, stacking the stirred livestock excrement on the bottom of the livestock barn, subjecting the stacked product to primary fermentation using aerobic cold active bacteria at 60-70 degrees C, turning the stacked material over after a pre-set period, subjecting the obtained product to secondary fermenting process, and performing final fermentation process until the moisture content of the secondary fermented product reaches 15-20 wt.%. An INDEPENDENT CLAIM is included for method of removing stink of the livestock shed, which involves sprinkling above-mentioned fermentation product to the livestock excretions at bottom surface and eliminating unpleasant odor within the livestock shed.
NOVELTY - A Chinese medicinal herb nutrient fertilizer comprises (in g) dried sheep droppings (30000), dried poultry litter (30000), dried rabbit dung (30000), pumpkin powder (30000), balsam pear powder (30000), sorghum flour (30000), pine needle meal (50000), wood ash powder (50000), bean orange powder (50000), monopotassium phosphate (20000), eucommia ulmoides (10000), lemery salt (5000), plantain seed powder (5000), elecampane (5000), dried tangerine or orange peel (3000), insecticide (3000), degerming agent (2000), towel gourd powder (5000g) and phenolic resin (15000).    USE - Chinese medicinal herb nutrient fertilizer for a red paeony root.    ADVANTAGE - The fertilizer is environment-friendly, and has rich nutrient content. The fertilizer ensures that a red paeony root has quick growing speed, thick leaves, large fruit, better disease preventing ability and strong pesticidal effect.
NOVELTY - A green multifunctional composite ecological organic liquid fertilizer comprises (in weight parts) medical stone powder (40-240), photosynthetic bacteria liquid (0.05-2), brown sugar (0.5-2), honey (0.5-2), yeast powder (0.04-0.2), liquorice (0.4-2), alum (0.1-2), folium Artemisiae argyi (0.5-2), calamus (0.3-2) and water (1760-1960), where granularity of the medical stone powder is of 200-400 meshes.    USE - Green multifunctional composite ecological organic liquid fertilizer.    ADVANTAGE - The fertilizer can increase phosphorus, compensate potassium and supply oxygen to provide rich nitrogen phosphorus potassium elements for crop. The fertilizer compensates elements of calcium, magnesium, sulfur, copper, iron, zinc, boron, molybdenum, manganese and silicon so as to avoid slow growth and cleaf blight output-decrease caused by lacking certain nutrient. The fertilizer can increase drought resistance, cold-proof ability, antifalling ability and anti-disease ability. The fertilizer loosens the soil and accelerates the soil to form granule structure, change physical and chemical properties, and realize nutrient supply of the whole process. The fertilizer has wide application range and strong affinity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing green multifunctional composite ecological organic liquid fertilizer.
NOVELTY - A pollution free pesticide composition manufacturing method involves manufacturing pyroligneous liquor. Salt is refined and mixed with a charcoal raw material. Charcoal is manufactured to heat a charcoal kiln after the recovery of vapor, where the charcoal is pulverized to form charcoal powder. The liquor with 1:10-10:1 weight ratio is mixed with water and charcoal powder, which are inturn mixed at a ratio of 1:50-100. Japanese apricot of 50-150g is mixed with the liquor. The liquor is fermented.    USE - Method for manufacturing pollution free pesticide composition to provide nutrition to plants.    ADVANTAGE - The method enables manufacturing charcoal powder that remains behind in soil, so that soil absorbing chemical fertilizer components are acidified and neutralized, and the heavy metal existing in soil can be adsorbed, thus reducing the risk of accumulation of heavy metal in the human body. The composition prevents infection of microorganism such as bacteria, spore and virus, thus improving the growth promotion, harvest enlargement and quality of the plants.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing pollution free pesticide composition.'(Drawing includes non-English language text)'
NOVELTY - An oxygen and hydrogen generation device is provided, which mainly contains at least an electro bath, an electrolyte supply tank, a coolant supply tank, an electrolyte storage tank, a coolant storage tank, and a power switchboard. Along the lateral sides of the electrolyte and the coolant supply tanks, level sensing tubes along with at least a level sensor are configured, respectively. Inside the electrolyte and coolant storage tanks, electrical pumps are provided which are controlled by the level sensors of the electrolyte and the coolant supply tanks, respectively. Whenever the electrolyte and the coolant inside the respective electrolyte and the coolant supply tanks have dropped below their respective level sensors, the electrical pumps are automatically engaged to refill the electrolyte and coolant supply tanks, without shutting down the device. Image 0/0
NOVELTY - A compound (1S, 2S, 3R, 5S)-pinanediol-L-phenylalanine-L-leucine boric acid ester preparation method involves performing triphosgene reactions on L-phenylalanine at 20-150 degrees C for 1-50 hours to obtain reaction solution. The reaction solution is concentrated. The concentrated solution is dissolved in organic solvent. (1R)-(S)-pinanediol-1-trifluoroacetate-3-methyl butane-1-boric acid ester is dissolved in alkali at -20-20 degrees C, and dripped in the reaction solution and agitated.    USE - Method for preparing compound (1S, 2S, 3R, 5S)-pinanediol-L-phenylalanine-L-leucine boric acid ester.    ADVANTAGE - The method enables preparing compound (1S, 2S, 3R, 5S)-pinanediol-L-phenylalanine-L-leucine boric acid ester with high yield in a simple and eco-friendly manner. The method enables preparing the ester for industrial production.
NOVELTY - An imatinib intermediate comprising substituted pyrimidine compound (I) method involves performing reduction process by reacting nitro substituted pyrimidine compound (II) with organic solvent in the presence of catalyst to obtain product.    USE - Method for preparing imatinib intermediate comprising substituted pyrimidine compound.    ADVANTAGE - The method enables preparing imatinib intermediate that is suitable for industrial production, in a simple and environment-friendly manner, and shortening the reaction time.    DETAILED DESCRIPTION - An imatinib intermediate comprising substituted pyrimidine compound of formula (I) method involves performing reduction process by reacting nitro substituted pyrimidine compound of formula (II) with organic solvent in the presence of catalyst to obtain product..
NOVELTY - An organic potassium fertilizer is prepared by fermenting apple pomace raw material and heating and hydrolyzing the raw material with potassium hydroxide solution to prepare biological organic potassium acid water-soluble organic matter. The biological organic potassium acid water-soluble organic matter is neutralized to remove excess potassium hydroxide with biological organic acid. The neutralized product is filtered to obtain organic potassium fertilizer.    USE - Organic potassium fertilizer.    ADVANTAGE - The fertilizer eliminates discharge of waste water, waste liquid and waste residue during producing process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an organic potassium fertilizer.
NOVELTY - A heater (4) maintains the temperature of oil according to maintenance or driving condition. A blowing pump (15) transmits the oil with moisture in vacuum chamber (9) to vacuum chamber (19). A blowing pump (21) transmits the oil in vacuum chamber (19) to heat exchanger. An ejector (29) lets steam evaporated from oil in vacuum chambers to outside. A check valve (32) and solenoid valve (33) prevents backward flow of water to vacuum chambers. A vacuum control valve (34) regularly controls the vacuum of vacuum chambers.    USE - Oil water removal unit for removing moisture in oil e.g. disposable edible oil and bio-diesel oil.    ADVANTAGE - The moisture contained in oil can be removed completely by oil water removal unit. The production efficiency of removal unit can be improved. The fuel consumption is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the oil water removal unit.    Heater (4)    Vacuum chambers (9,19)    Blowing pumps (15,21)    Ejector (29)    Check valve (32)    Solenoid valve (33)    Vacuum control valve (34)
NOVELTY - A trinary aluminum alloy contains an electrochemical noble element and an element weakening aluminum film, distributed into aluminum.    USE - Trinary aluminum alloy for producing hydrogen used for fuel cell used as power supply for mobile telephone, notebook personal computer, personal digital assistant, portable electronic equipments and vehicles (all claimed).    ADVANTAGE - The ternary aluminum alloy accelerates corrosion in an alkaline solution, and safely produces hydrogen at high speed through hydrolysis.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of trinary aluminum alloy; and    (2) use of trinary aluminum alloy.
NOVELTY - Method for deoderization of bad smelling organic waste, involves manufacturing fertilizer by crushing organic waste residues having a particle size of 150-180 mu m, pulverizing calcium oxide, mixing crushed residues and pulverized material and drying the mixture.    USE - The method is useful for deoderization of bad smelling organic waste which is useful for preparing fertilizer as by product (claimed).    ADVANTAGE - The fertilizer does not contain heavy metals. The method is economical and environmentally-friendly.
NOVELTY - A sodium hydrosulfide solution is reacted with dimethyl terephthalate in presence of an organic solvent solution to obtain methyl 4-formyl benzoate. A sodium bisulfite additive aqueous solution of methyl 4-formyl benzoate is separated from the obtained reaction mixture, and activated with hydroxylamine. The obtained product is filtered, separated, and dried to obtain hydroxyiminomethyl benzoate.    USE - Manufacture of hydroxyiminomethyl benzoate used as raw material for polymer, and intermediate for pharmaceuticals.    ADVANTAGE - The method efficiently and economically provides hydroxyiminomethyl benzoate having excellent recycling property and purity by simple method with reduced generation of byproduct.
NOVELTY - A 1-(2-chloro-5-thiazolemethyl)-3-methyl-5-amido-hexahydro triazine-2N-nitroimino compound (I) is new.    USE - New 1-(2-chloro-5-thiazolemethyl)-3-methyl-5-amido-hexahydro triazine-2N-nitroimino compound for preparing pesticide (claimed).    ADVANTAGE - The compound has better insecticidal effect and less toxicity, and is simple to prepare and use in an eco-friendly manner.    DETAILED DESCRIPTION - A 1-(2-chloro-5-thiazolemethyl)-3-methyl-5-amido-hexahydro triazine-2N-nitroimino compound of formula (I) is new.    R=alkyl, heterocyclyl, benzyl, substituted benzyl, substituted phenyl, or substituted aromatic ring.    INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing new nicotine clothianidin compound    (2) a pesticide.
NOVELTY - A clarithromycin preparation method involves subjecting (2', 4''-O-trimethylsilyl)-erythromycin A-9 (O-(1-ethoxy-1-methyl-ethyl)) oxime in methylation reaction and methylate de-protection reaction to obtain clarithromycin.    USE - Method for preparing clarithromycin.    ADVANTAGE - The method enables preparing clarithromycin in a simple, cost-effective and environment friendly manner, and achieving industrial production.
NOVELTY - A hydrocarbon fuel preparing method involves adding ethanol and white liquor to grease. The obtained mixture is saponified. The ethanol and fatty acid salt are decompressed, recycled and dried after finishing saponification process. Residual liquid is mixed with residual alkali and stirred. Phosphoric acid is added to the obtained liquid and reacted at constant temperature. The mixture is refined, and the ethanol is recycled to obtain lower layer phosphate. The fatty acid salt is added into a microwave pyrolysis reactor. Gaseous, liquid and residual solid products are collected.    USE - Method for preparing hydrocarbon fuel using soap decarboxylation.    ADVANTAGE - The method enables utilizing raw materials of biologic oil saponification so as to improve polarity of the raw materials, and preparing the hydrocarbon type fuel with better biodiesel oxidation stability and lower freezing point.    DETAILED DESCRIPTION - A hydrocarbon fuel preparing method involves adding 95% of ethanol and 0.5-30% of white liquor to grease for 0.1 to 1.5 times. The obtained mixture is saponified under condition of 40-100 degrees C for 0.5 to 3 hours. The ethanol and fatty acid salt are decompressed, recycled and dried after finishing saponification process. Residual liquid is mixed with residual alkali and stirred. 40% of phosphoric acid is added to the obtained liquid and reacted at constant temperature, where pH of the phosphoric acid is adjusted to 7-8. The mixture is refined, and the ethanol is recycled to obtain lower layer phosphate, where fertilizer is collected. The fatty acid salt is added into a microwave pyrolysis reactor for cracking decarboxylation. Gaseous, liquid and residual solid products are collected, where quality ratio of the products is 1:7:2, the liquid product yield reaches 65-75%, and the liquid product is naphtha, petrol, kerosene, diesel oil and lubricating oil in a ratio of 1:7:10:2:1.
NOVELTY - Composting raw wool cylinder waste comprises adding raw wool cylinder waste, water and composting strain, stirring, stacking in a trapezoid-shape, fermenting, increasing the fermentation temperature to 60-70 degrees C, turning, cooling, re-stacking in a trapezoid-shape, maintaining the temperature at 60-70 degrees C, fermenting until the moisture content of the material is reduced to 13-17%, flattening the fermented material until the moisture content is reduced to 10%, re-stacking the prepared material, sealing using a plastic sheet and aging for one week to obtain an organic fertilizer.    USE - The method is useful for composting raw wool cylinder waste.    ADVANTAGE - The method: improves the utilization rate of raw wool; reduces the waste disposal load; is efficient in processing the organic matter of waste; saves the fertilizer components which prevents the agglomeration of loose soil; and is environment-friendly and energy saving.    DETAILED DESCRIPTION - Composting raw wool cylinder waste comprises: (a) adding water (20-25% of the total weight of the raw wool cylinder waste) and composting strain (3-5% of the raw wool cylinder waste) to the raw wool cylinder waste, stirring, stacking in a trapezoid-shape and fermenting; (b) increasing the fermentation temperature to 60-70 degrees C, turning, cooling, re-stacking in a trapezoid-shape, maintaining the temperature at 60-70 degrees C and fermenting until the moisture content of the material is reduced to 13-17%; (c) flattening the fermented material until the moisture content is reduced to 10%; and (d) re-stacking the prepared material, sealing using a plastic sheet and aging for one week to obtain an organic fertilizer.
NOVELTY - Preparation of frangulin B involves taking and crushing cascara bark and adding ethanol into a microwave extracting device. The obtained extracting liquid is filtered, decompressed and recycled by utilizing ethanol. The obtained product is concentrated by utilizing ethyl acetate and isorpopanol/water. The concentrated product is subjected to counter-current extraction. The obtained product is decompressed and treated with ethyl acetate and ethanol. The obtained product is added with acetone and separated crystal. The obtained product is washed and dried to obtain the product.    USE - Frangulin B is used for inhibiting platelet aggregation and has antitumor activity.    ADVANTAGE - The method enables facilitating simple operation and preventing environment pollution. The method enables producing the product with high purity.    DETAILED DESCRIPTION - Preparation of frangulin B involves taking cascara bark, crushing and adding 8-12 times volume of ethanol with concentration of 50-70 percent into a microwave extracting device for microwave extraction, where extracting power is 300-600 watt. The obtained extracting liquid is filtered, decompressed and recycled by utilizing ethanol. The obtained product is concentrated by utilizing ethyl acetate and isorpopanol/water at a ratio of 3: 1. The concentrated product is subjected to counter-current extraction at 6-8 stages. The obtained product is decompressed and treated with ethyl acetate and ethanol. The treated product is passed through macro-porous absorption resin and collected eluent. The obtained product is added with acetone and separated crystal. The obtained product is washed and dried to obtain the product.
NOVELTY - An organic fertilizer producing method involves using livestock as raw material, mushroom, chaff and rotten acid soil as auxiliary material, and adding with organic matter-decomposing inoculant. The mixture is uniformly stirred. Blast air is utilized for fermenting compost. Ripening and packing processes are performed for producing organic fertilizer. A fermentation tank is built on slope. A metal applied layer is crossed by front and rear slopes to form suspend rock as an air channel. A static aeration system is formed by an external timing fan blower.    USE - Method for producing organic fertilizer by fermentation method.    ADVANTAGE - The method enables using an animal to save investment, and ensuring easy ferment operation, humus, easy popularization and sterilizing and deodorizing effects and high harmless degree product quality, thus improving production efficiency, and reducing pollution during production.    DETAILED DESCRIPTION - An organic fertilizer producing method involves using livestock as raw material, mushroom, chaff and rotten acid soil as auxiliary material, and adding with organic matter-decomposing inoculant. The mixture is uniformly stirred. Blast air is utilized for fermenting compost. Ripening and packing processes are performed for producing organic fertilizer. A fermentation tank is built on slope. A hill shaped part is built in multiple ramp staggered floors of the fermentation tank. A metal applied layer is crossed by front and rear slopes to form suspend rock as an air channel. A static aeration system is formed by an external timing fan blower.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for producing organic fertilizer.
NOVELTY - An organic fertilizer comprises (in weight parts) xylitol slag (800-1000), plant ash (200-300), wheat straw (200-300), bean pulp (80-100), urea (25-30), potassium dihydrogen phosphate (6-10) and heptahydrate magnesium sulfate (4-6).    USE - Organic fertilizer for vegetable of winter heating type greenhouse, early spring greenhouse and small tunneland land.    ADVANTAGE - The fertilizer has low production cost and has high pertinence, and reduces labor intensity and saves time. The fertilizer is environment-friendly, and improves quality of vegetable product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an organic fertilizer.
NOVELTY - A plant source pesticide contains effective components extracted from raw materials such as thunder god vine, henbane, tung tree and camptothecin.    USE - Plant source pesticide for preventing multiple pests.    ADVANTAGE - The pesticide has simple constituent, and avoids environment pollution. The pesticide does not generate any residues on grain and economic crop and ensures low toxicity to human and livestock. The pesticide does not generate drug resistance, so that the pesticide has better pesticidal effect. The pesticide can be prepared in a simple manner. The pesticide has high yield and high stability, and is easy to store and use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing plant source pesticide.
NOVELTY - Method involves mixing starting low-sulphur diesel fuel with a product of re-esterification of plant oil with an aliphatic alcohol - butyl ether of rape-seed oil acids obtained in the presence of concentrated sulphuric acid. The starting diesel fuel is preferably mixed with butyl ether of rape-seed oil acids in weight ratio between 99:1 and 95:5. Antioxidant additive Agidol-12 is additionally added to the said mixture in amount of 0.1 wt %.    USE - Chemistry.    ADVANTAGE - Obtaining diesel fuel with higher lubricating power.
NOVELTY - The manner of composting of distillery decoction, especially cereal or melas
NOVELTY - Apparatus comprises base (10) for loading an organic fertilizer producing unit and control operation unit. A feeding portion (20) feeds dead fish and primarily pulverizes the dead fish. The pulverized dead fish is transferred. A pulverizing portion (30) secondarily and thirdly pulverizes the transferred dead fish. A drying portion (40) dries the pulverized dead fish.    USE - The apparatus is useful for producing organic fertilizer.    ADVANTAGE - The apparatus simultaneously performs drying process and sterilizing process and maintains drying temperature of furnace at 280-350 degrees C.    DETAILED DESCRIPTION - Apparatus comprises base (10) for loading an organic fertilizer producing unit and control operation unit. A feeding portion (20) feeds dead fish and primarily pulverizes the dead fish. The pulverized dead fish is transferred. A pulverizing portion (30) secondarily and thirdly pulverizes the transferred dead fish. A drying portion (40) dries the pulverized dead fish. The pulverizing portion includes a first cylindrical structure (31), a second cylindrical structure (32), a third cylindrical structure, and a second gear motor (34). The drying portion includes a drying furnace and a stirring plate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of apparatus.    Base (10)    Feeding portion (20)    Pulverizing portion (30)    First cylindrical structure (31)    Second cylindrical structure (32)    Second gear motor (34)    Drying portion (40)
NOVELTY - A solid base catalyst comprises (wt.%) sodium pyrazine hydroxy ethylidene diphosphonic acid (Na2Cu3(Pz)(hedp)2(H2O2)) (92-96), and sodium hydroxide (8-4).    USE - A solid base catalyst for preparing a biodiesel used in the microwave transesterification (claimed).    ADVANTAGE - The solid base catalyst obtains high biodiesel production rate of 94%. The method for preparing the biodiesel allows fast reaction speed, simple operation, low energy consumption, and less pollution using soybean oil to prepare the biodiesel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the solid base catalyst, comprising adding 5-20 times water to dissolve copper chloride, copper acetate, or copper nitrate; adding 0.5-3 times hydroxy ethylidene diphosphonic acid and 0.5-2 times pyrazine; adding 4-12 times sodium hydroxide after stirring; placing the mixture in a reaction kettle to react for 24-72 hours at 120-160 degrees C; drying to obtain pyrazine hydroxy ethylidene diphosphonic acid sodium solid; grinding, filtering, and soaking in 0.1-1 mol/K sodium hydroxide solution for 24 hours; soaking for 8 hours in deionized water; and roasting for 3-6 hours at 250-320 degrees C; and    (2) preparing the biodiesel, comprising placing soybean oil in a reactor; radiating with microwave to remove moisture; adding methyl alcohol, where the molar ratio of the methyl alcohol and oil is 3:1-10:1; adding the catalyst, where the catalyst is 2-8% of the soybean oil, the output power of the microwave radiation is 240- 600 W; carrying out ester exchange reaction for 15-40 minutes; and separating the solid catalyst by filtering.
NOVELTY - A 2-8C aliphatic diamine is reacted with dialkyl carbonate in presence of 1-6C alcohol and water as reaction accelerators, at low temperature to obtain monocarbomate. The obtained monocarbonate is heated at high temperature to obtain aliphatic dicarbamate.    USE - Manufacture of aliphatic dicarbamate used as intermediate of insecticide.    ADVANTAGE - The method economically provides aliphatic dicarbamate with high yield and selectivity, without polluting the environment.
NOVELTY - Apparatus comprises agitating blade, hopper for injecting fermented manure containing mixture of sewage sludge, soil microbes and livestock excrement sample, hot wind injection device for spraying the hot air into fermenting device, stirrer for mixing manure and soil microbes, and uploading device for ejecting the dried fermented manure.    USE - The apparatus is useful for preparing fermented manure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) use of soil microbes chosen from Bacillus megaterium, B.polymyxa, B.stearothermophilus, and B.subtilis for preparing fermented manure; and (2) fermented manure obtained from soil microbes.
NOVELTY - The method involves performing photocatalytic decarboxylation of acetic acid by using titanium dioxide as a catalyst and photocatalyst hydrated amorphous titanium dioxide with doped anatase and rutile.    USE - Method for preparing mixture of hydrogen and aliphatic hydrocarbons i.e. methane.
NOVELTY - Composition comprises a low molecular weight silver-alginate with molecular weight of 3000-50000 Da, and a low molecular fucoidan with molecular weight of 3500-45000 Da.    USE - The composition is useful for controlling insects, and promoting growth of crops.    ADVANTAGE - The composition exhibits excellent antibacterial activity, reduces usage of chemical pesticide, hence it does not cause harm to human, is less labor-intensive and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the composition, which involves dissolving the silver alginate and fucoidan in water, adding surfactant to the dissolved products, dropping a insecticide chosen from matrine, nicotine and pyrethrin to the obtained solution and mixing the solution.
NOVELTY - A carbochemical hexane fraction refining method involves subjecting the hexane fraction to a hydrogen refining process in the presence of catalyst containing nickel (45-55 weight%), zirconium dioxide (1.5-3.5 weight%) and silicon oxide carrier at 100-200 degrees C and at 1-5 MPa.    USE - Method for refining a carbochemical hexane fraction.
NOVELTY - Vacuum is created in a reactor. Water is fed into the reactor and aluminium wire is passed between electrodes of the reactor. An electric pulse with energy 10-20 kJ/g is periodically transmitted to the electrodes and initial explosion of the aluminium wire takes place to obtain liquid aluminium nanoparticles in water, which form aluminium oxides and hydrogen which fills the space above the water. Further, explosion of the aluminium wire takes place in a hydrogen medium. The wire is exploded in water at temperature lower than 80 degrees C.    USE - Chemistry.    ADVANTAGE - Invention increases efficiency and reduces power consumption of the process and increases purity of hydrogen. 2 cl, 1 dwg, 1 tbl, 1 ex
NOVELTY - A polymer electrolyte membrane comprises hydrogen ion conductivity copolymer (I).    USE - Polymer electrolyte membrane for a membrane electrode assembly (MEA) of a polymer electrolyte fuel cell (all claimed).    ADVANTAGE - The membrane has improved water uptake and methanol penetration characteristic and better hydrogen ion conductivity, and can provide the alcohol monomer of unit polymer. The membrane improves performance and efficiency of the MEA.    DETAILED DESCRIPTION - A polymer electrolyte membrane comprises hydrogen ion conductivity copolymer of formula (I).    A1, B1= -S-, -C(=O)-, (dimethyl-phosphinoyl)-benzene or -S(=O)-;    C1=-S-,-SO2-, -C(CH3) 2 -,-C(CF3)2-, -P(O) (C6H5) - or -C=O-, C2=-S-,-SO2-,-C(CH3)2-, -C(CF3)2-, -P(O)(C6H5)- or -C=O-;and    n/(n+m)=0.3-0.5.    INDEPENDENT CLAIMS are also included for the following:    (1) a method for improving physical property of a polymer electrolyte membrane, which involves preparing a hydrogen ion conductivity copolymer (I) by copolymerizing 0.1-99.9 weight percent of monomer containing A functional group-containing compound of formula (II), B functional group containing compound of formula (III), C1 functional group containing compound of formula (IV) and C2 functional group-containing compound of formula (V)    (2) a polymer electrolyte fuel cell comprising a membrane electrode assembly.    Z=halo, -NO, F, cl or br.
NOVELTY - More than 95% of carbon dioxide is collected and separated from exhaust gas of iron manufacturing process by chemical absorption or adsorption. Carbon dioxide having a purity of more than 99.5% is obtained by removing moisture, acid material, corrosive material, and salt-producing material from the collected carbon dioxide. The refined carbon dioxide is put into urea manufacturing process. Moisture is removed using ethylene glycol, and acid material, corrosive material, and salt-producing material are removed by adsorption.    USE - Manufacture of urea using iron-manufacture exhaust gas e.g. FINEX off gas, blast furnace gas, and FINEX tail gas (all claimed), for use in fertilizers.    ADVANTAGE - The method stabilizes urea cost and reduces emission of carbon dioxide to the atmosphere.    DETAILED DESCRIPTION - More than 95% of carbon dioxide is collected and separated from exhaust gas of iron manufacturing process by chemical absorption or adsorption. Carbon dioxide having a purity of more than 99.5% is obtained by removing moisture, acid material, corrosive material, and salt-producing material from the collected carbon dioxide. The refined carbon dioxide is put into urea manufacturing process. Pure carbon dioxide is obtained by removing moisture using ethylene glycol, and removing acid material, corrosive material, and salt-producing material by adsorption using activated alumina or activated carbon. Inactivated gas is removed due to high-pressure liquefaction of carbon dioxide.
NOVELTY - A benzazole ring compound (I) and amide compound (II) are activated with an oxidizer under acid condition to obtain 2-aminobenzazole (III).    USE - Manufacture of 2-aminobenzazole used for pharmaceuticals.    ADVANTAGE - The method enables manufacture of 2-aminobenzazole with high yield, without harmful byproducts.    DETAILED DESCRIPTION - A benzazole ring compound of formula (I) and amide compound of formula: R5-C(=O)-N(-R7)-R6 (II) are activated with an oxidizer under acid condition to obtain 2-aminobenzazole of formula (III).    X=nitrogen, oxygen or sulfur;    R1-R4=H, 1-10C alkyl, cycloalkyl, 1-10C alkenyl, 3-7C cycloalkenyl having one or more double bond, 1-10C alkynyl, phenyl, naphthyl, silyl, nitro, halo, amine, amide, alcohol, alkoxy, thiol or heteroaryl containing nitrogen, oxygen and/or sulfur;    R5=H or methyl;and    R6,R7=H or heteroaryl substituted by 1-10C alkyl, cycloalkyl, 1-10C alkenyl, 3-7C cycloalkenyl having one or more double bond, 1-10C alkynyl, phenyl, naphthyl, silyl, nitrogen, oxygen or sulfur, and includes amino acid or its derivative having chiral carbon.    The main chain or main ring of benzazole ring compound (I) is substituted by functional group chosen from acetyl, ester and fluoroalkyl.
NOVELTY - A chlorine-containing plastic waste utilizing method involves obtaining chlorine-containing plastic waste fuel. Hydrochloric acid with high added value is prepared. Thermal cracking of chlorine containing plastic waste is performed in a cracking fluidized bed. The hydrochloric acid is catalytically converted to chlorine by utilizing a fixed bed catalyst. Thermal cracking oil is catalyzed and modified by a catalyzing tower to obtain fuel oil containing chlorine.    USE - Method for utilizing chlorine-containing plastic waste.    ADVANTAGE - The method enables eliminating the need for a high quality fuel, and realizing high efficient multi-component resource utilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for utilization of chlorine-containing plastic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for utilization of chlorine-containing plastic waste.'(Drawing includes non-English language text)'
NOVELTY - A biological diesel oil preparing method involves utilizing primary settling sludge generated by a sewage treatment plant or excess sludge as a raw material. Pure yeast is added in the raw material, and hydrolysis is performed. Hydrolyzed biological sludge mixed solution is taken, and methanol is added in the mixed solution. The methanol added solution is dripped in concentrated sludge. Concentrated sulfuric acid solution is stirred and reacted. The mixed liquid is naturally cooled to the room temperature by adding and mixing normal hexane to obtain biological diesel oil.    USE - Method for preparing biological diesel oil by utilizing mud from an urban sewage plant.    ADVANTAGE - The method enables improving conversion rate of biological diesel oil and reducing cost for manufacturing biological diesel oil from sludge by storing the enough residual sludge in esterification of macromolecular organic acid.    DETAILED DESCRIPTION - A biological diesel oil preparing method involves utilizing primary settling sludge generated by a sewage treatment plant or excess sludge as a raw material. 20-40 ml of pure yeast is added in the raw material, and hydrolysis is performed at 35 degrees C for 2-4 days. Hydrolyzed biological sludge mixed solution is taken, and 1-1.2 liter methanol is added in the mixed solution. 0.07-0.1 liter of the methanol added solution is dripped in every liter of concentrated sludge. Concentrated sulfuric acid solution with concentration of 98 percent is stirred and reacted at temperature of 70-80 degrees C. The mixed liquid is naturally cooled to the room temperature by adding and mixing normal hexane for 3-5 minutes at rotating speed of 3000-3500 revolutions per minute to obtain biological diesel oil.
NOVELTY - Invention relates to chemistry and may be used in production of hydrogen. Aluminium electrodes are fed into reactor to feed water with alkaline metal hydroxides traces into electrode zone. Contact current of 30-110 V, 5-10 A, is fed to electrodes to initiate voltaic arc between electrodes to disperse aluminium electrodes in voltaic arc so that aluminium nanopowder is produced to interact with water and, finally, to produce aluminium oxides and hydrogen gas. With voltaic arc extinguishing, aluminium electrodes are shifted unless arc is initiated while water with alkaline metal hydroxides traces is added with depletion.    USE - Chemistry.    ADVANTAGE - Higher efficiency and hydrogen purity at lower costs. 1 dwg
NOVELTY - Invention refers to fire-fighting chemical agents, particularly to gas compositions of chemically active substances for prevention of methane-air mixture ignition and explosion in industrial, transport and welfare facilities. As an inhibitor, the composition contains trifluoromethane of chemical formula CHF3 in the ratio to carbon dioxide as 1:3, provided introduction of the inhibitor in the protected volume in an amount not less than 5.5 vol. %.    USE - Fire-fighting means.    ADVANTAGE - Gas composition provides assured prevention of methane-air mixture ignition and explosion in the closed spaces, rooms in all the concentration of methane and from any means of initiation.
NOVELTY - Fuel contains lower aliphatic alcohol, alkyl acetate, where alkyl is lower alkyl, and water at following ratio of components, wt %: lower aliphatic alcohol - 66-70; said alkyl acetate - 15-22; water - rest.    USE - Oil and gas production.    ADVANTAGE - Production of dry combustion fuel without smoke and exhaust of toxic substances at ignition. 3 cl, 3 ex, 3 tbl
NOVELTY - Invention relates to chemistry. Aluminium wire is periodically fed into a reactor between electrodes in a medium of superheated saturated steam, or water is fed into the bottom part of the reactor and the aluminium wire reacts with water in the bottom part of the reactor and with saturated steam in the top part. An electrical pulse is periodically transmitted to the electrodes with energy density in the wire equal to 10-20 kJ/g and the aluminium wire is periodically exploded into liquid aluminium nanoparticles which react with saturated steam or water in the bottom part of the reactor and with saturated steam in the top part to form aluminium oxides and hydrogen gas. The aluminium wire is heated to melting point before explosion.    USE - Chemistry.    ADVANTAGE - Invention is intended to increase efficiency, reduce power consumption and increase purity of hydrogen. 1 dwg, 1 tbl, 1 ex
NOVELTY - Invention relates to chemistry. hydrogen is obtained by periodically feeding water and aluminium powder into a reactor between iron electrodes. The obtained aluminium-water suspension get into contact with the electrodes to which an electrical pulse is periodically transmitted with energy density in the said suspension equal to 5-15 kJ/g. The powder is dispersed to form liquid aluminium nanoparticles which react with water to form aluminium oxides and hydrogen gas.    USE - Chemistry.    ADVANTAGE - Invention increases efficiency and reduces power consumption of the process. 1 dwg, 1 tbl, 1 ex
NOVELTY - Harmful gas in carbon dioxide gas discharged during production of synthesized ammonia tail gas and synthesized ammonia, is removed. The synthesized ammonia tail gas and/or carbon dioxide gas is supplied in two paths under pressure, and mixed. The mixed gas is reacted in a methanation reaction furnace, and carbon dioxide is reacted with hydrogen to generate methane and water. The reacted gas is transferred into a gas purifier to remove water and carbon dioxide. The purified gas is transferred into a methane liquefier, cooled and rectified. The liquefied methane is separated and stored.    USE - Manufacture of liquefied methane.    ADVANTAGE - The liquefied methane is manufactured without discharging greenhouse gas, and energy in tail gas is recycled.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for preparing liquefied methane, which comprises a methanation reaction furnace for performing methanation reaction on harmful-gas-removed and boosted synthesized ammonia tail gas and carbon dioxide discharged during production of synthesized ammonia, gas purifier, and methane liquefier.
NOVELTY - Invention relates to chemistry and can be used in producing hydrogen. Iron wire is periodically fed into a reactor between electrodes in a medium of superheated saturated steam. An electrical discharge periodically occurs on the electrodes with voltage of 45 kV and the wire is periodically blown to small liquid metal particles which react with water vapour to form iron oxides and gaseous hydrogen.    USE - Chemistry.    ADVANTAGE - High efficiency of the process. 1 dwg, 1 ex
NOVELTY - A method for synthesizing anti-viral cidofovir drug comprising substituted oxirane compound (I) involves reacting chiral hydroxymethyl epoxypropane with halohydrocarbon under presence of organic PEG amine, a catalyst and solvent at ambient temperature for 0-50 degrees C to get substituted oxirane compound (I).    USE - Method for synthesizing anti-viral cidofovir drug.    ADVANTAGE - The method enables preparing anti-viral cidofovir drug with high yield of the cidofovir and high purity in a simple, inexpensive and environment-friendly manner.    DETAILED DESCRIPTION - A method for synthesizing anti-viral cidofovir drug comprising substituted oxirane compound of formula(I) involves reacting chiral hydroxymethyl epoxypropane with halohydrocarbon under presence of organic PEG amine, a catalyst and solvent at ambient temperature for 0-50 degrees C to get substituted oxirane compound (I).    R=benzyl, 1-4C alkyl, triphenyl methyl and derivative, toluenesulfonyl;and    X=Cl, Br or I.
NOVELTY - An anchor flower saponin preparing method involves taking elliptic anchor flower whole grass, crushing, and putting in a microwave extracting device for microwave extraction. Extracting liquid is filtered and decompressed, and ethanol is recycled and concentrated. The concentrated ethanol is added on a macroporous absorption resin column, and eluent is collected and added to a polyamide chromatographic column. Methylene dichloride-methanol mixed solvent is obtained, and a polyamide film is added with the solvent. Ethanol crystal is added, washed and dried.    USE - Method for preparing anchor flower saponin.    ADVANTAGE - The method enables simplifying the preparing process, reducing pollution and energy consumption, increasing the product purity and easily realizing industrial amplification.    DETAILED DESCRIPTION - An anchor flower saponin preparing method involves taking elliptic anchor flower whole grass, crushing, and putting in a microwave extracting device for microwave extraction, where mass concentration of the flower is 10-15 times to volume of 70-80% of ethanol, extracting power is 300-600 Watts and extraction is done for 1-3 times. Extracting liquid is filtered and decompressed, and the ethanol is recycled and concentrated. The concentrated ethanol is added on a macroporous absorption resin column, and eluent is collected and added to a polyamide chromatographic column. Methylene dichloride-methanol mixed solvent is obtained, and a polyamide film is added with the solvent. Ethanol crystal is added, washed and dried.
NOVELTY - A bio-diesel producing method involves adding palm fatty acid to a mixed esterifying agent, and supplying acid to four group series of continuous oscillation fluid esterifying towers for 2 hours of liquid hourly space velocity. Rough methyl alcohol containing acid is recycled by a methyl alcohol separation tower to obtain more than 97% of fatty acid methyl ester. Sulfuric acid is removed by two groups of series methyl alcohol washing and separating towers, where the acid value is below 0.5 mg of potassium hydroxide per gram. The methyl alcohol is distilled to obtain a product.    USE - Method for producing bio-diesel.    ADVANTAGE - The method enables increasing reliable and quick esterifying speed and yield, simplifying process, reducing cost, waste energy and environment pollution and reaching national BD100 standard.
NOVELTY - A bio-ethanol preparing method involves performing organic solvent preprocessing operation, and dipping softwood originated raw material in an organic solvent with a neutral catalyst at predetermined time and temperature.    USE - Method for preparing bio-ethanol.    ADVANTAGE - The method enables preparing bio-ethanol with reduced harmfulness, corrosive and toxic substances in a simple manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a catalyst preprocessing yield.'(Drawing includes non-English language text)'
NOVELTY - Method for preparing liquid fertilizer by aerobic fermentation, involves collecting sample from excrements stored in fermentation tank, performing trial fermentation by inoculating different amount of aerobic microorganism in the obtained sample for testing the amount of inoculation of the aerobic microorganism with respect to constellation of the excrements, inoculating aerobic microorganism in the fermentation tank, and performing fermentation by agitating the excrements stored in the fermentation tank with aeration.    USE - The method is useful for preparing liquid fertilizer for promoting growth of crops (claimed).    ADVANTAGE - The method is cost-effective.    DETAILED DESCRIPTION - Method for preparing liquid fertilizer by aerobic fermentation, involves (a) collecting sample from excrements stored in fermentation tank, (b) performing trial fermentation by inoculating different amount of aerobic microorganism in the obtained sample for testing the amount of inoculation of the aerobic microorganism with respect to constellation of the excrements, (c) inoculating aerobic microorganism in the fermentation tank, where the amount of inoculation of aerobic microorganism is the fermentation result of the trial fermentation, and (d) performing fermentation by agitating the excrements stored in the fermentation tank with aeration.
NOVELTY - An isoamyl salicylate preparing method involves orderly adding orthohydroxybenzoic acid and isoamylol to a reaction bottle, and adding concentrated sulfuric acid as catalyst during mixing. The obtained mixture is heated at 90-110 degrees C. The heated mixture is reacted for 5-6 hours. The reacted mixture is neutralized and washed. Obtained reaction liquid is poured to a liquid-division hopper after cooling the reaction liquid. The poured reaction liquid is maintained in vacuum at 15-18 mmHg. The reaction liquid is evaporated at 151-155 degrees C to obtain isoamyl salicylate.    USE - Method for preparing isoamyl salicylate that is utilized in fields of daily necessities, medicines and foods.    ADVANTAGE - The method enables preparing the isoamyl salicylate in a simple and inexpensive manner, increasing application range of the isoamyl salicylate, and avoiding generation of pollution.    DETAILED DESCRIPTION - An isoamyl salicylate preparing method involves orderly adding orthohydroxybenzoic acid and isoamylol to a reaction bottle equipped with a backflow condensation device and a temperature meter, and adding concentrated sulfuric acid as catalyst during the mixing. The obtained mixture is heated at 90-110 degrees C. The heated mixture is reacted for 5-6 hours. The reacted mixture is neutralized and washed. Obtained reaction liquid is poured to a liquid-division hopper after cooling the reaction liquid. An organic layer is cleaned by using sodium carbonate solution for three times till pH is 8-9. An oil layer is removed from a distillation kettle. The poured reaction liquid is maintained in vacuum at 15-18 mmHg. The reaction liquid is evaporated at 151-155 degrees C to obtain isoamyl salicylate.
NOVELTY - A 4,5-tryptophan-diketone production controlling method involves filling nitrogen in 5-hydroxytryptophan mother liquor in a concentration tank, opening vacuum to decompress, controlling the temperature, and concentrating the solution. The concentrated liquor is crystallized and infused, and nitrogen is filled in tank, cooled and filtered to obtain the crystal. The crystal obtained is transferred to saturated solution of water, infused into the metallic flat disk and frozen dried followed by sampling and detecting to be qualified.    USE - Method for controlling production of 4,5-tryptophan-diketone in tryptophan.    ADVANTAGE - The method enables controlling production of 4,5-tryptophan-diketon in tryptophan in an environment-friendly manner.    DETAILED DESCRIPTION - A 4,5-tryptophan-diketone production controlling method involves filling nitrogen into extracted and separated 5-hydroxytryptophan mother liquor in a concentration tank, opening vacuum to decompress to 0.5-0.9 MPa, controlling temperature at 45-70 degrees C, and concentrating the solution until specific weight is 1.0-1.2 baume degrees. The concentrated liquor is infused into the crystallizing tank for crystallization, and nitrogen is filled in tank, cooled to 4-20 degrees C for 3-5 hours and filtered to obtain the crystal. The crystal content is detected. The obtained crystal is transferred to saturated solution of water, infused into the metallic flat disk and frozen dried for 12-48 hours at -4 to -20 degrees C followed by sampling and detecting to be qualified.
NOVELTY - Preparation of 7-bromo-thieno(3,2-d)pyrimidin-4-ylamine involves reacting 7-bromo-4-chloro-thieno(3,2-d)pyrimidine with ammonia water as a reaction solvent to form 7-bromine-4-amino thienopyrimidine.    USE - Method for preparing 7-bromo-thieno(3,2-d)pyrimidin-4-ylamine that is used for preparing anti-tumor medicine.    ADVANTAGE - The method enables preparing 7-bromo-thieno(3,2-d)pyrimidin-4-ylamine with improved energy saving effect and better market need.
NOVELTY - A leonurine preparation method involves reacting guanidine-butyl ester compound (I) to obtain hydroxy amino butyl ester compound (II) that is reacted to obtain benzoic acid amino butyl ester compound (III). Benzoic acid amino butyl ester compound (III) is reacted to obtain phenolic hydroxyl syringate and amino butanol compound (IV) that is reacted to obtain amino butyric acid.    USE - Method for preparing leonurine.    ADVANTAGE - The method enables preparing leonurine with high purity in a simple and environment friendly manner, avoiding motherwort amine preparation through Gabriel amine forming method and reducing reagent usage.    DETAILED DESCRIPTION - A leonurine preparation method involves reacting guanidine-butyl ester compound of formula (I) to obtain hydroxy amino butyl ester compound of formula (II) that is reacted to obtain benzoic acid amino butyl ester compound of formula (III). Benzoic acid amino butyl ester compound of formula (III) is reacted to obtain phenolic hydroxyl syringate and amino butanol compound of formula (IV) that is reacted to obtain amino butyric acid..
NOVELTY - A phenyl sulfone compound (I) synthesizing method involves performing substitution reaction by aryl boric acid compound (II) and sulfinate compound (III) under existence of cuprous catalyst and ammonia water to obtain a phenyl sulfone compound (I).    USE - Method for synthesizing phenyl sulfone compound that is utilized for preparing medicine, polymer and natural product.    ADVANTAGE - The method enables preparing phenyl sulfone compound with high yield and tolerance in an ecofriendly manner.    DETAILED DESCRIPTION - A phenyl sulfone compound of formula (I) synthesizing method involves performing substitution reaction by aryl boric acid compound (II) and sulfinate compound of formula (R'-SO2M) under existence of cuprous catalyst and ammonia water to obtain a phenyl sulfone compound (I).    R=1-5 substituent groups connected on the benzene ring;    substituent groups=H, F, Cl, Br, I, 1-20C alkyl, 2-20C alkenyl, 6-20C aryl, halogen atom, OH, -NO2, -NH2, -NHR'', -COOR'', NHCOR'', -OR'' or -COR'';    R'=1-20C alkyl, 2-20C alkenyl, 6-20C aryl, halogen atom, OH, -NO2, -NH2, -NHR'', -COOR'', NHCOR'', -OR'' or -COR'';    R''=H, 1-6C alkyl, 2-6C alkenyl, 2-6C alkynyl, phenyl or benzyl;and    M=Li, Na, K, Rb or Cs    .
NOVELTY - A biomass environment-friendly carbon manufacturing method involves mixing (in volume weight ratio) sawdust (35-38), coal powder (40), straw powder (2), clay powder (8), lime (8), cement or starch (2-5) and sodium carbonate or other smoke removing agent (2), and crushing raw materials. Water is uniformly added by micro carbon-making machine or mechanical charcoal machine, cold pressing or heat pressing, where cooling intensity is 90KG/root, heat intensity is 75FG/root, and thermal stability is 98 percent.    USE - Method for manufacturing biomass environment-friendly carbon.    ADVANTAGE - The method enables manufacturing carbon having long burning time, complete combustion, non-residue and non-corrosion to boiler and cooker, providing excellent phosphorus potassium compound fertilizer after burning, easily obtaining raw material, simplifying manufacturing process, reducing cost and time, saving energy, and recycling the crops straw, sawdust and waste.
NOVELTY - A synchronous fruit slag oil and polyphenol extracting method involves taking olive processing waste residue, and crushing waste slag soaked in non-polar organic solvent and polar mixed solvent of water and organic solvent to obtain mixing material liquid. Brown pigment is extracted from material liquid by microwave process, and the water is added to the non-polar organic solvent. The obtained product is decompressed, concentrated and dried in vacuum to obtain crude fruit polyphenol solid powder by vacuum by vacuum.    USE - Method for synchronously extracting fruit slag oil and polyphenol from olive processing waste residue.    ADVANTAGE - The method enables extracting the fruit slag oil and polyphenol from olive processing waste residue in short time and with low energy consumption and high extraction efficiency.    DETAILED DESCRIPTION - A synchronous fruit slag oil and polyphenol extracting method involves taking olive processing waste residue, and crushing waste slag soaked in non-polar organic solvent and polar mixed solvent of water and organic solvent to obtain mixing material liquid. Brown pigment is extracted from material liquid by microwave process, and the water is added to the non-polar organic solvent. An auxiliary extract is ultrasonic extracted by utilizing a condensation device, and the obtained material liquid is filtered or centrifuged. Dregs and a liquid layer in the obtained material liquid are removed to obtain crude fruit slag oil and polyphenol solution. The obtained product is decompressed, concentrated and dried in vacuum to obtain crude fruit polyphenol solid powder by vacuum by vacuum.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a synchronous fruit slag oil and polyphenol extracting method.'(Drawing includes non-English language text)'
NOVELTY - The device has hydrogen generator (15), water tank (14), mixing inlet (17), and radiating pipe (16). The hydrogen generator of two electrode plates is provided with a neutral plate, and fixing plates are provided with two electrode plates, neutral plate and sealing rubber ring. A nut is provided for pressing fixing plates. The electrode plate and neutral plate provided with small holes are formed corresponding to each other. Two fixing plates are respectively provided with small circular hole, and power supply and nut are fixed on the electrode plate through bolt.    USE - Vehicle combustion supporting device for generating hydrogen.    ADVANTAGE - The photovoltaic power system combustion supporting device can be ensured for generating instant current for proper hydrogen, so that effective utilization of the hydrogen in the vehicle can be enabled for generating the current. The electrolytic hydrogen can be enabled to effectively improve the combustion efficiency. The oil saving and energy saving can be achieved. The carbon emission can be reduced for environment protection.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the vehicle combustion supporting device.    Water tank (14)    Hydrogen generator (15)    Radiating pipe (16)    Mixing inlet (17)    Water outlet (18)
NOVELTY - Method for producing granular organic fertilizer, involves weighing feces of human and animal, bran and microbial strain, stirring and stacking the mixture, fermenting the mixture, dispersing the mixture, stacking the fermented mixture, fermenting the mixture for second time, obtaining fermented product, stacking the product and fermenting mixture for third time, detecting temperature of the mixture, transferring the mixture and continuously fermenting to obtain crude organic fertilizer, sieving crude organic fertilizer to remove impurities and obtaining product.    USE - The method is useful for producing granular organic fertilizer.    ADVANTAGE - The granular organic fertilizer can be produced with no odor in soil. The method improves radiating efficiency of organic fertilizer particle hardness as stacking fermentation is carried out.    DETAILED DESCRIPTION - Method for producing granular organic fertilizer, involves (a) weighing (in parts weight) feces of human and animal (60-80), bran (20-40) and microbial strain (3-5), stirring the mixture until the water content is 40-60%, stacking the mixture such that the width is 2 m and height is 1.2-1.5 m and fermenting the mixture for first time at 90 degrees C, (b) dispersing the mixture evenly until the water content is 30-35%, further stacking the mixture such that in 2 m wide and 1.2-1.5 m high pile and fermenting the mixture for second time at 90 degrees C, (c) dispersing the mixture evenly until the water content is 20-25%, further stacking the mixture such that in 2 m wide and 1.2-1.5 m high pile and fermenting the mixture for third time at 60-80 degrees C, (d) detecting the temperature of the mixture, where the temperature is 60-80 degrees C, transferring the mixture and continuously fermenting for 2-3 days to obtain crude organic fertilizer, (e) sieving crude organic fertilizer to remove impurities in pellet form, and (f) drying granular organic fertilizer and packaging the organic fertilizer.
NOVELTY - An L-carnosine discoloring method involves removing protective group of L-carnosine to obtain L-carnosine coarse product water solution, and utilizing a pH value adjusting agent for adjusting pH value of the solution to alkalinity state to obtain discoloring liquid. Anion exchange resin is utilized for absorbing the discoloring liquid. Washing solvent is utilized for cleaning the absorbed discoloring liquid. The washing solvent is added to the L-carnosine coarse product water solution for performing a discoloring process.    USE - Method for discoloring L-carnosine.    ADVANTAGE - The method enables changing active carbon discoloring technology into anion exchange resin discoloring technology, so that discoloring effect can be improved in an environment friendly manner. The method enables reducing material loss due to absorbing the L-carnosine by utilizing the washing solvent circularly so as to guarantee yield and quality of the L-carnosine.
NOVELTY - The apparatus has a hydrolysis tub provided at a lower side of a livestock shed. The livestock shed is connected to an inlet port. An organic compound fermentor is connected to the hydrolysis tub. A connection pipe is connected with a liquefied fertilizer reservoir. An aerobic microorganism filter is arranged in the liquefied fertilizer. A liquefied fertilizer stabilization bath filters processing water of an aerobic reactor through the connection pipe. An oxygen supply pipe is installed inside the aerobic reactor. A separation film is installed in the aerobic reactor.    USE - Cattle shed excretion circulation type treatment apparatus for fermenting organic compounds.    ADVANTAGE - The apparatus improves oxygen supply to the organic wastewater unit. The apparatus has better profitability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cattle shed excretion circulation type treatment apparatus.'(Drawing includes non-English language text)'
NOVELTY - Automatic composter comprises a curing tray (70), a material feed hopper (20), a tub (10), a revolving transport unit (30) and a ventilation device (40), where the material feed hopper is provided above inlet end of a structure. A heating device is provided for forced oxygenation of material. The structure, a shaft, the revolving transport unit and the ventilation devices are constructively and functionally arranged to each others. The material is processed at 45 degrees C for 4-6 hours to activate thermophilic bacteria and mesophilic bacteria.    USE - Automatic composter for composting process.    ADVANTAGE - The automatic composter is worked efficiently in short duration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for composting, which involves:    (A) preparing organic waste and crushing it in order to optimize oxygen permeability of particles;    (B) pressing crushed material to remove liquid and humidity;    (C) adding organic reaction accelerator, where moisture is regulated by a spray solution of enzymes with generating rich amount of reaction accelerator and organic waste;    (D) performing accelerated aerobic composting in the composter, which comprises food-organic material in the tub (10);    (E) transporting material throughout the period of processing inside the structure for 7-10 days;    (F) processing material in oxygen-rich atmosphere at 45 degrees C;    (G) controlling pathogenic bacteria;    (H) keeping the mixture for 5-8 days in the structure;    (I) Rotating and reacting the materials in the structure; and    (J) processing the mixture with bacterial and solutions to obtain finished product.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the automatic composter.    Tub (10)    Material feed hopper (20)    Revolving transport unit (30)    Ventilation device (40)    Curing tray (70)
NOVELTY - Biodiesel is produced from waste grease by performing esterification ester exchange reaction on acid-containing waste grease and alcohol to obtain biodiesel and crude glycerol mixture, performing phase separation to obtain mixed glycerol layer; acidizing the mixed glycerol layer; evaporating and recycling the separated methanol; separating the salt, fatty acid and methyl ester from the crude glycerol; reacting the crude glycerol with aldehyde, ketone and/or acid; centrifugally separating the reaction product; and refining to separate glycerol ketal or acetal and glycerol aliphatic ester.    USE - Method for producing biodiesel from waste grease (claimed).    ADVANTAGE - The method has reduced production cost and enables efficient conversion of waste grease into valuable products while protecting the environment. The obtained crude glycerol can be utilized to provide pour point depressant in biodiesel, thus the pollution associated with crude glycerol can be eliminated.    DETAILED DESCRIPTION - Biodiesel is produced from waste grease by (A) performing esterification ester exchange reaction on acid-containing waste grease raw material and alcohol to obtain biodiesel and crude glycerol mixture, performing phase separation to obtain mixed glycerol layer; (B) acidizing the mixed glycerol layer; evaporating and recycling the separated methanol; separating the salt, fatty acid and methyl ester from the crude glycerol; (C) adding aldehyde, ketone and/or acid into the separated crude glycerol to react; centrifugally separating the reaction product to obtain salt and mixed product consisting of glycerol ketal or acetal and glycerol aliphatic ester; and (D) refining the mixed product to separate the glycerol ketal or acetal and glycerol aliphatic ester.
NOVELTY - A waste paint sludge bio-drying method involves injecting a thermophilic microorganism (30) into an organic waste (10) for fermenting the organic waste. A waste paint sludge and organic waste mixture is prepared. A waste paint sludge (20) is injected into the fermented organic waste. An end product (50) of the waste paint sludge and organic waste mixture is aged.    USE - Method for bio-drying waste paint sludge to manufacture a high energy end product that is utilized as an energy source including compost and is utilized as a material resource including a paving material in a road.    ADVANTAGE - The method enables improving effectiveness of fermentation process of the waste paint sludge by utilizing the thermophilic microorganism.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a waste paint sludge bio-drying system.'(Drawing includes non-English language text)'    Organic waste (10)    Waste paint sludge (20)    Thermophilic microorganism (30)    End product of waste paint sludge and organic waste mixture (50)
NOVELTY - A microbial fertilizer producing method involves crushing and burning straw, animal excrement, urea, domestic production garbage and fermenting agent. The water is added the burned product, mixed and stirred uniformly. The pH value is adjusted to 7-8 through quicklime. The obtained product is stacked to ferment at leeward sunny position. Air permeable covering objects such as grass curtain are adopted to cover so as to ferment. The organic fertilizer is obtained when the fermenting stack emits ammonia smell and aromatic smell and a large number of white hypha is arranged in the stack.    USE - Method for producing microbial fertilizer.    ADVANTAGE - The method enables producing the microbial fertilizer in a simple manner and with low production cost and short production period. The microbial fertilizer can be suitably popularized and applied in large range.    DETAILED DESCRIPTION - A microbial fertilizer producing method involves crushing and burning (in wt.%) straw (25-35), animal excrement (30-35), urea (2-5), domestic production rubbish (20-30) and fermenting agent (2-3). Water is added to the burned product, mixed and stirred uniformly. The pH value is adjusted to 7-8 through quicklime when water content is 55-65 wt. %. The obtained product is stacked to ferment at leeward sunny position. Air permeable covering objects such as grass curtain, are adopted to cover so as to ferment. The fermenting temperature is maintained between 55-65 degrees C and overturned when the temperature of the fermenting stack exceeds 65 degrees C. The organic fertilizer is obtained when the fermenting stack emits ammonia smell and aromatic smell, and a large number of white hypha is arranged in the stack.
NOVELTY - A soil improvement agent preparation method involves adding water in excrement of cattle and sheep, and stirring until solid content is 5-15%. Spartina alterniflora is crushed and uniformly mixed with the excrement of cattle and sheep in a weight ratio of 1:1-3:1 in a drum, to obtain a mixture. The obtained mixture is subjected to aerobic oxidation using microbial inoculum. Air is passed in the drum in a ratio of 2-6 m3 of air/m3 of mixture/d. The mixture is stirred and the flowing of air is controlled to 2-3 m3 of air/m3 of mixture/d, to obtain finished product.    USE - Method for preparing soil improvement agent.    ADVANTAGE - The method enables preparing soil improvement agent in a simple manner. The soil improvement agent has high physicochemical property and better crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a reaction device for preparing oil improvement agent.
NOVELTY - An organic compound fertilizer is obtained by mixing human and animal excrement with bean cake or peanut cake or sesame cake according to a certain proportion for processing, insolating, smashing, completely burning with crop straw for generating plant ash to mix according to a certain proportion, crushing, and passing through 3-5 mm mesh sieve.    USE - Organic compound fertilizer (claimed) for green vegetables, and used as additional fertilizer and base fertilizer for seeding or planting.    ADVANTAGE - The organic compound fertilizer is manufactured by simple, easy and economical method by using inexpensive raw materials. The fertilizer has favorable fertilization property and is used as additional fertilizer at any time by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing the organic compound fertilizer.
NOVELTY - A humic acid organic fertilizer producing method involves mixing crushed tobacco waste with alcohol waste according to proportion of 40-80:20-60. 0.6 percent of bio-bactericide is added with the obtained product. Three materials are uniformly stirred and mixed, and solid state natural fermentation is performed for 10-25 days at room temperature. Water content is cured and controlled to below 15 percent to obtain a humic acid organic fertilizer.    USE - Method for producing humic acid organic fertilizer.    ADVANTAGE - The method enables producing the humic acid organic fertilizer with wide raw material source, simple process, excellent performance and environment-friendly effect.
NOVELTY - A biological organic fertilizer comprises (in weight parts) bone powder (1-3), farm fertilizer (10-25), biological bacteria (0.5-1), active calcium (18-27), trace element compound (1-5), humic acid (20-30), nitrogen fertilizer (10-20), phosphate fertilizer (5-14) and potash fertilizer (3-8) and water content rate of the farm fertilizer is 10-18%, where the active calcium comprising calcium oxide (12500), saccharified enzyme, lipase and/or protease (250). The microelement compound comprising ammonium molybdate, borax, ferrous sulfate and zinc sulfate.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer containing bone powder is rich in organic calcium and microelement, decomposes soil acid pest, improves soil ecological environment, increases soil pH and solves the soil hardening problem.    DETAILED DESCRIPTION - A biological organic fertilizer comprises (in weight parts) bone powder (1-3), farm fertilizer (10-25), biological bacteria (0.5-1), active calcium (18-27), trace element compound (1-5), humic acid (20-30), nitrogen fertilizer (10-20), phosphate fertilizer (5-14) and potash fertilizer (3-8) and water content rate of the farm fertilizer is 10-18%, where the active calcium comprising calcium oxide (12500), saccharified enzyme, lipase and/or protease (250). The microelement compound comprises ammonium molybdate (5-10), borax (20-30), ferrous sulfate (20-30) and zinc sulfate (8-15). The humic acid is black humic acid, fulvic acid and brown humic acid. An INDEPENDENT CLAIM is also included for a method for preparing a biological organic fertilizer.
NOVELTY - A vegetable oil is prepared by shattering a plant chosen from glycine max,Brassica campestris, corn, artichoke containing starch,Ipomoea batatas, or potatoes into small pieces. The shattered pieces are added with a solid catalyzer that is chosen from sodium hydroxide, potassium hydroxide, sodium carbonate, ammonia alkali, or ion-exchange resin, or an acid to obtain fatty acid. Glycerol ester of the fatty acid is converted into methanol and ethanol ester using distillation process.    USE - Vegetable oil for producing biodiesel fuel.    ADVANTAGE - The oil that is used for producing biodiesel fuel is prepared from plants such that the biodiesel fuel has better combustion effect and emits less amount of carbon dioxide. The biodiesel fuel can be maintained in a liquid state in winter as the oil is made as gel while facilitating flow of fuel by using minute fuel injection systems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing biodiesel fuel.
NOVELTY - An organic waste treatment apparatus has a methane fermentation part for fermenting organic waste with methane and producing biogas. A degassing part collects ammonia in waste water generated in the methane fermentation part. An oxidizer generates energy by burning the biogas generated in the methane fermentation part. A nitrogen oxide processing unit processes nitrogen oxide generated in the oxidizer during combustion by using ammonia collected in the degassing part.    USE - Organic waste treatment apparatus.    ADVANTAGE - The apparatus removes hydrogen sulfide within the gas and obtains energy through biogas combustion process. The apparatus improves profitability through methane fermentation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an organic waste treatment apparatus.'(Drawing includes non-English language text)'
NOVELTY - The device has a microorganism feeder (100) provided with a supply tube (160) to supply a food rubbish treating unit (10) through an on/off valve (150). A supply pump (130) is connected with the on/off valve. A latch unit (110) is combined in the food rubbish treating unit. An inlet tube (120) is provided with the microorganism feeder. A tuning knob (151) is connected with the on/off valve and the supply pump through a connection pipe (140). The microorganism feeder is rotatively moved in a lined paper projection (210) of a catching ring (200).    USE - Food waste disposer supplying device.    ADVANTAGE - The device implements mounting structure, thus ensuring convenient installation. The device controls position of the microorganism feeder, thus obtaining sink space efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a food waste disposer supplying device.    Food rubbish treating unit (10)    Microorganism feeder (100)    Latch unit (110)    Inlet tube (120)    Supply pump (130)    Connection pipe (140)    On/off valve (150)    Tuning knob (151)    Supply tube (160)    Catching ring (200)    Lined paper projection (210)
NOVELTY - Acrolein is obtained from waste glycerol and reactive niobium compounds.    USE - Acrolein used for producing biodiesel.    ADVANTAGE - The acrolein enables to large scale production of biodiesel.
NOVELTY - Device comprises a gear motor (9), stirring blades (21), rails (110) and a unit for storing waste, where composting involves using the device. A trough is disposed closely to a longitudinal external wall (11) of ridges (115,117) with a slurry delivery system. The slurry delivery system has a waste spraying pump, which is fixed to a basic device structure. Discharge tubes are mounted in parallel manner to the tubular frames at their outer ends. A hose sprinkler is connected to the pump with the discharge tubes. A car is mounted, where transverse displacement is performed by the gear motor.    USE - Device for composting purpose (claimed).    ADVANTAGE - The device has automatic function to position the stirring system at specific points of the ridges without manual intervention with improved efficiency of homogenization.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Gear motor (9)    Longitudinal external wall (11)    Stirring blades (21)    Rails (110)    Ridges (115,117)
NOVELTY - Equipment comprises a reactor associated with other elements such as fluid filter (6) to make easier electrolysis process. The reactor is coupled to a heat exchanger (2), which circulates liquid. A liquid supply pump (4) and decanter (3) are provided for interconnecting a circulation pump, which sends a liquid to the reactor before passing through a filter. A control panel (7) is interconnected electrically to the reactor and circulation pump for operation of the process.    USE - Equipment for production of hydrogen by electrolysis for industrial and other uses.    ADVANTAGE - The equipment has simple and compact structure and performs functional process at room temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing hydrogen by electrolysis, which involves supplying liquid into interior of decanters through pump.    DESCRIPTION OF DRAWING(S) - The drawing shows a Perspective view of the equipment.    Heat exchanger (2)    Decanter (3)    Liquid supply pump (4)    Fluid filter (6)    Control panel (7)
NOVELTY - Producing oxygen and hydrogen gases involves performing automatic water electrolysis, where bi-polar plate with circular edge is utilized to obtain oxygen and hydrogen gases. Internal pressure of the bi-polar plate promotes tight sealing of the assembly.    USE - Method for producing oxygen and hydrogen gases.    ADVANTAGE - The oxygen and hydrogen gases producing method is simple and improved.
NOVELTY - The apparatus has a mixing fermenter (10) discharging dried waste. A circulation pipe (50), a stirring axis (81), and a heat supply unit (90) are fixed in a floor of the mixing fermenter. An air feeding unit (100) is fixed in a lower part of a waste discharging unit (30). The circulation pipe is installed on a top part of a post (40) by the stirring axis and is built-in a center part of the mixing fermenter that is rotated with a rotating unit (60). A penetration hole is formed on a ceiling of the mixing fermenter. A blocking plate is set up in a communication path (71) of the ceiling.    USE - Stirring type dry-fermentation apparatus for organic waste.    ADVANTAGE - The apparatus can prevent leakage of bad smell to outside through a gap between the ceiling of the mixing fermenter and the communication path of a diaphragm seal, prevent fracturing of a waste lump generated during mixing and generation of a hollow, improve mixing and drying efficiency of the hollow and provide heating source supplied to the floor of the mixing fermenter, thus improving drying effect of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a stirring type dry-fermentation apparatus.    Mixing fermenter (10)    Waste discharging unit (30)    Post (40)    Circulation pipe (50)    Rotating unit (60)    Communication path (71)    Stirring axis (81)    Heat supply unit (90)    Air feeding unit (100)
NOVELTY - A microalgae culturing method involves inducing photosynthesis of light reaction in a domed lexan house by irradiating electric power from biogas power plant, carbon source and LED red light. Liquid fertilizer is provided into the culture medium. A culture environment of the microalgae is optimized by horizontal feed of nitrogen source and vertical feed of carbon in the culture medium by tightly shutting the lexan house.    USE - Method for culturing microalgae that is used as a raw material for biodiesel, in a domed lexan house.    ADVANTAGE - The method enables culturing microalgae with high lipid local content, so that the microalgae production with high concentration is achieved regardless of the mass production of the microalgae and climatic condition.
NOVELTY - An oil extraction method involves removing chlorophyll in contact with extracted oil to an absorber, where the extracted oil is converted to bio-diesel after removing the chlorophyll.    USE - Method for extracting oil from micro-algae to produce bio-diesel.    ADVANTAGE - The method enables producing bio-diesel in an economical manner with increased production and high-quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing bio-diesel. '(Drawing includes non-English language text)'
NOVELTY - A saccharide material producing method involves acidifying marine algae with an extraction solvent using an acid agent. The acidified marine algae and extraction solvent mixture is processed with a plasma.    USE - Method for preparing a saccharide material that is utilized for producing a biofuel e.g. alcohol such as methanol, ethanol, propanol, butanol and acetone (all claimed).    ADVANTAGE - The method enables preparing high yield of the saccharide material, thus producing high yield of biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing biofuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for preparing a saccharide material.'(Drawing includes non-English language text)'
NOVELTY - A saccharides material manufacturing method involves processing marine algae with plasma. The plasma processed with the marine algae is subjected to acid process with extraction solvent containing acid agent.    USE - Method for manufacturing saccharides material used in bio-fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing bio-fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing saccharides material. '(Drawing includes non-English language text)'
NOVELTY - Compost comprises cocopeat, peat, castor meal, rice bran, microorganism promoter, and palm kernel expeller.    USE - The compost is useful for improving productivity of crops.    ADVANTAGE - The compost modifies the structure and physical characteristics of soil, is environmentally-friendly and inexpensive and can be stored for a long period of time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing the compost, which involves mixing the above-cited components, fermenting the mixture and removing impurities from the fermented product.
NOVELTY - Method of processing food waste, involves mixing biotite with pottery stone in weight ratio of 8:2, pulverizing the mixture, adding sulfur powder (0.1-0.5) to pulverized mixture, culturing soil microorganisms separated from biotite of mixed mineral, mixing culture with food waste, fermenting and aging the mixture, and processing the aged product into a pellet shape.    USE - The method is useful for processing food waste for pottery stone fertilizer (claimed) for promoting disease resistance of plants.    ADVANTAGE - The method is cost-effective, and controls acidity of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pottery stone fertilizer prepared by performing the above-cited steps (a) and (b).
NOVELTY - An inflammable minerals and alkali aqueous solution are injected in a batch-type reactor in which rotary vane is installed, at 20-80 degrees C, pulverized, mixed at 70-100 degrees C for 1-10 minutes and speed of 2000-3500 rpm, centrifuged, and the solution of humic acid salts is separated. The weight ratio of inflammable minerals and alkali aqueous solution is 1:2-6.    USE - Method of extracting humic acid salts from inflammable minerals.    ADVANTAGE - The method efficiently extracts humic acid salts from inflammable minerals with high yield, by a simple process without polluting environment.
NOVELTY - The desalinization plant (1) has renewable-energy generation unit (10) for generating electricity using renewable energy. A hydrogen generating unit (20) is provided for generating hydrogen by electrolyzing sea water with the generated electricity. A supplying unit (30) is installed on regional system for charging the hydrogen in a fuel cell for supplying the electricity and produced fresh water to consumers.    USE - Distribution type desalinization plant.    ADVANTAGE - The dispersion type desalination plant is provided to electrolyze the sea water using renewable energy for preventing the environmental pollution and reducing the fuel cost. The profitability of consumer is improved. The economic efficiency of desalination plant is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the distribution type desalinization plant. (Drawing includes non-English language text)    Distribution type desalinization plant (1)    Renewable-energy generating unit (10)    Hydrogen generating unit (20)    Supplying unit (30)
NOVELTY - A meropenem preparation method involves adding and reacting (1R,5R,6S)-6-((1R)-1-hydroxy)-1-methyl-2-diphenylphosphoacyloxy-carbapenicill-2-ene-3-p-nitryl phenyl carboxylate, (2R,4S)-4-sulfydryl-2-dimethylaminoformoxyl-1-p-nitryl phenyl carbonyl pyrrolidine and alkaline quaternary ammonium salt into a reaction bottle. Palladium/carbon catalyst is added in the materials. The obtained product is extracted to separate out an organic layer. The obtained product is dried, concentrated and crystallized by utilizing isopropanol to obtain a solid product.    USE - Method for preparing meropenem.    ADVANTAGE - The method enables preparing the meropenem in a simple and environment-friendly manner.    DETAILED DESCRIPTION - A meropenem preparation method involves (1R,5R,6S)-6-((1R)-1-hydroxy)-1-methyl-2-diphenylphosphoacyloxy-carbapenicill-2-ene-3-p-nitryl phenyl carboxylate, (2R,4S)-4-sulfydryl-2-dimethylaminoformoxyl-1-p-nitryl phenyl carbonyl pyrrolidine and alkaline quaternary ammonium salt into a reaction bottle. The added materials are stirred, reacted and tracked by thin-layer chromatography (TLC). Palladium/carbon catalyst of 5 wt % is added in the materials after the reaction is finished. Reduction process is performed in the presence of hydrogen gas. The obtained product is tracked by the TLC and extracted by toluene after the reaction to separate out an organic layer. The obtained product is dried, concentrated and crystallized by utilizing isopropanol to obtain a solid product, where the involves (1R,5R,6S)-6-((1R)-1-hydroxy)-1-methyl-2-diphenylphosphoacyloxy-carbapenicill-2-ene-3-p-nitryl phenyl carboxylate and (2R,4S)-4-sulfydryl-2-dimethylaminoformoxyl-1-p-nitryl phenyl carbonyl pyrrolidine are added at a ratio of 1: 1-2, (1R,5R,6S)-6-((1R)-1-hydroxy)-1-methyl-2-diphenylphosphoacyloxy-carbapenicill-2-ene-3-p-nitryl phenyl carboxylate and alkali salt are added at a ratio of 1: 1-3 at a reaction temperature of 20 to 30 degrees C.
NOVELTY - A fish made biological organic fertilizer preparing method involves crushing freshwater fish leftover material into powder, putting the freshwater fish leftover material powder into a fermentation pool, adding edible phosphoric acid in the fermentation pool, adding water in the fermentation pool and adding biological fermenting agent in the fermentation pool, where fermentation temperature in the pool is controlled at 16-35 degrees C for 5 days. The fermentation liquid is finally filtered to obtain organic fertilizer.    USE - Method for preparing fish made biological organic fertilizer.    ADVANTAGE - The method enables improving nutrient activity of soil and fertility of the soil and improving quality of a product.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for preparing fish made biological organic fertilizer.'(Drawing includes non-English language text)'
NOVELTY - An organic ground surface cover preparing method involves cutting and crushing wood or herbaceous plant into particles with length not greater than 6 cm and thickness not greater than 3 cm. The crushed material is sterilized followed by continuously maintaining for 5-10 days at high temperature of 50-60 degrees C, and classifying organic matter using a grading sieve.    USE - Method for preparing an organic ground surface cover that is utilized to prevent a plant disease and pests.    ADVANTAGE - The method enables preparing the organic ground surface cover in an inexpensive and environment-friendly manner, and reducing wastage of branches generated by tree trimming and forest cultivating.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an organic ground surface cover preparing method.'(Drawing includes non-English language text)'
NOVELTY - Disclosed is a cost effective and eco-friendly continuous process for the preparation of escitalopram, (S enantiomer of citalopram) and its acid addition salts from racemic diol intermediate with high yield and purity. Also a process for recovering racemic diol intermediate from mother liquor containing salts of unwanted enantiomer, is disclosed. Image 0/0
NOVELTY - A waterproof film and drainage structure are formed on bottom surface of barren region, to form waterproof agent layer. A fresh water shrimp drainage module having garden structural layer is formed on the waterproof agent layer. A filtration module is provided on the fresh water shrimp drainage module. Sand is coated on the filter layer to form sand layer. A planting soil layer is formed on the sand layer. Plants are planted on the planting soil layer, to obtain artificial garden. The planting soil layer has a base layer and a surface layer formed on the base layer.    USE - Manufacture of artificial garden.    ADVANTAGE - The method enables manufacture of artificial garden, without environmental pollution.    DETAILED DESCRIPTION - A waterproof film and drainage structure are formed on bottom surface of barren region, to form waterproof agent layer. A fresh water shrimp drainage module having garden structural layer is formed on the waterproof agent layer. A filtration module is provided on the fresh water shrimp drainage module. Sand is coated on the filter layer to form sand layer. A planting soil layer is formed on the sand layer. Plants are planted on the planting soil layer, to obtain artificial garden. The planting soil layer has a base layer and a surface layer formed on the base layer. The base layer contains (in parts weight) clay aggregate (20-30), inorganic binder (20-30), ground granulated blast-furnace slag (1-5), waste concrete recycling aggregate (10-15), quartz (5-10) and admixture (1-2) with respect to crushed aggregate (100). The surface layer contains clay aggregate (10-20), inorganic binder (10-15), ground granulated blast-furnace slag (10-15), negative ion-containing material (5-10), quartz (5-10) and admixture (1-2) with respect to crushed aggregate (100).
NOVELTY - A composition comprises enzyme activity supplement (100 weight parts) mixed with effluent of organic waste (10-20 weight parts). The mixed product is fermented for 10-30 days by maintaining pH of 5.5-9 to prepare metabolic product. Solidity organic waste is mixed with microorganism inoculation powder (250-300 weight parts) and the metabolic product. The obtained product is mixed with water control agent (80-120 weight parts) to treat the organic waste.    USE - Composition for treating solid organic waste to manufacture compost (claimed).    ADVANTAGE - The composition avoids bad smell generation during treatment of the solid organic waste, thus avoiding environmental pollution. The composition can be used for manufacturing the compost with high-quality, and improves degraded nature of the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating solid organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for treating solid organic waste.'(Drawing includes non-English language text)'
NOVELTY - This invention is related to a novel photocatalytic electrode and its preparation method for use in a hydrogen-generating photoelectrochemical cell (PEC) via splitting of water. The photocatalytic electrode, consisting of a carbon material-based electrode base and a coated photocatalyst layer, uses powdered photocatalysts and can be employed as the photoanode of a PEC. The photocatalyst layer is made by mixing a suitable amount of powdered photocatalyst, ionomer binder and conductive carbon black powder, and then coated evenly onto an electrode base. Based on this invention, a variety of difficult-to-handle photocatalysts in powder forms can be readily prepared into useful photoanodes for applications in PECs. Simple in photocatalytic electrode preparation and easy in control of the photocatalyst layer composition with good electrode performance are the advantages.
NOVELTY - Invention relates to agriculture and can be used to produce fertiliser based on semi-liquid manure. The method involves mixing manure and water-absorbing material, adding mineral substances to a compost mixture, biothermal ageing of the compost mixture. Anhydrous calcium chloride, ammonia nitrogen and ammonium nitrate are added at the compost mixture in the ratio compost mixture: calcium chloride: nitrogen equal to 100:5.5"..."7.0:0.4"..."0.7 in weight parts. The compost mixture has biothemal ageing period of 5-6 days.    USE - Chemistry.    ADVANTAGE - Invention reduces duration biothermal ageing of compost mixtures based on semi-liquid manure to 5-6 days and simplifies that process by avoiding the need to stir the mixture during ageing. 1 tbl, 9 ex
NOVELTY - An iron-based composite oxygen carrier is formed by carrying ferric oxide as an active ingredient on a mesoporous silicon-based molecular sieve, where the mesoporous silicon-based molecular sieve is hexagonal mobil crystalline material (MCM)-41 or SBA-15, and mass percents of the mesoporous silicon-based molecular sieve and the ferric oxide are 50-95% and 5-50%, respectively.    USE - Oxygen carrier for use in chemical chain combustion process of gaseous and solid fuels e.g. hydrogen, carbon monoxide, methane, mixed combustible gas, coal and biomass.    ADVANTAGE - The carrier has an extremely large specific surface area, and can disperse ferric oxide highly, thus preventing combustion of the ferric oxide by avoiding reaction of an inert carrier such as silicon dioxide with the ferric oxide, and hence avoiding loss of the ferric oxide. The carrier provides better reaction activity, stability and wear resistance, and prolongs service life of gaseous and solid fuels in chemical chain combustion process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an iron-based composite oxygen carrier.
NOVELTY - Preparation of 3-isobutyl-9,10-dimethoxy-1,3,4,6,7,11b-hexahydro-pyrido(2,1-a)isoquinolin-2-one (I) comprises reacting 6,7-dimethoxy-3,4-dihydro-isoquinoline hydrochloride with 3-dimethylaminomethyl-5-methyl-hexan-2-one in the presence of water as solvent.    USE - (I) are useful as vesicular monoamine transporter inhibitor. No biological data given.    ADVANTAGE - The method is environmentally friendly and provides (I) in higher yields.
NOVELTY - A food residue processing method involves mixing a food residue with hygroscopic spacer, and adding a feeding maggot to obtain a mixture. The maggot is separated from the mixture. The maggot is a raw material for extracting protein and chitin.    USE - Method for processing food residue utilized for processing fertilizer.    ADVANTAGE - The food residue can be processed in simple and eco-friendly manner.
NOVELTY - Before oxidation with a chromium (VI) compound, betulin is pre-dispersed in a donor coordination solution (acetone, pyridine, dimethylformamide, diethyl ether) while exposed to ultrasound, and the chromium (VI) compound (chromium oxide (Cr2O3) or potassium dichromate (K2Cr2O7) or potassium chromate (K2CrO4) or pyridinium dichromate ((C5H5NH)2Cr2O72-) or chloropyridinium chromate ((C5H5NH)+Cl2O3-) in form of an aqueous solution is pre-deposited via sorption impregnation onto a solid substrate made from active aluminium oxide (Al2O3) or silica gel (SiO2) with specific surface area of not less than 210 m/g. After the oxidation reaction, the solid substrate is removed after 1-120 minutes from the obtained dispersion of reaction products which is a mixture of betulonic and betulinic acid. The oxidation reaction products are then purified by diluting the dispersion with water 5-10 times at room temperature. The dispersion phase is removed by filtration and the obtained residue is washed 5-10 times with water at temperature 50-100 degrees C, after which betulonic acid is reduced with sodium borohydride in an organic solvent to betulinic acid. The disclosed method enables to achieve betulinic acid output of up to 75-85% with respect to the starting betulin.    USE - Chemistry.    ADVANTAGE - Method has few steps and is short, avoids the use of a large amount of organic solvent, which reduces the cost of the end product and environmental pollution. 7 cl, 6 ex, 1 tbl
NOVELTY - Invention relates to agricultural biotechnologies of agricultural organic wastes processing and may be used in accelerated production of a microbiological fertiliser - a biohumus with application of a hybrid of a red California earthworm. The method includes introduction of worms into a moistened substrate, composting and separation of worms from biohumus. Chicken manure is used as a substrate, where 20% of finely ground straw is added, together with 10% of finished biohumus and 10% of alkalescent extract from the finished biohumus, with obligatory weekly mixing and moistening up to 80-90%. The produced substrate is placed in piles at open areas and is exposed to an accelerated biothermic composting within a month, with regular tillage for its enrichment with oxygen. Piles are formed at the open area, where worms are populated, and their vital functions are maintained with the help of piles covering with straw. A worm is moved by application of a pile with a chicken manure substrate to the working pile with the finished biohumus, and the worm moves into it.    USE - Agriculture.    ADVANTAGE - Production of processed chicken manure by means of a hybrid of a red California earthworm. 3 cl, 4 dwg
NOVELTY - A distributed rural household garbage treating system has a garbage sorting machine connected with anaerobic and aerobic bioreactors in parallel via discharging pipes. The anaerobic and aerobic bioreactors are connected with an anaerobic leachate collecting pool and an aerobic leachate collecting pool via pipelines. The anaerobic leachate collecting pool and the aerobic leachate collecting pool are connected with a peristaltic pump. Each anaerobic and aerobic bioreactor is connected with an air compressor.    USE - Distributed rural household garbage treating system.    ADVANTAGE - The system is convenient to use, and improves bioreactor efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating household garbage via a distributed rural household garbage treating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a distributed rural household garbage treating system.
NOVELTY - Invention relates to the field of plant growing. In the method on soil surface of a separate field at least one multilayer bed is developed, which includes layers of manure and wastes of crops. The multilayer bed is soaked until quantity of compost worms reaches critical mass. Then at least one lengthy pile is created, which includes layers of manure and organic wastes. Piles are cured until quantity of compost worms reaches critical mass. At least one multilayer bed is created on the agricultural field with periodical addition of manure and crop wastes into these beds.    USE - Agriculture.    ADVANTAGE - Method makes it possible to increase efficiency of soil enrichment with simultaneous utilisation of agricultural production wastes. 14 cl
NOVELTY - Invention relates to agricultural production, particularly, to complete treatment and reclamation of animal framing wastes to produce electric and thermal power, circulation water and fertilisers. Liquid phase of overfermented dropping is evaporated to dry concentrated fertiliser. Note here that steam is converted to water to be used for process needs. Portion of homogeneous mass is combusted to clean obtained biogas by passing its through water to produce biomethane to be fed to consumer. Water is saturated with organic substances to be used as liquid fertiliser. Air from production premises is collected to facilitate combustion of said homogeneous mass with increased heat emission. Residue of combustion is used as a mineral fertiliser. Off-gases are cleaned from solid volatile admixtures by passing them through water and saturating with mineral substances for use as mineral fertilisers. Purified off-gas is used to generate electric power to be fed to green houses.    USE - Process engineering.    ADVANTAGE - Higher efficiency. 1 dwg
NOVELTY - Invention refers to agriculture, namely to production of fertilisers from agricultural production wastes. The line of organic waste processing into bioproducts comprises reservoirs for initial components joined to a unit of preliminary mixture preparation, having an accessory for mixing and grinding. Device to decontaminate the mixture is arranged in the form of fermenters equipped with sensors of temperature and gas analyser, discharge conveyors and dosing gates. Upper part of fermenters is communicated with a unit of preliminary mixture preparation, representing reservoirs with discharge conveyors, which are arranged on the whole area of these reservoirs bottom and are united with a guide jacket with the discharge device of the mixer. The mixer is located under the discharge conveyors, above which grinding beaters are fixed. Perforated tubes of rectangular section are installed on the bottom of fermenters in process slots at inner sides of discharge conveyors. Height of pipes is equal to process slot height. Perforation is arranged on sides of pipes with reduction of perforation diametre from feed manifold from 8 to 4 mm, with perforation pitch of 100 mm. The belt discharge conveyor is joined to auger-roller press, which in its turn is joined to drying drum.    USE - Agriculture.    ADVANTAGE - Invention provides for convenience of service and higher reliability in the line operation. 2 cl, 3 dwg
NOVELTY - Method for manufacturing N-acetyl thiazolidin 4-carboxylic acid of chemical formula (I), involves reacting (in moles) formaldehyde (0.95-1.1), acetic anhydride (0.95-1.1), and L-cysteine hydrochloride monohydrate (1.1) in bioreactor.    USE - The method is useful for manufacturing N-acetyl thiazolidin 4-carboxylic acid (claimed) used as plant growth regulator.    ADVANTAGE - The N-acetyl thiazolidin 4-carboxylic acid improves productivity and quality of plant, and is environmentally-friendly.
NOVELTY - Producing biodiesel by catalyzing high-acid-value Cornus wilsoniana oil with solid acid and solid base catalyst comprises: (a) soaking solid acid and a solid base catalyst, drying in an oven at 110 degrees C; (b) roasting the solid acid catalyst and the solid base catalyst; (c) placing the solid acid on upper part and the solid base on lower part of a tubular reactor; (d) vacuumizing in the tubular reactor and preheating; and (e) continuously pumping methyl alcohol gas and feeding the preheated Cornus wilsoniana oil from the reactor, and continuously catalyzing.    USE - The method is useful for producing bio-diesel by catalyzing high-acid-value Cornus wilsoniana oil with solid acid and solid base catalyst.    ADVANTAGE - The method: employs mild reaction conditions, utilizes high activity catalysts, and is continuous, which does not corrode device; simplifies post-processing steps, produces biodiesel with high yield (98%); and meets the requirement of developing industrial and eco-friendly bio-diesel.    DETAILED DESCRIPTION - Producing bio-diesel by catalyzing high-acid-value Cornus wilsoniana oil with solid acid and solid base catalyst comprises: (a) soaking a solid acid and a solid base catalyst at room temperature to obtain an aqueous solution, loading 0.1-0.5 g/g, drying in an oven at 110 degrees C; (b) roasting the solid acid catalyst and the solid base catalyst for 3-5 hours at 300-800 degrees C; (c) placing the solid acid on upper part and the solid base on lower part of a tubular reactor; (d) vacuumizing in the tubular reactor and preheating at 80-300 degrees C; and (e) continuously pumping methyl alcohol gas and feeding the preheated Cornus wilsoniana oil from the upper part of the reactor, and continuously catalyzing for 1-20 hours.
NOVELTY - Food waste is pulverized using a pulverizer, and screened. The water content of screened food waste is reduced and a solvent is supplied. The solvent with dissolved fats is removed and recycled. The fats-separated food waste is phase-separated and sent for storage through a feed pump.    USE - Separation of fats and oils from food waste, organic sludge, and livestock waste for reuse as fuel e.g. biodiesel used for cooling and heating applications.
NOVELTY - Vacuum chamber of a plasma-arc reactor 1 is filled with hydrocarbon gas. An electric arc is generated by touching graphite electrodes 3 and 4. High-temperature pyrolysis is performed. Hydrocarbon gas is continuously fed into the reactor chamber 1. Carbon nanostructures grow on a silicon plate 2. The silicon plate 2 has the shape of a circular disc in which catalyst particles are deposited. The hydrogen produced comes out through a palladium filter 5 and pumped into a reservoir 7 by a compressor pump 6.    USE - Chemistry.    ADVANTAGE - Invention enables to obtain single- and multilayer carbon nanotubes without impurities of other modifications of carbon and hydrogen. 3 cl, 1 dwg
(ES2362852-A1)   NOVELTY - Treating sewage sludge involves performing hydrolysis and extraction of metals from the sludge. The sludge is centrifuged and supernatant is separated. The remaining sludge is treated in anaerobic microaerophilic conditions in anaerobic digester for removing hydrogen sulfide.    USE - Method for treating sewage sludge used in producing biogas.    ADVANTAGE - The method enables to treat sewage sludge and produce biogas of good quality.
NOVELTY - An additive comprises cresol phenolic and other aromatic compounds obtained from condensation of vapors produced in pyrolysis of coal minerals, and also obtained from condensation of vapors produced in pyrolysis of lignocellulosic biomass and other organic wastes.    USE - Additive used for gasoline, alcohol, kerosene and diesel.    ADVANTAGE - The additive enables to optimize performance and efficiency of internal combustion systems.
NOVELTY - The device has an electrolytic cylinder (1) provided with an adsorption and condensation unit (2). The cylinder is divided into a compartment for placing four electrolysis chambers with electrodes. A tip cap (6) passes gas into a rubber pipe (30) through a check valve (29) and inputs into an input end (19) of the condensation unit. A continuous disjunctive flow unit and a filling unit are stored within cabinets that are made of stainless steel mesh. Liquid is injected into a joint space by a spherical porous filler that is provided on a stabilizing compartment.    USE - Hydrogen and oxygen electrolyzing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hydrogen and oxygen electrolyzing device.    Electrolytic cylinder (1)    Adsorption and condensation unit (2)    Tip cap (6)    Input end (19)    Check valve (29)    Rubber pipe (30)
NOVELTY - Preparing anionic clay involves performing transesterification reactions by reacting animal fats and pure vegetable oil at 40-300 degrees C in presence of a catalyst. The catalyst contains monovalent, divalent and trivalent metal oxide. The obtained material is processed by filtration, centrifugation or solid-liquid extraction process to obtain the desired product.    USE - Method for preparing anionic clay for obtaining fatty acid alkyl esters, glycerin and biodiesel.
NOVELTY - The method involves decomposing liquid phase in the presence of a zeolite catalyst, and separating vapor phase in presence of a base catalyst.    USE - Method for reducing triacylglyceride acidity of catalytic products during cracking of vegetable oils and animal fats that is utilized as fuels in diesel engine.
NOVELTY - The present invention relates to a pesticide composition containing banana oil, pepper powder, urea and milk powder. The banana oil consists of ethyl acetate, n-butyl acetate, n-butanol, acetone, benzene, and dimethyl benzene. The banana oil is diluted with water in an appropriate ratio and then is mixed with pepper powder to have superior pesticidal efficacy. The urea is diluted with water in an appropriate ratio and then is mixed with milk powder to have superior efficacy of leaf-protection. With the said compositions, the pesticide disclosed in this invention has the practical advancement with no toxicity and pollution.
NOVELTY - Invention is intended for use in systems to produce organic fertilisers from liquid manure of farm animals and also for processing of organic wastes in municipal engineering. Line of manure recycling to produce biogas and fertilisers consists of manure collector, anaerobic bioreactor, pump, heat exchanger-condenser of heat pump joined into single circulation circuit, settling tank-accumulator of fertilisers with heat exchanger-evaporator of heat pump. Heat exchangers are joined to each other by means of compressor with gas motor drive on biogas to form thermodynamic circuit of heat pump. Heat exchanger-condenser of heat pump is arranged in the form of vertical pipe with hollow walls and is installed coaxially inside anaerobic bioreactor, heat exchanger-evaporator of heat pump is arranged in the form of submersible coil and is located in lower part of settling tank-accumulator of fertilisers. Between anaerobic bioreactor and settling tank-accumulator of fertilisers there is at least one additional bioreactor provided with pump and heat exchanger arranged in a manner similar to heat exchanger capacitor, in which heat energy of cooling liquid and exhaust gases is used from gas motor drive of heat pump compressor drive.    USE - Agriculture.    ADVANTAGE - Improved weight and dimension characteristics, increased efficiency of main process equipment of biogas and biosludge line. 1 dwg
NOVELTY - Proposed method comprises the following stages: milling organic wastes to produce pasty mass; adding ferments of microbiological origin to obtain the mix; mixing and heating said mix to cause pyrolytic reactions, and simultaneous drying and sterilisation in vacuum. Described mix makes solid compostless organic fertiliser.    USE - Process engineering.    ADVANTAGE - Shorter treatment of organic wastes and production of compostless organic fertiliser. 9 cl, 4 dwg
NOVELTY - Device (1) includes molybdenum disilicide cathode (3) and a stainless steel anode (2), where cathode and anode are supplied with power through solar photovoltaic arrangement.    USE - Device for producing electrolytic hydrogen (claimed).    ADVANTAGE - The device produces hydrogen without producing smoke and waste, where only waste product is water vapor. The device produces unlimited source of clean and cheap energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Device (1)    Stainless steel anode (2)    Molybdenum disilicide cathode (3)
NOVELTY - Disclosed is a method of producing granular ammonium nitrate which involves neutralisation of nitric acid with gaseous ammonia, evaporation of the obtained solution until obtaining a highly concentrated melt which contains ammonium nitrate in amount of not less than 99.5%, spraying the melt into a granulation tower having at least one vibrogranulator, while feeding air in a counterflow at a rate of 7.0-7.8 t/h per m2 of the cross-section of the tower and output of the obtained granules in amount of 1.0-1.2 t/h per m2 of the cross-section of the tower, cooling the obtained granules with air in fluidised bed apparatus, where after cooling the granules to temperature not over 45 degrees C, spent air at temperature 60 - 70 degrees C comes out of the fluidised bed apparatus into the bottom part of the granulation tower, where it mixes with air sucked from the atmosphere in volume ratio of 1:1, spent air and juice vapour from the neutralisation and evaporation steps are mixed with spent air from the granulation tower, the vapour-air mixture formed is washed in a gas cleaner, while sprinkling the trays of the gas cleaner with a circulating ammonium nitrate solution and further filtered through a multilayer fibrous non-woven material which contains ultrafine fibre, while sprinkling the front layer of the material with condensate of the juice vapour.    USE - Chemistry.    ADVANTAGE - Invention enables to intensify the process while improving the quality of the end product and reducing harmful emissions into the atmosphere. 3 cl, 1 dwg, 1 ex
NOVELTY - Choerospondias axillaries material is soaked in (40%) phosphoric acid at constant temperature for 48 hours and carbonized at 500 degrees C or more for 3 hours under nitrogen atmosphere, to obtain black solid granules. The obtained black solid granules is added to concentrated sulfuric acid and sulfonation reaction is carried out at 60-140 degrees C for 2-6 hours. The resultant product is stirred, washed using distilled water at 100 degrees C and dried, to obtain carbon-based solid acid catalyst.    USE - Granular carbon-based solid acid catalyst used for manufacture of biodiesel.    ADVANTAGE - The catalyst has improved stability and recyclability.
NOVELTY - Reduction of acid value of biodiesel oil comprises mixing and reacting biodiesel oil-containing redundant fatty acid with inorganic strong alkaline solution in reactor, adding inorganic calcium salt solution to mix and react, processing mixing liquid, washing with water, separating, drying and fractionating in vacuum.    USE - Method for reducing acid value of biodiesel oil (claimed).
NOVELTY - The gas purifier has an air chamber (1) that is provided with inlet pipe (3), washing liquid inlet and washing liquid outlet (14). A through pipe (6) is connected with air chamber of drying room (8). A vessel is provided with a single-way control valve and a drying agent inlet. The drying agent inlet is provided on the drying chamber (7), desiccant outlet (13) and exhaust pipe (10).    USE - Biogas purifier used in household appliance.    ADVANTAGE - The purity of the biogas methane can be improved, to increase the fuel value of gas. The energy utilization rate of the biogas purifier can be increased. The structure of the biogas purifier can be simplified, so that the biogas purifier operation can be operated conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the biogas purifier.    Air chamber (1)    Inlet pipe (3)    Through pipe (6)    Drying chamber (7)    Drying room (8)    Exhaust pipe (10)    Desiccant outlet (13)    Washing liquid outlet (14)
NOVELTY - A high-speed food waste biological treatment system comprises at least three stages of anaerobic digestion reactor. It adopts underground design. The anaerobic digestion reactor comprises high-temperature acid hydrolysis reactor, high temperature methane-producing reactor, biogas residue storage thermal reactor, and heat storage slurry reactor.    USE - A high-speed food waste biological treatment system.    ADVANTAGE - The system uses multistage anaerobic digestion technology and underground engineering design, and has simple structure, compact structure, low investment, small floor area, biological pretreatment of municipal refuse treatment effect, and good social and economic benefit.    DETAILED DESCRIPTION - A high-speed food waste biological treatment system comprises at least three stages of anaerobic digestion reactor. It adopts underground design. The anaerobic digestion reactor comprises high temperature acid hydrolysis reactor, high temperature methane-producing reactor, biogas residue storage thermal reactor, and heat storage slurry reactor. The acidification reactor is provided with flowing window preprocessed waste inlet, and high temperature acid hydrolysis reactor. The storage residue thermal reactor is provided with a material conveying pipeline. The upper part of the reactor is provided with an overflow liquid connected to the storage thermal reactor and high temperature acid hydrolysis reactor. The high temperature methane-producing reactor is provided with a heater connected with power system through pipeline. The digestion reactors have heat preservation layer, high temperature methane-producing reactor, and storing biogas. The biogas slurry heat insulating top part of the reactor is provided with the upper part of the side face of the liquid cavity of the gas discharge nozzle.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of a high-speed food waste biological treatment system.
NOVELTY - The fermenting bed has a chicken cage that is provided with fixed rail (4) through the fermenting bed padding groove (5) and groove side wall. The rail is provided with an automatic padding raking machine (6). An automatic atomizing bacterial supplementing system (3) is located below the chicken cage. A nozzle of the automatic atomizing bacterial supplementing system is set parallel and opposite to the padding layer.    USE - Fully-degradable fermenting bed for chicken manure of laying hen house.    ADVANTAGE - The padding material can be raked in the fermenting bed. The microorganism compound bacterial of the fermenting bed can be supplemented according to the degradation demand of the chicken manure of laying hen house.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fully-degradable fermenting bed for chicken manure of laying hen house.    Water drinking device (1)    Automatic atomizing bacterial supplementing system (3)    Fixed rail (4)    Fermenting bed padding groove (5)    Automatic padding raking machine (6)
NOVELTY - A sulfonated solid carbon-acid catalyst preparing method involves mixing biomass chosen from dextrose, fructose, sucrose, maltose, cellulose, furfural and starch with an aromatic compound chosen from benzyl chloride, benzyl alcohol, diphenyldichloromethane, phenol or chlorobenzene, and heat-processing the obtained mixture to remove solvent , and to obtain carbon material rich aromatic ring . The obtained product is sequentially sulfonated using concentrated sulfuric acid and surface treated with solid carbon-acid catalyst.    USE - Method for preparing sulfonated solid carbon-acid catalyst that is utilized during esterification, alkylation reaction, cellulose hydrolysis, fine chemical synthesis and biodiesel preparation (all claimed).    ADVANTAGE - The method enables preparing solid acid catalyst with high acid content, reactivity, recyclability and stability while controlling the acid content in an effective manner.
NOVELTY - A biologic organic fertilizer preparing method involves uniformly mixing (in wt.%) pig manure (5-40), chicken manure (5-50), cow manure (5-40), turf (5-15), vegetable cake (5-10), saw powder (5-35) and bran (5-10) to form mixture. 1-20 weight percent of biologic active water is added. The mixture containing the water is stacked and turned to promote the water of solid fermentation to steam. The mixture is again centrally stacked and fermented until fermenting and curing operation is finished. The mixture is dried, crushed, screened and packaged to obtain biologic organic fertilizer.    USE - Method for preparing biologic organic fertilizer.    ADVANTAGE - The method enables preparing biologic organic fertilizer with less content of harmful element, so that soil quality is improved, crop production is increased, and quality of the crop is enhanced. The method enables reducing soil pesticide residue and improving quality of the saline-alkali soil.    DETAILED DESCRIPTION - A biologic organic fertilizer preparing method involves uniformly mixing (in wt.%) pig manure (5-40), chicken manure (5-50), cow manure (5-40), turf (5-15), vegetable cake (5-10), saw powder (5-35) and bran (5-10) to form mixture. 1-20 weight percent of biologic active water having concentration of 5-50 percent is added. pH value is adjusted to 6.9-8.9. The mixture containing the biologic active water is stacked and turned one time for each of 2-7 days to promote the water of solid fermentation to steam and supply oxygen. The mixture is again centrally stacked and fermented until fermenting and curing operation is finished. The mixture is dried, crushed, screened and packaged to obtain biologic organic fertilizer. An INDEPENDENT CLAIM is also included for a biologic organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a method for preparing biologic organic fertilizer. '(Drawing includes non-English language text)'
NOVELTY - A fruit and vegetable residue fermentative organic fertilizer comprises (in weight parts) apple pomace (400-100), pear residue, vegetable slag, sludge (600-1800), livestock manure (500-1000) and activating agent (0.5-1.5).    USE - Fruit and vegetable residue fermentative organic fertilizer.    ADVANTAGE - The fertilizer is rich in nutrition, and has high efficiency. The fertilizer avoids the environment pollution caused by rotten of fruit and vegetable slags.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing a fruit and vegetable residue fermentative organic fertilizer.
NOVELTY - A metal anode consists of porous metal material as substrate loaded with catalyst on surface. The metal material has porosity volume of 30-60 vol.%, porosity of 60-99%, average aperture of 1-100 micron, Young's modulus of 0.5-37 GPa and compressive strength of 0.04-2.2 GPa.    USE - Metal anode for use in membrane electrolysis of sodium carbonate solution (claimed).    ADVANTAGE - The metal anode reduces oxygen evolution over potential and power consumption.
NOVELTY - Contamination removing involves introducing carbon dioxide (2) in aqueous solution by decanting biowaste. The biowaste oil is transformed into biodiesel (6) by adding sodium methoxide (5). The aqueous phase is deposited by introducing calcium hydroxide for forming calcium carbonate precipitate and ammonia gas. The formed ammonia gas is captured and mixed with methane produced in gasification to produce water, which contains nitrates, phosphates and calcium nitrate and is suitable for irrigation.    USE - Method for removing contamination of biowaste (claimed).    ADVANTAGE - The method enables to remove contamination with high efficiency in an eco-friendly and cost-effective manner, and also provides energy in the form of by-product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the contamination removing method.    Settling tank (1)    Carbon dioxide (2)    Ammonium carbonate (3)    Sodium methoxide (5)    Biodiesel (6)
NOVELTY - Hydrogen and ammonia production involves introducing ammonia gas in water for forming ammonium ions. The formed ammonium ions are passed through a filter filled with iron at an electrical potential (2) of 12 volts. The ammonium ions produce ammonia gas and hydrogen gas.    USE - Method for producing hydrogen and ammonia from ammonia used in hydrogen fuel cells for recharging batteries and producing electricity for electric motors.    ADVANTAGE - The method enables to produce hydrogen and ammonia in an eco-friendly and cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hydrogen and ammonia production method. (Drawing includes non-English language text).    Reservoir (1)    Electrical potential (2)    Hydrogen fuel cell (3)    Batteries (4)    Electric motor (5)
NOVELTY - A 2-bromo-4,5-dimethoxybenzoic acid is prepared by (A) reacting 3,4-dimethoxytoluene, sulfuric acid, hydrogen peroxide and metal bromide at 30-60 degrees C and molar feed ratio of 1:0.5-0.8:1-1.2:1-1.2 to obtain 2-bromo-4,5-dimethoxytoluene; and (B) reacting 2-bromo-4,5-dimethoxytoluene at 50-90 degrees C in water solution with potassium permanganate and tetrabutyl ammonium bromide at molar feed ratio of 1:3-3.5:0.02-0.10 to obtain 2-bromo-4,5-dimethoxybenzoic acid.    USE - Method for preparing 2-bromo-4,5-dimethoxybenzoic acid (claimed).    ADVANTAGE - The method has cheap cost of the raw material, is easy to obtain, has high product yield, is environmental friendly, has warm reaction condition and simple operation, and is suitable for industrial large-scale production.
NOVELTY - The pool has water pressure chamber whose one side is provided as semi-oval shape and other side is provided with liquid outlet pipe. A top end of a water pressure chamber is covered.    USE - Reinforced plastic biogas pool.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reinforced plastic biogas pool.
NOVELTY - A recombinant Saccharomyces cerevisiae strain obtained by obtaining guanosine triphosphatase (GTPase) activating protein (gap) gene fragment from Pichia pastoris GS115 clone, inserting the gene fragment in pYES2 vector containing galactose-inducible promoter, connecting xylose reductase gene xy11 segment and xylitol dehydrogenase gene xy12 segment in series together, inserting the connected fragment in constitutive gap in vector, constructing PYES2-GAP-xy11-xy12 plasmid, and inserting recombinant plasmid into S.cerevisiae, is new.    USE - The S.cerevisiae is useful for fermenting straw to produce fuel, preferably ethanol (claimed).    ADVANTAGE - The S.cerevisiae has high activity, enables mass production of ethanol cost-effectively, and reduces environmental pollution.
NOVELTY - The method involves placing iron in air reactor fluidized bed (1) of hydrogen production system. The fuel gas containing carbon is feed to lower end (f) of fuel reactor fluidized bed. The steam is fed to steam reactor fluidized bed lower end (d) of hydrogen production system. The smoke discharged out of fuel reactor (4-1) is entered to fuel reactor bottom air chamber (6-2). The nickel oxide is reacted with fuel reactor outlet, and reached to air cyclone separator (8-4) of heating system through transition section (8-2) and lifting tube (8-3).    USE - Method for performing production of hydrogen and separation of carbon dioxide.    ADVANTAGE - The production of hydrogen and separation of carbon dioxide can be performed effectively.    DETAILED DESCRIPTION - The iron is reacted with the oxygen of air to generate iron oxide which is passed through air reactor transition section (1-2) and air reactor lifting tube (1-3). An INDEPENDENT CLAIM is included for device for performing production of hydrogen and separation of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen production and carbon dioxide separation device.    Air reactor fluidized bed (1)    Air reactor transition section (1-2)    Air reactor lifting tube (1-3)    Fuel reactor (4-1)    Fuel reactor bottom air chamber (6-2)    Air reactor transition section (8-2)    Air reactor lifting tube (8-3)    Air cyclone separator (8-4)    Steam reactor fluidized bed lower end of hydrogen production system (d)    Lower end of fuel reactor fluidized bed (f)
NOVELTY - Preparation of fatty acid methyl ester comprises adding water into mixture of plant oil or fatty acid in methanol; adding mixture into reactor to carry out esterification; and decompressing and distilling to generate fatty acid methyl ester and water.    USE - Preparation of fatty acid methyl ester.    ADVANTAGE - The method reduces supercritical reaction temperature and oil ratio in one-step method for preparing biodiesel fuel, and reduces fuel energy consumption during preparation of biodiesel. It does not need catalyst, does not generate wastewater waste gas, and does not cause any environment pollution.
NOVELTY - 1-Substituted phenyl-4-substituted phenyl-5-substituted salicylaldimine-1,2,3-triazole derivative (I) is new.    USE - New 1-substituted phenyl-4-substituted phenyl-5-substituted salicylaldimine-1,2,3-triazole derivative (I) used as antifungal and antibacterial agent.    ADVANTAGE - Compound (I) has strong activity against Candida albicans, Escherichia coli and Staphylococcus aureus; broad antifungal/antibacterial spectrum; and high efficiency. Preparation method is simple and environment friendly, and has low cost and high yield.    DETAILED DESCRIPTION - 1-Substituted phenyl-4-substituted phenyl-5-substituted salicylaldimine-1,2,3-triazole derivative of formula (I) is new.    R1=Z, 4-SO3H, 3-SO3H, 4-COOH, or 3-COOH;    R2=Z, 4-CF3, or 3-CF3;    Z=H, 4-Cl, 3-Cl, 4-Br, 3-Br, 4-CH3, 3-CH3, 4-OCH3, 3-OCH3, 4-NO2, or 3-NO2; and    X=H, 5-Cl, 5-Br, 3,5-Cl,Cl, or 3,5-Br,Br.    An INDEPENDENT CLAIM is included for preparation of compound (I).
NOVELTY - Fatty acid, methanol and sulfuric acid with initial acid value of 170-275 mg potassium hydroxide (KOH)/g are added to a three-opening bottle as an esterification reactor. The resultant mixture is heated to 65 plus minus 5 degrees C, stirred, and backflow processing is carried out in reactor, and acid value is adjusted to 25-35 mgKOH/g. Methanol is continuously fed to three-opening bottle. The moisture content and methanol generated by esterification are removed by a condensation device, and reaction is terminated, when the acid value is less than 1.0 mg/g, to obtain biodiesel.    USE - Preparation of biodiesel.    ADVANTAGE - The method provides biodiesel by a simple process, in short time, with reduced consumption of acid. The purification of biodiesel is easy, as fatty acid methyl ester and water are generated as reaction products.    DETAILED DESCRIPTION - Fatty acid, methanol and sulfuric acid with initial acid value of 170-275 mg potassium hydroxide (KOH)/g are added to a three-opening bottle as an esterification reactor. The amount of methanol is 80% of fatty-acid weight. The concentration of sulfuric acid is 98% and amount of sulfuric acid is 0.5-1.0% of the fatty-acid weight. The resultant mixture is heated to 65 plus minus 5 degrees C, stirred, and backflow processing is carried out in reactor, and acid value is adjusted to 25-35 mgKOH/g. Methanol is continuously fed to three-opening bottle at 100 plus minus 5 degrees C with a flow rate of 1.0-1.5 mL/minute. The moisture content and methanol generated by esterification are removed by a condensation device, and the reaction is terminated, when the acid value is less than 1.0 mgKOH/g, to obtain biodiesel.
NOVELTY - A solid alkali catalyst comprises calcium oxide, magnesium oxide and zinc oxide in the mass ratio of (1.0-3.2):(0.6-3.9):(1.0-16.5).    USE - Solid alkali catalyst used for catalyzing ester exchange reaction of plant oil and methanol to prepare biodiesel (claimed).    ADVANTAGE - The solid catalyst is manufactured economically by a simple process and with improved efficiency. The catalyst catalyzes the ester exchange reaction quickly and effectively to obtain biodiesel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of the solid alkali catalyst, which involves mixing calcium nitrate, magnesium nitrate and zinc nitrate in distilled water to obtain nitrate mixed solution, dissolving potassium carbonate, sodium carbonate or ammonium carbonate in distilled water to obtain carbonate solution, stirring the nitrate solution and carbonate solution, at pH of 6-8, and reacting for 3-4 hours to form a deposit, filtering and washing the deposit with hot water to obtain white filter cake, drying the cake, grinding and calcining the dried cake in microwave muffle furnace; and    (2) use of the catalyst for biodiesel conversion.
NOVELTY - Dechlorinated tobacco waste organic fertilizer and artificial peat obtained by performing dechlorination and fermentation to tobacco waste, is claimed. The chlorine content of the organic fertilizer is less than or equal to 1%, and the chlorine content of the artificial peat is less than or equal to 0.3%.    USE - Used as dechlorinated tobacco waste organic fertilizer and artificial peat. The extract of tobacco waste obtained through solid-liquid separation is useful as: a liquid organic fertilizer and a medium for many fermentation processes (all claimed).    ADVANTAGE - The method is simple; uses easily available raw material; is suitable for large scale production; and can greatly reduce the ionic strength of the artificial peat. The physical and chemical properties and the using effect of the artificial peat obtained from the method are close to or reach the level of the natural peat.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing the dechlorinated tobacco waste organic fertilizer and the artificial peat, comprising performing dechlorination process to the tobacco waste.
NOVELTY - Rapid fermentation device for producing fertilizer from straw comprises a number of divergent tubes. The divergent tubes are uniformly mounted on the circumference of a divergent tube seat. The divergent tubes are densely distributed with radiating holes. A pipe joint a (1) is installed on the divergent tube seat to form a hot air divergent device (5).    USE - Used as a rapid fermentation device for producing fertilizer from straw.    DESCRIPTION OF DRAWING(S) - The drawing shows a rapid fermentation device for producing fertilizer from straw.    Pipe joint a (1)    Main pipeline (4)    Hot air divergent device (5)    Fermenting tank (6)    Pipe joint b (10)
NOVELTY - Base fertilizer comprises (in wt.%) fermented cake fertilizer (19-23), biogas residue (43-47), common calcium superphosphate (17-21), potassium nitrate (2.3-2.7), borax (0.27-0.32), zinc sulfate heptahydrate (0.8-0.9), potassium sulfate (9.5-9.9), potassium humate (0.05-0.15) and mixed bacterial manure (0.64-0.68). The fertilizer is prepared by (i) drying, crushing and sieving the fermented cake fertilizer with a 20-mesh sieve, then uniformly mixing; (ii) uniformly mixing; (iii) adding the remaining raw materials, uniformly agitating, packing, sealing, and storing the product in a shady place.    USE - The base fertilizer is useful for cultivating tobacco, and increasing disease resistance in tobacco.    ADVANTAGE - The fertilizer can repair, or protect the soil micro-ecological environment; improves the quality of flue-cured tobacco, and thus it produces tobacco in a continuous and healthy manner.    DETAILED DESCRIPTION - Base fertilizer comprises (in wt.%) fermented cake fertilizer (19-23), biogas residue (43-47), common calcium superphosphate (17-21), potassium nitrate (2.3-2.7), borax (0.27-0.32), zinc sulfate heptahydrate (0.8-0.9), potassium sulfate (9.5-9.9), potassium humate (0.05-0.15) and mixed bacterial manure (0.64-0.68). The fertilizer is prepared by (i) drying, crushing and sieving the fermented cake fertilizer with a 20-mesh sieve, then uniformly mixing the material as a base mixture of the fertilizer, and maintaining the moisture content at 19 plus minus 4%; (ii) uniformly mixing by pouring the mixed bacterial manure to the base mixture; (iii) adding the remaining raw materials to the base mixture, then uniformly agitating, packing, sealing, and storing the product in a shady place.
NOVELTY - A linezolid is prepared by reacting a phenyl derivative with a morpholin, hydrogenating obtained product in the presence of palladium/carbon catalyst, adding potassium carbonate and benzyl chloroformate to the hydrogenated product, and adding tert-butyllithium and an acetate derivative.    USE - Method of preparing linezolid.    ADVANTAGE - The method does not require silica gel column for purification, and is environment-friendly.    DETAILED DESCRIPTION - A linezolid is prepared by reacting a phenyl derivative of formula (I) with a morpholin, hydrogenating obtained product in the presence of palladium/carbon catalyst, adding potassium carbonate and benzyl chloroformate to the hydrogenated product, and adding tert-butyllithium and an acetate derivative of formula Cl-CH2-CH(OCH3COO)-CH2-CH3COONH.
NOVELTY - Producing organic vegetables based on earthworm biological engineering, comprises (i) using human and animal excreta and vegetable waste for fermenting to produce earthworm feed, (ii) using the feed to cultivate earthworms, (iii) utilizing the metabolites for producing e.g. an organic fertilizer, and using the earthworms for production of biological preparation, (iv) using the organic and biological fertilizers to prepare red fertilizer, (v) applying e.g. the organic fertilizer for vegetable planting, and (vi) in the step (v), adding excreta in the vegetable waste, and repeating all the steps.    USE - The method is useful for producing organic vegetables based on earthworm biological engineering.    ADVANTAGE - The method is ecofriendly and cost-effective, saves resources, ensures high yield of green organic vegetables, and improves production efficiency and quality of vegetables without using synthetic chemical fertilizers and agricultural pesticides.    DETAILED DESCRIPTION - Producing organic vegetables based on earthworm biological engineering, comprises (i) using human and animal excreta and vegetable waste for fermenting to produce earthworm feed, (ii) using the earthworm feed obtained from the step (i) for cultivate earthworms, (iii) utilizing the metabolites produced from the step (ii) to producing an organic fertilizer, a soil conditioner and a seedling substrate, and using the earthworms obtained form the step (ii) for in-vivo production of a biological preparation for preventing diseases and insect pests, (iv) using the organic and biological fertilizers obtained from the step (iii) to prepare red fertilizer, (v) applying the organic fertilizer, soil conditioner, red fertilizer, seedling substrate and biological preparation to prevent the diseases and insect pests for vegetable planting, and (vi) in the step (v), adding the human and animal excreta in the produced vegetable waste, and repeating all the steps from (i) to (vi).
NOVELTY - Producing ammonium nitrate by using waste ammonium hydroxide and waste nitric acid, comprises selecting raw materials, distilling, neutralizing, concentrating, crystallizing, filtering and drying, where the raw material comprises more than 7% of waste ammonium hydroxide, performing distillation in a distillation kettle, adding strong oxidation catalyst, heating to 55-93 degrees C, neutralizing with nitric acid (5-69%), and controlling pH to 4-6.    USE - The method is useful for producing ammonium nitrate by using waste ammonium hydroxide and nitric acid.    ADVANTAGE - The method is simple, quick, economical, environment-friendly and suitable for township and village enterprises, and it completely utilizes the resources of waste ammonium hydroxide and waste nitric acid.
NOVELTY - An ozagrel crude drug preparing method involves utilizing 3-p-tolyl-acrylic acid ethyl ester as an initial raw material. N-bromosuccinimide bromination is carried out to prepare 3-(4-bromomethyl-phenyl)-acrylic acid ethyl ester. Condensation reaction is carried out with imidazole to generate ozagrel ethyl ester. Hydrolysis is carried out under basic condition, and acidification is carried out to prepare ozagrel crude product. The ozagrel crude product is refined.    USE - Method for preparing ozagrel crude drug in an industry.    ADVANTAGE - The method enables improving catalyst refining effect, increasing product yield and quality, avoiding usage of a toxic reagent and an expensive reagent, and reducing environment pollution and production cost.
NOVELTY - Application of coronatine for preparing plant defoliant and boll-opening products, is claimed.    USE - The coronatine is useful for preparing the plant defoliant and boll-opening products (all claimed).    ADVANTAGE - The coronatine is ecofriendly, has little dosage and good effect, where coronatine (100 mg/l) ensures more than 80% of defoliation rate after being sprayed onto the cotton plants for 14 days, ensures same treatment effect as compared to that of thidiazuron (300 mg/l), and ensures 72.7-76.8% of the boll opening rate, which is better than that of thidiazuron.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for:    (1) preparing the cotton defoliant, comprising fermenting coronatine in a liquid culture medium for producing strain, collecting the fermentation liquid, and extracting coronatine from the obtained fermentation liquid, where the obtained coronatine is cotton defoliant; and    (2) increasing cotton defoliation rate and boll opening rate, comprising spraying coronatine aqueous solution (10-1000 mg/l) or spraying cotton defoliant aqueous solution (10-1000 mg/l) on stem and leaves of the cotton plants to obtain 35-75% of boll opening rate.
NOVELTY - A methanol petroleum comprises (in wt.%) methanol (15-30), petroleum (67-83) and annexing agent (2-3).    USE - Methanol petroleum for vehicle. Uses include but are not limited to passenger car, forklift, moped, agricultural vehicle, motorcycle, load carrier and forklift lorry.    ADVANTAGE - The petroleum has simple preparation process and better property. The methanol petroleum can be mixed with the national petroleum regardless of ratio. The petroleum satisfies discharge index with environmental protection request.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a methanol petroleum.
NOVELTY - Bio-organic fertilizer with edible mushroom residues comprises (in wt.%) edible mushroom residues (75-80), urea (8-10), monoammonium phosphate (5-8), potassium sulfate (4-6), bacteria (1-1.5) and regulator (0.2-0.3).    USE - The organic fertilizer is useful in agricultural production.    ADVANTAGE - The organic fertilizer improves the soil, increases soil fertility, reduces fertilizer loss, and improves the utilization rate, the crop yield and the quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-organic fertilizer with edible mushroom residues, comprising: (i) mechanically and uniformly turning the crushed and dried mushroom residues and the bacteria, piling and fermenting by decreasing the fermentation temperature of the fermentation material to 40-45 degrees C in 24 hours and to 58-63 degrees C in 48 hours, curing and dehydrating for 7 days; and (ii) drying and crushing the fermented material, uniformly mixing with urea, monoammonium phosphate, potassium sulfate and regulator to obtain the qualified granular organic fertilizer product by extruding, pelleting and sieving in a dry manner.
NOVELTY - Preparing fertilizer culture for planting dandelion, comprises taking (in wt.%) chicken manure (10-16), rabbit manure (8-12), soybean cake powder (12-16), rape powder (6-8), rice powder (10-12), cotton powder (4-8), pumpkin stem leaf powder (2-6), garlic powder (2-6), mulberry powder (3), pine needle powder (2-4), semen cassiae powder (1-3), Camellia (8-10), lotus leaf powder (2-4), radix paeoniae alba (2-4), bulbus fritillariae cirrhosae (2-4), safflower (2-4) and Angelica (2-4).    USE - The method is useful for preparing fertilizer culture for planting dandelion.    ADVANTAGE - The method is simple. The fertilizer makes the dandelion: growth dense and strong; to receive high luminosity; and to prevent disease, and successfully overcome the disadvantages of various nutrient fertilizers, which easily cause the dandelion leaf surface yellow, rare flowering, light weight, bad disease, and susceptible to defects of various plant diseases and insect pests.
NOVELTY - A flumetsulam synthesizing method involves using 3-(2,4,6-trimethylphenylsulfonyl)-1,2,4-triazole, triphosgene (immobilized phosgene) or diphosgene and diethylamine as materials, acetylating the materials, and aminating the materials in an alkaline condition.    USE - Method for synthesizing flumetsulam.    ADVANTAGE - The method enables obtaining the materials easily, reducing cost, improving synthesis yield, and meeting production requirement. The flumetsulam is environment-friendly and easy for industrial production.
NOVELTY - Nutritional fertilizer for tail mushroom comprises (in wt.%): towel gourd powder (35-55), soybean powder (25-45), Cyperus rotundus powder (10-16), dried sheep manure (1.5-2), bitter gourd powder (0.5-1), pine needle powder (0.5-1), wood ash (0.5-1), motherwort powder (1.5-2), bitter gourd powder (0.1-0.3), honeysuckle powder (0.1-0.3), puffing powder (0.1-0.3) and hawthorn powder (0.5-0.8).    USE - Used as a nutritional fertilizer for tail mushroom.    ADVANTAGE - The organic fertilizer: generates large amount of beneficial microorganisms; satisfies the growth requirement of tail mushroom, produces tender, tasty, rich nutritional tail mushroom with quick growth rate; increases the yield; and overcomes lack of nutrition e.g. impotence shrinkage, slow growth, small size tail mushroom, less weight, poor resistance to disease, leaf blight fungal disease susceptibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the nutritional fertilizer comprising: mixing prescribed amount of towel gourd powder, soybean powder, Cyperus rotundus powder, dried sheep manure, bitter gourd powder and motherwort powder, transferring into a crusher and crushing into 100 mesh particles, adding pine needle powder, wood ash powder, balsam pear powder, honeysuckle powder, puffing powder and hawthorn powder into a stirrer and stirring for 300 minutes, adding in a ratio of 1:1.3-1:1.5 and fermenting for 72 hours.
NOVELTY - Biological organic fertilizer comprises (in wt.%) citrus peel (65-75), rice (5-8), wooden meal (4-5), Stevia rebaudiana residue (0-5), livestock and poultry manure (10-20) and fertilizer and biological strain (1-2).    USE - Used as a biological organic fertilizer.    ADVANTAGE - The fertilizer: has high national standard index in comparison with the conventional fertilizer; improves water, fertilizer, gas, and heat conditions to make the soil looser and fertile after applying to soil; promotes crop root growth, and yield, improves the quality of the product; and is produced from the waste residue of industrial orange waste residue, thus the waste is recycled and protects the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the biological organic fertilizer, comprising: (a) adding lime (10-15 kg) to each ton of orange peel residue to adjust the pH to 7, and crushing and mixing uniformly, (b) adding chaff, wooden meal, sweet Stevia rebaudiana slag, uniformly mixing until the moisture content is 50-60% to obtain a mixed material, (c) degrading by adding crude fiber degradable special complex strain in a ratio of 1kg to 5-10, and culturing for 6-8 hours, uniformly spraying or mixing in the mixed material, stacking to heap, covering with grass or negative pressure aeration method for primary crude fiber degradation for 3-4 days, (d) compost processing according to claim 1 according to the proportion and livestock and poultry manure, adding the activated composite strain compost (1 kg), uniformly mixing, stacking growing ridge fermenting the compost process to 10 ton material, turning once in every 5-7 days, turning 3-4 times to complete the composting, and (e) adding functional bacteria, drying until the moisture content is 25-30%, adding activated functional strain, mixing with organic fertilizer (1 kg-10 ton), sieve grading or granulating, packing and storing.
NOVELTY - Organic fertilizer of ginseng comprises (in parts by wt.) sawdust (20-40), chicken manure (10-20), soybean curd residue (10-20), bark (10-20) and corn powder (10-20).    USE - The organic fertilizer of ginseng is useful for increasing the soil organic matter, and providing large amount of nutrients needed by plants.    ADVANTAGE - The organic fertilizer ensures balanced nutrition and good efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the organic fertilizer of ginseng, comprising (i) fermenting the materials by (i.a) mixing the sawdust, corn powder, soybean curd residue and bark powder according to the proportion, turning the materials in a turning tank for 10-30 days, and (i.b) preserving the fertilizer by piling the turned materials to preserve the fertilizer, turning in every 5-20 days for 5-12 months, (ii) fermenting the chicken manure by introducing the chicken manure into a fermenting tank, and turning once in every 5-7 days continuously for 60-120 days, and (ii) processing the fermented fertilizer by mixing the fermented material with the fermented chicken manure in a ratio of 10-15%, crushing, and sieving to obtain the organic fertilizer.
NOVELTY - A nitrogen source fertilizer comprises waste crops straw as matrix, and solid nitrogen organisms. The fertilizer is prepared by fine crushing corn, broomcorn and other crop straws; drying; adding mild humus domestic animal manure enriched with solid nitrogen microorganisms, human excrement, urine, root soil, trace elements of iron and molybdenum; inoculating solid nitrogen organisms; mixing uniformly; and stacking.    USE - A nitrogen source fertilizer for use as base fertilizer or seedbed fertilizer for irrigating root, or preventing disease of the soil.    ADVANTAGE - The fertilizer can enrich the soil for long time, solves agrichemical pollution, and enhances resistance of the crops thus improving product quality.
NOVELTY - Preparation of a biogas liquid fertilizer comprises loading fresh biogas liquid; adding fermented molasses; inoculating microorganism leaven, and inoculating Bacillus and photosynthetic bacteria in the fresh biogas liquid; shaking or stirring to ferment aerobically; and storing the fermented biogas liquid fertilizer with mixed bacteria at normal temperature or refrigerating temperature.    USE - Method for the preparation of a biogas liquid fertilizer (claimed).    ADVANTAGE - The method has simple operation, is inexpensive, has no irritant odor, and has high fertilization efficiency.
NOVELTY - Preparation of an organic fertilizer comprises pre-processing cyanide of a fine chemical product during associated natural gas ammonia oxidation of iminodiacetonitrile slag to obtain a pile of fermented waste residue base material; mixing and preparing a stack of the fermented waste residue base material to a biomass substrate; uniformly mixing a fermentation microbial inoculum source and the fermented base material to ferment for 15-45 days at 15-85 degrees C; and uniformly mixing, pelletizing, and drying.    USE - Method for the preparation of an organic fertilizer (claimed).    ADVANTAGE - The method can harmlessly process toxic nitrile in the iminodiacetonitrile waste toxic nitrile compound in the slag.    DETAILED DESCRIPTION - Preparation of an organic fertilizer comprises:    (A) pre-processing cyanide of a fine chemical product during associated natural gas ammonia oxidation of iminodiacetonitrile slag to obtain a pile of fermented waste residue base material;    (B) mixing and preparing a stack of the fermented waste residue base material of polypropylene resin to a biomass substrate at a mass ratio of 1:2-5 to prepare fermented base material;    (C) uniformly mixing a fermentation microbial inoculum source and the fermented base material at a mass ratio of 1:10:15 to ferment for 15-45 days at 15-85 degrees C and at a pH of 5-7.5 to obtain an organic fertilizer raw material, nitrogen, phosphorus, and potassium nutrient; and    (D) uniformly mixing, pelletizing, and drying.
NOVELTY - An organic granular fertilizer comprises (wt.%) seaweed extract (15-25), alginic acid (1.5-4), fermented pig manure (15-25), bean pulp (10-15), humic acid (15-25), and clay (15-35).    USE - Organic granular fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the organic granular fertilizer, comprising mixing and crushing the raw materials, spraying water into crushed materials, performing disc or drum granulation and drying.
NOVELTY - Rural-urban garbage fermentation liquor is prepared using (in parts weight): efficient microbes (EM) liquor (1-5), bulking agent (1-15) and leavening agent (1-10). The EM liquor is prepared by obtaining Sporotrichum thermophile, Phanerochaete chrysosporium, Lactobacillus bulgaricus and Saccharomycetes into solution containing brown sugar, rice vinegar and Chinese distilled spirits, mixing the obtained materials uniformly, and culturing the microorganism.    USE - The rural-urban garbage fermentation liquor is used as organic fertilizer for controlling pathogens.    ADVANTAGE - The method converts rural-urban garbage into non-toxic, pollution-free and non-residual organic fertilizer, and increases production and quality of agricultural products.    DETAILED DESCRIPTION - Rural-urban garbage fermentation liquor is prepared using (in parts weight): efficient microbes (EM) liquor (1-5), bulking agent (1-15) and leavening agent (1-10). The EM liquor is prepared by obtaining Sporotrichum thermophile, Phanerochaete chrysosporium, Lactobacillus bulgaricus and Saccharomycetes in a ratio of 1:1:1:1 into 50 ml of solution containing brown sugar (20-40 g), rice vinegar (100 ml) and Chinese distilled spirits (100 ml) with alcohol content of 30-35 volume/volume%, mixing the obtained materials uniformly, and culturing the microorganism at 28-32 degrees c for 5-7 days. An INDEPENDENT CLAIM is included for method of preparing the above-mentioned fermentation liquor, which involves adding EM liquor, bulking agent and leavening agent, stirring the mixture uniformly, and adjusting pH of the mixture to 4.6-4.8 using caustic soda.
NOVELTY - A biological organic-inorganic composite fertilizer comprises (in wt. %) multi-element composite microbe bactericide (5-10), humic acid (10-15), chicken manure (10-15), ammonium sulfate (10-15), grass peat soil (10-15), coal ash (3-6), nitrogen fertilizer (8-12), phosphate fertilizer (10-15), potassium fertilizer (10-15), clay (2-4), alleviant (1-2) and fossil powder (5-8).    USE - Biological organic-inorganic composite fertilizer.    ADVANTAGE - The composite fertilizer has different strains, and is convenient to use and inexpensive. The composite fertilizer is fermented within a short time, and reduces environmental pollution.
NOVELTY - A tirofiban hydrochloride is prepared by weighing tirofiban and placing in reaction vessel, and adding hydrochloric acid; heating at 75-100 degrees C while mixing, preserving the temperature and mixing for 30 minutes, adding 1% (w/w) active carbon, stirring and decoloring at 75-100 degrees C for 30 minutes, decompressing and filtering, cooling to 0-30 degrees C when mixing the filtering liquid. and maintaining the crystal for 24 hours; and separating the crystal, cleaning using purified water to obtain white solid, and drying.    USE - Method for preparing tirofiban hydrochloride.    ADVANTAGE - The method has simple salifying condition with low carbon emission, provides environmental protection, has high product purity and has no organic solvent residue. The obtained crystal has high purity and does not have the organic solvent residue.    DETAILED DESCRIPTION - Preparing tirofiban hydrochloride comprises:    (A) weighing tirofiban and placing in reaction vessel, and adding hydrochloric acid (10-30 times (v/w), 0.5-1.5 mol/L) of the weight of tirofiban;    (B) heating at 75-100 degrees C while mixing to completely dissolve the tirofiban, preserving the temperature and mixing for 30 minutes after dissolving, adding 1% (w/w) active carbon, stirring and decoloring at 75-100 degrees C for 30 minutes, decompressing and filtering, cooling to 0-30 degrees C when mixing the filtering liquid. and maintaining the crystal for 24 hours; and    (C) separating the crystal, cleaning using purified water to obtain white solid, and drying and maintaining the constant weight at 40-50 degrees C.
NOVELTY - An environment-friendly methanol diesel oil comprises (in wt.%) methanol (5-20), diesel oil (20-80), composite additives (5-20), and auxiliaries (10-40).    USE - Environment-friendly methanol diesel oil for vehicles.    ADVANTAGE - The oil reduces emission of pollutants while ensuring cetane number of the diesel oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an environment-friendly methanol diesel oil preparation method.
NOVELTY - A biogas desulfurizing agent regenerating method involves removing foam from a changed desulfurizing agent, putting a residual granular agent at a shadow and cool place, and naturally ventilating and drying the desulfurizing agent for 2-3 days. The dried desulfurizing agent is placed on a cement ground to change into brown and packed by a plastic bag.    USE - Method for regenerating a biogas desulfurizing agent.    ADVANTAGE - The method enables regenerating the biogas desulfurizing agent with high recycling rate of 80% in a simple manner.
NOVELTY - A kitchen rubbish utilizing method involves pre-processing, sorting, crushing, dehydrating and degreasing kitchen rubbish material. Waste water oil is separated, and material of a solid part is processed after dehydration treatment to the fermenter to recycle anaerobic fermentation biogas. Fermentation process is finished for solid-liquid separation and waste water filtering discharge. Waste residue is entered into next working process, and 10-15% of sludge slag and 10-30% of biomass material are provided in 60-70% of straw and dry pressed to obtain biomass fuel according to mass ratio.    USE - Method for utilizing kitchen rubbish to prepare biomass fuel.    ADVANTAGE - The method enables realizing the kitchen rubbish recycling, changing waste into biomass fuel, reducing the kitchen rubbish, and processing the sludge and waste such as straw in biomass waste. The obtained product has complete combustion and no secondary pollution, and realizes comprehensive treatment of rubbish.    DETAILED DESCRIPTION - A kitchen rubbish utilizing method involves pre-processing, sorting, crushing, dehydrating and degreasing kitchen rubbish material, and pre-processing solid-liquid separation process. Oil containing waste water oil is separated, and material of a solid part is processed after dehydration treatment to the fermenter to recycle anaerobic fermentation biogas. Fermentation process is finished for solid-liquid separation and waste water filtering discharge. Waste residue is entered into next working process, and 10-15% of sawdust sludge slag and 10-30% of biomass material are evenly provided in 60-70% of straw and dry pressed to obtain biomass fuel according to mass ratio.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for utilizing kitchen rubbish to prepare biomass fuel.'(Drawing includes non-English language text)'
NOVELTY - A granular insecticidal composition comprises (pts. wt.) chlorpyrifos (3-5), imidacloprid (2-3), adsorbent (1-20), stabilizer (0.1-2), synergist (0.1-2), dispersant (1-5), binder (1-10), coloring agent (0.1-1), and carrier (55-90).    USE - Granular composition used for controlling ground insects.    ADVANTAGE - The composition is environment friendly; has fertilizing effect, low toxicity, and long useful life; and improves soil properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composition by uniformly mixing chlorpyrifos, imidacloprid and adsorbent, and adding water to form wet micropowder; screening carrier to 20-40 mesh particles, premixing micropowder and carrier in coating and prilling machine, sequentially adding stabilizer, synergist, dispersant, binder and coloring agent, stirring, and uniformly mixing; and drying, weighing, and packaging.
NOVELTY - A cow dung ferment machine comprises closed fermentation tank body having a heat insulating layer on its inner wall and a perpendicular bisector fixed with a hollow rotating shaft having stirring blades; a blower on lower cavity of the tank body; a rotating shaft cavity fixed with a single ratchet wheel; a rail type lifting frame; a rail type lifting hopper; and a discharging port at the bottom of the fermentation tank.    USE - A cow dung ferment machine for producing high-quality organic fertilizer.    ADVANTAGE - The machine requires small floor area, has high automation degree and simple operation, and does not require water and auxiliary material for washing.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a cow dung ferment machine.
NOVELTY - Stevioside production craft comprises Stevia soaking and adding blocking agent.    USE - Method of stevioside production craft (claimed).    ADVANTAGE - The method prevents tannin in soaking extracting, reduces half of the processing of solute in tannin and acid, and has less pollution.
NOVELTY - Preparing bupropion hydrobromide crystalline form, comprises (i) heating pure bupropion hydrobromide crystalline form or crystalline form with chemical purity at 150-210 degrees C, maintaining for 0.5-10 hours, and cooling to room temperature to obtain bupropion hydrobromide crystal form.    USE - The method is useful for preparing bupropion hydrobromide crystalline form.    ADVANTAGE - The method is simple, environment-friendly and suitable for industrial production, and it produces bupropion hydrobromide crystalline form without impurities.
NOVELTY - A phytosterol is extracted from dragon fruit stem by crushing dry dragon fruit stem powder, screening using 200 mesh sieve, adding into an extracting kettle, raising temperature to 45-55 degrees C, feeding mixed fluid of entrainer and carbon dioxide at a flow rate of 15-20 l/hour, controlling pressure at 25-35 MPa, extracting for 3-5 hours, injecting the fluid in extraction kettle into a cyclone separator controlled at 25-40 degrees C and pressure of 4-10 MPa, separating the solid phytosterol from the fluid phase, and collecting the phytosterol at the bottom part of the cyclone separator.    USE - Method of extracting phytosterol from dragon fruit stem.    ADVANTAGE - The method is environmental friendly and safe, prepares product having high purity, and has improved extracting efficiency.    DETAILED DESCRIPTION - A phytosterol is extracted from dragon fruit stem by crushing dry dragon fruit stem powder, screening using 200 mesh sieve to obtain powder having moisture content of less than or equal to 5, adding into an extracting kettle, raising temperature to 45-55 degrees C, feeding mixed fluid of entrainer and carbon dioxide at a flow rate of 15-20 l/hour, controlling pressure at 25-35 MPa, extracting for 3-5 hours, injecting the fluid in extraction kettle into a cyclone separator controlled at 25-40 degrees C and pressure of 4-10 MPa, separating the solid phytosterol from the fluid phase, and collecting the phytosterol at the bottom part of the cyclone separator. The entrainer has a mass concentration of 5-20%; and is a mixed solution of water, ethanol and acetone having a volume ratio of 1:4-7:2-5.
NOVELTY - Catering swills are treated by performing first-step treatment using grid, breaking machine, fermentation regulating tank, and shaftless spiral sludge transmission machine; performing second-step treatment using oil-water separator; performing third-step treatment using anaerobic tower, and biogas-water separator; performing fourth-step treatment using anaerobic tower, aerobic tank, and sedimentation tank; and performing fifth-step treatment using anaerobic tower to obtain biogas slurry, and concentrating to obtain organic fertilizer.    USE - Method for industrial treatment of catering swills (claimed).    ADVANTAGE - The method uses simple device that is easy to install and use. It has low cost, is clean and environment-friendly, is free of discharge, and is capable of making use of resources.    DETAILED DESCRIPTION - Industrial treatment of catering swills comprises:    (A) performing first-step treatment using grid, mechanical grid, breaking machine, fermentation regulating tank, belt filter press, shaftless spiral sludge transmission machine, sludge cake, high-temperature disinfection dryer, and packaging machine;    (B) performing second-step treatment using water tank, oil tank, oil-water separator, and oil and biodiesel tank;    (C) performing third-step treatment using intermediate tank, anaerobic tower, biogas-water separator, gas receiver, igniting and heating system, and boiler;    (D) performing fourth-step treatment using anaerobic tower, aerobic tank, secondary sedimentation tank and clean water recovery tank; and    (E) performing fifth-step treatment using anaerobic tower to obtain biogas slurry, and concentrating to obtain organic fertilizer.
NOVELTY - A diesel oil comprises (in wt.%) bio-methanol (60-80), international standard diesel oil or basic oil (20-40), and assistant (5).    USE - Diesel oil for cars, steamers and locomotives.    ADVANTAGE - The oil utilizes high proportion of cheap and combustible liquid biomethanol with relatively great reserve, increases the replacement rate of petroleum component, saves energy resources and increases environmental friendliness, and has excellent power performance, corrosion-resistant property, wide application range, stable quality and simple production.
NOVELTY - An ethanol petroleum comprises (in wt %) ethanol (10-25), petroleum (67-85), additive (2-3) and methanol (3-5).    USE - Ethanol petroleum for use in a motor vehicle. Uses include but are not limited to car, passenger car, lorry, agricultural vehicle, motorcycle, loading vehicle and forklift.    ADVANTAGE - The ethanol petroleum is prepared in simple and environment-friendly manner with better performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing ethanol petroleum.
NOVELTY - Full rice nutrition fertilizer is prepared by crushing crab pool mud, cow dung, starch, white limestone powder, carbon dust, and crop straw to obtain a mixture; and adding azotobacter into the mixture to ferment.    USE - Full rice nutrition fertilizer.    ADVANTAGE - The fertilizer can provide air and nutriment for azotobacter to promote its propagation, and provide nitrogen, potassium, sodium, magnesium, and sulfur for rice to make the rice contain the trace elements such as potassium, sodium, magnesium, and sulfur. It increases the nutrition of rice by ecosystem approach.
NOVELTY - A micro-emulsification biodiesel comprises diesel, water, microemulsifier, solubilizer, assist agent and catalysis combustion-supporting agent at a weight ratio of 30-100:3-22:2-20:0.1-80:1-19:0.1-6.    USE - Micro-emulsification biodiesel.    ADVANTAGE - The biodiesel has high burning and utilizing efficiency, and small pollutant discharge amount. The biodiesel saves nonrenewable mineral quality, substitutes by biomass, saves energy and reduces discharge, and has low production cost.
NOVELTY - A biomass molded fuel is prepared by adding (in mass %) silicon sol (0.4-0.8) into slaked lime (0.5-1), and mixing the silicon sol and the slaked lime uniformly. The mixture is heated to form biomass that is shaped and densified to form biomass molded fuel.    USE - Biomass molded fuel for use as a sintering fuel (claimed) for sintering iron ore.    ADVANTAGE - The biomass molded fuel enables complete utilization of coke powder, thus reducing discharge of carbon oxides, sulfur oxides and nitrogen oxides during sintering of iron ore.
NOVELTY - A biological organic fertilizer is prepared using (in parts weight) nutritional soil (1000), Japanese ferment expanding bacteria (5-10), modified zeolite powder (4-8), chicken or duck (10-18), rice bran (16-22), and ore powder (8-12). The fertilizer is obtained by uniformly stirring the raw materials, fermenting, and turning everyday according to the temperature. The temperature on first and second day is 60-70 degrees C, the temperature on third and fourth day is 40-50 degrees C, and the temperature on fifth and sixth day is normal.    USE - Biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer efficiently improves agricultural yield, is environmentally-friendly and economical, and enables effective usage of domestic refuse.
NOVELTY - Preparing ginger culture material comprises taking (in wt.%) bean cake powder (35-55), sheep manure (25-45), pine needle powder (10-16), hawthorn powder (1.5-2), balsam pear powder (0.5-1), mulberry powder (0.1-0.3), liquorice powder (1.5-2), Chrysanthemum stem powder (0.5-1), Pinellia (0.1-0.3), towel gourd leaf powder (0.1-0.3), bulbus Fritillaria cirrhosa (0.1-0.3) and Sterculia lychnophora (0.5-0.8).    USE - The method is useful for preparing ginger culture material.    ADVANTAGE - The culture material: has large amount of beneficial microorganisms and particulate organic fertilizer components, which enables the growth and development of ginger; and produces ginger, which is tender, tasty, rich in nutrients and has large size, weight, rapid growth rate and is less vulnerable to diseases.
NOVELTY - Machine comprises a mechanical control unit and biochemical processor comprising high-efficient microorganism, where the biochemical processor provided with electromechanical control unit controls mechanical stirring and temperature control device. The high-efficient microorganism is Bacillus, preferably B.subtilis.    USE - The machine is useful for degrading sludge.    ADVANTAGE - The device reduces discharge of harmful substance.
NOVELTY - Industrial preparation of lamivudine (I) comprises reacting 5-1, 3-2 acid ((1'R, 2'S, 5'R) -5'-2'-(1-methyl ethyl) cyclohexyl) ester (II) with an acylating agent, generating glycosylation reaction with acyl silanization cytosine or with single silanization pyrimidine Schiff base, and then reducing, deformylating or hydrolyzing.    USE - Method for industrial preparation of lamivudine.    ADVANTAGE - The method is simple, has inexpensive raw material price, simple operation, safe and reliable production, high yield, less three wastes pollution, and is suitable for industrial production.    DETAILED DESCRIPTION - Industrial preparation of lamivudine (I) comprises (A) reacting 5-1, 3-2 acid ((1'R, 2'S, 5'R) -5'-2'-(1-methyl ethyl) cyclohexyl) ester (II) with an acylating agent to obtain acylate compound of formula (III); (B) generating glycosylation reaction with acyl silanization cytosine of formula (IVA) to obtain the compound (VA) or with single silanization pyrimidine Schiff base of formula (IVB) to obtain compound of formula (VB); and (C) then reducing, deformylating or hydrolyzing to obtain lamivudine (I).    R=alkyl, aryl or sulfonyl;    Y'=phenyl, methyl phenyl, methylphenyl, m-phenyl , o-hydroxyphenyl, or benzyl; and    X=formyl, acetyl, propionyl, isopropyl acyl, butyryl.
NOVELTY - A 5-hydroxyl tryptophan acid extracting method involves grinding griffonia seeds, mixing obtained powder with purified water (1-4 times) in a mass ratio of 1:6-10, and subjecting the obtained mixture to ultrasonic extraction for 1-4 hours. The obtained extract is passed through 60-mesh screen and then filtered through 0.1-5 m ultrafiltration membrane. The filtrate is concentrated, recrystallized and centrifuged, and obtained crystals are dried in a hot air at 65-70 degrees C for 5 hours to obtain a target product.    USE - Method for extracting 5-hydroxyl tryptophan acid from griffonia seeds.    ADVANTAGE - The method ensures purity of obtained product through high performance liquid chromatography (HPLC) detection to be greater than 99 percent and conversion rate to be more than 70 percent. The method enables avoiding usage of organic solvent, so that the product is free from organic solvent residue problem. The product is environmental-friendly.
NOVELTY - A 5-sulfosalicylic acid purifying method involves dissolving 5-sulfosalicylic acid in deionized water by stirring at 40-60 degrees C for 5-8 hours, and adding activated carbon to the obtained solution. The activated carbon is filtered and the filtrate is passed through 4A molecular sieve separation column provided with a heater at a rate of 10-20 ml/min. Temperature of the column is maintained at 70-95 degrees C, and the collected liquid is concentrated at 100 degrees C and re-crystallized to obtain pure 5-sulfosalicylic acid.    USE - Method for purifying 5-sulfosalicylic acid.    ADVANTAGE - The method ensures safe, simple and convenient purification process and enables saving energy. The active carbon and the separation column are activated to be reutilized, thus satisfying demand on green chemistry and environmental protection. The purified 5-sulfosalicylic acid has stable quality and industrialization production prospect.
NOVELTY - Fertilizer composition comprises anaerobically fermented Ulva pertusa and Brassica campestris    USE - Fertilizer composition for green tea cultivation.    ADVANTAGE - The composition has high quality green tea with improved savory taste, amino acid content and theanine content. The method enables manufacturing the composition in an environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing the fertilizer composition.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart illustrating a method for manufacturing fertilizer composition.'(Drawing includes non-English language text)'
NOVELTY - Fertilizer composition with Cassia twig herbal medicine, comprises (in wt.%) sheep manure (8-10), dried pig manure (15-23), duck manure (6-8), cottonseed meal (8-12), colza cake powder (4-6), wheat straw powder (1-3), corn straw powder (2-4), pumpkin stem leaf powder (2-4), peanut stem leaf powder (8-12), towel gourd stem and leaf powder (10-12), Sorghum leaf powder (6-8), cotton powder (3-5), garlic powder (1-3), pine needle powder (2-4) and tea seed powder (4-6).    USE - The composition is useful for treating diseases e.g. leaf blight, and preventing insects.    ADVANTAGE - The composition increases the yield of Cassia twig, growth rate of plant with a height of 20 cm, and width of 15 cm, and production of flowers, and fruits; produces leaves with thick surface having high molecular weight medicine; provides nutrients; and produces large well developed roots.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the composition, comprising (i) mixing the powder according to the proportion, then stirring the mixture in a stirrer for 180 minutes, taking out, and crushing the mixture in a crusher to a powdered form of 300 meshes, and again stirring the powdered mixture in the stirrer for 180 minutes, then taking out, and fermenting by completely pouring the mixture to a fermenting tank; (ii) adding excrement in the ratio 1:1.3, compacting, pressing for 168 hours, and tightly covering by a plastic cloth, then turning the mixture for the first time by correspondingly turning the lower layer from the upper layer, inner layer to outer layer, inner side to outer side, and then outer side to inner side; (iii) adding excrement according to the proportion of 1:1.3, stacking, compacting, pressing for 168 hours, then turning for the second time, piling, and fermenting for 168 hours, to obtain the qualified product.
NOVELTY - Membrane filtration and condensation of gibberellin comprises filtering gibberellin fermentation liquid by plate frame filter to obtain filtrate and washing liquid; filtering filtrate and washing liquid to obtain ultrafiltrate and ultra-condensation liquid; returning ultrafiltrate to plate frame for continuous filtering to obtain ultrafiltrate; carrying out primary condensation at 3-5 v/v on ultrafiltrate by roll nanofilter membrane; carrying out secondary condensation at 1.5-3 v/v by tube nano-filter membrane to obtain condensed liquid.    USE - Membrane filtration and condensation of gibberellin used as plant growth regulator.    ADVANTAGE - The method reduces water, electricity and gas consumption; improves condensation efficiency; and carries out operation at normal temperature. It improves content of heat sensitive main effective components of gibberellin.
NOVELTY - A biomass cavity type coal comprises (in wt. %) biomass (13-54), coal (10-20), inferior coal (20-35), dry sludge (10-20) and desulfurization agent (6-12).    USE - Biomass cavity type coal.
NOVELTY - An air fuel energy condensed machine has a feeding port, crushing machine, mixing machine, filter, discharge opening and a drying unit, where the drying unit is provided with an evaporator, condenser, throttle valve and a compressor of a heat pump machine, fan and an oven. The crushing machine crushes firewood raw material into powder, where the powder is mixed with mud using the mixing machine. The firewood raw material is pressed into a high density clod.    USE - Air fuel energy condensed machine for use in household applications. Can also be used for large scale applications.    ADVANTAGE - The machine avoids complicated wood filling, and ensures safe, sanitary and convenient transportation. The machine can be operated in an environment-friendly manner.
NOVELTY - A half-automatic fuel condensing machine has a drying unit provided with an evaporator, a condenser, a throttle valve and a compressor of a heat pump machine set, a fan and an oven. A wind power unit is provided with a blade and planetary transmission. Firewood is utilized as raw material that is crushed into powder. The crushed powder is taken in a mixing machine. The obtained slurry raw material is filtered and placed in the oven. The condenser is provided at an end of the evaporator. The raw material is dried and condensed using the condenser.    USE - Half-automatic fuel condensing machine for use in home and large scale manufacturing industries.    ADVANTAGE - The machine is convenient to transport and environment-friendly.    DETAILED DESCRIPTION - A half-automatic fuel condensing machine has a drying unit provided with a wind power unit that is combined with a heat pump machine set for preparing heat. A condensing fuel unit is provided with a feeding port, a crushing machine, a mixing machine, a filter and a discharge opening. The drying unit is provided with an evaporator, a condenser, a throttle valve and a compressor of the heat pump machine set, a fan and an oven. The wind power unit is provided with a blade and planetary transmission. Firewood is utilized as raw material and is taken from material inlet. The raw material is crushed into powder. The crushed powder is taken in the mixing machine. The obtained slurry raw material is filtered and placed in the baking oven. The condenser is provided at an end of the evaporator. The raw material is dried and condensed using the condenser.
NOVELTY - A solar fuel condensing machine is composed of a feeding port, crushing machine, mixing machine, filter, discharge opening and a drying unit, where the drying unit is composed of a heat collector, water storage tank, heat conducting tube and a fan. The crushing machine crushes firewood raw material into powder, where the powder is mixed with mud using a mixing machine. The firewood raw material is pressed into a high density clod. A heat collecting tube collects solar energy.    USE - Solar fuel condensing machine for use in household applications. Can also be used for large scale manufacture.    ADVANTAGE - The machine avoids complicated wood filling and ensures safe, sanitary and convenient transportation, and is operated in an environment-friendly manner.
NOVELTY - A biological fuel powder is prepared by crushing plant fruit, fruit shell, root, stem, leaf and grain shell into irregular particles with diameter of 0.01mm-1.2mm.    USE - Biological fuel powder.    ADVANTAGE - The biological fuel powder solves the problem of fuel demand and reduces discharge of harmful substance. The biological fuel powder has low manufacturing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing biological fuel powder.
NOVELTY - A high purity ginsenoside rhenium (Re) is prepared by crushing ginseng buds, adding methanol, ethanol or water as a solvent, performing ultrasonic extraction for 25 minutes, repeatedly extracting for 3 times, and removing filter dregs, where the filtrate is the coarse ginseng bud extract.    USE - Method for the preparation of high purity ginsenoside Re (claimed).    ADVANTAGE - The method is simple, environment-friendly, and energy-saving, and obtains ginsenoside Re with more than 98% purity .    DETAILED DESCRIPTION - Preparation of high purity ginsenoside Re comprises:    (A) crushing ginseng buds, adding methanol, ethanol or water as a solvent, performing ultrasonic extraction for 25 minutes, repeatedly extracting for 3 times, and removing filter dregs, where the filtrate is the coarse ginseng bud extract;    (B) putting the active carbons with a particle size of 1-35 mu m in 5% diluted hydrochloric acid, stirring for 1 hour at room temperature and then taking out, then adding deionized water and washing it, putting in an oven at 120 degrees C and drying;    (C) filling the processed active carbons in a glass column, where the column is filled with active carbons, and then making into the active carbon column;    (D) putting the coarse ginseng bud extract through the active carbon column at the flow rate of 3-9 BV/hour, where the collected eluent is the solution containing ginsenoside Re; and    (E) evaporating the eluent to dryness and then obtaining sample powder, and then dissolving with a mobile phase, and selecting 23 vol.% acetonitrile water solution on the preparative high performance liquid chromatography as the mobile phase, purifying the sample under the conditions of a feed amount of 20-200 mg and a flow rate of 8-20 ml/minute, collecting products, removing the solvent, and obtaining the ginsenoside Re.
NOVELTY - An indirect gasification method involves collecting wood composite biomass at a nearby source. Sawdust is manufactured by pulverizing the wood composite biomass by using a move mode grinding device. The wood composite biomass material is collected, and aquatic bio oil is manufactured and thermally decomposed in a move mode reactor. The aquatic bio oil is separated from tar, and pure combustibility synthetic gas is manufactured through gasification by reforming the separated aquatic bio oil.    USE - Indirect gasification method for producing combustibility synthetic gas from wood composite biomass.    ADVANTAGE - The method enables producing the pure combustibility synthetic gas without tar and dust, reducing trucking expenses, and facilitating carrying and storage of the bio oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an indirect gasification method. '(Drawing includes non-English language text)'
NOVELTY - Method for processing livestock waste, involves (a) preparing filter medium (500) and heating the medium at 1000 degrees C for 12-48 hours, and (b) filtering the heated medium to separate liquid component and residue containing livestock waste.    USE - The method is useful for processing livestock waste into fertilizer and livestock shed cleaning agent. The fertilizer is chosen from liquid fertilizer or ball fertilizer (all claimed).    ADVANTAGE - The method is inexpensive, simple and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition for cleaning livestock shed, which comprises the liquid component.
NOVELTY - A synergistic pesticidal composition contains dinotefuran and flubendiamide at weight ratio of 1:100-200. The total content of two active components in the composition is 1-90 wt.%.    USE - Pesticidal composition, i.e. emulsion, suspension, wettable powder, and water-dispersible granules, used for rice, vegetable and other crops (all claimed).    ADVANTAGE - The composition has synergistic effect and better effect compared to single pesticide, reduces dosage of active component, and is environment friendly.
NOVELTY - Estradiol and estradiol benzoate are prepared by adding estrone or estrone benzoate, sodium borohydride, or potassium borohydride reducing agent and quat. ammonium compound catalyst in a reactor at a molar ratio of 1:0.4-2:0.05-10 and taking water as a solvent; reacting for 10 hours at 0-100 degrees C while stirring to obtain a solid and liquid reaction product; and filtering the solid and liquid reaction product and recrystallizing the methanol at room temperature to obtain estradiol or estradiol benzoate.    USE - Method for preparation of estradiol and estradiol benzoate (claimed).    ADVANTAGE - The method does not need organic solvent as solvent, and is environment-friendly, high in yield, and easy for industrial production.
NOVELTY - Method for preparing colistin sulfate premix, involves (a) adjusting pH of fermentation solution containing colistin using acid, adding filter aid to the solution and filtering the solution, (b) concentrating the filtrate, (c) adjusting the pH of the concentrated solution using alkali and filtering the solution and obtaining filter cake, stirring the filter cake, adding sulfuric acid and adjusting pH of the solution and obtaining acidized solution, (d) adding the acidized solution in fluid bed pelleting machine equipped with carrier and pelleting the solution.    USE - The method is useful for preparing colistin sulfate premix.    ADVANTAGE - The method is rapid, environmentally-friendly as it consumes less amount of water and has high yield rate.    DETAILED DESCRIPTION - Method for preparing colistin sulfate premix, involves (a) adjusting pH of fermentation solution containing colistin to 2-3.5 using acid, adding filter aid (2-5 wt.%) to the solution and stirring and filtering the solution, (b) concentrating the filtrate at -0.095 to -0.098 mPa and 50-90 degrees C and obtaining solution with liquid phase content of 25000-35000 g/ml, (c) adjusting the pH of the concentrated solution to 10-12 using alkali and stirring the solution for 0.5-4 hours, leaving the solution undisturbed for 2-4 hours at 0-10 degrees C, filtering the solution in vacuum and obtaining filter cake, stirring the filter cake, adding diluted sulfuric acid and adjusting pH of the solution to 3-7 and obtaining acidized solution, (d) adding the acidized solution in fluid bed pelleting machine equipped with carrier, where the proportion of acidized fluid to the carrier is 60-80%, air inlet temperature is 140-200 degrees C and outlet temperature is 70-120 degrees C and pelleting the solution for 0.5-3 hours.
NOVELTY - A high-purity theaflavin is separated from black tea pigment solution by packing macroporous resin on posts; packing black tea pigment solution on posts as post packing amount with post volume of 50-150%, in which post packing flow speed is 2 bed volume/hour (BV/h); performing gradient elution using 20-60 vol.% alcohol, in which elution velocity is 1 BV/h, 2BV/h or 3 BV/h, and elution volume is 2-5 BV; collecting high purity theaflavin elution liquid; and drying by atomizing or drying by freezing, and obtaining high-purity theaflavin.    USE - Method for separating high-purity theaflavin from black tea pigment solution (claimed).    ADVANTAGE - The method has simple process, low energy consumption, and safe operation. It is suitable for realizing large scale process production.
NOVELTY - Production of biodiesel comprises impurity removing pre-treatment, pre-reacting, acid catalyzing and layering water-washing.    USE - Method for producing biodiesel by illegal cooking oil (claimed).    ADVANTAGE - The method produces high yield, and largely improves production efficiency.
NOVELTY - A hydrogen-manufacturing system comprises a solid fuel and a liquid fuel. The solid fuel is mixture of a sodium borohydride, an aluminum powder and an alkali. The liquid fuel is an aqueous solution of catalyst.    USE - System is used for manufacturing hydrogen (claimed) used for portable power supply for vehicles and military applications.    ADVANTAGE - The hydrogen is economically manufactured with high yield and high fuel conversion property, by the hydrogen-manufacturing system, using the simple method under controlled reaction conditions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen, which involves adding transition metal salt solution as hydrogen-manufacturing reaction control agent, to solid fuel to instantly control manufacture of hydrogen.
NOVELTY - Method of synthesizing lansoprazole, involves using 2-(3,4-dimethyl-pyridin-2-ylmethylsulfanyl)-1H-benzoimidazole as raw material, hydrogen peroxide as oxidant and compound metal oxide as catalyst, and preparing the lansoprazole through catalytic oxidation reaction.    USE - The method is useful for synthesizing lansoprazole.    ADVANTAGE - The method can be performed simply and cost-effectively, causes less pollution to the environment, produces high yield of highly pure lansoprazole, and is suitable for industrial production.    DETAILED DESCRIPTION - Method of synthesizing lansoprazole, involves using 2-(3,4-dimethyl-pyridin-2-ylmethylsulfanyl)-1H-benzoimidazole as raw material, hydrogen peroxide as oxidant and compound metal oxide as catalyst, and preparing the lansoprazole through catalytic oxidation reaction. The compound metal oxide catalyst is obtained by mixing metal oxide and auxiliary components, and roasting the mixture at 450-800 degrees C for 0.5-3 hours, where the mass ratio of the metal oxide to the auxiliary components is 1:1-10. The metal oxide is oxide of one metal or mixture of oxide of several metals in any ratio. The metal is chosen from sodium, potassium, beryllium, magnesium, calcium, barium, zinc, aluminum, silver, vanadium, tungsten, molybdenum, cobalt, lead, platinum, copper, nickel, zirconium, tantalum and palladium. The auxiliary components are chosen from one or more mixture of boride, silicide and molecular sieve.
NOVELTY - Producing hydrogen by reforming methanol vapor comprises mixing raw materials methanol and water at a mol ratio of 1: (0.8-2.0) in the fixed bed reactor under 410-460 degrees C and reaction air speed of 3000-23000 /hour, after gasifying at 410-460 degrees C, contacting with zinc oxide/gahnite (ZnO/ZnAl2O4) catalyst in the fixed bed reactor, generating the reforming gas enriching the hydrogen, separating to produce the pure hydrogen gas product.    USE - Method for producing hydrogen by reforming methanol vapor.    ADVANTAGE - The method has high reaction air speed, high reaction conversion rate, low carbon monoxide (CO) concentration, simple catalyst preparation, good stability and low cost; and is suitable for industrial production.
NOVELTY - Ammonia water recycling system comprises an ammonia water absorbing groove, a circulating pump, a heat exchanger and an ejector, which are orderly connected to form a circular loop structure. The heat exchanger uses a freezing medium free of chlorine ions.    USE - The ammonia water recycling system is useful for the production process of vitamin B1.    ADVANTAGE - The system eliminates the influence of chloride ions, and eliminates the potential safety hazard.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the ammonia water recycling system for the production process of vitamin B1.
NOVELTY - Rapid decomposition device comprises water inlet connected with water heater which is connected with water source; water outlet connected to activation nutrient solution generator through pipeline; nutrient fluid generator connected with rotten decomposing device having spraying device through pipeline pump; and rotten outlet device connected with rotary drying device by slurry pump. The drying device has discharging end connected with feeding port of material conveyer which is connected with cyclone separator, dust collecting pipe, and dust inlet of cyclone separator.    USE - Rapid decomposition device used for producing organic fertilizer from chicken manure.    ADVANTAGE - The rapid decomposition device has simple structure, convenient to operate, low labor intensity, short production period, high production efficiency, reduces environment pollution, and realizes rapid decomposition of chicken manure for producing organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of rapid decomposition device.
NOVELTY - The device has garbage dehydrating system that is connected with garbage feeding system (3). The oil is extracted from oil-water separation system (4). A dewatering system (1) is connected with discharging system (5). An oil-water separation system is connected with sewage tank (8) and power system (9). A controller is connected with control system (10). A feed inlet is provided in hopper of dewatering system. A material discharging system is formed with discharge hole. A material collecting device and packing device are connected with material discharging system.    USE - Device for classifying rubbish source in kitchen.    ADVANTAGE - The water resource can be utilized effectively. The processing ability of the classifying device can be improved. The failure rate of the classifying device can be reduced. High degree automation of the classifying device can be achieved. The operation and maintenance of the classifying device can be simplified. The classifying device can be utilized conveniently. The need for chemical additive can be eliminated. High dehydration rate of the garbage can be achieved. The production efficiency of the classifying device can be improved. The energy consumption of the classifying device can be reduced. The emission effect of the classifying device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the classifying device.    Dewatering system (1)    Garbage feeding system (3)    Oil-water separation system (4)    Discharging system (5)    Sewage tank (8)    Power system (9)    Control system (10)
NOVELTY - An eggplant culturing material is prepared by mixing rapeseed cake powder (32-45), rabbit manure (25-40), wheat straw powder (12-19), rice husk powder (3.6-6.7), wood ash powder (3.5-4), carrot leaf powder (0.5-1), soybean stem leaf powder (1.7-2), mulberry leaf powder (0.5-1), licorice powder (0.1-0.3), bone powder (0.1-0.3), fertilizer (0.1-0.3), and plantain seed powder (0.5-0.8).    USE - Method for preparing culturing material (claimed) used for promoting growth of eggplant.    ADVANTAGE - The method can obtain culturing material which contains ingredients for generating large amount of beneficial microorganism and which can satisfy growth requirement of eggplant. The culturing material can quicken growth of eggplant. The produced eggplant has big weight, is tender, delicious, and nutritious.
NOVELTY - A culturing material is prepared by mixing (wt.%) dairy manure (35-55), rabbit manure (25-45), soybean cake powder (10-16), rice husk powder (1.5-2), wood ash powder (0.5-1), peanut stem leaf powder (1.5-2), mushroom powder (0.5-1), pine needle powder (0.5-1), rice straw powder (0.1-0.3), fertilizer (0.1-0.3), garlic powder (0.1-0.3), and safflower powder (0.5-0.8).    USE - Method of preparing culturing material (claimed) used for promoting growth in orange.    ADVANTAGE - The method can obtain culturing material that can quicken growth rate of orange, and provide orange with rich nutrition. The produced orange is big and weighs heavy, and has delicious taste.
NOVELTY - The ammoniation granulating cylinder comprises cylinder housing, a feed opening, an inlet pipe and an acid inlet pipe. The acid mixing tube and the cylinder are arranged in parallel with respect to each other. The acid inlet pipe is set as a three-segmented structure, and the three different sections of the pipe are connected together. A water inlet pipe and a dilute acid distribution pipe are arranged in the wall of the diluting pipe, and several nozzles are arranged on the acid distribution pipe wall.    USE - Ammoniation granulating cylinder used in production of compound fertilizer.    ADVANTAGE - The compound fertilizer can be manufactured at low cost, and the operability and yield of the cylinder can be improved, while reducing the energy consumption and production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side perspective view of the ammoniation granulating cylinder.
NOVELTY - The device has storage tank (20) for storing fuel, and fuel reformer (40) which performs pure oxygen combustion process in order to reform the fuel supplied from the storage tank. A carbon dioxide capturing and storing module (60) separates the carbon dioxide from the hydrogen generated by the reformation reaction and stores the separated carbon dioxide. A fuel cell generation system (80) generates electricity using the hydrogen. The power system (100) electrolyzes water by using the surplus power of the fuel cell generation system and produces oxygen and hydrogen.    USE - Carbon dioxide collecting device for use in ship.    ADVANTAGE - Oxygen with high purity can be produced, and additional electricity can be generated. The deposition of the carbon dioxide is facilitated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for carbon dioxide collecting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the carbon dioxide collecting device. (Drawing includes non-English language text)    Storage tank (20)    Fuel reformer (40)    Carbon dioxide capturing and storing module (60)    Fuel cell generation system (80)    Power system (100)
NOVELTY - A methane-oxygen generator has anode, cathode, electrolyte layer provided between anode and cathode, and porous catalyst layer provided between cathode and electrolyte layer.    USE - Generator is used for manufacturing methane and oxygen (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of methane and oxygen.
NOVELTY - An esterification connection of mother nucleus and branch chain in synthesis of docetaxel comprises taking 1-hexylpyridinium hexafluorophosphate ionic liquid as esterification solvent; providing reaction substances (2asterisk,4S,5R)-N-tert-butylcarbonyl-2-(4'-methoxyl)phenyl-4-phenyl-1,3-oxycyclopentane-5-formic acid and 7,10-di(2, 2, 2-trichlorocarbethoxy)-10-deacetyl Baccatin III; using dicyclohexylcarbodiimide/4-dimethylaminopyridine as dewatering agent and catalyst; using ethyl acetate to extract product; and carrying out esterifying.    USE - Method for esterification connection of mother nucleus and branch chain in synthesis of docetaxel (claimed).    ADVANTAGE - The method has high efficiency, moderate condition, and simple operation. It has environment benefits. The ionic liquid reaction solvent is recycled.    DETAILED DESCRIPTION - Esterification connection of mother nucleus and branch chain in synthesis of docetaxel comprises:    (A) taking 1-hexylpyridinium hexafluorophosphate ionic liquid as esterification solvent;    (B) providing reaction substances (2asterisk,4S,5R)-N-tert-butylcarbonyl-2-(4'-methoxyl)phenyl-4-phenyl-1,3-oxycyclopentane-5-formic acid and 7,10-di(2, 2, 2-trichlorocarbethoxy)-10-deacetyl Baccatin III;    (C) using dicyclohexylcarbodiimide/4-Dimethylaminopyridine as dewatering agent and catalyst, where reaction condition is moderate and yield is high;    (D) using ethyl acetate to extract product, using 10% of sodium carbonate solution (3x 15 mL) and saturated edible salt water (3x 15 mL) to wash organic phase, and using anhydrous sodium sulfate to dry product;    (E) directly adding same-amount of reaction substance in original reaction system, repeatedly carrying out esterifying, repeatedly using reaction system for 5 times, and obtaining stable yield.
NOVELTY - The method involves supplying natural gas through evaporation of a single coolant, and circulating the gas in a heat exchange region with a precooling closed loop cooling cycle. The natural gas is precooled in another heat exchange region through the evaporation of another single coolant and circulated with liquefaction of another closed loop cooling cycle. The liquefied natural gas is expanded for circulating a third closed loop cooling cycle in a third heat exchange region through an indirect heat exchange region. A nitrogen refrigerant is compressed for precooling the nitrogen refrigerant.    USE - Method for liquefying natural gas.    ADVANTAGE - The method enables realizing simple operation and high reliability, maintaining a cascade framework, and increasing remaining capacity to a compressor.    DETAILED DESCRIPTION - The single coolants are selected from propane refrigerant and ethylene refrigerant.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram illustrating a natural gas liquefaction method.
NOVELTY - A solidity biomass fuel manufacturing method involves manufacturing solidity mixing biomass fuel and drying solidity mixing biomass fuel comprising soil, lime and silica. The soil, lime and silica are pulverized to size less than 0.1-20 mm. A foreign substance of a biomass material is selected and removed. Biomass water is mixed with the biomass material. The obtained product is compression-molded at room temperature or high temperature.    USE - Method for manufacturing solidity biomass fuel that is utilized in a boiler.    ADVANTAGE - The method enables mutually mixing the biomass material with soil, the lime and silica so as to enable manufacturing solidity biomass fuel in effective manner,, and preventing environment pollution.
NOVELTY - The reformer has fuel/air inlet (116) and fuel/air preheating path (118) through which the fuel is passed, and air is preheated at upper end of path. A burner (120) burns the fuel passing through air/fuel preheating barrel furnace. A combustion chamber (122) is positioned at burner lower side. A combustion gas outlet (124) through which the combustion gas is moved using combustion gas passage (126). The combustion chamber pipe (130) is placed at interval and combustion gas passage contacts with modified catalyst layer (108) and raw material/water preheating chamber (106).    USE - Vapor reformer for use in hydrogen production apparatus.    ADVANTAGE - The feed rate of water and raw material is reduced through the raw material/water preheat disappointment spiral channel formation and minority carrier storage effect installation, such that the water and raw material can be absorbed efficiently, and hence the efficiency of the vapor reformer can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the vapor reformer. (Drawing includes non-English language Text)    Raw material/water preheating chamber (106)    Modified catalyst layer (108)    Fuel/air inlet (116)    Fuel/air preheating path (118)    Burner (120)    Combustion chamber (122)    Combustion gas outlet (124)    Combustion gas passage (126)    Combustion chamber pipe (130)
NOVELTY - The sensor has a detection station provided with a carbon nanotube, and metal material bonded to form ligand in the carbon nanotube. An output unit converts resistance value into current or voltage according to gas density detected on the detection station. The gas density detected on the detection station is compared with fixed gas density. A controller determines whether warning signal is to be generated according to the comparison result, and an alert portion outputs the warning signal to the controller according to a control command.    USE - Sensor for detecting noxious gas e.g. carbon monoxide, nitrogen oxide, Propane gas, ethylene, methane, benzene or ammonia (all claimed), generated by a vehicle in restrictive of building and parking lot.    ADVANTAGE - The sensor has high sensing function and rapid response speed and regeneration speed in gas density of low concentration. The sensor utilizes the metal material, so that the sensor has excellent gas selectivity. The sensor utilizes the carbon nanotube, so that the sensor has excellent electron emission and chemical reactivity. The sensor has wide surface area and high voltage. The sensor arouses attention to a user located in the nearby or the user managing the sensor when the electrical resistance value increases over the definite value being generated the warning signal. The malfunction of the gas sensor is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a noxious gas detection method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a noxious gas detecting sensor. '(Drawing includes non-English language text)'
NOVELTY - A chlorpropham is produced by bubbling and degassing isopropyl chlorocarbonate at 5-40 degrees C; controlling geometric isomer of chloroaniline to 0.2%; adding chloroaniline to caustic soda liquid; adding processed isopropyl chlorocarbonate; processing the reaction solution with dilute acid; adjusting pH value to 6-8; adding deionized water to laminate the water, the lower layer oil being the chlorpropham crude product; and dehydrating the crude product and obtaining target product.    USE - Method for production of chlorpropham (claimed).    ADVANTAGE - The method improves product quality and reduces production energy consumption by pre-processing the raw materials and acidifying the compound solution.
NOVELTY - The apparatus has hydrocarbon reforming unit that is connected to drive unit and provided with reforming plate for reforming source gas with heat exchange. The drive unit is provided with connection pipe connected to the hydrocarbon reforming unit. A fuel tube is connected between fuel supply source and connection pipe. An ignition pipe with ignition catalyst is installed at side of connection pipe. A micro channel heater including ON/OFF valve is arranged between ignition pipe and connection pipe.    USE - Hydrocarbon reforming apparatus for use in hydrogen manufacturing system.    ADVANTAGE - The required heat supply can be facilitated by micro channel heater and the heating atmospheric reactor system can be simplified. The hydrocarbon reforming apparatus is compact. The combustion device is not exposed to superheat for long time and the oxidation activity of catalyst can be maintained. The loss of the oxidation catalyst is reduced and working efficiency of apparatus is improved. The practical utilization of hydrocarbon reforming apparatus is improved. The mass production of hydrogen is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrocarbon reforming apparatus.
NOVELTY - An 2-aminopyrrole triazine derivative (I) is new.    USE - 2-Aminopyrrole triazine derivative used for selectively killing tumor cells.    ADVANTAGE - The compound can promote ubiquitination degradation of Hsp90 so as to block up targets in the tumor multiplication growth signal path and stop growth of tumor. It has short production cycle, low cost and low side effects, and is environmentally-friendly.    DETAILED DESCRIPTION - An 2-aminopyrrole triazine derivative of formula (I) is new.    R1a, R1b =OH, 1-8C alkyl, 2-8C alkenyl, 2-8C alkynyl, 6-14C aryl, 2-9C heteroaryl, 2-9C isocycloalkyl, or 3-8C cycloalkyl;    R2, R3=Cl, F, 1-3C alkyl, or 1-3C alkyl substituted with F; and    R4=functional group selected from -(1-6C alkenyl)-OH, -O-(1-6C alkyl), -(1-6C alkenyl)-O-(1-6C alkyl), -(1-6C alkenyl)p-(1-6C alkenyl)p-(1-6C aryl), -(1-6C alkenyl)p-O-(1-6C alkenyl)p-(3-10C cycloalkyl), -(1-6C alkenyl)p-O-(1-6C alkenyl)p-(5-10C heterocyclyl), -(1-6C alkenyl)p-O-(1-6C alkenyl)p-(3-10C heterocyclyl), -(1-6C alkenyl)p-O-(2-6C alkenyl), -O-(2-6C alkenyl)-(3-10C heterocyclyl), -O-(2-6C alkyl)-(3-10C heterocyclyl), or 1-8C alkoxy.    N.B.: p is not defined.
NOVELTY - The method involves forming a catalyst layer made of transition metal material i.e. stainless steel, on a surface of a metal particle through a deposition process or sputtering process after etching the metal particle. The catalyst layer formed on the metal material is inserted into an electric furnace for radially synthesizing the catalyst layer at temperature of 600-900 degree Celsius by utilizing catalyst reaction. Hydrocarbon gas as electricity is made to flow inside the electric furnace. A carbon nanotube of sea urchin shape is formed on the catalyst layer of the metal particle surface.    USE - Method for manufacturing a sea urchin shaped carbon nanotube for a fuel cell separator (claimed).    ADVANTAGE - The method enables producing the carbon nanotube with high dispersibility without chemical reaction. The method enables improving electric conductance and mechanical strength of the carbon nanotube, so that dispersion of the carbon nanotube is possible even in dried state, manufacturing of a conductive film and a separator for a fuel cell is facilitated, and mass production of the carbon nanotube is possible.    DETAILED DESCRIPTION - The metal particle is a transition metal-free case. The hydrocarbon gas is selected from one of ethyne gas, methane gas, ethylene gas and ethane gas. The diameter of the spherical metal particle is 0.01-10 micrometer. The metal particle is made of one of nickel, iron, copper, aluminum, stainless steel, carbon steel and aluminum alloy. The length of the synthesized carbon nanotube is 0.1-200 micrometer. INDEPENDENT CLAIMS are also included for the following:    (1) a conductive additive-polymer composite    (2) a fuel cell separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation illustrating tensile strength of conductive additive-polymer composite.'(Drawing includes non-English language text)'
NOVELTY - A catalyst for producing hydrogen by methanol vapor modifying comprises amorphous zinc oxide (ZnO) and zinc aluminate (ZnAl2O4) of spinel structure. The ZnO is highly dispersed on the surface of the ZnAl2O4. Mass ratio of ZnO to ZnAl2O4 is (1-10):100.    USE - Catalyst for producing hydrogen by methanol vapor modifying (claimed).    ADVANTAGE - The methanol percent conversion is over 96%. The method has high hydrogen (H2) yield coefficient and low carbon monoxide (CO) selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of the catalyst comprising preparing soluble salt of zinc and aluminum into a mixed water solution raw material; conducting coprecipitation to ammonia water or soluble carbonate water solution and the mixed raw material; controlling the feeding speed of a certain amount of ammonia water or soluble carbonate water solution; controlling pH of the reaction system to 7-8; stirring until fully precipitated; aging, washing, oven drying and sintering at 400-600 degrees C; and then preparing the nano ZnAl2O4 spinel; and preparing the zinc nitrate into water solution with needed concentration; soaking to the ZnAl2O4 according to the loading amount needed by the catalyst, where the soaking process can be divided into one or more than one times; oven drying and sintering at 350-500 degrees C, and then obtaining the ZnO/ZnAl2O4 catalyst; and    (2) application of catalyst for producing hydrogen by methanol vapor modifying, where catalytic reaction temperature of the raw material with molar ratio of water to methanol at 1.2-1.8 is 410-460 degrees C; methanol gaseous-phase airspeed is 3000-23000 /hour; and the raw material contacts the catalyst in normal pressure condition to generate the modified gas rich in hydrogen.
NOVELTY - A power generation and cogeneration synthesis ammonia raw material gas is obtained by putting a pre-treated crude methane gas into low-temperature anti-sulfur converting device to convert carbon monoxide into hydrogen, obtaining high purity hydrogen via decompression absorbing device, compounding the high purity hydrogen and high purity nitrogen of air separation plant into ammonia raw material gas at a ratio of 3:1, and taking the tail gas as the refining fuel gas.    USE - Process for obtaining a power generation and cogeneration synthesis ammonia raw material gas (claimed).    ADVANTAGE - The process meets the needs of synthesis ammonia, and has low running cost, obvious environment protection effect, and high resource utilization rate.
NOVELTY - The apparatus (100) has a heat collecting system with a pump unit (110) that controls the flow rate of water. A mass flow meter unit (120-122) controls flow rates of nitrogen, hydrogen, and the sweep gas. A sand bath unit (130) heats water at a temperature of 200-500 degrees C to generate water of vapor state. An electrolysis stack (150A) discharges hydrogen, water, and nitrogen components as a result of electrolysis to a cathode, and discharges oxygen and sweep gas to an anode. A condenser unit (170) eliminates the water component, and discharges the rest component.    USE - Apparatus for producing high-temperature electrolysis hydrogen.    ADVANTAGE - Since the electrolysis stack discharges hydrogen, water, and nitrogen components as a result of electrolysis to cathode, the highly efficient hydrogen can be generated in electrolysis stack. The energy efficiency of the apparatus can be maximized by collecting the high-temperature heat of hydrogen, oxygen and sweep gas discharged from electrolysis stack. Thus, the cost of apparatus can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen production apparatus. (Drawing includes non-English language text)    Hydrogen production apparatus (100)    Pump unit (110)    Mass flow meter unit (120-122)    Sand bath unit (130)    Electrolysis stack (150A)    Condenser unit (170)
NOVELTY - The device has an air supplying pipe (101), and a fuel supplying pipe (103) including an ignition catalyst (105). An upper plate (100) is provided with a reformed gas exhaust pipe (102), and a lower plate (250) is provided with a waste gas discharging pipe (253). An air pre-heating unit has air preheating plates (110,130) to mix and combust air supplied from the air supplying pipe with fuel. A reformate reaction unit is provided with a reforming plate (190) and a reformation-preheating unit.    USE - Hydrogen reforming device used in hydrogen production system.    ADVANTAGE - The efficiency of the hydrogen reforming device can be improved effectively by using gas containing hydrogen as fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a disassembled perspective view of the hydrogen reforming device.    Air supplying pipe (101)    Reformed gas exhaust pipe (102)    Fuel supplying pipe (103)    Ignition catalyst (105)    Air preheating plates (110,130)    Reforming plate (190)    Lower plate (250)    Waste gas discharging pipe (253)
NOVELTY - Magnesium hydride is hydrolyzed using water in presence of magnesium chloride hexahydrate at 20-70 degrees C under high pressure, to obtain hydrogen. The hydrogen generation rate is 0.01-0.15 LPM/1 g of magnesium hydride.    USE - Production of hydrogen used as fuel for fuel cell used for vehicle (both claimed).    ADVANTAGE - The hydrogen is manufactured efficiently, easily and economically.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen generation storage system;    (2) fuel cell; and    (3) vehicle.
NOVELTY - The molten material in melting furnace (4) of heat insulator manufacturing device (8) is discharged through tap hole. The used coal components are put in material to form air bubbles. Cooling water is provided to control temperature and strength of insulator to manufacture insulator. The gases produced in chemical hydrogen production device (5) during pyrolysis, melting, and incineration are used as energy through heat recovery system and provided to hydrogen producing reactor so that high-purity hydrogen is produced in real time through metallic catalyzed oxidation.    USE - Complex system for producing hydrogen by waste pyrolysis melting incineration.    ADVANTAGE - The gases produced in chemical hydrogen production device during incineration are used as energy through heat recovery system and provided to reactor so that high-purity hydrogen is produced. Hence the re-synthesis of dioxins is prevented, and the molten materials are recycled into insulators.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the Complex system for hydrogen production.    Melting furnace (4)    Chemical hydrogen production device (5)    Fuel cell (6)    Heat insulator manufacturing device (8)    Solar collector (9)
NOVELTY - A composite thermal storage material comprises (vol.%) zeolite or aluminum oxide or calcined lime (30-90), and metal foam (10-70), where calcium chloride or magnesium chloride is filled in a hollow cavity of metal foam grain.    USE - Composite thermal storage material used for methane combustion and thermal energy collection (claimed).    ADVANTAGE - The composite thermal storage material collects and uses the heat energy from combustion of methane. It is highly safe, low in cost, simple in preparation and good in thermal storage ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the composite material, comprising:    (A) totally dissolving anhydrous calcium chloride or magnesium chloride to obtain calcium chloride or magnesium chloride saturated solution;    (B) copper foam or aluminum foam having grain diameter of 1-5 mm into the calcium chloride or magnesium chloride saturated solution, screening the mixed materials, and taking the copper foam or aluminum foam, heating it and evaporating moisture;    (C) mixing the evaporated copper or aluminum foam with zeolite or aluminum oxide or calcined lime to obtain blank of thermal storage material;    (D) putting the blank into a high temperature electric oven at 400 degrees C and baking for 2 hours continuously; and    (E) drying the processed material and naturally cooling to obtain the target product.
NOVELTY - A fuel producing method involves pulverizing palm tree berries into powder by using a pulverizing device, and drying the palm tree fruit powder to reduce moisture content to 5-10 percent. The dried palm tree fruit powder is made into pellet by using a pellet machine. The shaped pellet is treated with alcohol of 1-10 percent. A coating film of 0.05-0.2mm thickness is formed on a surface of the alcohol treated pellet. The coated pellet is dried to produce fuel.    USE - Method for producing fuel.    ADVANTAGE - The method enables increasing lighting power and firing effectiveness by coating the pellet with paraffin.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a fuel producing method.'(Drawing includes non-English language text)'
NOVELTY - Method of producing active phenol compound using microorganism, involves culturing bacterial strain to obtain activated bacteria, subjecting the strain to fermentation, adding inducer to fermented strain for biological transformation, filtering and concentrating the medium to obtain crude extract, subjecting extract to gradient alcohol-precipitation, extracting the precipitate using solvents, and subjecting extract to chromatography to obtain O,O-1,1'-di(2-hydroxy-3,4,5-trimethyl)phenyl oxo bridge and 4,5,6-trimethyl-1,2-pyrocatechol.    USE - The method is useful for inducing organism using rosin to produce active phenol compound having bacteriostatic effect, antiviral effect, anticancer effect, antiradiation effect and anti-sensitive effect and resistance to oxidation (claimed).    ADVANTAGE - The method has high selectivity, is performed under gentle reaction conditions and inexpensive and environmentally-friendly.    DETAILED DESCRIPTION - Method for producing active phenol compound by bioconversion of rosin into phenol compound using microorganism, involves culturing microorganism bacterial strain A5+ in potato dextrose agar (PDA) culture medium to obtain activated bacterial strain, transferring bacterial starin to potato dextrose broth (PDB) culture medium, subjecting the strain to fermentation for 48-72 hours, adding inducer to the fermented bacterial strain for biological transformation, filtering the fermented liquid, concentrating the filtrate to obtain crude extract, subjecting the extract to gradient alcohol-precipitation, extracting the precipitate using petroleum ether and ethyl acetate, and subjecting the extact to thin-layer chromatography, silica column chromatography, LH-20 gel chromatography and high-efficient liquid phase chromatography for separating and purifying O,O-1,1'-di(2-hydroxy-3,4,5-trimethyl)phenyl oxo bridge and 4,5,6-trimethyl-1,2-pyrocatechol.
NOVELTY - A high-purity silibinin is new. The content of high-purity silibinin is 97-101%.    USE - High-purity silibinin.    ADVANTAGE - The quality and yield of high-purity silibinin product are improved greatly. The method reduces impurity interference, separation purification difficult and environmental pollution. It is simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the high-purity silibinin.
NOVELTY - A rice straw charcoal coal is prepared by mixing rice straw and pulverized coal. The mixture is compressed to form a mold frame, where an oxygen hole (2) is formed in middle of the mold frame.    USE - Rice straw charcoal coal.    ADVANTAGE - The rice straw charcoal coal has antibacterial effect so as to remove bad smell and save taste and smell of meat.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a rice straw charcoal coal.'(Drawing includes non-English language text)'    Rice straw charcoal coal (1)    Oxygen hole (2)
NOVELTY - Separation of four steroid saponins (I), (II), (III), and (IV) from garlic comprises employing high-speed countercurrent chromatography with evaporative light scattering detector to respectively collect flow elements of garlic steroid saponins (I), (II), (III), and (IV) according to spectrum of evaporative light scattering detector; mixing fixed phase (upper phase) and fluid phase (lower phase) of high-speed countercurrent chromatography by n-butyl alcohol, glacial acetic acid, and aqueous ammonium acetate solution; and delaminating.    USE - Separation of four steroid saponins from garlic.    ADVANTAGE - The separation method does not use solid phase carrier. It has no irreversible absorption, no sample loss, and no pollution. It achieves efficient and fast preparation of garlic steroid saponin at low cost, thus obtaining garlic steroid saponin with purity higher than 90%.    DETAILED DESCRIPTION - Separation of four steroid saponins (I), (II), (III), and (IV) from garlic comprises employing high-speed countercurrent chromatography with evaporative light scattering detector to respectively collect flow elements of garlic steroid saponins (I), (II), (III), and (IV) according to spectrum of evaporative light scattering detector; mixing fixed phase (upper phase) and fluid phase (lower phase) of high-speed countercurrent chromatography by n-butyl alcohol, glacial acetic acid, and aqueous ammonium acetate solution; and delaminating.    Gal=beta-galactose;    Glc=beta-glucose;and    Xyl =beta-xyl.
NOVELTY - A mixed fuel comprises a mixture of organic compounds (A,B). The organic compound (A) has energy density higher than the organic compound (B). The organic compound (B) has oxidation reaction velocity higher than the organic compound (A). The organic compound (A) is 2-5C alkyl alcohol and the organic compound (B) is 1-3C carboxylic acid or carboxylate.    USE - Mixed fuel for a direct liquid fuel cell (claimed).    ADVANTAGE - The mixed fuel ensures stable and high power supply even in apparatus requiring a wide temperature range and high voltage difference, and is safe and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a direct liquid fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating the relative value of generation current with respect to the mixing ratio of ethanol and formate, at a low voltage of -0.7 V. (Drawing includes non-English language text).
NOVELTY - The apparatus has a molten carbonate fuel cell (102) which produces electricity by receiving hydrogen generated from a liquefied natural gas (LNG) tank (100). A water electrolysis circuit (108) receives surplus power of the molten carbonate fuel cell and produces hydrogen by electrolyzing water. A polymeric electrolyte membrane fuel cell (112) produces additional electricity by receiving hydrogen from water electrolysis circuit. A control unit (114) operates the polymer electrolyte fuel cell.    USE - Load follower apparatus for fuel cell generation system of ship.    ADVANTAGE - The service life of the load follower apparatus can be improved effectively. The additional electricity can be easily produced by supplying additional power to polymer electrolyte fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for load following method for fuel cell generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the load follower apparatus for the fuel cell generation system.    LNC Tank (100)    Molten carbonate fuel cell (102)    Water electrolysis circuit (108)    Polymeric electrolyte membrane fuel cell (112)    Control unit (114)
NOVELTY - The method involves supplying waste to processing chamber by material supplier (1) and stirring waste by agitator (201). The processing furnace is heated to 100-300 degrees C by burner (203) in heating chamber (202). The waste is supplied into heat-decomposing furnace (200) through a discharging hole (204) for heat-decomposing the waste at 100-300 degrees C. The waste is discharged to heat-decomposing furnace (300) by screw feeder (205) and is decomposed at 400-500 degrees C. The mixed gas from gasifier (400) is passed through reforming unit (404) of purifier (403) to obtain hydrogen.    USE - Continuous processing method for recycling waste into fuel.    ADVANTAGE - The productivity of fuel from waste can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the continuous processing method for recycling waste. (Drawing includes non-English language text)    Material supplier (1)    Heat-decomposing furnaces (200,300)    Agitator (201)    Heating chamber (202)    Burner (203)    Discharging hole (204)    Screw feeder (205)    Gasifier (400)    Purifier (403)    Reforming unit (404)
NOVELTY - Poly-generation comprehensive utilization device of biomass comprises a spiral feeder. The spiral feeder is connected with a microwave pyrolysis chamber. The microwave pyrolysis chamber is connected with a microwave reforming chamber through a gas pipe and a solid pipe. The upper end of the microwave reforming chamber is connected with a synthetic gas storage tank, and the lower end of the microwave reforming chamber thereof is connected with a semi-coke collecting chamber and a regeneration chamber.    USE - The poly-generation comprehensive utilization device of biomass is useful for chemical products e.g. ammonia, dimethyl ether and chemical fertilizer.    ADVANTAGE - The device can achieve the directional conversion from biomass to synthesis gas through microwave irradiation; utilizes gas semi-coke produced by pyrogenation as reforming catalyst for regeneration and reutilization; is integrated with microwave pyrolysis and reforming double technologies; can improve conversion rate of synthesis gas by 10%.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the poly-generation comprehensive utilization device of biomass.
NOVELTY - The method involves cooling a product to obtain an intermediate product (6). The intermediary product is made to contact with cooling medium i.e. water. The intermediary product is mixed with a binding agent by utilizing a binder, where the binding agent is fluid yeast, linguine, betadine, and corn weak water. A grinding process is performed as a separate grinding after indirectly cooling the intermediary product. A torrefied base product (4) is heated to a relatively high temperature of 280-350 degree Celsius. A helical screw is arranged on a central axis that rotates in a drum.    USE - Method for manufacturing end product e.g. pellets and brick, from torrefied base product i.e. wood.    ADVANTAGE - The method enables utilizing simple technique and consuming less energy, obtaining safe and reliable intermediary product, crushing of pre-product and compacting of the intermediary product in a simple manner. The method enables sufficiently cooling the product in a safe manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for a manufacturing end product from torrefied base product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram illustrating a method for manufacturing end product from torrefied base product.    Torrefied base product (4)    Pre-product (5)    Intermediate product (6)    End product (7)
NOVELTY - Farmland ginseng-planting soil conditioner comprises (in wt.%) chicken manure (30-50), soybean dregs (20-40) and sawdust (20-40).    USE - The soil conditioner is useful for improving farmland ginseng-planting soil.    ADVANTAGE - The soil conditioner solves the problems of: low organic matter content, low microorganism quantity, weak physical and chemical properties of farmland soil, severe ginseng disease, low yields and poor quality.
NOVELTY - A phosphate product is prepared by heating a liquid waste containing phosphorus to 80 plus minus 5 degrees C. Amine salt is added until pH is 4-7. Double decomposition reaction is performed to generate ammonium dihydrogen phosphate solution. The conversion rate of the waste phosphoric acid in the reaction is larger than 98%. A bleaching agent at 3-5% of total weight of the liquid waste is added in the reacted solution. The ammonium dihydrogen phosphate solution is filtered after bleaching. It is then cooled, crystallized, centrifuged, and dried to obtain the finished product.    USE - Method for preparation of a phosphate product (claimed).    ADVANTAGE - The method has simple technique, recycles the waste, and protects the environment.
NOVELTY - Method for preparing organic-inorganic compound fertilizer, involves using (in parts): monosodium glutamate waste (10), lees (15), plant straw (25), castor cake (5), livestock and poultry excrement (15), canal mud (10), plant ash (5), organic fertilizer leaven (10), water (100), organic deodorizer (suitable quantity), potassium sulfate (30), monoammonium phosphate (36), urea (30), and zinc sulfate (4).    USE - The method is useful for preparing granular organic-inorganic compound fertilizer (claimed) for providing nutrition to plant and promoting plant growth.    ADVANTAGE - The method is performed using simple techniques and is cost-effective. The fertilizer has long term efficiency, and comprises all the six macroelements necessary for plant growth e.g. nitrogen, phosphorus and potassium, and also content of organic nutrient substances e.g. humic acid and other organic matter is high, hence the fertilizer meets all the nutritional requirement of plants. The fertilizer has improved nitrogen fixation, phosphate solubilization and potassium release effects. The fertilizer also exhibits synergistic and quick acting effect for promoting balanced absorption of nutrients in crop, hence healthy growth of the crop root is ensured and nutrient absorption ability is also increased, thus robust plant growth with high disease resistance against stubbles-borne diseases. The fertilizer is also capable of reducing deficiency symptom in plants to a greater extent.
NOVELTY - Fertilizer comprises (in wt.%): dried sheep manure (5-7), dried dairy manure (2-4), dried chicken manure (16-20), bean cake powder (8-12), grass powder (10-12), cotton seed cake powder (4-6), cotton seed hull (6-8), corn straw (4-6), urea (10-14), potassium (4-8), potassium chloride (2-4), carbendazim (2-4), trichlorfon (3-5) and chlorinated rubber (6-8).    USE - As fertilizer for Kochia scoparia (claimed).    ADVANTAGE - The fertilizer is free from pollution and has high content of various nutrients and enables the plant to grow rapidly with thick leaves, dense flowers, large fruits, well-developed root parts and provides disease and pest resistance abilities to the plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves mixing the above-mentioned materials, placing the mixture in mixer and stirring for 90 minutes, removing the mixture from the mixer and crushing the mixture to obtain 80 mesh size particles, stirring the mixture in the mixer for 160 minutes, removing the mixture from the mixer and adding human excrement diluted in water to the materials in the ratio 1:1.5, uniformly stirring the mixture and stacking the mixture, compacting the stacked material by pressing with plastic cloth and fermenting for 26 hours, turning the mixture from top to bottom and inner layer to outer layer, adding human excrement diluted in water to the materials in the ratio of 1:1.5 and uniformly stirring the mixture to obtain stack, compacting the stacked material by pressing with plastic cloth, fermenting the materials for 50 hours and turning the mixture once again, stacking the material and fermenting for 70 hours.
NOVELTY - An animal manure carbon fertilizer is produced by (a) adding organic particles to the animal manure, (b) drying and pelleting, (c) carbonizing, (d) cooling with water, (e) sieving, and (f) mixing and pelleting.    USE - Method for producing animal manure carbon fertilizer which can be used as slow-releasing synergist of fertilizer compositions to fix the fertilizer and the moisture, prolong the effect of the fertilizer and improve the using rate of the fertilizer.    ADVANTAGE - The method is able to provide animal manure carbon fertilizer having multiple holes, high specific surface area, high light absorbing rate and thus, capable of improving the biological environment of the soil during use. The animal manure carbon fertilizer contains large amount of nitrogen, phosphorus and potassium. Further, it has enhanced absorbing performance and functions in slow-releasing manner thus, improving the using rate of the fertilizer.
NOVELTY - Wastewater in 2,4-dichlorophenol pesticide production is pre-processed by preparing emulsion, retrieving 2,4-dichlorophenol from the wastewater by a liquid-membrane separating process, and demulsifying.    USE - Method of pre-processing wastewater in 2,4-dichlorophenol pesticide production.    ADVANTAGE - The method reduces pollution; and has removal rate of 2,4-dichlorophenol of more than 99%, removal rate of chemical oxygen demand of more than 57%, and improved biodegradability.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart of a method of pre-processing wastewater in 2,4-dichlorophenol pesticide production. Drawing includes non-English language text.
NOVELTY - A holed coal briquette manufacturing method involves dehydrating sewage sludge and producing sludge carbide by charring the dried sewage sludge. Anthracite coal (70-90 wt.%) and charcoal are mixed with the sludge carbide to produce mixed fuel coal to manufacture holed coal briquette of fixed size.    USE - Method for manufacturing a holed coal briquette.    ADVANTAGE - The method enables preventing environmental contamination by producing generative fuel at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for manufacturing a holed coal briquette. '(Drawing includes non-English language text)'
NOVELTY - Preparation of tryptophan involves adding crude tryptophan to mixed solvent, heating, adding active carbon and adsorbing for 0.5 hour, filtering to remove active carbon, and film filtering; slowly crystallizing filtrate under stirring, further cooling by physical method, and filtering; and washing obtained white crystal, adjusting pH, filtering, drying to obtain pure product, and recycling mother liquor. The mixed solvent comprises purified water, low-grade fatty alcohol or low-grade fatty ketone, and low-grade fatty acid.    USE - Method for preparing tryptophan (claimed).    ADVANTAGE - The tryptophan has 95% light transmission rate. The mother liquor can be recycled after simple processing, and does not cause pollution.
NOVELTY - Preparation of an extreme pressure wear-resistant lubrication additive comprises synthesizing fatty acid diethanolamide by reacting biodiesel and iminodiethanol for 3-5 hours at 100-140 degrees C, and taking solid base as catalyst for performing decompression and distillation reactant methanol; and mixing the fatty acid diethanolamide with phosphorylation reagent, reacting for 1-6 hours at 60-100 degrees C, and standing for leveling after reaction.    USE - Method for the preparation of an extreme pressure wear-resistant lubrication additive (claimed).    ADVANTAGE - The method uses the biodiesel produced through agriculture and forestry waste oil with low price as the raw material, thus avoiding the use of plant oil for reaction from the effect of generating by-product glycerol. It uses solid base as the catalyst, thus improving transformation rate to more than 80%, and the solid base only needs sedimentation for separation. The method is simple, has mild condition, has short reaction time, and is environment friendly.
NOVELTY - A synthetic-gas inner-temperature and specific-heat-measuring system has a detecting unit and a calculating unit. The detecting unit comprises a gas flow meter (10), a hydrogen concentration measuring unit (30), a carbon monoxide concentration measuring unit (50), a methane concentration measuring unit (60), a temperature-fall gas flow meter and a temperature-fall gas thermometer. The gas flow meter is installed on outlet of a gasifying reactor (100) and measures the flow rate of gas after temperature fall. The gas thermometer measures the temperature of gas after temperature fall.    USE - System is used for measuring inner temperature and specific heat of synthetic gas of gasifying reactor.    ADVANTAGE - The system stably and accurately measures inner temperature and specific heat of synthetic gas of gasifying reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows the system for measuring inner temperature and specific heat of synthetic gas of gasifying reactor.    Gas flow meter (10)    Hydrogen concentration measuring unit (30)    Carbon monoxide concentration measuring unit (50)    Methane concentration measuring unit (60)    Gasifying reactor (100)
NOVELTY - The hydrogen water cooler and heater has electrolytic cell (40) that electrolyzes water to produce oxygen and hydrogen. The dissolver (60) is provided to produce hydrogen water by dissolving the hydrogen generated from the electrolytic cell. The hydrogen water from dissolver is received in cold water bucket (50). The cold water bucket is connected with a hot water sterilization caulk and a flash heater to discharge hot hydrogen water. The calcium removing filter is made of tourmaline, zeolite, ceramic alumina and magnetite.    USE - Hydrogen water cooler and heater.    ADVANTAGE - The hydrogen water can be effectively produced based on the predetermined concentration. The hydrogen water is sterilized in the form of cold water, warn water and ice water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen water cleaner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen water cooler and heater. (Drawing includes non-English language text)    Electrolytic cell (40)    Cold water bucket (50)    Dissolver (60)
NOVELTY - The system has reservoir (10) which stores raw material, and supplying unit (20) that supplies overheated vapor to raw material so that moisture containing raw material is obtained. A dry distillation furnace (30) is provided with dry distillation units (310,320) to decompose raw material by heating process. A hydrogen reformer (50) is provided with separate heating unit so that reformer contacts with heated steam and dry distillation gas is produced in furnace. A purifier (60) is provided to remove impurity contained in synthetic gas produced in reformer.    USE - System for gasifying carbonaceous raw material into synthetic gas.    ADVANTAGE - The hydrogen reformer is provided with separate heating unit so that reformer contacts with heated steam and dry distillation gas is produced in furnace. Hence the raw material can be continuously reformed into synthetic gas, and the structure of the system is simplified.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for gasifying carbonaceous raw material into synthetic gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for gasifying carbonaceous raw material into synthetic gas.(Drawing includes non-English language text).    Reservoir (10)    Supplying unit (20)    Dry distillation furnace (30)    Hydrogen reformer (50)    Purifier (60)    Dry distillation units (310,320)
NOVELTY - A separator composition comprises (in weight%) polymeric clay (25-75), calcium chloride powder (5-40), carbon nanotube powder (0.1-5) as conductive material, activated coal powder (1-25), and carrageenan (0.5-15) as gelatin stabilizer.    USE - Composition is used for separator for polymeric battery.    ADVANTAGE - The separator formed using the composition provides battery with excellent stability.
NOVELTY - The hydrogen generator has housing (10) in which water is filled, and the rolling portion (20) is installed inside the housing. The wires (41,42) are rolled around the rolling portion, while a gas outlet is formed in the housing. The wires are connected to the respective polarities of storage battery.    USE - Hydrogen generator for generating hydrogen used as fuel in engine of vehicle (both claimed).    ADVANTAGE - The device is simple in structure. The handling and installation of hydrogen generator are performed easily and efficiently. The hydrogen is generated easily in large amount.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of hydrogen generator.    Hydrogen generator (1000)
NOVELTY - Domestic sewage comprehensive utilization system comprises methane chamber connected with an ecological wetland inturn connected with an adjusting pool by ecological wetland pipeline or water passages. The adjusting tank is connected in series to an aerobic treatment pool, a disinfection tank of sodium hypochlorite and a clean water tank through pipeline. The clean water tank connected through a pipeline or by water passages to an irrigation pipeline. The sewage generated by household, catering enterprises or 'farm house' is externally connected with a discharging pipeline.    USE - The system is useful for generating sewage by using household, catering enterprises or 'farm house'.    ADVANTAGE - The system: has a high utilization rate of biogas (methane); is convenient to handle in rural areas; and reduces the impact of sewage in rural areas.
NOVELTY - Desulfurization tower comprises a tower body and a circulation device. The tower body is provided with a methanol inlet and a methanol outlet. The bottom part of inner cavity of tower body is provided with alkaline solution area. The alkali solution by a circulating device from the upper part of the alkaline solution inlet enters into the upper end and return to the alkali solution area. The top and bottom part of methanol inlet is provided with alkaline solution inlet and alkaline solution outlet, respectively. The methanol inlet and alkaline solution inlet is arranged on top of tower body.    USE - The desulfurization tower is useful for bio-diesel production.    ADVANTAGE - The tower can avoid the methanol tower and methanol pipeline corrosion; extends the service life of methanol tower and conveying pipeline; can prevent the leakage to solve potential safety hazards.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the desulfurization tower.
NOVELTY - A hydrogen hybrid power device comprises a current meter (1); a switch (2); a fuse (3); a cracking mechanism; a current controller (7) having output end connected with end of cracking mechanism; a power supply (4) having a cathode connected with the current input end of the controller; a cooler; a cooling liquid; filters having end connected with an engine or boiler gas inlet channel; hollow pipes; an electrolyte aqueous solution; and a lead wire. The power supply, the fuse and the switch are connected with one end of the switch.    USE - A hydrogen hybrid power device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a hydrogen hybrid power device.    Current meter (1)    Switch (2)    Fuse (3)    Power supply (4)    Current controller (7)
NOVELTY - A neutron absorption ball comprises inner core and shell layer coated on surface of the inner core.    USE - Neutron absorption ball used in nuclear reactor.    ADVANTAGE - The neutron absorption ball optimizes abrasion resistance, thermal impact resistance and mechanical property, reduces moisture rate, and has prolonged service life.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of neutron absorption ball comprising preparing shell layer by chemical vapor deposition.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the neutron absorption ball.
NOVELTY - A molecular sieve modifying method involves soaking sodium beta type molecular sieve in 3M sulfuric acid solution and saturated water solution of boric acid or aqueous solution of 3M acidic salt ammonium nitrate, and uniformly stirring the mixture. The mixture is allowed to stand for 1 hour, and filtered and dried at room temperature for 24 hours followed by drying at 100 degrees C. The dried mixture is ground and heated at 500 degrees C in air for 4 hours to obtain modified A/H-Na beta type molecular sieve, where A is anionic sulfate ion, anionic borate ion or cationic hydrogen ion.    USE - Method for modifying molecular sieve to increase methane and nitrogen gas separating factors.    ADVANTAGE - The method enables providing modified molecular sieve with better adsorptivity, selectivity and methane and nitrogen separating effect.
NOVELTY - Fertilizer comprises (in wt.%): dried human excrement (8-12), dried sheep manure (12-18), dried dairy manure (10-16), bean cake powder (8-10), corn core powder (6-8), wheat straw powder (4-6), grass ash (2-6), urea (12-18), tea powder (2-4), Polygonum powder (4-6), yellow sagebrush powder (4-8), ginkgo powder (1-3), rhizoma alismatis powder (1-3), Fritillaria cirrhosa powder (1-3) and safflower powder (1-3).    USE - As fertilizer for Aster plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves stirring the above-mentioned materials in mixer for 90 minutes, removing the mixture from the mixer and crushing the mixture in grain crusher to obtain powder, stacking the powder in fermenting tank, tightly covering the materials using plastic sheet and compacting the materials, hermetically fermenting the materials for 72 hours, turning the materials for first time, adding human excrement water (1:0.6) to the materials at the time of turning the stacked materials, uniformly spattering required amount of human excrement diluted water on the stacked materials, turning the stacked materials, compacting the materials, continuously fermenting the materials for 72 hours, maintaining the temperature at 80 degrees C, turning the stacked materials for each 72 hours, adding human excrement diluted water (1:0.6) to the materials at each time of turning the stacked materials and turning the stacked materials for 7 times.
NOVELTY - The equipment has a pressure sensor (B13-1) whose signal output end is connected with a pressure signal input end of a programmable logic controller (PLC) (B17). A control signal output end of the pressure sensor is connected with the PLC. A control signal output end of the PLC controls opening and closing of a gas-drive plunger booster pump (B6) through an electromagnetic valve (B5-0). Four pneumatic control valves (B8-1-B8-4) control an open and close gas circuit of four solenoid pilot actuated valves (B5-1-B5-4).    USE - Gas-drive pressure based hydrogen charging equipment.    ADVANTAGE - The equipment can perform full and real hydrogen storage, and fast charge and discharge test of high pressure hydrogen storage tank, and can ensure leakage prevention ability of the hydrogen storage tank when repeatedly bearing charging and discharging of hydrogen, so that charging and discharging of hydrogen is performed in quick, effective and reliable manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a gas-drive pressure based hydrogen charging method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas-drive pressure based hydrogen charging equipment.    Electromagnetic valve (B5-0)    Solenoid pilot actuated valves (B5-1-B5-4)    Gas-drive plunger booster pump (B6)    Pneumatic control valves (B8-1-B8-4)    Pressure sensor (B13-1)    PLC (B17)
NOVELTY - Supercritical carbon dioxide extraction of total flavones from hemsley rockvine, comprises crushing the hemsley rockvine to 60-80 meshes, adding into supercritical carbon dioxide extracting tank containing liquid carbon dioxide and cosolvent at a pressure 20-30MPa, temperature of 40-50 degrees C, extracting for 2-3 hours, splitter analyzing, recycling, and drying to obtain hemsley rockvine total flavonoids.    USE - The method is useful for supercritical carbon dioxide extraction of total flavones from hemsley rockvine.    ADVANTAGE - The method is simple, environmental-friendly and suitable for industrial production; and has high production efficiency.
NOVELTY - Heat pump working medium comprises (in wt.%) 1,1-difluoroethane (HFC-152a) (5-30), 1,1,1,2-tetrafluoroethane (HFC-134a) (0-60), ethyl fluoride (HFC-161) (10-70) and a hydrocarbon component (1-30), where the hydrocarbon component is isobutane (HC-600a), n-butane (HC-600) and/or propane (HC-290).    USE - The heat pump working medium is useful as a long-term substitute for hydrochlorofluorocarbon-22.    ADVANTAGE - The working medium: reduces amount of filling, improves energy efficiency ratio and saves resource and energy resource; has ozone depletion potential value of zero, low global warming potential value, high condensing temperature under same pressure, high heating capacity, and convenient and environment friendly performance.
NOVELTY - Preparation of 2-chloromethyl-3-methyl-4-trifluoroethoxy pyridine (IV) comprises under nitrogen protection, using methylene dichloride as reaction solvent; in the presence of triethylamine, reacting 2,3-dimethyl-4-trifluoroethoxy pyridine-N-oxide (I) with phosphorus oxychloride; and obtaining (IV).    USE - Preparation of compound (IV) (claimed) i.e. lansoprazole intermediate.    ADVANTAGE - The method shortens the three-step reaction of the traditional method into one-step reaction; reduces reaction time and industrial residue emission; saves the raw material; and is suitable for industrial production.
NOVELTY - Processing of sewage containing coal tar comprises preparing coal gas and Lan charcoal in coal carbonization gas making part (S1); in coal gas separation part (S2), separating gas to acquire separating ring coal gas, coal tar and sewage containing coal tar; in sewage evaporation system, evaporating sewage containing coal tar to acquire steam; and in sewage gas making part (S10), under condition that oxidant and carbon raw material exist, using steam as coal gasification agent to be converted into coal gas.    USE - Processing of sewage containing coal tar.    ADVANTAGE - The method is integrated with technique for producing Lan charcoal to form environmentally friendly type, large scale, industrial type and circular economy type coal conversion process route with low investment, high raw material use rate, and high product value.    DESCRIPTION OF DRAWING(S) - The drawing shows a process diagram for processing of sewage containing coal tar (Drawing includes non-English language text).    Coal carbonization gas making part (S1)    Coal gas separation part (S2)    Sewage gas making part (S10)    Sewage evaporation system (WG)
NOVELTY - A plant propagation medium comprises a manure having a moisture content of 10-35 wt.% with a salt level sufficient to achieve a conductivity of less than 0.35 dS/m.    USE - A plant propagation medium.    ADVANTAGE - The plant propagation medium is non-dusting, pathogen and odor free.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a pad comprising the plant propagation medium, and natural or synthetic fibers;    (2) a method of growing plants comprising providing the plant propagation medium; planting plants or plant seeds in the plant propagation medium; and growing the planted plants or plants from the planted plant seeds in the plant propagation medium; and    (3) a method of manufacturing a manure product comprising providing a slurry of manure; separating solids from the slurry of manure; and drying the separated solids at a temperature sufficient to kill pathogens and produce a manure product having a moisture content of 10-35 wt.% with a salt level to achieve a conductivity of less than 0.35 dS/m.
NOVELTY - A clove leaf extract comprises (wt.%) clove swertiamarin (19.91-30.39), clove flavone and phenolic acid (32.6-43.18), and impurities (27.01-47.49). The total weight of the clove swertiamarin and the clove flavone and general phenolic acid is 52.51-72.99 wt.%.    USE - Clove leaf extract.    ADVANTAGE - The extract has enriched active components of clove leaf and reduced content of impurities. The preparation of the extract utilizes macroporous adsorbent resin and ethyl alcohol solution for eluting, has low cost, is convenient to operate, and does not cause pollution to the environment, and obtains product that conforms to requirements for medical extracts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the clove leaf extract, comprising:    (A) grinding clove leaves, extracting with 50-95% alcohol, then filtering the extracted liquid and concentrating;    (B) adding distilled water into the concentrated liquid, standing, centrifuging, and taking the liquid supernatant for concentrating; and    (C) treating the concentrated liquid supernatant via a macroporous adsorbent resin column, eluting with 0-50% alcohol and 50-90% alcohol respectively, collecting 50-90% of alcohol eluted liquids, and concentrating to obtain the clove leaf extract.
NOVELTY - The apparatus has a molder molding light weight combustibility life waste selected from an air elutriator that is connected with a crusher to crush the combustibility life waste. A pulverizing device pulverizes the combustibility life waste passing through a magnetic separator that separates ferrous metal from the crushed combustibility life waste. A vibrating feeder separates a load from the combustibility life waste. The combustibility life waste is flowed into a rotary chamber. A metering feeder supplies the combustibility life waste to the chamber.    USE - Apparatus for manufacturing solid fuel from living waste.    ADVANTAGE - The apparatus has high combustibility, thus reducing manufacturing cost of the solid fuel. The apparatus is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of an apparatus for manufacturing solid fuel from living waste.    Rotating blade (14)    Cover (15)    Mesh net (17)    Inlet duct (23)    Exhaust duct (24)
NOVELTY - Comprehensive processing of black liquor comprises: collecting black liquor, carrying out flue gas desulfurization in a boiler, separating and depositing the grey water, carrying out physical-chemical treatment, anaerobic treatment and aerobic treatment and treating the sludge.    USE - The method is useful for comprehensive processing of black liquor.    ADVANTAGE - The method: treats waste by fully using carbon dioxide in the smoke in the boiler; generates methane, which can be reused; has less investment and low operation cost; and emits the waste water of black liquor according to the standard requirements.
NOVELTY - Organic waste processing device comprises an electromechanical control unit and a biochemical processor containing efficient microbes, i.e., functional bacteria. The biochemical processor is internally provided with a mechanical mixing arm and a temperature control device controlled by the electromechanical control unit. The efficient functional bacteria comprise Bacillus, preferably Bacillus subtilis.    USE - Used as an organic waste processing device.    ADVANTAGE - The device utilizes the efficient functional bacterial colony, which makes the organic waste processing effect achieve the national discharge standards, and reduces the discharging amount of harmful substances considerably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the organic waste processing device.
NOVELTY - Preparation of hydrogen from strong electrolyte aqueous solution comprises applying 0.5 V oriented in an electrolysis full circuit with a length of less than 10 cm and a cross section of more than 1000 square.    USE - Method for the preparation of hydrogen from strong electrolyte aqueous solution (claimed).    ADVANTAGE - The method produces hydrogen by electrolysis with low voltage and large current thus saving energy.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of a system used in the preparation of hydrogen.    Rectangular permanent magnet (4)    Container body (8)    Electrodes (11)    Gas chambers (14)    Channel (16)
NOVELTY - The method involves taking oily microalgae that are cultured and separated to obtain microalgae. Dilute microalgae are led in a reactor. Sufficient amount of hydrogen is continuously filled into the reactor. A catalyst with pressure of 20 to 80 bar Mega Pascals and temperature of 200 to 500 degrees centigrade is added in the reactor, where the catalyst is a load type nickel catalyst. A gas-liquid mixture is separated into liquid and gas phase products in a gas-liquid separating device. Biological diesel oil is separated via an oil-water separation device and stored in a storage tank.    USE - Method for directly producing biodiesel by utilizing microalgae.    ADVANTAGE - The method enables utilizing load type catalyst containing nickel to generate a product without any environment pollution and with low energy consumption, thus obtaining biological diesel with a cetane number of high combustion heat value, and hence increasing fuel demand.    DETAILED DESCRIPTION - The reactor is a kettle reactor, a fixed bed reactor, a fluidized bed reactor or a bubbling tower reactor.
NOVELTY - The device has bed reactor (1) that is connected with separating azeotrope of methanol and methyl and oil separator through pipeline. A piston flow reaction device (3) is provided with methanol and alkali inlet. A film evaporator is provided with glycerin and crude biological diesel oil outlet. A pervaporation membrane component (7) is connected to methanol receiving tank by methanol condensation system (11).    USE - Biodiesel production device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biodiesel production device.    Bed reactor (1)    Piston flow reaction device (3)    Pervaporation membrane component (7)    Methanol condensation system (11)
NOVELTY - The bioreactor has an ultrasonic transducer that is connected with an ultrasonic power supply and control device. The different frequencies of oscillators in transducer are combined to form a double or triple frequency ultrasonic transducer. A membrane assembly is processed on-line by the control of the power supply periodically. The combined frequency ultrasonic transducer (5) is located in the upflow area of the reactor and connected with combined frequency ultrasonic power supply and control device (4) that is located out of reactor filled with particles.    USE - Device for on-line control of membrane pollution of membrane bioreactor of fluidized bed for sewage treatment.    ADVANTAGE - The sound wave characteristics of the combined frequency ultrasonic transducer can be improved to eliminate the stationary field generated from the single frequency ultrasonic transducer. The uniform sound field of the transducer is ensured so as to improve the on-line cleaning effect of the ultrasonic transducer. The durability of the membrane assembly is ensured effectively. The overall structure of the device is simplified while ensuring convenient operation and easy automatic control.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for on-line control of membrane pollution of membrane bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the structure of device for on-line control of membrane pollution of membrane bioreactor. (Drawing includes non-English language text)    Fluidized bed (3)    Combined frequency ultrasonic power supply and control device (4)    Combined frequency ultrasonic transducer (5)    Aeration device (7)    Air pump (8)
NOVELTY - The device has an electrolysis tank in which hydrogen and oxygen is produced that is subjected to treatment of hydrogen water separation, oxygen water separation, cooled, washed and condensed. The treated hydrogen and oxygen are filled in gas adjustable balance unit which includes hollow cavity that is divided to hydrogen and oxygen gas cavities by film sheet. The hydrogen gas cavity is provided with hydrogen gas inlet and outlet. The oxygen gas cavity is provided with oxygen gas inlet and outlet. The inner wall of oxygen gas cavity is provided with bump.    USE - Device for producing hydrogen by water electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of the device for producing hydrogen by water electrolysis. (Drawing includes non-English language text)
NOVELTY - A 4-hydroxy pyrazolo (3,4-d) pyrimidine synthesis method involves adding 3-amino-4-pyrazole carbosamide hemisulfate and formamide under inert gas. The temperature is raised, and the white solid is separated. The reactant is cooled at 5-10 degrees C under inert gas, and the product is crystallized and separated out from formamide solution. Purified water is added to the crystal product in ratio of 1:8-15 and washed for 0.5-3 hours until pH of the eluate is more than 6. The crystal product is dried to obtain 4-hydroxy pyrazolo (3, 4-d)-pyrimidine.    USE - Method for synthesizing 4-hydroxy pyrazolo (3,4-d)-pyrimidine.    ADVANTAGE - The method enables saving energy, reducing requirement of a production device and reducing production cost. The method enables synthesizing the 4-hydroxy pyrazolo (3,4-d)-pyrimidine with high quality and high yield in an economic manner.    DETAILED DESCRIPTION - A 4-hydroxy pyrazolo (3,4-d) pyrimidine synthesis method involves adding 3-amino-4-pyrazole carbosamide hemisulfate and formamide in a molar ratio of 1:10-15 in a reaction kettle at constant temperature under inert gas. The temperature is raised, and the white solid is separated. The reactant is cooled at 5-10 degrees C under inert gas, and the product is crystallized and separated out from formamide solution. The liquid is recycled, filtered and transferred in a pulping kettle. Purified water is added to the crystal product in ratio of 1:8-15 and washed for 0.5-3 hours until pH of the eluate is more than 6. The crystal product is dried to obtain 4-hydroxy pyrazolo (3, 4-d)-pyrimidine.
NOVELTY - Preparing pure-silica zeolite molecular sieve film concentrated with ethanol fuel comprises: (i) grinding and flattening poly-porous silicon dioxide ceramic pipe carrier, cleaning and processing at high temperature; (ii) preparing a synthetic liquid from sodium hydroxide, tetrapropyl ammonium bromide and silica sol; (iii) fixing poly-porous silicon dioxide ceramic pipe carrier through a polytetrafluoroethylene support, adding synthetic liquid, aging, crystallizing, cooling, washing to neutral state; and (iv) activating the dry molecular sieve film to remove mold agent in sieve hole passages.    USE - The method is useful for preparing pure-silica zeolite molecular sieve film concentrated with ethanol fuel.    ADVANTAGE - The method improves the performance of synthetic silicalite-1 molecular sieve film and raw material utility ratio, and it is economical and suitable for industrial production with good repeatability.    DETAILED DESCRIPTION - Preparing pure-silica zeolite molecular sieve film concentrated with ethanol fuel comprises:    (i) grinding and flattening the poly-porous silicon dioxide ceramic pipe carrier, performing ultrasonic cleaning with distilled water, processing at a higher temperature for further use;    (ii) weighing sodium hydroxide, tetrapropyl ammonium bromide (TPABr) and silica sol, and preparing a synthetic liquid, where the molar ratio of TPABr, sodium oxide, silica and water in the liquid is 1:0.25:10:300-2000;    (iii) fixing the poly-porous silicon dioxide ceramic pipe carrier through a polytetrafluoroethylene support, adding the synthetic liquid, aging in an oven, crystallizing at 180 degrees C, taking out, naturally cooling to room temperature, washing to neutral state by using distilled water; and    (iv) activating the dry molecular sieve film at 400-600 degrees C to remove the mold agent in the molecular sieve hole passages.
NOVELTY - A polygenerated biomass is utilized by taking biomass raw material to microwave pyrolysis chamber for microwave heating cracking after naturally drying, crushing, and adding with inert gases; leading obtained pyrolysis gas into microwave reforming chamber, under function of microwave radiation and semi-coke, and further microwave heating reforming the pyrolysis gas into synthesis gas; and taking semi-coke after catalytic reforming to microwave reforming chamber for catalytic reaction after regenerating, or directly using as fuel or fertilizer.    USE - Method for utilizing polygenerated biomass used to obtain synthesis gas useful for synthesizing ammonia, dimethyl ether and chemical fertilizer.    ADVANTAGE - The method uses microwave irradiation to realize the direct transformation from biomass to synthesis gas. The semi-coke that is not suitable for recycling can be directly returned or mixed with fertilizer as composite fertilizer and then returned to field, increasing carbon content of soil, and improving soil fertility. Conversion ratio of the synthesis gas is increased by 10%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for utilization of polygenerated biomass.
NOVELTY - The device has a body whose bottom is provided with a hole. A fan is fixed in a first channel for the supplying gas. A second channel is provided on an upper part of the body. Another fan is fixed in the latter channel for exiting gas from a bioreactor. A bottom of the bioreactor is provided with a third channel for supplying air into a mixer. A carbon-container is attached with the mixer. A computer controlled fermentation unit is controlled through internet.    USE - Manure processing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a manure processing device.
NOVELTY - Production of organic-inorganic compound fertilizer involves decomposing phosphorite with nitric acid, adding humic acid, stirring, and filtering; crushing separated solid substance, reacting with ammonia, pelletizing, washing exhaust gas with decalcified acidolysis liquid, discharging, and adding washing solution to pelletizing machine after reaching certain concentration; and drying, sieving, cooling, and packaging.    USE - Method for producing organic-inorganic compound fertilizer (claimed).    ADVANTAGE - Discharge of waste residue to the environment is avoided, and the resource is comprehensively utilized.
NOVELTY - A glutamic acid is produced in biotin sub-right-amount fermentation by using corn-soaking water to replace corn steep liquor in the biotin proper fermentation to prepare fermentation culture medium to produce glutamic acid.    USE - Method for producing glutamic acid in biotin sub-right-amount fermentation (claimed).    ADVANTAGE - The method has convenient operation, saves water and energy, reduces fermentation cost of the glutamic acid, and is suitable for being promoted in the production. It saves primary water for material, saves energy consumed by vaporization and condensation of corn-soaking water, solves the problem of environment pollution and energy consumption caused by producing corn steep liquor by corn-soaking water, and improves the acid yield and saccharic acid conversion rate.
NOVELTY - Organic selenium enriched eggplant having total selenium content of 10-300 mu g/kg and organic selenium content greater than or equal to 80%, is claimed.    USE - The method is useful for producing organic selenium enriched eggplant.    ADVANTAGE - The method: produces eggplant which has rich and uniform selenium content; enhances the proportion of the organic selenium and solves the problem of the selenium content stability of the eggplant; and can produce eggplant in large-scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing organic selenium enriched eggplant, comprising culturing an organic selenium enriched eggplant seedling in a selenium enriched eggplant culture medium comprising nano selenium plant nutrient, field soil, mature livestock manure, horse manure or rice bran, pond mud and plant ash, where the mass ratio of the nano selenium plant nutrient to field soil, mature livestock manure, horse manure to rice bran (0.001-0.1):(2-8):(1-4):(1-4), transplanting to a field for soil cultivation and collecting the organic selenium enriched eggplant.
NOVELTY - Separation and extraction of cepharanthine comprises crushing dried and insoluble root; adding 2-3 liter water and 0.5-5 ml mixed biological enzyme per kilogram crushed substance; after 1 hour, adding 9-11 liter of 1-2% hydrochloric acid water solution; warming at 90 degrees C; carrying out soaking for 3 hours; separating liquid; adding 9-11 liter of 1-2% hydrochloric acid water solution to slag; extracting solution for 3 hours; filtering product; combining filter liquids; and absorbing through cation exchange column or cation cellulose column.    USE - Separation and extraction of cepharanthine.    ADVANTAGE - The method has simple operation, small pollution, low cost, provides cepharanthine at high yield and high purity.    DETAILED DESCRIPTION - Separation and extraction of cepharanthine comprises taking dried and insoluble root; crushing root; adding 2-3 liter water and 0.5-5 ml mixed biological enzyme per kilogram crushed substance; after 1 hour, adding 9-11 liter of 1-2% hydrochloric acid water solution; warming at 90 degrees C; carrying out soaking for 3 hours; separating liquid; adding 9-11 liter of 1-2% hydrochloric acid water solution to slag; extracting solution for 3 hours; filtering product; combining filter liquids; absorbing through cation exchange column or cation cellulose column; enriching cepharanthine; taking solution which is saturated by adding sodium hydroxide to 60-90% ethanol water solution as eluting liquid; carrying out elution; collecting eluting liquid in cepharanthine section; regulating pH to 7; condensing and recovering ethanol; filtering product; dissolving deposit using absolute ethyl alcohol; eluting and purifying using anion column; collecting eluting liquid in cepharanthine section; condensing; and crystallizing and drying cepharanthine.
NOVELTY - Recycling aspirin from aspirin-lysine mother liquor, comprises adding activated carbon into the aspirin-lysine mother liquor after recycling ethanol, decoloring, acidifying the decolored solution, heating, separating out the aspirin, and centrifugally filtering, washing and drying.    USE - The method is useful for recycling aspirin from aspirin-lysine mother liquor.    ADVANTAGE - The method reduces chemical oxygen demand in the wastewater, thus environment-friendly, it changes the wastes into valuables and it is economical.
NOVELTY - Separation of glyphosine solid from glyphosate mother liquor includes treating glyphosate production mother liquor by concentrating and removing salt; recycling concentrated mother liquor with high salt content; and adding acid into the concentrated mother liquor to regulate the pH and for further removing salt, filtering, neutralizing the filtrate with water, adding calcium chloride precipitating agent to separate out solid, fully reacting, filtering, regulating the pH of filter cake, ion exchanging, recycling calcium chloride, concentrating the acid solution, and filtering glyphosine.    USE - Separation of glyphosine solid from glyphosate mother liquor (claimed).    ADVANTAGE - The method recycles the waste; has reduced cost; and reduces pollution.    DETAILED DESCRIPTION - Separation of glyphosine solid from glyphosate mother liquor comprises taking glyphosate production mother liquor; treating by concentrating and removing salt; recycling the concentrated mother liquor with high salt content; and treating the concentrated mother liquor by adding acid into the concentrated mother liquor to regulate the pH and for further removing salt, filtering to obtain filtrate, adding water into the filtrate to neutralize, adding calcium chloride (CaCl2) precipitating agent to separate out solid, stirring for fully reacting, filtering to obtain filter cake of glyphosine calcium salt, regulating the pH of the filter cake containing glyphosine calcium salt by inorganic acid with a certain concentration for dissolving, adding acid dissolved solution into ion exchange resin, filtering, treating by ion exchange, regenerating the resin, recycling calcium chloride, concentrating the acid solution after being treated by CaCl2, and filtering glyphosine.
NOVELTY - Manufacture of manganese hydroxide, sodium sulfate, and ammonia comprises filtering a liquid waste from hydroquinone production; reacting the filtrate with sodium hydroxide solution at a mass ratio of 1:0.33-0.73 to obtain a mixture of manganese hydroxide, sodium sulfate, and ammonia; filtering the mixture; washing, drying, and crushing the filter cake to obtain manganese hydroxide; decompression filtering the clear filtrate, and condensing to obtain ammonia crystal; and distilling, cooling, and crystallizing the residual liquid to obtain sodium sulfate.    USE - Method for the manufacture of manganese hydroxide, sodium sulfate, and ammonium hydroxide (claimed).    ADVANTAGE - The method reduces the environment pollution of the liquid waste, and is simple.
NOVELTY - Biological organic fertilizer is obtained by fermenting (in parts weight) livestock excrement manure (6-8), rice hull (1-2), coal (0.5-1), rooting agent (0.5-1) and quick decomposition bacteria (0.002-0.003).    USE - The biological organic fertilizer is useful in agriculture for preventing diseases of crops.    ADVANTAGE - The fertilizer is environmentally-friendly as it does not cause pollution, improves amount of selenium and germanium, and prevents pollution caused by livestock waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biological organic fertilizer, which involves mixing evenly the above-mentioned components, stacking fermentation, turning once when temperature of the material reaches 55-60 degrees C, and turning once for every 1-2 days and in total for 2-3 times to obtain the fertilizer.
NOVELTY - A harmless treatment of garbage is performed by placing garbage into retort furnace; using completely separated air for external heating at 300-600 degrees C; drying garbage material, deodorizing, and sterilizing; performing pyrolysis and rapid condensing; and separating pyrolysis gas generated in the condensation step and non-condensable gas component.    USE - Method for harmless treatment of garbage (claimed).    ADVANTAGE - The method does not generate dioxin and secondary pollution.
NOVELTY - A courtyard seesaw-type organic garbage composting device comprises a primary fermentation chamber comprising material inlet on its upper part, two wind ventilating ports on its two sides, an opening and a pull plate on the bottom, and a liquid discharge hole arranged on the pull plate; a seesaw having an opening opposite opening of the primary fermentation chamber; and a secondary fermentation chamber comprising material outlet and wind ventilating port on one lateral side of its bottom.    USE - A courtyard seesaw-type organic garbage (preferably household domestic garbage) composting device (claimed).    ADVANTAGE - The device has fast composting efficiency.    DETAILED DESCRIPTION - A courtyard seesaw-type organic garbage composting device comprises:    (1) a primary fermentation chamber comprising material inlet on its upper part, two wind ventilating ports on its two sides, and an opening and a pull plate on the bottom, and a liquid discharge hole arranged on the pull plate;    (2) a seesaw having an opening opposite opening of the primary fermentation chamber; and    (3) a secondary fermentation chamber comprising material outlet and wind ventilating port on one lateral side of its bottom.    The secondary fermentation chamber is a barrel-shaped body with arc bottom and is fixed on the lower middle part of the seesaw. The primary fermentation chamber is fixed on the upper middle part of the seesaw and is interconnected with the second fermentation chamber through the opening of the seesaw. An INDEPENDENT CLAIM is included for a composting processing method.
NOVELTY - Brown botryococcus cell is used to extract bio-oil by culturing Brown botryococcus, and collecting to obtain wet algae body; putting algae body into stirring reactor, adding organic solvent, e.g. hexane, heptane, octane or n-dodecane, and auxiliary extracting agent, e.g. glycol dimethyl ether, dimethoxy propane, diethoxy methane or aldehyde for extracting solvent to bio-oil at room temperature and extracting, separating algae cell and collecting bio-oil with extraction solvent, where ratio of organic solvent and auxiliary extraction agent is 100:0.5-2.    USE - Brown botryococcus cell used to extract bio-oil.    ADVANTAGE - The method avoids the step of drying the traditional microalgae oil extracting, saves microalgae oil extracting cost and energy consumption. It also shortens Brown botryococcus culture time, reduces cultivation cost, improves the intensity of producing biodiesel with waste grease Brown botryococcus.    DETAILED DESCRIPTION - Use of Brown botryococcus cell to extract bio-oil comprises:    (A) culturing the Brown botryococcus, and collecting to obtain wet algae body;    (B) putting the wet algae body into stirring reactor, adding organic solvent, e.g. hexane, heptane, octane or n-dodecane, and auxiliary extracting agent, e.g. glycol dimethyl ether, dimethoxy propane, diethoxy methane or aldehyde for extracting solvent to bio-oil at room temperature and extracting, separating algae cell and collecting the bio-oil with extraction solvent, where ratio of organic solvent and auxiliary extraction agent is 100:0.5-2; and    (C) collecting bio-oil with extraction solvent by vacuum rotary evaporation, recycling extracting solvent to reuse, and collecting the obtained biomass oil.
NOVELTY - Preparation of biodiesel comprises separating raw material oil through hydrolysis to prepare fractions rich in saturated fatty acid and unsaturated fatty acid, esterifying on fraction rich in saturated fatty acid and short-chain alkanol, esterifying on fraction rich in unsaturated fatty acid and methanol, and mixing two fatty acid esters obtained through reaction.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method is simple, and has high in utilization ratio.
NOVELTY - Preparation of valnemulin hydrochloride comprises reacting pleuromutilin with p-toluenesulfonyl chloride; substituting by 1-amino-2-methyl-2-mercaptan hydrochloride; obtaining ((2-amino-1,1-dimethylethyl)sulfenyl)acetic acid(3aS,4R,5S,6S,8R,9R,9aR,10R)-6-vinyldecahydro-5-hydroxy-4,6,9,10-tetramethyl-1-oxo-3a,9-propanol-3aH-cyclopentadiene-cyclooctene-8-ester (I); reacting D-valine with methyl acetoacetate; reacting with isobutyl chloroacetate into anhydride; reacting with compound (I); protecting with hydrochloric acid; and obtaining valnemulin hydrochloride.    USE - Preparation of valnemulin hydrochloride (claimed).    ADVANTAGE - The method has mild reaction condition, simple post-treatment, high product content, and high yield; is easy to be implemented for large-scale production; provides product directly; uses less solvent; and reduces environmental pollution.
NOVELTY - A prasugrel preparing method involves performing Grignard reaction on 2-bromo-4,5,6,7-tetrahydro-thieno (3,2-c)pyridine (1) in tert-butyl peroxy benzoate to obtain 2-tert-butoxy-4,5,6,7-tetrahydro-thieno(3,2-c)pyridine (2). The resultant is heated and decomposed to obtain 5,6,7,7a-tetrahydro-4H-thieno(3,2-c)pyridin-2-one (3). The obtained product is acetylized with acetylizing reagent to obtain 2,4,5,6,7,7a-hexahydro-thieno(3,2-c)pyridin-2-yl acetic acid ester (4). The obtained product is condensed with 2-bromo-1-cyclopropyl-2-(2-fluoro-phenyl)-ethanone (5) to obtain prasugrel (6).    USE - Method for preparing prasugrel that is utilized as a platelet retardant.    ADVANTAGE - The method enables preparing eco-friendly prasugrel in a simple manner. The method enables utilizing low expensive materials that is easy to obtain. The method enables sterilizing reagents, ensuring labor protection and reducing generation of material wastes during production. The method enables increasing product yield, and preparing the prasugrel in mass production.    DETAILED DESCRIPTION - A prasugrel preparing method involves performing Grignard reaction on 2-bromo-4,5,6,7-tetrahydro-thieno (3,2-c)pyridine with specified structure in presence of magnesium powder and tert-butyl peroxy benzoate to obtain 2-tert-butoxy-4,5,6,7-tetrahydro-thieno(3,2-c)pyridine with specified structure. The resultant is heated and decomposed to obtain 5,6,7,7a-tetrahydro-4H-thieno(3,2-c)pyridin-2-one with specified structure. The obtained product is acetylized with acetylizing reagent to obtain 2,4,5,6,7,7a-hexahydro-thieno(3,2-c)pyridin-2-yl acetic acid ester with specified structure. The obtained product is condensed with 2-bromo-1-cyclopropyl-2-(2-fluoro-phenyl)-ethanone with specified structure to obtain prasugrel with specified structure.
NOVELTY - Organic matter-decomposing inoculant comprises (in parts weight): Aspergillus niger (10-20), Lactobacillus (10-20), Saccharomyces cerevisiae (20-30) and Bacillus subtilis (40-60).    USE - The inoculants is useful for decomposing organic matter, producing organic fertilizer, bio-organic fertilizer, organic and inorganic compound fertilizer or bio-organic and inorganic fertilizer, fermenting livestock manure, and treating industrial organic waste residue, sludge, organic waste, agricultural products, or waste material (all claimed). Can also be used in stimulating growth of plant, preventing disease causing insect and pests and improving disease resistance, drought resistance and cold-proof resistance in plant.    ADVANTAGE - The inoculant has synergistic property, rapidly decomposes organic material and effectively kills germs, ovum and weed seed in organic material, deodorizes organic material, and increases soil nutrient, and fertilizer utilization rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method of preparing the inoculant, involves (1) obtaining the above-cited components, and (2) mixing the obtained components uniformly, and drying, crushing and sieving the obtained mixture to obtain product;    (2) use of inoculant in fermenting livestock manure, by adding 2-4 wt.% of inoculant into the livestock excrement;    (3) use of inoculant in straw field, by applying 3-5 kg of inoculant and 6-10 kg of urea for each mu of straw field; and    (4) use of inoculant in industrial organic waste residue, sludge, organic waste, agricultural products, or waste material, by applying 3-6 wt.% of inoculant into the industrial organic waste residue, sludge, organic waste, agricultural products, or waste material and fermenting obtained product.
NOVELTY - Fertilizer comprises (in wt.%): dry chicken manure (4-6), dry sheep manure (4-6), dry dairy manure (14-18), dry rabbit manure (6-8), soybean cake (8-10), corn powder (4-6), pumpkin powder (2-4), lobster powder (1-3), chlorine fertilizer (12-14), compound fertilizer (8-10), urea (10-12), pesticide (3-5), trichlorfon agent (2-4), propargite (2-4) and polyurethane resin (4-6).    USE - The fertilizer is useful for promoting growth, and controlling diseases and insect pests in elecampane.    ADVANTAGE - The fertilizer is highly nutritious, increases yield of elecampane rapidly, causes no pollution, and ensure thick leaves, dense flowers, large fruits and roots. The method is cost-effective and simple.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves adding the raw materials into a stirrer, stirring the mixture for 90 minutes, crushing the mixture into particles of 60 meshes by crusher, stirring the stirred mixture for 150 minutes, fermenting the mixture, adding excrement water to the mixture in the ratio of 1:1.5, stacking the mixture uniformly, covering the stacks using a plastic cloth cover and fermenting for 22 hours, processing the mixture, turning the mixture from upper layer to lower layer and inner layer to outer layer, inside to outside and outside to inside, adding excrement water to the mixture in the ratio of 1:1.5, stacking the mixture, covering the stacks, fermenting the stacks for 45 hours, processing the stacks for second time, further stacking and fermenting the mixture for 70 hours, and adding the fermented product into a mould of 30 cm height, 25 cm width and 40 cm length.
NOVELTY - Preparation of high-purity levofloxacin hemihydrate comprises adding levofloxacin carboxylic acid and N-methyl piperazine to water; reacting without using basic catalyst; decompressing and evaporating reaction liquid; dissolving crude levofloxacin product in water; adding alkali to adjust pH of aqueous solution into alkaline; extracting aqueous solution; drying to obtain solid; adding polar solvent and water solution into solid to obtain polar solution; and cooling and crystallizing polar solution in gradient form to obtain levofloxacin hemihydrate.    USE - Preparation of high-purity levofloxacin hemihydrate.    ADVANTAGE - The method produces little toxicity, little environment pollution, and simple post treatment. It prepares levofloxacin hemihydrate high purity and low production cost.    DETAILED DESCRIPTION - Preparation of high-purity levofloxacin hemihydrate comprises adding levofloxacin carboxylic acid and N-methyl piperazine to water; reacting without using basic catalyst; decompressing and evaporating reaction liquid to obtain crude levofloxacin product; dissolving crude levofloxacin product to water to obtain aqueous solution; adding alkali to adjust pH of aqueous solution into alkaline; extracting aqueous solution using organic solvent; drying to evaporate to obtain solid; adding polar solvent and water solution into solid to obtain polar solution; and cooling and crystallizing polar solution in gradient form to obtain levofloxacin hemihydrate.
NOVELTY - Preparation of carbon oxidation catalyst comprises using activated carbon to prepare carbon oxidation catalyst via modifying and thermotechnical process.    USE - Method for preparing carbon oxidation catalyst used for glyphosate (claimed).    ADVANTAGE - The method has short reaction time, low average consumption, high probability of embedding active group on surface of activated carbon, improves conversion rate of the glyphosine, and increases yield of glyphosine.
NOVELTY - Preparation of tizanidine hydrochloride comprises reducing 4-chloro-2-nitro-aniline via catalytic hydrogenation; cyclizing 4-chloro-1,2-phenylenediamine with thionyl chloride and dimethylformamide; nitrifying 4-chloro-1,2-phenyldiazosulfide with nitric acid or sulfuric acid, reducing 4-chloro-3-nitro-1,2-phenyldiazosulfide via catalytic hydrogenation to obtain 4-chloro-2-amino-1,2-phenyldiazosulfide; condensing and salifying with toluene or thionyl chloride to obtain tizanidine; and further reacting hydrogen chloride and ethanol to obtain tizanidine hydrochloride.    USE - Preparation of tizanidine hydrochloride used as medical medicine.    ADVANTAGE - The method has simple post treatment process, easy operation, reduces environment pollution and corrosion of equipment, and has reduced production cost.
NOVELTY - Preparing highly pure glycerol comprises: (i) diluting industrial glycerol raw material with water to obtain a glycerol solution (10-50 wt.%), adding 0.5-1.5 mol/l hydrochloric acid (5-10 vol.% of glycerol solution); (ii) absorbing and exchanging solution by ion exchange resin column; (iii) heating to 60-95 degrees C, adding activated carbon (0.5-1.5 wt.% of glycerol solution), agitating and decoloring to remove activated carbon; (iv) filtering filtrate by a microporous film (0.2-0.3 mu m); and (v) vacuum concentrating filtrate at 110-115 degrees C, until relative density of liquor at 25 degrees C is not less than 1.257 g/ml.    USE - The highly pure glycerol is used as a medicinal injection.    ADVANTAGE - The method: produces glycerol with high purity; is simple and easy; consumes less energy (energy consumption is 1/5 of the multi-stage evaporation process); has clean and sanitary production environment; is economical, as it reduces the investment of the apparatus field; has high efficiency; and is environment-friendly.
NOVELTY - Manufacture of manganese hydroxide, lithium sulfate and ammonium hydroxide comprises filtering a liquid waste from hydroquinone production; reacting the filtrate with lithium hydroxide solution at a mass ratio of 1:0.12-0.52 to obtain a mixture of manganese hydroxide, lithium sulfate, and ammonia; filtering the mixture; washing, drying, and crushing the filter cake to obtain manganese hydroxide; decompression filtering the clear filtrate, and condensing to obtain ammonia; and distilling, cooling, and crystallizing the residual liquid to obtain lithium sulfate crystal.    USE - Method for the manufacture of manganese hydroxide, lithium sulfate, and ammonum hydroxide (claimed).    ADVANTAGE - The method reduces environment pollution of the liquid waste, and is simple.
NOVELTY - Manufacture of manganese hydroxide, magnesium sulfate, and ammonium hydroxide comprises filtering a liquid waste from hydroquinone; reacting the filtrate with magnesium hydroxide solution at a mass ratio of 1: 0.18-0.58 to obtain a mixture of manganese hydroxide, magnesium sulfate, and ammonium hydroxide; filtering the mixture; washing, drying, and crushing the filter cake to obtain manganese hydroxide; decompression filtering the clear filtrate, and condensing to obtain ammonium hydroxide; and distilling, cooling, and crystallizing the residual liquid to obtain magnesium sulfate crystal.    USE - Method for the manufacture of manganese hydroxide, magnesium sulfate, and ammonium hydroxide (claimed).    ADVANTAGE - The method reduces environment pollution, and is simple.
NOVELTY - Manganese hydroxide, zinc sulfate and ammonia are produced by filtering liquid waste generated by hydroquinone through filter to obtain filtrate; transferring obtained filtrate to reaction kettle, filling zinc hydroxide solution, and reacting; filtering obtained mixture in a filter; washing, drying, crushing and packaging filter cake to manganese hydroxide product; decompression filtering the clear filtrate , condensing and packaging to obtain ammonia product; distilling, cooling, crystallizing and packaging residual liquid in decompression distilling to obtain zinc sulfate crystal product.    USE - Method for manufacturing manganese hydroxide, zinc sulfate and ammonia (claimed).    ADVANTAGE - The method can completely use liquid waste, thus reducing environment pollution of liquid waste, and has simple technique and production equipment.    DETAILED DESCRIPTION - Manganese hydroxide, zinc sulfate and ammonia are produced by:    (A) filtering liquid waste generated by hydrochinone through filter to obtain filtrate;    (B) developing elementary substance residue filter cake to other products;    (C) transferring obtained filtrate to reaction kettle, filling zinc hydroxide solution, where mass ratio of filtrate to zinc hydroxide solution is 1:0.46-0.86, and reacting to obtain mixture I of manganese hydroxide, zinc sulfate and ammonia;    (D) filtering obtained mixture in a filter;    (E) washing, drying, crushing and packaging filter cake to manganese hydroxide product;    (F) decompression filtering the clear filtrate , condensing and packaging to obtain ammonia product; and    (G) distilling, cooling, crystallizing and packaging residual liquid in decompression distilling to obtain zinc sulfate crystal product.
NOVELTY - Condensing device comprises 108 horizontal stainless steel circulating pipes sequentially arranged in limited space to form heat exchanger area (250 m2). The connecting mode is that the pipes in the same line are connected in parallel manner. The pipes in the longitudinal line are connected in series. The auxiliary pipes are condensed water spraying pipe and two sets of condensing plans are used, one is wind power cooling and the other one is traditional condensed water cooling.    USE - The device is useful for distilling and purifying o-nitro-ethyl-benzene and in chemical and pharmaceutical fields.    ADVANTAGE - The device: utilizes the pipes in the longitudinal line connected in series to prevent air blocking phenomenon; consumes less energy and is environmental-friendly; can be used normally all the year round; reduces condensing temperature of o-nitro-ethyl-benzene from 155 degrees C to 30-50 degrees C; has good sealing and anti-corrosion effects; produces high yield; and has condensing effect on materials e.g. ammonia having phase change according to the scientific research.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the condensing device for distilling and purifying o-nitro-ethyl-benzene.
NOVELTY - The cell slot has a bipolar plate (4), a pole frame (1) set on the pole plate. The pole frame is between a gasket (2) and a diaphragm (3). The gasket and diaphragm are separated, and tightly pressed in the space formed by the bipolar plate and frame.    USE - Cell slot used in the field of electrolysis hydrogen production.    ADVANTAGE - Cell slot is convenient to make and reliable. Disassembly of gasket and membrane is convenient since the board and frame are separated. Saves manufacturing time and ensures good practicability since thermal melting for integrating the gasket and diaphragm is unnecessary.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic cross-sectional view of the structure of the cell slot.    Pole frame (1)    Gasket (2)    Diaphragm (3)    Pole plate (4)
NOVELTY - A fuel cell power generating device comprises anode (1), cathode (2), lead (5) and a resistor (12). The anode is connected with one end of the lead, and the other end of which is connected with the cathode. Two ends of the lead are further connected with the resistor. The device further comprises a cathode frame (3) and the anode frame (7). Anode box of multiple parallel carbon plates (1-1), where each carbon plate outer surface has a carbon coating (8) of the cathode material.    USE - A fuel cell power generating device used for water treatment in industrial sewage disposal area.    ADVANTAGE - The device solves the problems that anode biological affinity and conductivity is bad and the anode needs expensive catalyst to improve the reaction speed and it cannot be applied to the water treatment in the industrial sewage disposal area.    DETAILED DESCRIPTION - A fuel cell power generating device comprises anode (1), cathode (2), lead (5) and a resistor (12). The anode is connected with one end of the lead, and the other end of which is connected with the cathode. Two ends of the lead are further connected with the resistor. The device further comprises a cathode frame (3) and the anode frame (7). The cathode frame is arranged on the anode frame and is detachably connected. The anode is arranged in the anode frame, and a cathode column on the cathode frame. Anode box of multiple parallel carbon plates (1-1), where each carbon plate outer surface has a carbon coating (8) of the cathode material which is chromium-nickel-molybdenum nitride (00Cr17Ni12Mo2N), 00Cr17Ni13Mo2N, sus316 or sus316L.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the fuel cell power generating device.    Anode (1)    Carbon plate (1-1)    Cathode (2)    Cathode frame (3)    Lead (5)    Anode frame (7)    Carbon coating (8)    Resistor (12)
NOVELTY - Elimination of excess fatty acid from biodiesel comprises reacting biodiesel-containing excess fatty acid with alkali solution in mixing device, washing by water in centrifuge device, separating and eliminating saponifiable matter, and guiding mixed solution into next device.    USE - Method for eliminating excess fatty acid from biodiesel (claimed).    ADVANTAGE - The method eliminates excess fatty acid in biodiesel, and reduces concentration of alkali in each stage, acidity of product at the outlet of the centrifuge device, content of impurities, and acidity of biodiesel end product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the elimination of excess fatty acid from biodiesel (Drawing includes non-English language text).
NOVELTY - A biomass fluid fuel comprises biomass raw material particles with particle size of less than or equal to 150 (preferably less than or equal to 100) mu m and fuel additive dispersed into liquid fuel medium. The weight ratio of the biomass raw material particles to the liquid fuel medium is 1:10-1:1, preferably 1:5-1:1. The total content of the fuel additive is 0.5-3 (preferably 0.9-1.5) wt.% of the biomass fluid fuel.    USE - A biomass fluid fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass fluid fuel, comprising crushing biomass raw material and screening to obtain biomass raw material particles with particle size of less than or equal to 150 (preferably less than or equal to 100) mu m; mixing the biomass raw material particles with liquid fuel medium; and homogenizing the mixture and adding fuel additive.
NOVELTY - Method for pretreating lignocellulose by pressurized microwave, involves obtaining lignocellulose (4-6 g) which is dried to constant weight, crushing the lignocellulose to 10-40 meshes powder, adding distilled water to the powder, where solid-liquid ratio in the mixture is 1:5-20, and treating the obtained mixture in pressurized microwave for 2-15 minutes at 110-150 degrees c, where the pressure of pressurized microwave is 0.1-0.5 MPa, and the microwave frequency is 450 MHz.    USE - The method is useful for pretreating lignocellulose by pressurized microwave.    ADVANTAGE - The method is cost-effective, suitable for commercial production and rapid preferably 2-15 minutes, reduces water consumption and energy consumption, improves conversion rate of reducing sugar, causes no secondary pollution, and requires no addition of chemical reagent.
NOVELTY - Device comprises electromechanical control unit and biochemical processor containing functional microbes. The biochemical processor has mechanical mixing arm and temperature control device, where the mechanical mixing arm and temperature control device are controlled by electromechanical control unit. The microbes are Bacillus subtilis and spore forming Bacillus.    USE - The device is useful for bioprocessing organic waste.    ADVANTAGE - The device combines use of functional microorganism and hence processing effect of the organic waste reaches national emission standard, and reduces discharge amount of harmful substances considerably.
NOVELTY - The cylindrical anode plate (8) is composed of a cylinder with countless convex-shaped balls and with distributed water holes. The surface of cylinder is covered with titanium 0.1 to 3.5% and zirconium 0.1 to 3%, and takes the nickel base metal as the main housing. The anode is composed of a net shaped cylindrical housing made of 200 series of stainless steel metal net. The cathode plate (9) and the anode plates are separated by an insulator, and forming the cylinder of the concentric shaft.    USE - Hydrogen generating device for use in various fields and various industries.    ADVANTAGE - The hydrogen generating device is provided with low energy consumption, high energy conversion efficiency, high amount of gas, low production cost, high hydrogen voltage generation with no need of any pressurizing equipment. The device can be designed into the device of any size with fast and large gas generating amount in the batch way.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural view of the hydrogen generating device.    Electrolytic slot (1)    Anode plate (8)    Cathode plate (9)    Fog spray device (14)    Pressure limiter (15)
NOVELTY - A Bacillus thuringiensis biological pesticide is produced by taking an amount of dry kitchen garbage, when fermenting, accessing Bacillus thuringiensis and Bacillus subtilis mixed strain (10-30 mass%) to obtain biopesticide raw powder. The water content in culture medium initial is 45-60%. The pH value is 6.5-8.5. The thickness of the culture medium is 1-6 cm. The ferment time is 40-50 hours.    USE - Method for production of Bacillus thuringiensis biological pesticide (claimed) for agricultural production.    ADVANTAGE - The method improves kitchen waste utilization efficiency and product effect, achieves the purpose of recycling the kitchen garbage and popularizing green Bacillus thuringiensis biological pesticide.
NOVELTY - A specific catalyst is prepared by freeze-drying palladium and silver at - 25 to - 35 degrees C; grinding with a Raymond mill to a size of 120-mesh; adding platinum, rhenium, tin and iridium; calcining the mixture at 300-500 degrees C for 6-12 hours; vacuum dewatering for 3-8 hours; and calcining at 1300-1600 degrees C.    USE - Method of preparing a specific catalyst for directly synthesizing gasoline with methyl alcohol.    ADVANTAGE - The method prepares catalyst having improved catalysis conversion rate and prolong the service life, utilizes easy to obtain raw materials, and is low cost.
NOVELTY - Method of preparing scopolamine butylbromide, involves (a) heating, refluxing and reacting scopolamine with butyl bromide to obtain crude product of scopolamine butylbromide, and (b) purifying the obtained crude product.    USE - The method is useful for preparing scopolamine butylbromide.    ADVANTAGE - The scopolamine butylbromide is stable, and has good dissolution property as it contains butyl bromide, and excellent water-solubility. The method enables high yield of scopolamine butylbromide as scopolamine reacts with excessive amounts of butyl bromide at increased reaction temperature, has increased reaction speed and reduced reaction time, and does not use any medium. The butyl bromide is not only utilized as raw material but also as reaction solvent. The scopolamine butylbromide is environmentally-friendly and cost-effective as excessive amounts of the butyl bromide are easy to recycle and can be reusable.
NOVELTY - Method for preparing 2,5-dimethyl phenyl acetic acid, involves (a) mixing paraxylene, and ionic liquid with paraformaldehyde and concentrated hydrochloric acid, performing chloromethylation reaction, separating layers from the mixture, and distilling the upper organic layer to obtain 2,5-dimethyl benzyl chloride, and (b) adding 2,5-dimethyl benzyl chloride to acid binding agent and solvent in a reactor, hydrolyzing the mixture, adding liquid alkali to the reaction liquid, adding hydrochloric acid to the water layer, filtering the mixture, and drying the mixture.    USE - The method is useful for preparing 2,5-dimethyl phenyl acetic acid which is used in medicine and agricultural chemicals.    ADVANTAGE - The method is simple, cost-effective, and environmentally-friendly, and suitable for industrial production, and enables high yield of the product.    DETAILED DESCRIPTION - Method for preparing 2,5-dimethyl phenyl acetic acid, involves (a) mixing paraxylene as raw material, and ionic liquid as solvent with paraformaldehyde and concentrated hydrochloric acid, increasing the temperature, performing chloromethylation reaction by adding hydrogen chloride gas, maintaining the temperature for 0.5 hour, reducing the temperature, cooling the mixture, separating layers from the mixture, and distilling the upper organic layer to obtain 2,5-dimethyl benzyl chloride, where molar ratio of dimethylbenzene, paraformaldehyde and ionic liquid is 1:1.1-5:0.01-1, and (b) adding 2,5-dimethyl benzyl chloride to acid binding agent and solvent in a reactor under the presence of catalyst, hydrolyzing the mixture using carbon monoxide, reducing the temperature, adding liquid alkali to the reaction liquid under the presence of nitrogen, stirring the mixture for 1 hour, adding 36% hydrochloric acid to the water layer until pH of the mixture is regulated to 1, maintaining the temperature of the mixture for 1 hour, filtering the mixture, and drying the mixture to obtain the product.
NOVELTY - A pink oral preparation is prepared by extracting Chinese traditional herb materials comprising (pts.wt.) radix paeoniae alba (3), Ligusticum wallichii (3), radix angelicae tuhuo (3), dried Rehmannia root (3), peach kernel (3), and sweet potatoes (2).    USE - Method of preparing pink oral preparation (claimed).    ADVANTAGE - The method improves purity of product, simplifies the process condition, shortens the process period, reduces production cost, and avoids environmental pollution.
NOVELTY - Removal of carbon dioxide (CO2) from ammonia synthesis reforming gas comprises countercurrent or cross-flow contacting ammonia synthesis reforming gas with absorbing liquor in crane; producing large centrifugal force by rotating the filler in high speed; contacting the absorbing liquor with gas; and removing CO2, where volume flow ratio of gas-liquor is 10-60:1, absorbing liquor is polyethylene glycol dimethyl ether (NHD) solvent, absorbing pressure is 0.1-3.3 MPa, and absorbing temperature is - 5 to 5 degrees C.    USE - Removal of CO2 from ammonia synthesis reforming gas (claimed).    ADVANTAGE - The method has simple flow; and reduces apparatus maintenance cost and regeneration energy consumption of the whole decarbonizing process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for removing CO2 from ammonia synthesis reforming gas comprising crane, where gas in reforming working stage is infused from gas inlet of the crane, gas outlet of crane is connected with purified gas working stage, and liquid inlet of crane is connected with poor liquor groove filled with NHD solution through poor liquor pump; and ammonia cooler provided between liquid inlet of crane and poor liquor pump, where liquid outlet of crane is connected with rich liquor groove.
NOVELTY - Manganese sulfate and ammonia are produced by filtering waste liquid produced from hydroquinone; using filter cake to develop other product while transferring the filtrate to a reaction kettle; adding manganese hydrate solution to the filtrate, filtering, and distilling the filtrate; condensing the distillate, and packing to obtain ammonia; and distilling the remaining filtrate, cooling, crystallizing and packing. The mass ratio of filtrate and manganese hydrate solution is 1:0.47-0.87.    USE - Method of producing manganese sulfate and ammonia.    ADVANTAGE - The method is simple, and reduces environmental pollution.
NOVELTY - The device has a steam pocket (13) whose top portion is provided with a pipeline connected with a tube pass of a steam super-heater (2). The tube pass of steam super-heater is connected with an overheat steam collecting device (14). The tube pass of circulating water cooler (6) is connected with a circulating water cooing system (18). The tube pass of a water cooler (7) is connected with a water cooling system (17), and a top end of a horizontal molecular unit (11) is connected with the tube pass of the cool exchanger (8) and a circulator (9).    USE - System cooling device located behind ammonia converter for producing ammonia.    ADVANTAGE - The better cooling effect, and high separating efficiency of the system cooling device are achieved. The best heat energy and more reasonable system flow are achieved by the device. The cooling efficiency is improved, and the consumption of hydropower is reduced. The energy is saved, emission is reduced, and the clean production can be achieved by the device.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of system cooling device behind ammonia converter.    Stream super-heater (2)    Circulating water cooler (6)    Water cooler (7)    Cool exchanger (8)    Circulator (9)    Horizontal molecular unit (11)    Steam pocket (13)    Overheat steam collecting device (14)    Water cooling system (17)    Circulating water cooling system (18)
NOVELTY - Processing animal manure sewage and straw wastes comprises: removing sand and impurities from the animal manure sewage, preheating and sterilizing and performing thermophilic anaerobic fermentation to produce biogas; crushing the straw wastes, transporting into a stacking pool and stacking; mixing the anaerobic fermented animal manure sewage with the stacked straw wastes, controlling the solid liquid content of the mixture between 8-12%, fermenting and generating biogas; performing solid liquid separation for the fermented materials to obtain biogas residue and biogas slurry.    USE - The method is useful for processing animal manure sewage and straw wastes.    DETAILED DESCRIPTION - Processing animal manure sewage and straw wastes comprises: removing sand and impurities from the animal manure sewage, preheating and sterilizing and performing thermophilic anaerobic fermentation at 50-60 degrees C for 5-10 days to produce biogas; crushing the straw wastes to particle size of less than or equal to 20 mm, transporting into a stacking pool and stacking for 3-5 days; mixing the anaerobic fermented animal manure sewage with the stacked straw wastes, controlling the solid liquid content of the mixture between 8-12%, fermenting at 40 plus minus 1 degrees C for 20-35 days and generating biogas; performing solid liquid separation for the fermented materials to obtain biogas residue and biogas slurry; performing aerobic composting for the biogas residue to produce organic fertilizer, where the biogas liquid obtained from the process is used for irrigation or directly mixed with crushed straw wastes for compost; and purifying and pre-processing the generated biogas during the process of thermophilic fermentation and high temperature fermentation through the cogeneration device to provide electrical and thermal energy for supplying the redundant electric energy and heat energy outwards.
NOVELTY - A microorganism for oil displacement, where the microorganism is Protaminobacter albofiavus (CGMCC 4670), is new.    USE - The microorganism is used for oil displacement and is used in a composite oil displacement agent (all claimed).    ADVANTAGE - The microorganism and surfactant composite oil displacement agent can resist high temperature, resist salt, reduce viscosity of crude oil, reduce oil-water interface tension and the like. The microorganism and surfactant composite oil displacement agent is suitable for mining oil and capable of improving the recovery efficiency of the crude oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a composite oil displacement agent, containing the microorganism above.
NOVELTY - A combination of bacteria comprises Bacillus licheniformis, B. subtilis, B. lentus, B. megaterium, B. thuringiensis, and B. cereus. The microorganisms are cultured by sampling, culturing in culture medium, separating strain, analyzing, and identifying.    USE - Combination of bacteria for sludge processing (claimed).    ADVANTAGE - The bacteria are capable of decomposing organic compound and phosphorus in rural domestic sewage.
NOVELTY - Method of extracting and separating tryptophan liquid, involves adding hydrophobic amide-functionalized ionic liquid extraction agent and tryptophan water solution to treatment vessel at 20-60 degrees C and agitating speed of 330 revolutions/minute (rpm) under acidic condition, agitating the mixture for 20-30 minutes, heating the mixture, and separating water layer and extraction agent layer from the mixture.    USE - The method is useful for extracting and separating tryptophan liquid.    ADVANTAGE - The method does not pollute environment.    DETAILED DESCRIPTION - Method of extracting and separating tryptophan liquid, involves adding hydrophobic amide-functionalized ionic liquid extraction agent and tryptophan water solution to treatment vessel at 20-60 degrees C and agitating speed of 330 revolutions/minute (rpm) under acidic condition, agitating the mixture for 20-30 minutes, heating the mixture, and separating water layer and extraction agent layer from the mixture. The amino acid content of water layer is reduced by 69-88%. The concentration of the tryptophan water solution is 0.005-0.05 mol/l. The volume ratio of the amide-functionalized ionic liquid extraction agent to tryptophan water solution is 1:10-2:1. The cation of the amide-functionalized ionic liquid extraction agent is acylamino imidazolium cation. The anion is organic acid anion, preferably bis((trifluoromethyl)sulfonyl)amide (NTf2)-.
NOVELTY - Production device comprises window (11) arranged on one side of kettle body; electric control device (10) having output shaft provided with stirrer (2); acid catalyst tank; methanol tank (7); methanol alkali tank (9); electromagnetic valve (16) arranged on lower part of acid catalyst tank; filter screen (15) arranged on feeding port of reaction kettle; nozzle (13) arranged under upper cover plate; and static generator (3) arranged at lower part of electric control device.    USE - Production device used for producing biological diesel oil.    ADVANTAGE - The device has simple structure and easy to implement. The electric control device provides accurate automatic spraying of catalyst. The electrostatic generator shortens layered dehydration time of material. The production device produces biodiesel at high yield and good product quality while reducing environmental pollution.    DETAILED DESCRIPTION - Production device comprises window (11) arranged on one side of kettle body; electric control device (10) arranged on central part and has output shaft provided with stirrer (2); acid catalyst tank (5) provided in kettle body upper side; methanol tank (7) arranged on other side of kettle body; methanol alkali tank (9) arranged at inner side of reaction kettle; electromagnetic valve (16) arranged on lower part of acid catalyst tank; filter screen (15) arranged on feeding port of reaction kettle; nozzle (13) arranged under upper cover plate; and static generator (3) arranged at lower part of electric control device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of production device.    Stirrer (2)    Static generator (3)    Acid catalyst tank (5)    Methanol tank (7)    Methanol alkali tank (9)    Electric control device (10)    Window (11)    Nozzle (13)    Filter screen (15)    Electromagnetic valve (16)
NOVELTY - A pre-treatment of wastewater in production of oxyfluorfen comprises using complexing extracting technique for recycling resorcinol and hydroxy benzoic acid from production wastewater of oxyfluorfen. The method includes complexing and extracting; and carrying out reextraction via liquid alkali.    USE - Method for pre-treatment of wastewater in production of oxyfluorfen (claimed).    ADVANTAGE - The toxic pollutant can be removed and resource can also be recycled. The resorcinol and hydroxybenzoic acid recycled from the wastewater can be directly applied to the production technique. The removal rate of resorcinol and the hydroxybenzoic acid can reach 99%, more than 80% of chemical oxygen demand is reduced. The method can solve problem on discharging the production wastewater of oxyfluorfen pesticide after reaching standard.
NOVELTY - A gabapentin hydrochloride is synthesized by mixing 1,1-cyclohexanediacetic acid monoamide and organic solvent, subjecting mixture to Hoffman degradation reaction, heating, dehydrating, concentrating the product, separating the organic phase and the water phase, adding hydrochloric acid into the organic phase, separating the water phase and the organic phase, and concentrating the water phase to obtain the gabapentin hydrochloride.    USE - Method of synthesizing gabapentin hydrochloride.    ADVANTAGE - The method does not consume a large amount of inorganic acid thus generating lower volume of inorganic salt, has easy separation step, recycles material thus reducing production cost and zero emission of organic solvent, is simple and convenient, and has high yield.
NOVELTY - Solvent-thermal synthesis of losartan biphenyl tetrazole comprises taking losartan biphenyl and sodium azide as reaction raw material and taking 1,2-propanediol water solution as solvent; and synthesizing biphenyl tetrazole at 160-180 degrees C by taking mixture of ammonium chloride and metal fluoride (MF) catalyst, where M is alkali metal or ammonium base cation.    USE - Method for solvent-thermal synthesis of losartan biphenyl tetrazole (claimed).    ADVANTAGE - The reaction auxiliary agent is cheap and is non-toxic or has low toxin. The reaction auxiliary agent can be repeatedly used, thus reducing reaction cost. The reaction post-treatment is simple and industrial production can be processed. The manufacturing rate of method can reach 95%. Calculated by sodium azide, purity of crude product is 99%.
NOVELTY - A L-phenylalanine is crystallized by adding dropwise hydrochloric acid to alkali L-phenylalanine solution having a pH of 10-12 at 37-45 degrees C while stirring, reducing pH of the solution to 5-6, cooling, filtering, washing the crystals with ethanol, and vacuum-drying.    USE - Method of crystallizing L-phenylalanine.    ADVANTAGE - The method prepares product having uniformed size, is simple and environment-friendly, has good repeatability, does not require organic solvent, and can be applied to industrial production.
NOVELTY - Ceftiofur sodium preparation involves performing a reaction by using ceftiofur hydrochloride and alkali in organic solvent at -30 degrees C to 40 degrees C to obtain sodium salt solution of ceftiofur or free acid solution. The free acid of ceftiofur is processed by sodium 2-ethyl hexanoate to obtain ceftiofur sodium. A crystallization solvent is added for separating ceftiofur sodium. Ceftiofur sodium is concentrated by drying to obtain finished product.    USE - Method for preparing ceftiofur sodium, preferably (6R,7R)-7-(2-(2-aminothiazole-4-yl)-(Z)-2-(methoxylimino)acetamido)-3-((2-furancarbonyl) sulfomethyl)-3-cephem-4-carboxylate (claimed).    ADVANTAGE - The method enables to prepare ceftiofur sodium with more or less than 90% yield in a cost-effective and eco-friendly manner.
NOVELTY - Integrating algae biodiesel and algae fermentation recycling comprises supplying oxygen produced by microalgal growth and carbon dioxide produced by fermentation of algae in fermentation tank to each other to form a cyclic state.    USE - The method is useful for integrating algal biodiesel and algae fermentation recycling.
NOVELTY - Functional bacterial composition comprises Bacillus cereus, Bacillus licheniformis, Bacillus subtilis, Acinetobacter calcoaceticus and Paracoccus denitrificans. The process for culturing microorganisms comprises sampling, culturing in a medium, separating the target strain, analyzing the index value of the separated strain, identifying the species, matching and optimizing.    USE - The functional bacterial composition is useful for sewage treatment.    ADVANTAGE - The composition: decomposes organic matter in the process of rapid proliferation, has significant phosphorus removing effect in sewage and greatly reduces the discharge of sludge and hence meets the national discharge standard.
NOVELTY - A corn straw is pretreated by crushing the corn straw by passing through a sieve at diameter of 40 meshes; and pretreating the crushed corn straw at constant temperature of 80 degrees C for 120 minutes.    USE - Method for the pretreatment of corn straw (claimed).    ADVANTAGE - The method promotes the microbe of corn straw to degrade for decreasing the environmental pollution of chemical pretreatment.
NOVELTY - An accelerating agent comprises (pts.wt.) photosynthetic bacteria (20-30), Bacillus (20-30), yeast (20-30), Pseudomonas (10-20), and all digestive enzymes, where each gram of culture medium for single bacteria includes 50-80 billion bacteria.    USE - An accelerating agent for sludge culture of super-microorganism (claimed).    ADVANTAGE - The accelerating agent quickly cultures active sludge and removes ammonia nitrogen with high efficiency by aeration control and the reaction microorganism. It is environment-friendly, and has high adaptability and low yield of sludge.
NOVELTY - Preparation of biogas comprises absorbing and enriching organic substances in sewage using multi-pore ceramic; and performing anaerobic digestion for multi-pore ceramic in which organic substances are enriched.    USE - Preparation of biogas.    ADVANTAGE - The method has simple process and low cost, purifies sewage and reuses organic substances in sewage. It processes sewage while producing energy source synchronously.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) device for preparing biogas comprising tank body; water charging pipe arranged on lower part of tank body and connected with water distributor arranged on bottom of tank; overflowing pipe arranged on upper part of tank body; upper cover arranged on top of tank body; gas discharging pipe arranged on upper cover; filler frame for accommodating multi-pore ceramic and arranged in tank body; and holes formed on bottom and top cover of filler frame;and    (2) system for preparing biogas comprising several serial reacting units each comprising device for preparing biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of device for preparing biogas.
NOVELTY - 2,6-Diethyl aniline and ethylene oxide are reacted in presence of solvent and catalyst to obtain N-(1-methyl-2-hydroxyethyl)-2,6-diethyl aniline. The obtained N-(1-methyl-2-hydroxyethyl)-2,6-diethyl aniline and n-chloropropane are reacted under alkali condition and distilled, to obtain 2-ethyl-6-methyl-N-(1'-methoxy-propyl-2-n-methylaniline). The obtained 2-ethyl-6-methyl-N-(1'-methoxy-propyl-2-n-methylaniline) and chloroacetic chloride are reacted at common temperature, washed using water, distilled and dried, to obtain pretilachlor.    USE - Manufacture of pretilachlor.    ADVANTAGE - The method efficiently and economically provides pretilachlor without polluting the environment.
NOVELTY - A biological organic fertilizer is prepared by pre-processing and mixing a livestock excrement, straw, and peat at a weight ratio of 3-5:1-2:1-2; adding a high concentrated organic matter-decomposing inoculant agent, where a weight ratio of the total amount to high concentrated organic matter-decomposing inoculant agent is 5000-10000:1-2; mixing and fermenting for 7-10 days, stirring for 1-2 times/day, and mixing fermented material and functional composite microbial inoculum at a weight ratio of 5000-10000:1-2; and particle-making, and low temperature dry processing.    USE - A biological organic fertilizer.    ADVANTAGE - The fertilizer is inexpensive, and prepared using a simple and environment-friendly method.
NOVELTY - An efficient biomass solid fuel is prepared by adding a synergistic agent to crushed straws, followed by stirring and performing compression molding.    USE - Efficient biomass solid fuel.    ADVANTAGE - The fuel is highly pure, inexpensive, non-toxic, harmless, eco-friendly, simple and convenient to use, and has neutral pH value, thus preventing a metal surface from being corroded and human body from being injured. The addition of the synergistic agent to the fuel remarkably increases the fuel heat value, thus obtaining high-performance biomass solid fuel. The fuel has long preservation time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing biomass solid fuel.
NOVELTY - Production of a bio-oil rich in guaiacol comprises preparing a catalyst comprising sodium carbide solution; immersing a crushed biomass raw material in the solution, where the mass ratio of the biomass raw material to the catalyst as 8-10%; drying; placing the material in a fluidized bed cracking reactor to perform cracking at 450-480 degrees C and normal pressure for 40 minutes, with a nitrogen flow of 0.2 m3/hour; and condensing the distillate.    USE - Method for the production of a bio-oil rich in guaiacol (claimed).    ADVANTAGE - The raw material is from natural biomass, non-toxic, and inexpensive. The reaction process is simple, and environment-friendly.
NOVELTY - Upgrading a pyrolysis oil comprises sending the pyrolysis oil to a well-mixed reactor or a back-mixed reactor to produce an upgraded pyrolysis oil.    USE - The process is useful for producing biomass-derived pyrolysis oils.    ADVANTAGE - The process provides biomass-derived pyrolysis oils with increased phase stability.
NOVELTY - Deactivating biomass, involves: a) performing a disrupting stage by injecting an oxidizer agent into the biomass causing disruption of cellular membranes of cells in the biomass; and b) performing a rupture stage by: i) injecting a rupture gas into the biomass sufficient to pressurize the biomass to a second elevated pressure; ii) depressurizing the biomass; iii) repeating the steps of injecting and depressurizing at least 3 times to rupture the cell membranes and expose residual cell contents.    USE - For deactivating biomass i.e. activated sludge or algae to form biofuel which includes methane, carbon monoxide, and hydrogen (claimed).    ADVANTAGE - The method provides a large volume of activated sludge at once directly from secondary clarifier underflow; it can process any solid concentrations from low to very high (e.g. 3000-100000 mg/l); is not be susceptible to interference or blockage by debris causing equipment maintenance issues; requires much less energy to pressurize the small headspace, as compared to other more energy demanding techniques. There is no need for addition of acid or caustic, the method can be effective at room temperature in a matter of minutes. The process is batch-based, several units can be operated in parallel to handle continuous processing needs.
NOVELTY - Preparing gefitinib (V) or its intermediate comprises reacting an amine compound (IV) with N,N-dimethyl formamide dimethyl acetal and 3-chloro-4-fluoro aniline to obtain the compound (V).    USE - Method for preparing compound (V) or its intermediate (claimed).    ADVANTAGE - The method is environment-friendly, and can simplify purification process and increase yield rate.    DETAILED DESCRIPTION - Preparing gefitinib of formula (V) or its intermediate comprises reacting an amine compound of formula (IV) with N,N-dimethyl formamide dimethyl acetal and 3-chloro-4-fluoro aniline to obtain the compound (V).    X=Cl or Br.
NOVELTY - The system has an oil-gas filter connected to a discharge channel. An input end of the oil-gas filter is connected to a waste gas source part. An output end of the oil-gas filter is connected to a bottom part of the discharge channel. An acid cooler is fixed in an upper part of an absorption tower. A dust filter is connected to a bottom part of a compressor. A top part of a butane tower is connected to a product tank. The butane tower is connected to a reflux pump.    USE - Waste gas recycling and treating system.    ADVANTAGE - The system is simple in structure, and reduces pollution to environment and provides recycling of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a waste gas recycling and treating system.
NOVELTY - Mixed carbon source gasification molded coal comprises (wt.%) smoke-free dust coal (28-56), biomass carbon powder (38-66), and binder (5-7).    USE - The mixed carbon source gasification molded coal is used for synthetic ammonia (claimed). It is used as coal-based synthetic ammonia production raw material used to replace high quality anthracite coal.    ADVANTAGE - The mixed carbon source gasification molded coal solves the problems of non-high quality anthracite coal and solid molded coal used in prior art synthetic ammonia having high ash, low fixed carbon, high-residue gasification, and low synthetic ammonia system carbon conversion rate, leading to high synthetic ammonia integrated unit product energy consumption.
NOVELTY - A vertical anaerobic fermentation device includes a feeding nozzle (1), a fermentation tank (4) provided with a biogas outlet (2) at the top part and a discharging opening (3) at the bottom, a storage tank (5), a gas purifying pressurizing device (6), adjusting control tank (7), electric pump (8), and output pipe (10).    USE - Vertical anaerobic fermentation device for high concentration organic waste.    ADVANTAGE - The vertical anaerobic fermentation device has simple structure and convenient operation, can save energy, and is environment-friendly.    DETAILED DESCRIPTION - A vertical anaerobic fermentation device comprises a feeding nozzle (1), a fermentation tank (4) provided with a biogas outlet (2) at the top part and a discharging opening (3) at the bottom, a storage tank (5) connected with the methane outlet at the top of the fermenting tank, a gas purifying pressurizing device (6) connected with the air storage tank. The inlet nozzle of the fermentation tank is located on the upper part of the fermentation tank. An adjusting control tank is set at one side of the fermenting tank. The adjusting control tank (7) and the fermentation tank inlet nozzle are connected by an electric pump (8). An output pipe (10) with a first valve is set between the fermentation tank and the adjusting control tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the vertical anaerobic fermentation device.    Feeding nozzle (1)    Biogas outlet (2)    Discharging opening (3)    Fermentation tank (4)    Storage tank (5)    Gas purifying pressurizing device (6)    Adjusting control tank (7)    Electric pump (8)    Output pipe (10)
NOVELTY - The device has a shell whose front end is provided with a nuclear magnetic resonance (NWR) principle detection probe. A data processing unit is provided with an LED display unit and a CPU circuit. The NWR principle detecting probe and the LED display unit are connected with the shell. The CPU circuit is connected with an infrared signal receiving circuit by multiple interfaces. A power supply circuit is connected with NWR principle detecting probe, the LED display circuit and a frequency signal output circuit.    USE - Methane sensor device.    ADVANTAGE - The device has better effective display probe detection data, better gas type selectivity, high measuring speed, prolonged service life, high measurement precision, quick and stable measuring range, better calibration effect and small maintenance workload. The device can be effectively operated in an oxygen free environment. The device reduces concentration gas impact damage and avoids poisoning problems. The device utilizes a non-dispersive infra-red detection probe with automatic zero correction function and automatic fault detecting function, so that the device ensures low maintenance effect and high working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a methane sensor device.'(Drawing includes non-English language text)'
NOVELTY - Extraction of a Rheum total anthraquinone in a traditional Chinese medicine comprises feeding Rheum raw material particle in a leaching kettle at 30-80 degrees C and 7-50 MPa, and continuously filling 10-60 L/hour supercritical fluid and a cosolvent; extracting in a separation kettle at 10-80 degrees C and 4-22 MPa for 1.5-5 hours; and directly discharging the supercritical fluid flowing from the separation kettle or compressing and filling the supercritical fluid in the leaching kettle to be circularly used.    USE - Method for the extraction of a Rheum total anthraquinone in a traditional Chinese medicine (claimed).    ADVANTAGE - The method is simple and environment-friendly, and has strong specificity.    DETAILED DESCRIPTION - Extraction of a Rheum total anthraquinone in a traditional Chinese medicine comprises feeding Rheum raw material particle in a leaching kettle at 30-80 degrees C and 7-50 MPa, and continuously filling 10-60 L/hour supercritical fluid and a cosolvent; when the pressure of the high-pressure fluid flowing from the leaching kettle is decreased to a value lower than the critical pressure, the high-pressure fluid flowing from the leaching kettle enters a next stage of separation kettle to be separated, maintaining the separated Rheum extract in the separation kettle, where extracting in the separation kettle is carried out at 10-80 degrees C and 4-22 MPa for 1.5-5 hours; and directly discharging the supercritical fluid flowing from the separation kettle or compressing and filling the supercritical fluid in the leaching kettle to be circularly used.
NOVELTY - Extracting chimaphilin comprises crushing pyrolaceae, transferring into an extracting kettle, passing supercritical carbon dioxide, adding ethanol, carrying out supercritical carbon dioxide extraction, vacuum extracting and separating, dispersing the extract with ethanol, adding silica gel, mixing, vaporizing the solvent, pouring into a column, carrying out gradient elution using petroleum ether-ethyl acetate, combining the contents and based on thin layer chromatography tracking and monitoring, concentrating the eluent, drying, heating, filtering, recrystallizing and drying the crystals.    USE - The method is useful for extracting chimaphilin.    ADVANTAGE - The method is ecofriendly.    DETAILED DESCRIPTION - Extracting chimaphilin comprises: (i) crushing pyrolaceae, transferring into an extracting kettle, passing supercritical carbon dioxide, adding ethanol as a co-solvent, carrying out supercritical carbon dioxide extraction, vacuum extracting and separating the extract; (ii) dispersing the extract with a small amount of ethanol, adding silica gel, mixing, vaporizing the solvent, pouring into a column, carrying out gradient elution through petroleum ether-ethyl acetate, collecting the contents, combining the contents based on thin layer chromatography tracking and monitoring to obtain the eluent with enriched chimaphilin; and (iii) concentrating the eluent, drying at low temperature to obtain a dried product, heating the product and dissolving using ethanol, filtering out the crystals, recrystallizing using ethanol for 1-2 times, and drying the crystals at low temperature to obtain chimaphilin.
NOVELTY - Method for vertical flow fermentation of straw, involves feeding straw from upper portion or lower portion of vertical fermentation tank.    USE - The method is useful for vertical flow fermentation of straw which is used for producing biogas.    ADVANTAGE - The method improves gas production efficiency and the produced gas can be discharged easily.
NOVELTY - Method for preparing biodiesel using immobilized lipase catalytic Coptis wood oil, involves subjecting Coptis wood oil to transesterification reaction using pig pancreas lipase and methanol.    USE - The method is useful for preparing biodiesel.    ADVANTAGE - The immobilized lipase can be used continuously and repeatedly for 13 times, and has lipase activity of 80% or more after esterification reaction. The method improves utilization rate of lipase, and is cost-effective.
NOVELTY - Method for preparing biofuel using food waste, involves pre-treating food waste as fermentation raw material, saccharifying the food waste and preparing the food waste to fermentation culture medium, inoculating zymogenous bacteria in the fermentation culture medium to perform anaerobic fermentation, and separating solid from liquid to prepare biofuel. The method involves using Clostridium acetobutylicum to perform anaerobic fermentation on effective components in the food waste to obtain biofuel.    USE - The method is useful for preparing biofuel, preferably butanol.    ADVANTAGE - The method is simple and cost-effective, has excellent maneuverability, and does not need other additives.
NOVELTY - Improved craft of coke-oven civil gas is obtained by separating methane (95% or more) having carbon content of 99% or more from portion of the coke oven gas from coke production process, where the separated methane is taken as civil fuel gas, obtaining a separated hydrogen, nitrogen, carbon monoxide and methane as coke oven flue gas, and discharging the gas from the coke system.    USE - As improved craft of coke-oven civil gas.    DETAILED DESCRIPTION - Improved craft of coke-oven civil gas is obtained by separating methane (95% or more) having carbon content of 99% or more from portion of the coke oven gas from coke production process, where the separated methane is taken as civil fuel gas, obtaining a separated hydrogen, nitrogen, carbon monoxide and methane as coke oven flue gas, and returning the gas to the coke system. The specific process involves separating the dust from the coke-oven gas, removing acidic gas from the coke-oven gas, pressure swing absorbing and separating the concentrated methane and carbon material from the coke-oven gas.
NOVELTY - Method of pre-processing beer waste biochemically, involves breaking cell wall of beer wastewater using ozone, subjecting the beer wastewater, sludge, waste and fresh beer yeast slurry to sterilization, where the ozone amount is 0.3-0.8 g in each gram of waste beer dried substances, subjecting the sterilized mixture to high-pressure steam sterilization at 121 degrees C for 45 minutes, and utilizing steam-sterilized mixture for microorganism yeast culture.    USE - The method is useful for pre-processing beer waste biochemically, where the pre-processed beer waste is used as culture medium for culturing microorganisms.    ADVANTAGE - The releasing rate of nutrient component is greatly improved. The amino nitrogen content of culture medium is increased by 4-5 times. The amino nitrogen yield is 3-5%, hence it is very beneficial as culture medium to culture microorganism.
NOVELTY - The device has a hollow cavity that is divided into two gas cavities by a film sheet (1). One cavity is a hydrogen gas cavity (6) having a hydrogen outlet (4) and a hydrogen inlet (8), the other cavity is an oxygen gas cavity (7) having an oxygen outlet (5) and an oxygen inlet (9). A lug boss (10) is provided on inner wall of the oxygen gas cavity. The channel of the oxygen outlet passes through the lug boss on the inner wall of the oxygen gas cavity.    USE - Gas balancing device for making hydrogen by water-electrolysis.    ADVANTAGE - The internal structure of gas adjustable balance device is simple with obvious pressure balance effect. The pressure balance speed is fast, and the hydrogen generate time is shortened. The operation reliability is reinforced, and the device manufacturing cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the gas balancing device.    Film sheet (1)    Hydrogen outlet (4)    Oxygen outlet (5)    Hydrogen gas cavity (6)    Oxygen gas cavity (7)    Hydrogen inlet (8)    Oxygen inlet (9)    Lug boss (10)
NOVELTY - A remaining sludge is jointly treated by depositing remaining sludge of secondary sedimentation tank of a sewage treatment plant for 4-5 hours, removing supernatant, adding surfactant to the remaining sludge, adding complex enzyme solution dissolved in phosphate buffer to the remaining sludge to control mass ratio of the complex enzyme to dry sludge at 0.05-0.07:1, and subjecting to oscillating hydrolysis at 50 degrees C in water bath for 4-5 hours under anaerobic conditions.    USE - Method of jointly treating remaining sludge.    ADVANTAGE - The method widens the sludge harmless treatment, and utilizes sludge as resources thus reducing pollutions.    DETAILED DESCRIPTION - A remaining sludge is jointly treated by depositing remaining sludge of secondary sedimentation tank of a sewage treatment plant for 4-5 hours, removing supernatant, adding surfactant to the remaining sludge, adding complex enzyme solution dissolved in phosphate buffer to the remaining sludge to control mass ratio of the complex enzyme to dry sludge at 0.05-0.07:1, and subjecting to oscillating hydrolysis at 50 degrees C in water bath for 4-5 hours under anaerobic conditions. The mass ratio of surfactant to dry sludge is 0.08-0.12:1. The surfactant is sodium lauryl sulfate. The complex enzyme solution is a mixture of protease solution and amylase solution having a mass ratio of 3:1. The dry sludge is anhydrous sludge.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart of a method of jointly treating remaining sludge. Drawing includes non-English language text.
NOVELTY - Apparatus has (a) cooling tank, (b) temperature sensor, (c) cooling pump, (d) connection pipe, and (e) temperature controller. The upper side of the cooling tank is opened and the lower side of the cooling tank is connected to a processing tank. The temperature sensor is installed inside the processing tank and detects the temperature of the processing tank inside. The cooling pump is installed inside the processing tank and operated by the temperature sensor.    USE - The apparatus is useful for disposing organic wastewater.    ADVANTAGE - The apparatus is simple, cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Apparatus has (a) cooling tank, (b) temperature sensor, (c) cooling pump, (d) connection pipe, and (e) temperature controller. The upper side of the cooling tank is opened and the lower side of the cooling tank is connected to a processing tank. The temperature sensor is installed inside the processing tank and detects the temperature of the processing tank inside. The cooling pump is installed inside the processing tank and operated by the temperature sensor. The connection pipe conveys organic compound in the processing tank, inhaled by the cooling pump to the cooling tank from air through the upper opening of the cooling tank. The temperature controller is equipped with at least one injection nozzle installed at the connection pipe. A transparent water level gauge window for confirming water level of the organic wastewater time to time and bad smell deodorizing unit for collecting and deodorizing bad smell generated in organic wastewater are adhered. The inner temperature of the processing tank is always maintained at 20-30 degrees C to actively maintain activity of microorganism. The apparatus agitates, ferments, and decomposes organic wastewater. Photosynthetic bacteria in the processing tank are made into inorganic component.
NOVELTY - Waste liquid treatment of molasses alcohol comprises: (i) adding an adsorbent into the waste liquid to adsorb solid substances, separating out precipitates and a supernatant by sedimentation separation, (ii) subjecting the supernatant to a multi-stage sedimentation and clarification, removing the upper clarified liquor for future use, and returning the lower liquor with precipitates to the waste water of the step (i) for continuously treating after the sedimentation and clarification, and (iii) collecting separated precipitates to obtain a solid fertilizer after dewatering and drying.    USE - The method is useful for waste liquid treatment of molasses alcohol.    ADVANTAGE - The treatment method: ensures low equipment investment, simple operation and low energy consumption and is cost effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an organic fertilizer, comprising the above mentioned solid substances dried as raw materials and microbial strains, (3-10 kg per ton of dry granular sludge).
NOVELTY - Production of fertilizer component-containing natural mineral materials, involves crushing vermiculite, mixing the crushed material with water, adding sulfuric acid to the aqueous mixture, processing and agitating the mixture, aging the processed mixture, and filtering the aged mixture.    USE - Production of fertilizer component-containing natural mineral materials (claimed).    ADVANTAGE - The fertilizer component-containing natural mineral materials is produced by simple process and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizer component-containing natural mineral materials produced by the above-cited method.
NOVELTY - Organic fertilizer produced by biological bacteria and agricultural waste, is claimed. The organic fertilizer is prepared by combining microbiological flora e.g. Saccharomyces fungus and treated agricultural organic wastes. The main raw material for producing fungicide comprises strains, cotton seed meal, peat, corn meal and calcium carbonate.    USE - Used as an organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the organic fertilizer, comprising combining the biological bacteria and treated agricultural waste, where the treatment of agricultural organic waste comprises adding leaven in the mushroom residue and livestock excrement; quickly heating and sterilizing the mushroom residue and livestock excrement, deodorizing and drying the mushroom residue and livestock excrement; regulating and controlling the parameters e.g. temperature, humidity and pH of organic waste, adding fungicide which degrades mushroom residue and excrements in some days latter to achieve harmlessness and complete dissociation of solid waste.
NOVELTY - A biomass fuel particle comprises (wt.%) biomass fuel raw materials (70-80), palm meal (5-20) and medicine gunk alcohol deposition (5-20).    USE - Biomass fuel particle.    ADVANTAGE - The biomass fuel particle has smooth surface, compact texture, low cracking rate, high producing efficiency and low mechanical mold abrasion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation of biomass fuel particle comprising mixing (wt.%) biomass fuel raw materials (70-80), palm meal (5-20) and medicine gunk alcohol deposition (5-20) uniformly and compressing mixture into square blocks or cylindrical biomass fuel particles via special pressing block forming mechanical device.
NOVELTY - Vertical flow constructed wetland sewage treatment system comprises a main body (1) comprising impervious layer (2). The main body is distributed on a first baffle (3) and a second baffle (4). The first baffle and the lower end provided with a through hole (14). The first baffle and the second baffle body is divided into an inlet zone, a multi-stage baffle the treatment area and an absorbent area. The inlet zone setting the inlet pipe and a water distribution device set on an outlet pipe in the absorbent area.    USE - Used as a vertical flow constructed wetland sewage treatment system.    ADVANTAGE - The system: is suitable for multi-stage sewage treatment of different water qualities; intensively removes nitrogen from sewage purification ability; and increases the stability.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the vertical flow constructed wetland sewage treatment system.    Main body (1)    Impervious layer (2)    First baffle (3)    Second baffle (4)    Through hole (14)
NOVELTY - Methane gas generator comprises a deflector-type stirrer (10) and a disturber (11) mounted on a methane fermenting tank (1) of a methane pond A. The deflector type stirrer is arranged at outer periphery of methane fermenting tank. The disturber is located in middle of methane fermenting tank. The deflector-type stirrer is connected with disturber connected with a thermal insulating temperature raising controller (7). The thermal insulating temperature raising controller is connected with an air pump (8). A regulating valve and an electromagnetic valve are connected with set of cylinders.    USE - The methane gas generator is useful in cold region.    ADVANTAGE - The generator maintains the suitable temperature for strain fermentation; completely degrades the fermenting raw material; and has high yield.    DETAILED DESCRIPTION - Methane gas generator comprises a deflector-type stirrer (10) and a disturber (11) mounted on a methane fermenting tank (1) of a methane pond A. The deflector type stirrer is arranged at the outer periphery of the methane fermenting tank. The disturber is located in the middle of the methane fermenting tank. The deflector-type stirrer is connected with the disturber connected with a thermal insulating temperature raising controller (7). The thermal insulating temperature raising controller is connected with an air pump (8). A regulating valve and an electromagnetic valve are connected with the set of cylinders. A cracking cone is located at the top of a floating cover of the methane fermenting tank    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methane gas generator.    Methane fermenting tank (1)    Thermal insulating temperature raising controller (7)    Air pump (8)    Deflector-type stirrer (10)    Disturber (11)
NOVELTY - Highly-efficient domestic sewage treatment device comprises a sewage pool (1) provided with a ground source heat pump (2). A ground source heat pump outlet pipeline (21) is connected to a heat exchanger (3) set in the sewage pool. The ground source heat pump is provided with an inlet pipeline (22). The middle part of ground source heat pump inlet pipeline comprises an underground heat absorbing section.    USE - Used as an highly efficient domestic sewage treatment device.    ADVANTAGE - The highly efficient domestic sewage treatment device possesses a ground source heat pump and a heat exchanger located in the sewage pool, which increases the sewage temperature to accelerate the biological metabolism speed and to increase the sewage treatment efficiency; meets the needs of the sewage processing industry; and is simple; and has easy maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the highly-efficient domestic sewage treatment device.    Sewage pool (1)    Ground source heat pump (2)    Ground source heat pump outlet pipeline (21)    Ground source heat pump inlet pipeline (22)
NOVELTY - Preparation of cholestanone comprises using cholesterol and hydrogen and performing oxidation reaction of dihydrocholesterol for greater than or equal to 2 hours in solvent and an oxidant at greater than or equal to 25 degrees C until the reagent boiling point, separating and drying. The mole ratio of the oxidant to dihydrocholesterol is 1.5-3:1.    USE - Method for the preparation of cholestanone (claimed).    ADVANTAGE - The method has a yield of greater than or equal to 92%, and has a purity of greater than or equal to 97%. The hydrogenation and oxidation reaction are featured with mild condition, stable reaction, stable quality, simple technique, convenient operation, scale production, and small catalyst dosage. It recycles solvent; and has zero wastewater, waste gas, and solid waste emission.
NOVELTY - A high-clean methanol diesel fuel comprises (mass%): national standard diesel (20-80), methanol (10-45), cosolvent (10-35), methyl tertbutyl ether (2-10) and ethyl nitrate (0.01-2.5).    USE - High-clean methanol diesel fuel used as vehicle diesel fuel.    ADVANTAGE - The diesel fuel has high technical content, simple technique and stable product performance. The particle diameter of the product reaches 0.5-10 nm. The quality reaches standards of No. 0, No. 10# and No. 20 diesel fuels in GB252-2000.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the diesel fuel which comprises adding methanol and cosolvent into reaction kettle, and starting stirrer to mixing at 30 revolutions/minute (rpm); after 10 minutes, adding national standard diesel, methyl tertbutyl ether and ethyl nitrate and continuously stirring for 20 minutes at 80 rpm; using nano emulsifying machine to cut and emulsify reacted materials at 2880 rpm; and using high-energy static mixer to perform for 1-2 hours to produce desired methanol diesel fuel.
NOVELTY - Preparation of Nevirapine comprises reacting 2-chloro-3-picolinic acid and carbonyl-diimidazole to obtain activated amide; reacting activated amide with 2,6-dichloro-3-amino-4-methylpyridine to obtain N-(2,6-dichloro-4-methyl-3-pyridyl)-2-chloro-nicotinamide; carrying out nucleophilic substitution between N-(2,6-dichloro-4-methyl-3-pyridyl)-2-chloro-nicotinamide and cyclopropylamine and proceeding cyclization to obtain 2-chloro-Nevirapine; carrying out hydrogenation reaction between 2-chloro-Nevirapine and non-hydrogen hydrogen source in the presence of catalyst to obtain Nevirapine.    USE - Preparation of Nevirapine.    ADVANTAGE - The method has low cost and higher safety. It is environment-friendly and suitable for production.
NOVELTY - Method for preparing dicamba herbicide, involves (a) reacting 2,5-dichlorophenol with sodium alcoholate to obtain 2,5-sodium dichlorophenolate, (b) reacting the 2,5-sodium dichlorophenolate with supercritical carbon dioxide to obtain 3,6-dichlorosalicylic acid sodium salt, and (c) reacting the obtained 3,6-dichlorosalicylic acid with dimethyl carbonate to obtain 3,6-dichloro-2-methoxysalicylic acid, preferably dicamba.    USE - The method is useful for preparing dicamba herbicide for preventing and/or controlling weeds in wheat crop.    ADVANTAGE - The herbicide can be obtained in large amount with high quality. The method enables to reduce environmental pollution and consumes less energy.    DETAILED DESCRIPTION - Method for preparing dicamba herbicide, involves (a) selecting 2,5-dichlorophenol as raw material and reacting 2,5-dichlorophenol with sodium alcoholate to obtain 2,5-sodium dichlorophenolate, where the molar ratio of sodium alcoholate to 2,5-dichlorophenol is 1:1-1.05:1, (b) reacting the obtained 2,5-sodium dichlorophenolate with supercritical carbon dioxide in presence of anhydrous potassium carbonate in high pressure reaction kettle to obtain 3,6-dichlorosalicylic acid sodium salt, acidifying the obtained 3,6-dichlorosalicylic acid and controlling the pressure of the carbon dioxide at 5-10 Mpa, reaction temperature at 100-150 degrees C and reaction time for 3-4 hours, where the molar ratio of anhydrous potassium carbonate to 2,5-sodium dichlorophenolate is 1:1-3:1, and (c) reacting the obtained 3,6-dichlorosalicylic acid with dimethyl carbonate in presence of basic catalyst at 120-150 degrees C to obtain 3,6-dichloro-2-methoxysalicylic acid, preferably dicamba, where the molar ratio of dimethyl carbonate to 3,6-dichlorosalicylic acid is 1:1-5:1.
NOVELTY - Preparation of an alpha -cyclopropylcarbonyl-2-fluorobenzyl halide (I) comprises reacting cyclopropyl-2-fluorobenzyl ketone and a catalyst while blending in a solvent-free medium, and controlling the reaction temperature to 0-70 degrees C; and reacting with a halogenating reagent for 0.5-3 hours.    USE - Method for the preparation of an alpha -cyclopropylcarbonyl-2-fluorobenzyl halide (I) used as a prasugrel intermediate (claimed).    ADVANTAGE - The method has short halogenation reaction, low reaction temperature, high purity of product, and high yield. It is stable, safe, and saves energy resource thus providing environmental protection. The method does not use free radical initiator. The (I) has a yield of not less than 95% and purity of not less than 93%.    DETAILED DESCRIPTION - Preparation of an alpha -cyclopropylcarbonyl-2-fluorobenzyl halide of formula (I) comprises:    (A) reacting cyclopropyl-2-fluorobenzyl ketone (II) and a catalyst while blending in a solvent-free medium, and controlling the reaction temperature to 0-70 degrees C; and    (B) reacting with a halogenating reagent for 0.5-3 hours.    X=Cl or Br.
NOVELTY - Alisol C monoacetate is prepared by extracting Alisma orientalis with ethanol using microwave, recycling ethanol and concentrating; performing countercurrent extraction with ethyl acetate-water mixed solvent, recycling solvent and concentrating; adsorbing through macroporous absorption resin, eluting with 50-80% ethanol, collecting eluent, and concentrating; adding on silica gel chromatographic column, using methanol-ethyl acetate mixed solvent to elute, and concentrating eluents of eighth to twelfth parts of column volume; and adding methanol to crystallize, washing and drying.    USE - Method for preparing alisol C monoacetate (claimed).    ADVANTAGE - The method has convenient operation, less pollution and low energy consumption, and obtains alisol C monoacetate having high purity and suitable for industrialized production.    DETAILED DESCRIPTION - Preparation alisol C monoacetate comprises: (A) adding 6-10 times 60-85% ethanol into Alisma orientalis, feeding in microwave extraction device to extract with microwave at 300-600 W for 1-3 times for 3-10 minutes each time, combining the extract liquor, decompressing and recycling ethanol and concentrating; (B) performing 5-8 stages of countercurrent extraction with ethyl acetate-water mixed solvent (10:2), combining the extract liquor, decompressing and recycling the solvent and concentrating; (C) adsorbing through macroporous absorption resin, eluting with 50-80% ethanol, collecting 3-8 times eluent, decompressing and recycling ethanol and concentrating; (D) adding on silica gel chromatographic column, using methanol-ethyl acetate mixed solvent (5:1) to elute, collecting the eluent according to column volume, combining the eluents of the eighth to twelfth parts of column volume, and concentrating; and (E) adding methanol to crystallize, separating and crystallizing, washing and drying to obtain the product.
NOVELTY - A seed treatment comprises before seeding, weighing 5% uniconazole powder and corresponding amount of seeds; adding the mixture into a plastic bag, weaving bag, or a container; bundling a bag and sealing the container; mixing uniconazole powder and seed uniformly; and seeding.    USE - Method for seed treatment, preferably for the conditions of use amount of seed in a unit of area less than 20 kg and small-scale crop production with families as a unit (claimed).    ADVANTAGE - The method helps crops grow strongly using uniconazole; uses less amount of medicines; provides no pollution and low cost; is acceptable by farmers; and saves water and reduces operation.
NOVELTY - Charging device for methane production by straw fermentation comprises charging barrel, charging oil cylinder, and piston. First feeding hole, second feeding hole, first discharging hole, and second discharging hole are arranged on the charging barrel. The piston is provided in the charging barrel and fixed on a telescopic rod of the charging oil cylinder. The piston divides the charging barrel into a left cavity and a right cavity. The first feeding hole and first discharging hole are formed on the left cavity.    USE - Charging device for methane production by straw fermentation.    DETAILED DESCRIPTION - Charging device for methane production by straw fermentation comprises charging barrel, charging oil cylinder, and piston. First feeding hole, second feeding hole, first discharging hole, and second discharging hole are arranged on the charging barrel. The piston is provided in the charging barrel and fixed on a telescopic rod of the charging oil cylinder. The piston divides the charging barrel into a left cavity and a right cavity. The first feeding hole and first discharging hole are formed on the left cavity. The second feeding hole and second discharging hole are formed on the right cavity. The first and second feeding holes are communicated with a straw storage pool. The first and second discharging holes are communicated with methane fermentation tank. First valve, second valve, third valve, and fourth valve are arranged on the first feeding hole, first discharging hole, second feeding hole, and second feeding hole, respectively.
NOVELTY - Highway plants waste movable composting device comprises electric generator, centrifugal fan, ventilating duct, and composting body. The ventilating main pipe is connected with the centrifugal fan. The electric generator and centrifugal fan are detachable and movable to realize multi-point composting on the highway at the same time.    USE - Highway plants waste movable composting device used to obtain compost product, which can be directly used as highway greening soil (claimed).    ADVANTAGE - The device has low cost and simple structure, realizing convenient installation and reuse; uses forced ventilation for oxygen supply, satisfying the oxygen need for compost, degradation, and decomposition, thus, shortening the composting period; and solves the problems of resource waste and environmental pollution caused by highway plants waste. The composting materials are fully degraded after aerobic degradation and the compost product meets the quality standards and organic fertilizer standard.
NOVELTY - The biomass fuel comprises (pts. wt.): printing and dyeing sludge (20-40), sawdust (20-40) and flour factory waste (30-60).    USE - Biomass fuel.    ADVANTAGE - The fuel has thermal value of less than or equal to 6000 kcal/kg and has low unit thermal cost. The sulfur content is lower than 0.02%. The fuel is clean energy. The method can make printing and dyeing sludge be harmless, reduced and recycled completely. It realizes targets of treating wastes with wastes and recycling wastes by processing printing and dyeing sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the biomass fuel which comprises uniformly agitating printing and dyeing sludge, sawdust and flour factory waste, preparing the mixed material; fermenting prepared mixed material for 20-50 hours at normal temperature; and extruding and granulating mixed material, controlling water content to 15%, and preparing biomass fuel.
NOVELTY - Continuously converting oil into fatty acid esters of low-carbon alcohol comprises conveying low-carbon alcohol and oil in a volume ratio of 0.5-1:1 into a pre-heater by using a constant flow pump, preheating and mixing, and immediately conveying into a large aperture tubular reactor sectionally filled with solid acid and solid alkali, reacting at 120-140 degrees C for 2-5 minutes, where the pressure drop between the material inlet and material outlet is 5-8 MPa and continuously converting the oil into fatty acid esters of low-carbon alcohol.    USE - The method is useful for continuously converting oil into fatty acid esters of low-carbon alcohol.    ADVANTAGE - The method: is suitable for conversion of oil with high acid value; has no restriction on the acid value of the raw material oil, high contact rate between the low-carbon alcohol and oil, and also between the reactant and catalyst surface; has high reaction rate and controllable processing parameters; and continuously converts the oil into fatty acid esters of low-carbon alcohol with high efficiency.
NOVELTY - Preparation of biogas and bio-dry ice using water hyacinth includes pretreating water hyacinth and pumping into methane fermentation tank, preparing methane gas, removing hydrogen sulfide, carbon monoxide, nitrogen, and oxygen; preparing biogas by compressing filtered gas, passing amine liquid to remove carbon dioxide, removing water by molecular sieve, and finally through the mixed refrigerant liquefaction process, filling to obtain biogas; and preparing bio-dry ice by collecting amine liquid, introducing into compressor by buffer tank, pressing, and cooling to obtain liquid carbon dioxide.    USE - Preparation of biogas and bio-dry ice using water hyacinth (claimed).    ADVANTAGE - The method improves biogas utilization rate and greatly improves production efficiency.    DETAILED DESCRIPTION - Preparation of biogas and bio-dry ice using water hyacinth includes pretreating water hyacinth and pumping into methane fermentation tank, preparing methane gas, and removing hydrogen sulfide, carbon monoxide, nitrogen, and oxygen; preparing biogas by compressing filtered gas at 3.0-4.0 MPa (gauge), passing amine liquid to remove carbon dioxide, removing water by molecular sieve, and finally through the mixed refrigerant liquefaction process, filling to obtain biogas; and preparing bio-dry ice by collecting amine liquid, introducing into compressor by buffer tank, pressing, and cooling to obtain liquid carbon dioxide, i.e. bio-dry ice.
NOVELTY - Functional bacterial composition comprises five microorganisms chosen from Bacillus cereus, B.subtilis, calcium acetate Acinetobacter and denitrified Paracoccus. The above-cited microorganisms are cultured by sampling the microorganisms in target environment, culturing the microorganisms in culture medium, separating target strain, subjecting the target strain to index analysis, identifying species of target strain and optimizing the separated strain.    USE - The functional bacterial composition is useful for processing sewage.    ADVANTAGE - The composition exhibits rapid proliferation of bacteria for decomposing organic substances in sewage, removes phosphorus in sewage, meets national emission standards, and reduces sludge.
NOVELTY - Preparing biodiesel, by preparing Acer truncatum oil, mixing A.truncatum oil with methanol and alkaline catalyst, subjecting the mixture to esterification reaction, reacting the mixture, adding concentrated sulfuric acid to the mixture, washing the mixture, adding weak alkali solution to the mixture, stirring the mixture, precipitating the mixture for separating series of grains, washing the obtained material, subjecting the crude methyl ester layer to flash evaporation, collecting the fractions from the product, and obtaining the biodiesel.    USE - The method is useful for preparing biodiesel.    ADVANTAGE - The method is simple and enables high yield of biodiesel to 90% or more.    DETAILED DESCRIPTION - Method of preparing biodiesel, involves (a) preparing Acer truncatum oil, (b) mixing (parts weight) A.truncatum oil (100) with methanol (30-40) at a concentration of 99.5% or more and alkaline catalyst (1.0-2), subjecting the mixture to esterification reaction, reacting the mixture at 70-75 degrees C for 2-3 hours, adding concentrated sulfuric acid (4-6) to the mixture, and washing the mixture for removing byproducts of the reaction after 2.5-3 hours of esterification reaction, (c) rising the temperature of the reaction product to 67-73 degrees C, adding weak alkali solution (0.05-0.15) at the concentration of 4-8% to the mixture, rising the temperature of the mixture to 90-95 degrees C, stirring the mixture at 50-60, preferably 15-20 revolutions/minutes and 90-95 degrees C for 3-8 hours, maintaining and precipitating the mixture for separating series of grains completely, and washing the obtained material using warm water, and (d) subjecting the crude methyl ester layer to flash evaporation using dehydrator at 1000-2000, preferably 1-200 Pa, collecting the fractions from the product at 135-220 degrees C, and obtaining the biodiesel.
NOVELTY - Method for preparing biodiesel by continuous ester exchange of oil, involves using mixed solvent containing (in wt.%) furfuryl alcohol (5-15), butanone or acetone (50-90) and 4-7C hydrocarbons (5-15), where the whole weight of the raw materials is 100%.    USE - The method is useful for preparing biodiesel.    ADVANTAGE - The biodiesel has proper boiling point and cost, and can be recycled easily. The lower alcohol and the mixed solvent can be recycled and reused.
NOVELTY - Chemical synthesis of dehydroepiandrosterone comprises providing acetic acid pregnancy double enol ketone as raw material, and performing oximation, rearrangement, hydrolysis and refining.    USE - The method is useful for chemical synthesis of dehydroepiandrosterone.    ADVANTAGE - The method is simple with mild reaction condition; produces product of high yield; and causes less pollution in the environment.
NOVELTY - The reducer has a sink overflow part connected with a main body. A crushing space and a sedimentation space are formed inside the main body. A high speed grinding part is provided with a grinding blade that is rotated by a motor. The crushing space is connected to the sink overflow part. A precipitation part is provided with a filter box. A stir edge separates pulverized food waste that is ejected from the high speed grinding part. A microorganism feeding hopper supplies microorganism to the food waste that is pulverized between the precipitation part and high speed grinding part.    USE - Food trash reducer for a sink.    ADVANTAGE - The reducer prevents fine particle food waste in purification function degradation and bad small generation of a sewage treatment apparatus. The reducer improves high speed grinding part.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a food trash reducer.
NOVELTY - The apparatus has a solid-liquid separator separating waste from a dry digestion tank according to solid material and fluid organic waste. An input hopper injects sewage sludge, food waste and high-concentrated organic waste from livestock excretions. An input hopper injects sewage sludge, food waste and high-concentrated organic waste from the livestock excretions. A raw material storing unit stores the high-concentrated organic waste. A tub heats and crushes the high-concentrated organic waste through heat supplied from outside. A mixer mixes the high-concentrated organic waste.    USE - Dry-wet serial anaerobic digestion apparatus for producing biogas.    ADVANTAGE - The apparatus reduces installation and operating costs. The apparatus reduces processing time. The apparatus is simple in structure and simple to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a dry-wet serial anaerobic digestion method for producing biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a dry-wet serial anaerobic digestion apparatus.'(Drawing includes non-English language text)'
NOVELTY - A method for pre-treating glycerin-containing waste involves heating glycerin-containing waste. Methanol (3 wt.%) which is generated with biodiesel manufacture process is removed, an acid is added into the glycerin-containing waste, and fatty acid and matter-of-non-glycerin (MONG) component are separated from the waste.    USE - Method for pre-treating glycerin-containing waste that is used as carbon source for culture medium in bio-ethanol manufacturing process.    ADVANTAGE - The method enables pre-treating glycerin-containing waste in an efficient manner.
NOVELTY - Method for producing biodiesel, involves pre-treating biomass by removing chlorophyll and cell wall from concentrated microalgae, extracting bio-oil from the biomass, esterifying the bio-oil using alcohol in the presence of acid catalyst, isolating deoxidized bio-oil, subjecting the deoxidized bio-oil to trans-esterification for separating unpurified biodiesel, and removing impurities from the unpurified biodiesel to synthesize biodiesel.    USE - The method is useful for producing biodiesel (claimed) used as alternate energy for fossil fuels.    ADVANTAGE - The method produces biodiesel using microalgae that are capable of growing in a small space regardless of climate condition or environment chosen from sunlight, moisture content and carbon dioxide, and hence it supports stable supply of the diesel. The method is environmentally-friendly, cost effective and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDDENT CLAIM is included for biodiesel obtained by the above-mentioned method.
NOVELTY - The apparatus (500) has a reaction bath (510), where range biogas is generated from an anaerobic digester. A culture medium (520) is added to the reaction bath to cultivate microorganisms. The cultivated microorganisms remove hydrogen sulfide from the biogas. A primary valve (530) blocks the biogas to flow out from the reaction bath. A secondary valve (540) blocks flow of air into the reaction bath. A tertiary valve (580) discharges purification biogas generated in the reaction bath to a biogas reservoir. A controller (560) controls on/off states of the valves.    USE - Hydrogen sulfide removal apparatus for a biogas plant used at e.g. domestic animal farmhouse and village unit energization business area.    ADVANTAGE - The apparatus reduces the hydrogen sulfide content in the biogas to less than 10 parts per million (ppm), thus preventing corrosion of apparatus during biogas conversion process. The system has reduced investment cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a hydrogen sulfide removal apparatus.'(Drawing includes non-English language text)'    Hydrogen sulfide removal apparatus (500)    Reaction bath (510)    Culture medium (520)    Primary valve (530)    Secondary valve (540)    Controller (560)    Tertiary valve (580)
NOVELTY - A biogas manufacturing method involves hydrolyzing organic waste by irradiating ultrasound, and subjecting the hydrolyzed organic waste to anaerobic fermentation process.    USE - Method for manufacturing biogas.    ADVANTAGE - The method enables manufacturing biogas in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for biogas production apparatus.
NOVELTY - Pre-treatment of waste water during production of atrazine comprises (i) performing air rectification to recycle ethylamine and isopropamide from the waste water, and (ii) analyzing atrazine in the recycled waste water in presence of an acid.    USE - The method is useful for the pre-treatment of the waste water during production of atrazine.    ADVANTAGE - The method: is simple and easy; changes wastes of the waste water into resources; enables direct application of ammonium salt, which is recycled during the air rectification, and the direct application of atrazine in to processing of atrazine wettable powder; produces less than 3 mg/l of atrazine in the waste water, which meets plant discharging standards in the national heterocyclic pesticides and industrial water pollutant discharge standards; removes more than 75% of chemical oxygen demand; improves bio-chemical feasibility; and reduces subsequent bio-chemical load.
NOVELTY - An acid is added to mother liquor obtained from cephalosporin production unit, and the mother liquor is distilled. Alkali is added to the distilled mother liquor, and light component is collected at the top of the tower, and heavy component is supplied to the tower. The material from the tower is supplied to sub-rectifying tower, to recover isopropanol solution. The recovered isopropanol solution is supplied to a pervaporation membrane separator, and the recovered isopropanol product is supplied to the cephalosporin production unit and recycled as solvent.    USE - Recovery of waste isopropanol solvent during production of cephalosporin.    ADVANTAGE - The waste isopropanol solvent is efficiently recovered using simple method.    DETAILED DESCRIPTION - An acid is added to mother liquor obtained from cephalosporin production unit to adjust pH to 2-4, to remove organic alkali component from the solvent. The resulting mixture is heated, and the mother liquor is distilled at 70-100 degrees C. Alkali is added to the distilled mother liquor to adjust the pH to 8-11, to further remove the organic acid component from the solvent. The mother liquor is placed in a rectifying tower for rectification separation, and the light component is collected at the top of the tower, and the heavy component is supplied to the tower. The material from the tower is supplied to sub-rectifying tower, to recover isopropanol solution. The recovered isopropanol solution is supplied to a pervaporation membrane separator for alcohol-water separation, and the product is dewatered. The recovered isopropanol product is supplied to the cephalosporin production unit and recycled as solvent.
NOVELTY - A combustible gas is produced by adding water regulator and malt to sludge discharged to adjust water content to 40-65%, mixing, subjecting mixture to aerobic fermentation, pressing to form into blocks, and subjecting to a gasification furnace for high or mild temperature pyrolysis and gasification under the condition of restraining ventilation.    USE - Method of producing a combustible gas.
NOVELTY - The device has a large size waste reservoir (B) storing large size combustible waste. A large size waste crusher (C) shatters the large size combustible waste that is stored in the large size waste reservoir. A waste crusher (E) shatters waste that is stored in a waste reservoir (A). A magnetic separator (G) removes ferrous metal from a crushed material that is ejected from the waste crusher. A near infrared ray optical selector (I) removes PVC from the crushed material that is ejected from the grain size screen. A dryer (L) is provided with a gas disposal equipment part (S).    USE - Solid fuel waste pre-treatment device.    ADVANTAGE - The device has better reliability. The separate crusher can crush the large size and general waste, so that the device secures stability of the process. The filter bag is provided with the dryer, so that the device prevents fire accidents in a better manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a solid fuel waste pre-treatment device.    Waste reservoir (A)    Large size waste reservoir (B)    Large size waste crusher (C)    Waste crusher (E)    Magnetic separator (G)    Near infrared ray optical selector (I)    Dryer (L)    Gas disposal equipment part (S)
NOVELTY - Cow dung-carbon reaction tank comprises a reaction tank (1) and a flue device (2), where the flue device is installed at the center of the reaction tank. The flue device comprises a combustion furnace (21) and a chimney channel (22). The chimney channel is installed on the combustion furnace.    USE - Used as a cow dung-carbon reaction tank.    ADVANTAGE - The device solves the problem of environmental pollution caused by cattle dung discharge by converting the waste into manure.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the cow dung-carbon reaction tank.    Reaction tank (1)    Flue device (2)    Combustion furnace (21)    Chimney channel (22)
NOVELTY - Method for extracting heavy metal from protein food using diluted acid, involves crushing the protein food to obtain crushed protein food, adding diluted acid to the crushed food and extracting the metal from solution, and removing insoluble material, ultra filtering the metal and concentrating the solution.    USE - The method is useful for extracting heavy metals from protein food chosen from aquatic food and agricultural food and used for sample pre-treatment of heavy metals using enzyme linked immunosorbent assay. The aquatic food is oyster, shrimp, fish or shellfish and agricultural food is chicken, duck, goose, pig, ox or sheep (all claimed). The heavy metals are copper, lead and cadmium.    ADVANTAGE - The method has mild reaction condition, is environmentally-friendly, convenient and rapid compared to existing method, as it uses enzyme linked immunosorbent assay.
NOVELTY - A fuel ethanol is prepared by hydrolyzing green algae powder under an acidic condition to obtain hydrolyzate containing monosaccharide substance; and performing anaerobic fermentation to the hydrolyzate containing the monosaccharide substance with zymophyte, separating and purifying to obtain the ethanol.    USE - Method for the preparation of fuel ethanol (claimed).    ADVANTAGE - The method has wide range of raw materials.
NOVELTY - Sewage treatment tank comprises a tank body with a cavity, where the tank body comprises a top cover, and the inner wall of the top cover and the tank body form a cavity. The cavity is provided with a microwave transducer, which is arranged on the lower surface of the top cover. The top cover is provided with a through hole, which is inserted with medicinal pipe. The medicinal pipe passes into through hole cavity.    USE - Used as a sewage treatment tank.    ADVANTAGE - The tank utilizes microwave wave radiation for treating sewage; and improves the sewage processing efficiency, and reduces the sewage processing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the sewage treatment tank.
NOVELTY - The slot machine has an electrolytic tank that is provided with an electrode connected with vehicular power supply of hydrogen-oxygen outlet. An electrolytic cell is divided into independent slots equipped with electrode plate. The electrode plate is electrically connected with the electrode. The hydrogen gas outlet of tank is arranged outside the electrolytic cell.    USE - Slot machine for vehicle.    ADVANTAGE - The slot machine prevents voltage fluctuation and generates stable current.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolytic cell.
NOVELTY - Sludge washing and biological treatment system comprises sludge washing pool, organic sludge sedimentation tank and sewage well, which have buried design. The sludge washing pool is sloped from bottom of sludge inlet end surface to its lowest part. It has lowest bottom provided with sludge pump and pipeline. The organic sludge sedimentation tank is adjacent to sludge washing pool. The lowest bottom of sludge washing pool is lower than washing tank so that it shares partition wall with precipitating pool, which is provided with washing mud outlet.    USE - Sludge washing and biological treatment system.    ADVANTAGE - The sludge washing and biological treatment system adopts new-type engineering underground, has concrete structure, and low construction cost. It biologically dries dehydrated sludge with high processing efficiency, fast speed, low cost, and provides high yield of biogas and organic fertilizer.    DETAILED DESCRIPTION - Sludge washing and biological treatment system comprises sludge washing pool, organic sludge sedimentation tank and sewage well, which have buried design. The sludge washing pool is slope from bottom of sludge inlet end surface to its lowest part. It has lowest bottom provided with sludge pump and pipeline. The organic sludge sedimentation tank is adjacent to sludge washing pool. The lowest bottom of sludge washing pool is lower than washing tank so that it shares partition wall with precipitating pool, which is provided with washing mud outlet. The organic sludge sedimentation tank is provided with sludge inlet which is connected with sewage well. The sewage well is lower than washing sludge inlet of organic sludge sedimentation tank. It is provided with sewage pump which is connected with sludge inlet and sewage processing system or sewage sedimentation tank sludge washing pool through pipeline.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of sludge washing and biological treatment system.
NOVELTY - Straws are mixed with carbon, dried, provided in hollow bars and pressed. The resultant product is subjected to destructive distillation and carbonization. The resultant product is cooled to obtain porous straw coke. The resultant product is crushed and sieved. The resultant product is mixed with obtained wooden coke, alumina powder and additive in ratio of 3:2:0.05. The mixed product is reacted in a trolley-type high-temperature reaction furnace at 1460-1950 degrees C for 3-10 hours, to obtain greyish-green crystals or powdered hydrolytic coal.    USE - Manufacture of hydrolytic coal e.g. greyish-green hydrolytic coal or yellow crystal hydrolytic coal used for generation of combustible gas e.g. methane in hydrolysis reaction for cooking gas.    ADVANTAGE - The method is economical, and provides hydrolytic coal by simple process.    DETAILED DESCRIPTION - Straws of rice, wheat, maize, bean, potato, oil material and cotton and carbonized. The straws are mixed with carbon and dried. The resultant product is provided in a hollow bars having diameter of 60-80 mm, and pressed at 250-300 degrees C and at pressure of 125-130 MPa. The resultant product is subjected to destructive distillation at 600-700 degrees C for 1-2 hours and carbonization. The resultant product is cooled to room temperature to obtain porous straw coke. The resultant product is crushed and sieved using 40-80 mesh sieve. The resultant product is mixed with obtained wooden coke, alumina powder and additive in ratio of 3:2:0.05. The mixed product is reacted in a trolley-type high-temperature reaction furnace at 1460-1950 degrees C for 3-10 hours, to obtain hydrolytic coal.
NOVELTY - Treating farm manure sewage produced by manure water-soaking process comprises (i) separating solid and liquid from manure sewage to form solid and sewage, (ii) regulating the solid to be solid leavening having the solid content of 6-12%, (iii) carrying out anaerobic fermentation for the solid leavening to produce bio-gas residue, bio-gas liquid and bio-gas, (iv) carrying out anaerobic fermentation for the sewage produced in step (i) and the bio-gas liquid produced in step (iii) to produce bio-gas and aqueous fertilizer, and (v) collecting the bio-gas.    USE - The method is useful for treating farm manure sewage produced by manure water-soaking process.    ADVANTAGE - The method can improve bio-gas output by 15-30%, and saves anaerobic reactor volume by 50-80%; can produce bio-gas residue fertilizer to assure fertilizer sterilizing effect; and does not need to change the breeding mode or control water content of pig manure.
NOVELTY - The device has a filter removing foreign substance from air, and a heater heating the air. A microorganism culture part cultures high temperature aerobic microorganism by using the heated air, where the microorganism is one among bacillus stearothermophilus bacillus subtilis, bulgaricus, clostridium thermosaccharolyticum, desulfotomaculum nigricans, lactic acid bacteria, acidophilus or plantarum. A speed-up unit speeds up the microorganism culture part. Fine charcoal i.e. oak charcoal, powder is filled inside a chamber, where particle size of the powder is 5-10 mm.    USE - Device for fermenting excrement of high temperature aerobic microorganism e.g. bacillus stearothermophilus, bacillus subtilis, bulgaricus, clostridium thermosaccharolyticum, desulfotomaculum nigricans, lactic acid bacteria, acidophilus and plantarum (all claimed). Can also be used for fermenting excrement of a livestock.    ADVANTAGE - The device can improve temperature ramp-up rate of an inner aeration tank part by circulating pressure of the air inside the aeration tank part. The device ensures that fermentation efficiency of the microorganism and livestock excretions can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a high temperature aerobic microorganism excrement fermenting device.
NOVELTY - The plant includes reaction and storage tanks, control panels, mixers, filters, pipes, a gas compressor, a gas boiler and lamps.    USE - Plant, particularly mobile plant for transesterification of vegetable oils and animal fats via basic catalysis for obtaining biofuel.    ADVANTAGE - The plant ensures improving structure of the plant.
NOVELTY - The system has a water pump (22) pumping effluent from an effluent waterspout (10). An extractor (50) is provided with a settling tank (30) that is connected to make the effluent flow to a medicine storage tank (24). An inline mixer (20) coheres with the effluent to remove impurities. A solid-liquid separation part is provided with the settling tank to transfer the effluent to a pumping water treatment tank (40). Sludge is precipitated from the settling tank for dehydrating and separating the effluent into a cake condition. The inline mixer is provided with multiple vents (26).    USE - Waste water treatment system.    ADVANTAGE - The system increases precipitation efficiency without providing separate sludge thickener, and maintains drainage in a better manner. The system is economic to use with a simple structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a waste water treatment system.'(Drawing includes non-English language text)'    Effluent waterspout (10)    Inline mixer (20)    Water pump (22)    Medicine storage tank (24)    Vents (26)    Settling tank (30)    Pumping water treatment tank (40)    Extractor (50)
NOVELTY - The system has a pre-processor pre-processing a biomass to iron ion containment solution. A fuel cell portion stores the iron ion containment solution. The pre-processor generates another iron ion containment solution that is made to flow into a cathode chamber of the fuel cell portion. The fuel cell portion is provided with the cathode chamber, a cathode, a proton exchanging membrane, an anode and a bipolar chamber. A power of hydrogen (pH) range of the iron ion containment solution is 3 to 5. An openable partition wall separates the pre-processor and the cathode chamber.    USE - Bio mass pretreatment system.    ADVANTAGE - The system generates electricity in a better manner. The mass fabrication process reduces iron ion trivalency, so that the system preprocesses the biomass in a better manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass pretreating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bio mass pretreatment system.'(Drawing includes non-English language text)'
NOVELTY - The apparatus has a collection screw (242) collecting a fermentation product that is piled up by a bucket conveyor (244). A fracturing bucket drum (246) crushes the fermentation product in front of the collection screw. Multiple fracturing buckets (248) are formed in a surface of the fracturing bucket drum. The fracturing buckets are spirally arranged in a side end shift of the fracturing bucket drum. Multiple vertical screws are formed in front of the fracturing bucket drum. A sparger is formed in front of the fracturing bucket drum.    USE - Fermentation material e.g. livestock waste, organic sludge, rice hulls, sawdust and food waste, composting machine.    ADVANTAGE - The apparatus facilitates mixing of the fermentation product by diffusing the liquid organic compound, thus preventing generation of bad smell in the fermentation product.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a fermentation material composting machine.    Collection screw (242)    Bucket conveyor (244)    Fracturing bucket drum (246)    Fracturing buckets (248)    Scattering wing (254)
NOVELTY - The equipment has a sub-frame (2) fixed in upper parts of a waste matter storage tank according to a rail (60). An upper frame part (10) is mounted on a top part of the sub-frame. A bucket unit (20) is provided with a bucket part (23). A rotation part (24) is connected to the bucket part whose side is supported in the upper frame part. Multiple buckets (21) are equipped with a chain (23a) in a constant interval. A rotary unit (30) is installed at a side lower part of the upper frame part. A controller controls the bucket, rotation part, and the rotary unit.    USE - Compost raw material e.g. food waste, sawdust, and rice hulls or oil cake of rice bran, manufacturing equipment.    ADVANTAGE - The equipment is simple in structure and convenient to maintain and repair.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of a compost raw material manufacturing equipment.    Sub-frame (2)    Upper frame part (10)    Bucket unit (20)    Buckets (21)    Bucket part (23)    Chain (23a)    Rotation part (24)    Rotary unit (30)    Rail (60)
NOVELTY - The system has a mixed tide (130) connected to an air-conditioner (400) and a fermentor (140). Strip lines (160, 170) are respectively formed in the air-conditioner and the fermentor. Bio-gas (30) is generated in food (100) and the fermentor. The strip lines are emitted through an exhaust line (300). A scrubber (40) and a regenerative part (50) are connected to an atmosphere unit. The bio-gas is generated in an anaerobic digester (210). The bio-gas is utilized as electric power supply in the system.    USE - Waste food recycling system.    ADVANTAGE - The system processes rubbish of food like after dehydration process and ensures that food waste can be utilized as compost with the fermentor. The system enables transfer of fermentation adulteration process of a succeeding bath in a simultaneous manner with an air conveyer so as to reduce cost and space requirements in an effective manner. The system recycles biogas by a transfer line and enables generation of the bio-gas from the anaerobic digestion part for digesting anaerobic so as to avoid generation of bad smell gas during emission process. The system processes the rubbish, which emits unpleasant odor to atmosphere in a sealed state. The generator is driven by liquefied natural gas fuel, thus avoiding the need for a separate refining equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a waste food recycling system.'(Drawing includes non-English language text)'    Bio-gas (30)    Scrubber (40)    Regenerative part (50)    Food (100)    Mixed tide (130)    Fermentor (140)    Strip lines (160, 170)    Anaerobic digester (210)    Exhaust line (300)    Air-conditioner (400)
NOVELTY - The apparatus has a reaction bath provided with an influx of carbon dioxide inclusion biogas from an anaerobic digester. An ultrasonic generator (730) generates ultrasound to feed water, and generates steam at an inner side of the reaction bath. A partition wall (740) is mounted at the inner side of the reaction bath in a zigzag manner to form a movement route of the carbon dioxide inclusion biogas. A purging station (720) purifies the feed water flowing into the reaction bath. The ultrasonic generator is operated at room temperature.    USE - Methane gas purifying apparatus for a biogas production system.    ADVANTAGE - The apparatus separates carbon dioxide from the biogas produced from organic waste, so that energy production efficiency and methane gas purity are increased. The carbon dioxide is reused, and the greenhouse gas exhaustion is suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a methane gas purifying apparatus.'(Drawing includes non-English language text)'    Purging station (720)    Ultrasonic generator (730)    Partition wall (740)
NOVELTY - Alkali-free imatinib (I) is prepared by subjecting N-(5-(4-(4-methylpiperazine methyl benzamido)-2-methyl phenyl)-4-(3-pyridyl)-2-pyrimidinamine) (II) and p-chloromethyl benzoyl chloride (III) to amidation under alkaline condition in organic solvent, and directly adding N-methyl piperazine (IV) into the reaction to perform alkylation.    USE - Method for preparing alkali-free imatinib (I) (claimed).    ADVANTAGE - The method can purify intermediate without separation along with short step, simple reaction condition, simple post-treatment, easy control of the whole reaction operation and low apparatus requirement. It is suitable for industrial production. The used solvent has low price, and it can be recycled. The solvent has low toxicity, less pollution, low energy consumption, low cost, high total yield and good quality.
NOVELTY - Catalyst is an activated carbon catalyst having specific surface area of 700-900 m2/g, methylene blue adsorption of larger than 158 mg.g, iodine adsorption of greater than 749 mg.g, and phenol adsorption of greater than 179.5 mg.g.    USE - Catalyst for synthesis of glyphosate (claimed).    ADVANTAGE - The catalyst reduces the generation of formic acid during the synthesis of glyphosate, thus, reducing the impurity generation and improving the synthesis yield of glyphosate. The glyphosate synthesis using the catalyst realizes energy conservation; is environmentally friendly; and achieves production cost reduction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesis of glyphosate using the catalyst comprising providing catalyst and N-phosphonomethyliminodiacetic acid at 0.05-0.15:1 weight ratio; mixing with water; obtaining N-phosphonomethyliminodiacetic acid slurry; putting the slurry into a high-voltage reactor; increasing temperature to 45-65 degrees C; adding oxidizing agent at 0.2-1.0 MPa; oxidizing until the transformation rate of N-phosphonomethyliminodiacetic acid is greater than 99.5%; crystallizing by decreasing the temperature of the oxidized material and filtering; using deionized water to wash the filter cake; replacing the mother liquor; obtaining filter cake A and filter liquid A; using water to dissolve the filter cake A; obtaining slurry material; adding alkali material to dissolve the glyphosate; filtering; and obtaining filter cake B and filter liquid B, which is the glyphosate solution.
NOVELTY - A thiophanate-methyl raw material is prepared by using water-soluble solvent as reaction solvent.    USE - Method for preparing thiophanate-methyl raw material (claimed).    ADVANTAGE - The main raw material sodium thiocyanate does not need to be dried again. The original moisture requirement is less than 0.2%, which greatly saves energy consumption and saves large amount of physical labor. The usage amount of catalyst is reduced to about 1/4 of original amount, thus smell in the product disappears, which is benefit for applying drug to the product. The product is converted without large amount of water, thus greatly reducing wastewater amount; and is more green and environment-friendly. The method does not need cooking, thus avoiding appearance of secondary products, reducing product cost, and greatly improving product yield, product quality and product content. The product content is improved to average of 98.6% from original 97%, part of content reaching 99%.
NOVELTY - The unit has a storage unit supplying dry sludge to a grinding part. An input part quantitatively supplies pulverized dry sludge to an airstream transport unit. A feed port injects the dry sludge in a furnace to a fuel mixing combustion part, which is connected to an airstream transport unit. An airstream transport unit is consecutively supplied with transported fluid. A coal thermoelectric power generation fuel mixing combustion part is positioned at a rear side of a coal supply pipe. The airstream transport unit transports multiple transport pipes.    USE - Dry sludge combustion processing unit for generating coal thermoelectric power generation fuel.    ADVANTAGE - The unit is environment-friendly. The unit improves smooth exhaustion, and prevents blockage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a dry sludge combustion processing unit for generating coal thermoelectric power generation fuel.'(Drawing includes non-English language text)'
NOVELTY - An air purifier comprises (in parts weight) acetic acid (1-3), ethanol (15-20), butane (0.1-0.5), essence (0.1-0.4) and water (8-15).    USE - Air purifier.    ADVANTAGE - The air purifier efficiently absorbs dissociative formaldehyde in the air, benzene, ammonia and organic material, and kills bacteria, and is environmentally-friendly.
NOVELTY - Antiwear agent comprises biodiesel and its derivative. The biodiesel comprises aliphatic ester A generated from reaction of animal fat and vegetable oil, and microalgae grease and microorganism grease with low-carbon alcohol having carbon chain length of 1-5. The biodiesel derivative is dibasic alcohol aliphatic ester B obtained by performing ester exchange reaction of aliphatic ester A with one or two of glycol, propylene glycol, butylene glycol, pentyl glycol and condensed glycol.    USE - The antiwear agent is useful for petroleum diesel oil (claimed).    ADVANTAGE - The agent reduces emission of harmful substance, is environmentally-friendly, and improves lubricating property of diesel fuel.    DETAILED DESCRIPTION - Antiwear agent comprises biodiesel and its derivative. The biodiesel comprises aliphatic ester A generated from reaction of animal fat and vegetable oil, and microalgae grease and microorganism grease with low-carbon alcohol having carbon chain length of 1-5. The biodiesel derivative is (a) dibasic alcohol aliphatic ester B obtained by performing ester exchange reaction of aliphatic ester A with one or two of glycol, propylene glycol, butylene glycol, pentyl glycol and condensed glycol, (b) monosubstituted or disubstituted amide C generated from reaction of aliphatic ester A and diethanol amine, (c) polyalcohol ester D formed by reaction of aliphatic ester A with glycerol, sorbitol, xylitol, glucitol and polysaccharide alcohol, or (d) mixture of dibasic alcohol aliphatic ester B, monosubstituted amide or disubstituted amide C and polyalcohol ester D. An INDEPENDENT CLAIM is included for method of using the antiwear agent for petroleum diesel oil, which involves adding the antiwear agent to above-mentioned petroleum diesel oil, where content of the anti-wear agent in the petroleum diesel oil is 0.8-5 wt.%, and content of the biodiesel derivative in the diesel fuel is 50-500 ppm.
NOVELTY - The system has a preprocessor drying delivered vegetable material and removing residual moisture from a vegetable material carrier. A milking machine compresses the vegetable materials by rotating a screw, and is installed at a lower part of the preprocessor. Multiple precipitators precipitate vegetable oil obtained from the milking machine through a milking discharger, and a refiner separates residue component contained in the vegetable oil. A pump is connected to a circulating pipe via which an end is connected to an inner side of the precipitator.    USE - Bio-fuel manufacturing system for a vehicle.    ADVANTAGE - The system reduces fuel manufacturing cost, and generates environment-friendly fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bio-fuel manufacturing system.
NOVELTY - The apparatus has a petroleum fluid reservoir tub (20) equipped with a heating unit (21). An animal fat storage tank (10) stores domestic animal fat. The animal fat is dissolved with a petroleum oil treatment reagent for generating bio fuel and heated at 80-170 centigrade degrees by the heating unit. A vent (22) ejects the dissolved mixing bio fuel. An animal fat supply tube (70) is arranged at a lower part of the fluid reservoir tub. A residual solid material exhaust part (40) is equipped at a lower part of a sieve part (30). A condenser (60) is fixed to a pressure control valve (50).    USE - Domestic animal fat mixing bio fuel producing apparatus.    ADVANTAGE - The apparatus ensures better fuel combustibility by utilizing the domestic animal fat, thus reducing fuel production cost. The apparatus is inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a domestic animal fat mixing bio fuel producing apparatus.    Animal fat storage tank (10)    Petroleum fluid reservoir tub (20)    Heating unit (21)    Vent (22)    Sieve part (30)    Residual solid material exhaust part (40)    Pressure control valve (50)    Condenser (60)    Animal fat supply tube (70)
NOVELTY - An olmesartan medoxomil is prepared by alkylating an imidazole derivative and phenyl derivative in an organic solvent in the presence of alkali to obtain product A; hydrolyzing obtained product A; adding a dioxolane derivative; esterifying the mixture; and removing triphenylmethyl protective group from the obtained product.    USE - Method of preparing an olmesartan medoxomil.    ADVANTAGE - The method prepares product having high content and impurity of less than 0.1%, can be applied to industrial production, has mild reaction condition, does not use highly toxic solvent, and is environment-friendly.    DETAILED DESCRIPTION - An olmesartan medoxomil is prepared by alkylating an imidazole derivative of formula (I) and phenyl derivative of formula (II) in an organic solvent in the presence of alkali to obtain product A; hydrolyzing obtained product A; adding a dioxolane derivative of formula (III); esterifying the mixture; and removing triphenylmethyl protective group from the obtained product.
NOVELTY - Preparing 5-chloro-3-(1-(pyrrolidin-1-ylmethyl)-1,2,3,4-tetrahydroisoquinoline-2-carbonyl)-2,3-dihydro-1H-inden-1-one tartarate (I), comprises reacting 1-(pyrrolidin-1-ylmethyl)-1,2,3,4-tetrahydroisoquinoline (III) with 6-chloro-3-oxo-2,3-dihydro-1H-indene-1-carboxylic acid (IV) in presence of thionyl chloride as condensing agent, triethylamine as acid-binding agent and 4-dimethylaminopyridine as catalyst to obtain 5-chloro-3-(1-(pyrrolidin-1-ylmethyl)-1,2,3,4-tetrahydroisoquinoline-2-carbonyl)-2,3-dihydro-1H-inden-1-one (II) and reacting it with tartaric acid to obtain (I).    USE - (I) is useful for treating analgesia.    ADVANTAGE - The method: utilizes easily available raw materials; has convenient post-treatment; produces product with high yield; avoids the use of toxic reagent potassium cyanide; and meets the requirements of green chemistry.    DETAILED DESCRIPTION - An INDEPENDENT Claim is also included for preparing the compound (IV).
NOVELTY - The device has a filter tube inserted into a reactor part. A mesh unit is formed in a right angle existence part to filter a foreign substance. A reactant supply unit reacts through multiple continuous reactor parts. A pump unit is included in the reactant supply unit to supply the reactor part, which mixes a maintenance supplying material with alcohol. The filter tube is detachably connected to the right angle existence part through an insertion type. A single frequency is generated in a microwave generator part.    USE - Continuous flow heating biodiesel manufacturing device.    ADVANTAGE - The device improves production yield of the substitute fuel, thus improving reaction efficiency. The device separates stirring unit with the need of raw material. The device utilizes the miniature microwave generator, thus reducing production cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a continuous flow heating biodiesel manufacturing device.
NOVELTY - The method involves using an equivalent pressure sample injecting mode with a large flow blowing substituting sampling. A quantifying tube is filled with 7N electronic grade hyperpure ammonia to fast detect impurity concentration variation. A sample to be detected is placed into a separating system that is processed under an anticorrosion anti-absorption treatment. Trace impurity is separated. The sample to be detected is input into a direct current discharging helium ionization detector (DID) to obtain an analyzing result.    USE - Method for analyzing 7N electronic grade hyperpure ammonia trace impurity.    ADVANTAGE - The method enables providing stable state analyzing value in short time with precision quantification so as to provide low detection limit and short analyzing cycle.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a quantifying tube.
NOVELTY - The fermenter has a fermenter body arranged in an inner side of a main body. A heater is arranged in an outer side of the main body. A heating pipe laying part is installed at a side of the main body. An upper side of the main body is provided in an inner surface of a heat insulator. Multiple holes are formed in the main body. An inner surface of a cover is formed in the fermenter body. A heat insulator is arranged in exterior of the main body. An inner surface of the heat insulator is installed at the inner surface of the cover.    USE - Fermenter for use in a biogas manufacturing device.    ADVANTAGE - The fermenter improves thermal efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a fermenter of the biogas manufacturing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a fermenter.
NOVELTY - The system has a biomass feeder supplying a biomass and connected to an upper side of a rapid thermal disintegration reaction device. A fluid yarn feeder supplies a fluid yarn at high temperature of the rapid thermal disintegration reaction device, which is piled to a lower part of the fluid yarn. A transporter is transferred to an outer side of the rapid thermal disintegration reaction device. The fluid yarn is transferred by a transporter in the fluid yarn feeder with a cyclic supply part. A heating slope part is formed in a reactor main body.    USE - Bio-stock manufacturing system.    ADVANTAGE - The system improves rapid thermal degradability of the biomass, and reduces manufacturing cost. The system is simple in structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a bio-stock manufacturing system.
NOVELTY - The digester has a granule sludge placed in a reaction bath (100). Dehydrogenase (DHA) is provided in the granule sludge. An ultrasonic oscillator (210) is installed at a lower layer of the reaction bath, and irradiates ultrasound to increase activity of biogas producing microorganism and mobility of the granule sludge. A controller (300) controls operation time interval of the ultrasonic oscillator.    USE - Anaerobic digester.    ADVANTAGE - The digester prevents compaction of the granule sludge according to increase activity of methane gas production bacteria by setting up the ultrasonic oscillator so as to increase biogas creation amount. The digester increases mobility of the granule sludge, thus ensuring process efficiency of the digester with high organic loading rate and processing organic wastage of high volatility suspension concentration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an anaerobic digester.    Reaction bath (100)    Ultrasonic oscillator (210)    Controller (300)
NOVELTY - The machine has a coking chamber (10) provided with carbonized rubbish that is put into a stirrer (20). The stirrer is installed inside the coking chamber. A combustion chamber (30) is arranged with a stack of the coking chamber. A dry distillation gas unit (40) is connected with the coking chamber and the combustion chamber. A gas resolution part (50) is installed inside the combustion chamber. An electric heater heats a lower part of the coking chamber, an outer wall side of a lower flank and multiple electro thermal pins.    USE - Rubbish e.g. food wastes, domestic waste and polymer rubbish, carbonizing machine. Uses include but are not limited to an apartment, a hospital, a school, an army unit, a government office, a hotel, a book province, a warship, an excursion ship, a large-scale populating facility including a merchant ship, a living equipment and a living space.    ADVANTAGE - The machine has high thermal efficiency, and avoids generation of noise, smoke, contaminant and toxic gas. The machine is environmental-friendly. The machine avoids leakage of gas, smoke and tar during packing of coking chamber melting away to superheat. The machine can automically perform heating, drying and discharge process of carbide and carbonization. The machine can process all kinds of food wastes, domestic waste and polymer rubbish. The machine is easy and convenient to install and operate. The machine reduces purchase and running cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a rubbish e.g. domestic waste.    Coking chamber (10)    Stirrer (20)    Combustion chamber (30)    Dry distillation gas unit (40)    Gas resolution part (50)
NOVELTY - Preparation of lidocaine comprises preparing intermediate acetyl chloride-2,6-dimethylaniline from raw materials of 2,6-dimethylaniline and chloroacetic chloride; and carrying out a reaction between the generated intermediate and diethylamine to obtain the lidocaine. Acetone is employed as a solvent and carbonate as a catalyst in the reaction process.    USE - Preparation method of lidocaine.    ADVANTAGE - The method is simple and suitable for industrial application; and employs non-toxic and non-irritating acetone as solvent which is capable of being recycled, thus, is environmentally-friendly. Complex steps of washing with acid firstly and washing with alkaline secondly in intermediate post-processing are not required, which avoids unnecessary loss. Thus, yield coefficients of the intermediate and the lidocaine are both relatively high which achieve more than 99%.
NOVELTY - Preparing prilocaine or prilocaine hydrochloride comprises (a1) adding the prilocaine intermediate alpha -chloro-o-propionamido-methylbenzene and potassium carbonate to acetone in turn, or (a2) adding o-toluidine and potassium carbonate to acetone, slowly dropping alpha -chloro-propionyl chloride to ice water bath, controlling the temperature in the flask within 30 degrees C, removing the ice water bath after dropping, and taking reaction at room temperature (b) adding propylamine, heating to 70 degrees C, reflowing, and (c) treating so as to obtain the prilocaine or prilocaine hydrochloride.    USE - Preparation method of prilocaine.    ADVANTAGE - The method replaces the low-toxic methylbenzene solvent that is not friendly to the environment of the traditional method with basically non-toxic environment-friendly common solvent acetone. The environment-friendly prilocaine hydrochloride can be industrially produced without influencing the yield.
NOVELTY - The cab aerosol consists of 9 percent menthol, 0.7 percent sucrose fatty acid monoester, 17 percent C2-C4 alkane and water.    USE - Cab aerosol.    ADVANTAGE - Provides cab aerosol that is reasonably prescribed and provides good use effect while being low in production cost.
NOVELTY - Roller lifting machine for lifting machine or roller comprises a drive hydraulic cylinder (7), which is connected with an oil cylinder swinging arm (4). The oil cylinder swinging arm is connected with a lifting shaft (3). The two lifting swinging arms (5) are fixedly connected to the lifting shaft. The two lifting pull rods (6) are connected with the two lifting swinging arms. The lifting shaft is connected with a roller.    USE - Used as a roller lifting mechanism for lifting machine or roller for an organic compost production machine which turns, stirs and aerates material.    ADVANTAGE - The roller lifting mechanism ensures same amplitude of the two lifting arms through the rotating lifting shaft, and hence enables double-side lifting or falling from the same height.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the roller lifting mechanism for lifting machine or roller.    Lifting shaft (3)    Oil cylinder swinging arm (4)    Lifting swinging arms (5)    Lifting pull rods (6)    Drive hydraulic cylinder (7)
NOVELTY - Double-effect bio-gas purifier comprises a biogas input pipe (2) arranged on a primary purifier assembly (8) and a secondary purifier assembly (7). The biogas input pipe is connected to the primary purifier assembly through a primary submersible pipe (8-2). The end of the primary submersible pipe is provided with a primary filtering film (8-4). The top of the primary purifier assembly is connected to the top of the secondary purifier assembly through a primary purify gas pipeline. The secondary purifier assembly is provided with a secondary purifying gas tube and a submersible pipe.    USE - Used as a double-effect bio-gas purifier.    ADVANTAGE - The device is economical, has anticorrosive property, and improves the operation efficiency.    DETAILED DESCRIPTION - Double-effect bio-gas purifier comprises a biogas input pipe (2) arranged on a primary purifier assembly (8) and a secondary purifier assembly (7). The biogas input pipe is connected to the primary purifier assembly through a primary submersible pipe (8-2). The end of the primary submersible pipe is provided with a primary filtering film (8-4). The top of the primary purifier assembly is connected to the top of the secondary purifier assembly through a primary purify gas pipeline. The secondary purifier assembly is provided with a secondary purifying gas tube and a submersible pipe. The primary purifier assembly is provided with a secondary filter. The submersible pipe is connected to the lower end of the secondary filter. The submersible pipe is provided with a second-stage filter membrane    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the double-effect bio-gas purifier.    Biogas input pipe (1)    Secondary purifier assembly (2)    Primary purifier assembly (8)    Primary submersible pipe (8-2)    Primary filtering film (8-4)
NOVELTY - High recovery device comprises more than 60 units of gas washing tower, recovery tower, and bag-type filter which is provided with air outlet. The air outlet is connected with air compressor.    USE - High recovery device.    ADVANTAGE - The high recovery device has simple structure, collects clean air in high altitude, directly uses effluent filtering, and has low air processing cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of high recovery device.
NOVELTY - Dry fermentation organic garbage processor comprises belt conveyor, feed hopper with conical tip at lower part, U-shaped heating pipe steam heating device, hydrolysis acid production reactor, solid infiltration bed, spray pipe, liquid two-phase anaerobic reactor, membrane filter, and dryer which are orderly connected.    USE - Dry fermentation organic garbage processor.    ADVANTAGE - The garbage processor is safe and provides highly efficient recycling and treatment of organic garbage.
NOVELTY - The system has a circulation valve that is connected to a supply line structure for circulating the enriched water to a buffer tank (400). The buffer tank is connected to a concentration hydraulic class line structure and a concentration hydraulic class line structure so that the enriched water is flowed into an acid fermenter (200) and a digeater (300).    USE - Organic waste treatment system.    ADVANTAGE - The volume of the enriched water within the buffer tank is decreased than the volume of the methane fermentation liquid within the buffer tank, and the stirring effect of the buffer tank is improved. The separation effect of the solid-liquid separating film tub is improved, and the enriched water is ejected at a high concentration. The gas generation amount is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic waste treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of organic waste treatment system. (Drawing includes non-English language text)    Acid fermenter (200)    Digeater (300)    Buffer tank (400)    Solid-liquid separating film tub (500)    Permeated water storage tank (520)
NOVELTY - The gasifier (10) has microalgae feeder (20) that is provided with feed pump (23) installed on flow path of microalgae reservoir (21). A microalgae supply tube (22) is provided for transferring the stored microalgae to supercritical reactor and microalgae supply tube. A supercritical reactor (30) is provided with synthetic gas exhaust pipe (33) ejecting the synthetic gas generated in reaction bath (31) for gasifying the microalgae supplied from microalgae supply tube. A furnace (32) installed in reaction bath applies heat in reaction bath for supercritical reaction.    USE - Supercritical water gasifier for synthetic gas conversion of microalgae.    ADVANTAGE - The synthetic gas conversion process of microalgae can be performed with simple structure and reduced energy production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthetic gas production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of supercritical water gasifier.    Gasifier (10)    Microalgae feeder (20)    Microalgae reservoir (21)    Microalgae supply tube (22)    Feed pump (23)    Supercritical reactor (30)    Reaction bath (31)    Furnace (32)    Synthetic gas exhaust pipe (33)
NOVELTY - The burner has a dryer (10) which is provided at a center portion of a drying room (20). The drying room is segmented by a board. A rice hull coking chamber (40) is provided at left and right portions of a box type construction structure. A rice hull carbonizing machine (30) is built in the rice hull coking chamber. The radiant heat from the rice hull coking chamber is directly acted on the drying room.    USE - Carbonized rice hull burner.    ADVANTAGE - The production yield of the carbonized rice hull can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the carbonized rice hull burner.    Dryer (10)    Drying room (20)    Rice hull carbonizing machine (30)    Rice hull coking chamber (40)    External casing (50)
NOVELTY - An organic nitrogen source of yeast culture medium is produced by (A) after collecting algal bloom microalgae biomass, 2-4 times cleaning by tap water, and performing solid-liquid separation by filtering; (B) mixing separated wet biomass and processing liquid at ratio of 1:3 in stainless steel container, heating, stirring, controlling temperature at 70-95 degrees C for 2-4 hours; and (C) filtering, separating and collecting supernatant, performing decoloration, vacuum drying and crushing treatment to obtain the product.    USE - Method for producing organic nitrogen source of yeast culture medium (claimed).    ADVANTAGE - The method can reclaim nitrogen element in raw material of microalgae biomass in high level and realize resource utilization of the waste.
NOVELTY - Preparing firewood bar from cassava slag comprises taking the wet cassava slag generated in the cassava starch producing process as initial raw material, drying the material to form dry slag and molding the dry slag to obtain firewood bars. The moisture content in the dry slag is 10-15% and the temperature is 230-280 degrees C during the molding of dry slag into bars.    USE - The firewood bar is useful for producing charcoal (claimed).    ADVANTAGE - The prepared firewood bar and charcoal product obtained from firewood bar has excellent biomass energy i.e. low ash content, low sulfur content, low carbon content and high heat productivity. The method is suitable for industrialized process to obtain dry slag, firewood bar, and charcoal and form a cyclic economical and ecological chain of cassava slag-biomass energy, thus is environmental-friendly.
NOVELTY - The device has reaction chamber (2,3) contacted with air storage tank (1) through gas pipeline (4). The air storage tank gas pipeline is provided with an emptying valve (6) and gas outlet valve (7). A reaction chamber and air storage tank gas pipeline is provided with emptying valve (8) and air outlet valve (9). The reaction chamber and reaction room are connected through ferment liquid reflux pipe (5). A ferment liquid reflux pipe is provided with a stop valve (10).    USE - Anaerobic fermentation device for producing biogas of straw.    ADVANTAGE - The operation and structure of fermentation device can be simplified. The efficiency of fermentation device can be improved. The cost of fermentation device can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic fermentation device for producing biogas of straw.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the fermentation device.    Air storage tank (1)    Reaction chamber (2,3)    Gas pipeline (4)    Ferment liquid reflux pipe (5)    Emptying valves (6,8)    Gas outlet valve (7)    Air outlet valve (9)    Stop valve (10)
NOVELTY - Processing waste water generated in preparation of citric acid comprises filtering the waste water by using a membrane with a bore diameter of 0.1-0.6 mu m. The waste water contains citric acid, hetero acids, organic pigments, calcium salts and fermentation residues.    USE - The method is useful for processing waste water generated in the preparation of citric acid.    ADVANTAGE - The method for preparing citric acid increases the cyclic utilization efficiency of waste water, effectively reduces the usage of raw material, saves energy, reduces the emission and it is economical. The method for processing is simple, easy and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the citric acid, comprising mixing the starch material with water to get a starch slurry, performing enzymolysis on the starch slurry, and inoculating Aspergillus niger in the fermentation culture medium containing the enzymolysis product, and fermenting to produce citric acid, where the water is the processed waste water.
NOVELTY - Producing ethanol fuel using large seaweed biomass as raw material, involves (a) cleaning large algal biomass, and crushing biomass to obtain mash liquid, (b) crushing the mash liquid, adding hydrolysis catalyst to the liquid, hydrolyzing the biomass to obtain mash liquid, and regulating pH, (c) adding activated carbon and zeolite or adsorption resin to the liquid, (d) sterilizing the processed liquid, (e) hydrolyzing the liquid, and (f) inoculating fermenting strain, and stirring or shaking the liquid.    USE - The method is useful for producing ethanol fuel.    ADVANTAGE - The method improves fermentation of microorganism with respect to algal biomass conversion, when compared with existing technology, has excellent conversion efficiency, preferably 48% or more, and mass produces ethanol.    DETAILED DESCRIPTION - Method for producing ethanol fuel using large seaweed biomass as raw material, involves (a) cleaning large algal biomass, removing surface impurity, crushing the biomass to particle having diameter of 50 mm, and crushing the obtained particle to obtain mash liquid, where the weight ratio of seaweed biomass dry weight to water is 1:10-1:30, (b) crushing the mash liquid, adding hydrolysis catalyst to the liquid, hydrolyzing the biomass to obtain mash liquid, and regulating pH of hydrolysis mash liquid to 5-7, (c) adding activated carbon and zeolite or adsorption resin to the liquid, detoxifying the liquid for 20-300 minutes, and removing solid substance from the hydrolyzed mash liquid, (d) sterilizing the processed liquid, (e) hydrolyzing the liquid by adding nitrogen source substance (0.1-5 g/l), and (f) inoculating fermenting strain (0.5-5 g/l) to the liquid, fermenting the liquid at 30-35 degrees c, and stirring or shaking the liquid for 8 days.
NOVELTY - Method for producing butanol fuel using duckweed as raw material, involves preparing medium for fermentation, reducing viscosity of the fermentation culture medium, preparing butanol producing microbial seed liquid, inoculating the seed liquid, and fermenting the culture medium.    USE - The method is useful for producing butanol fuel useful in existing gasoline supply and distribution system and in combination with other biological fuels e.g. ethanol.    ADVANTAGE - The method is simple, cost-effective and can be easily industrialized. The butanol content in the fermented solution is 8.01-9.61 g/l, and is 63.77-67.84% of the total solvent. The concentration and fermentation yield of the fermentation final product is same as that obtained by using corn as raw material, and the ratio of the butanol in the total solvent is higher than that in the process involving corn as raw material.
NOVELTY - Pre-treating biomass gradient by vapor steaming comprises (i) introducing the biomass raw materials into a vapor steaming tank filled with gas medium, and carrying out vapor steaming; (ii) carrying out low pressure vapor steaming, then continuously filling gas medium for improving the cooking temperature and pressure; and (iii) processing gradient vapor steaming, releasing the raw materials either by discharging the materials with gas phase medium together, or after the gas phase medium is released, and collecting the materials from the vapor steaming tank.    USE - The method is useful for traditional brewing and degumming of the natural plant fiber.    ADVANTAGE - The method makes the biomass to withstand different temperature and pressure from low to high for a certain time; evenly heats the biomass, and thus improves the uniformity of the gas phase medium with material reaction, and the pre-processing effect.    DETAILED DESCRIPTION - Pre-treating biomass gradient by vapor steaming comprises (i) introducing the biomass raw materials into a vapor steaming tank filled with gas medium, and carrying out vapor steaming at a pressure of 0.2-0.7 MPa, and continuing vapor steaming for 4-60 minutes; (ii) carrying out low pressure vapor steaming, then continuously filling gas medium for improving the cooking temperature and pressure to 0.71-2.8 MPa, and continuing vapor steaming for 0.5-30 minutes; and (iii) processing gradient vapor steaming, releasing the raw materials either by discharging the materials with gas phase medium together, or after the gas phase medium is released, and collecting the materials from the vapor steaming tank.
NOVELTY - The method involves preparing fuel anode slurry, which is made of fuel anode active material, binder and solvent. A fuel anode active layer (110) is formed and arranged at a side of a supporter (120). The binder is dissolved, and the fuel anode active layer is formed by pre-processing a fuel cell (100). The binder is made of polymer and dissolved at 100-450 degree Celsius. The supporter is provided with a metal mesh and metal foam.    USE - Method for manufacturing a molten carbonate fuel cell anode.    ADVANTAGE - The method enables improving production yield of a molten carbonate fuel cell anode, reducing processing cost, and improving the performance and service life of the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell comprising a fuel anode.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a molten carbonate fuel cell anode.    Fuel cell (100)    Fuel anode active layer (110)    Supporter (120)
NOVELTY - Synthesizing pesticide herbicide intermediate ethylsulfonyl acetonitrile includes mixing sodium tungstate (ammonium tungstate), methyl trioctyl ammonium bisulfate, phenyl phosphinic acid and hydrogen peroxide, and reacting; at low temperature, slowly dripping ethylsulfanyl acetonitrile, and reacting; using ethyl acetate to extract the aqueous layer, and combining the organic phase; using sodium hydrogen sulfite to wash for once; drying anhydrous magnesium sulfate, filtering, decompressing and concentrating to obtain light yellow liquid ethylsulfonyl acetonitrile.    USE - Method for synthesizing pesticide herbicide intermediate ethylsulfonyl acetonitrile (claimed).    ADVANTAGE - The method is environment-friendly, has mild reaction conditions and simple operations, does not produce organic waste, and has easily controllable reaction, high product yield and content.    DETAILED DESCRIPTION - Synthesizing pesticide herbicide intermediate ethylsulfonyl acetonitrile comprises:    (A) mixing sodium tungsten oxide hydrate (ammonium tungsten oxide), (CH3(n-C3H17)3N)HSO4, and phenyl phosphinic acid and 30% of hydrogen peroxide, reacting for half an hour at room temperature;    (B) at low temperature, slowly dripping ethylsulfanyl acetonitrile, after finishing dripping, reacting for 3-7 hours at 25-90 degrees C; decreasing temperature to room temperature, moving it to an extracting bottle to layer;    (C) using ethyl acetate to extract the water layer for twice, combining the organic phase; using 3-5% of sodium hydrogen sulfite to wash for once; and    (D) drying anhydrous magnesium sulfate, filtering, decompressing and concentrating to obtain light yellow liquid ethylsulfonyl acetonitrile.
NOVELTY - The facility has filter and oil water separator which are located in oil collecting groove (10). Wastewater pump (12) is arranged between groove and settling tank (13). Oil pump (14) is arranged between settling tank and deodorization tank (15). Tail gas absorption system connected with filter, separator, settling tank, and deodorization tank, is comprised of absorption tower (18), filling tower and active carbon. Heating device of deodorization tank is controlled by water jet vacuum system. Residue processing system is comprised of conveyor (20) and filter (21).    USE - Industrial processing facility of catering waste.    ADVANTAGE - Catering waste are processed physically and chemically in sealed condition without waste gas, waste residue or wastewater emission. Waste grease is separated from the catering waste by separation, deodorization and discoloring technologies for producing biological diesel and lubricant. The wastes are recovered chemically and physically to obtain biomass and purified water during production. The secondary pollution during waste grease refining and separation is solved thoroughly. Waste water, waste gas and waste residue can be reused.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the industrial processing facility of catering waste. (Drawing includes non-English language text)    Oil collecting groove (10)    Wastewater pump (12)    Settling tank (13)    Oil pump (14)    Deodorization tank (15)    Absorption tower (18)    Conveyor (20)    Filter (21)
NOVELTY - A polybasic light coordinated hydride hydrogen storage material MCaAlH6 (I), is new.    USE - The polybasic light coordinated hydride hydrogen storage material is useful in hydrogen storage and fuel battery hydrogen supplying source (claimed).    ADVANTAGE - The method is cost-effective and suitable for large scale production, and requires less energy. The polybasic light coordinated hydride hydrogen storage material has excellent hydrogen discharging property.    DETAILED DESCRIPTION - A polybasic light coordinated hydride hydrogen storage material of formula: MCaAlH6 (I), is new.    M=alkali metal elements Li and Na.    An INDEPENDENT CLAIM is included for method for preparing the above-cited polybasic light coordinated hydride hydrogen storage material.
NOVELTY - The method involves generating synthetic gas through a biomass gasifier. Biodiesel fuel and the synthetic gas are sprayed to generate a wet cleaning medium for removing aero gel form heavy biomass tar. A hot synthesis gas containing cleaning medium is cooled by spraying water. The aero gel form heavy biomass tar is previously removed during biodiesel fuel jet cleaning process. The biodiesel fuel is cooled in a biodiesel fuel oil corp.    USE - Method for removing biomass tar in synthetic gas generated in a biomass gasifier.    ADVANTAGE - The method enables removing the biomass tar from biomass content in an effective manner, thus increasing detarring rate of the synthetic gas in the biomass content.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating biomass tar removing method.
NOVELTY - The apparatus has a decomposition tank filled with microorganism sludge and organic waste water. An acid formation tank (1) is provided for forming the sludge and organic waste water stream and hydrolysis acid. A methane generating tank (2) generates the wastewater streams and methane. A circulating pipe (3-1) transfers the waste water from the methane generating tank to the acid formation tank. A pressure pump (4) is fixed with the circulating pipe. A venturi tube (5) is equipped with the circulating pipe. Valves are fixed to the venturi tube for supplying the wastewater.    USE - Apparatus for disposing microorganism sludge and organic waste water.    ADVANTAGE - The apparatus has high organic wastewater and sludge decomposition efficiency and high sludge processing efficiency. The apparatus increases high biogas productivity, and avoids environmental pollution. The apparatus reduces generation rate of solid residue. The apparatus saves sewage treatment cost in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a microorganism sludge and organic waste water disposing apparatus.'(Drawing includes non-English language text)'    Acid formation tank (1)    Methane generating tank (2)    Circulating pipe (3-1)    Pressure pump (4)    Venturi tube (5)
NOVELTY - Method for preparing compost using dead livestock, involves grinding the dead livestock animals finely, adding silicic acid to the pulverized product, stirring the mixture using a stirring device and sterilizing pathogens in the obtained product, and compressing the product and separating sludge from the sterilized product.    USE - The method is useful for preparing compost using dead livestock animals e.g. cattle.    ADVANTAGE - The method prevents environmental contamination as the dead organic materials are degraded. The apparatus and the method are economical, easy for application in several places, and enable active management of unforeseen domestic animals ruin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for preparing the above-mentioned compost, which comprises a pulverizer for pulverizing dead livestock, specific silicic acid storage for sterilizing the pulverized livestock animals, pulverized livestock particles present at the lower portion of the specific silicic acid storage, a dissolving tank for performing primary sterilizing operation with respect to the pulverized dead livestock, and a pressurizing separator for generating sludge by pressurizing the sterilized dead livestock.
NOVELTY - The method involves collecting sewage sludge, gasoline and coal mixture. A phase of the mixture is generated by performing a drying process to irradiate microwave on the collected sewage sludge, gasoline and coal mixture. Coal and gasoline in the collected sewage sludge, gasoline and coal mixture are agitated. Hot air of microwave radiation is dried by a hybrid dryer. A stirring stage for the coal is provided with 200 meshes, where weight percent ratio of oil at the stirring stage and coal is 0.05-0.6:1, and weight percent ratio of sewage sludge and coal is 0.1-1:1.    USE - Fuel manufacturing method.    ADVANTAGE - The method enables improving the energy efficiency and easily performing the combustion process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of a fuel manufacturing method. '(Drawing includes non-English language text)'
NOVELTY - The method involves collecting and mixing sewage sludge, petrol and coal to form a mixture. High pressure synthetic gas is generated from the mixture through a hydrothermal reaction that is performed by reaction of catalyst i.e. coal.    USE - High pressure synthetic gas producing method.    ADVANTAGE - The method enables improving energy efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a high pressure synthetic gas producing method.'(Drawing includes non-English language text)'
NOVELTY - Method of producing intermediate of cephalosporin antibiotic derivative (I), involves adjusting pH using inorganic acid, deprotecting a protective group of carboxyl group, adding cresol or phenol to a compound (II) or adding sinta cross-linked enzyme crystal (CLEC)-plasminogen activator (PA) enzyme with adjusting pH with base, and agitating and deprotecting the protective group of amino group.    USE - The method is useful for producing intermediate of cephalosporin antibiotic derivative for treating laryngopharyngitis, acute bronchitis, tonsillitis, pneumonia and tympanitis caused by bacteria.    ADVANTAGE - The method is convenient to use, and environmentally-friendly, and has excellent stability, reproducibility, and actuality. The enzyme reduces time of the amino group deprotection rate, and improves the yield of the derivative.    DETAILED DESCRIPTION - Method of producing intermediate of cephalosporin antibiotic derivative of formula (I) by adjusting pH using inorganic acid, involves deprotecting a protective group of carboxyl group, adding cresol or phenol to a compound of formula (II) or adding sinta Cross-linked enzyme crystal (CLEC)-plasminogen activator (PA) enzyme with adjusting pH with base, and agitating and deprotecting the protective group of amino group.    R=H, prophenyl, and (4-methylthiazole-5-yl) vinyl;and    x=3-6.    INDEPENDENT CLAIMS are included for the following:    (1) method for producing crystallohydrate of the intermediate cephalosporin by the above-mentioned method; and    (2) cephalosporin derivative is produced using the CLEC-PA enzyme.
NOVELTY - The system has a feeder (1) powdering wastewater sludge, and another feeder (2) powdering a waste lime that is dried. A third feeder (3) grinds a waste coal, and a fourth feeder (4) grinds a food waste. A porous zeolite filter is provided with gas pollutants for filtering a fuel supplied from a fuel tank (13). A drier (12) purifies a gas ejected form a hot water boiler (14), where the gas is passed through a filter containing negative ion, activated charcoal and hydroxyl group and a dust collection purification unit (15).    USE - Wastewater sludge fuel resource system.    ADVANTAGE - The system is convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a wastewater sludge fuel resource system.    Feeders (1, 2, 3, 4)    Drier (12)    Fuel tank (13)    Hot water boiler (14)    Dust collection purification unit (15)
NOVELTY - The apparatus has a livestock excretion supply tube supplying livestock excretion liquid to an agricultural by-product influx container (110). An agricultural by-product is supplied to the influx container. A flower and bird hot painting part (120) heats the livestock excretion liquid. An anaerobic digestion tub (140) is provided with the agricultural by-product. The influx container comprises a cylinder hopper (111). A slope screw (121) is equipped in a lower part of the painting part. Two feeding lines (131, 132) are equipped at a side of a livestock excretion liquid made part (130).    USE - Agricultural waste and livestock excretions anaerobic absorption apparatus.    ADVANTAGE - The apparatus reduces residence time of the anaerobic digestion, thus improving anaerobic digestion efficiency, and hence increasing biogas productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an agricultural waste and livestock excretions anaerobic absorption method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of an agricultural waste and livestock excretions anaerobic absorption apparatus.'(Drawing includes non-English language text)'    Agricultural by-product influx container (110)    Cylinder hopper (111)    Flower and bird hot painting part (120)    Slope screw (121)    Livestock excretion liquid made part (130)    Feeding lines (131, 132)    Anaerobic digestion tub (140)
NOVELTY - The digester (400) has an anaerobic digester part (420) provided with a temperature tub. The temperature tub is heated with another temperature tub in order to remove pathogenic microorganism existing within an organic waste and hydrolyze. Another anaerobic digester part (430) is installed in order to collect biogas from the organic waste. A solar cell (410) converts solar energy into electric power. The former anaerobic digester part is maintained at temperature of 50-59 degree Celsius. The latter anaerobic digester part is maintained in the temperature of 30-40 degree Celsius.    USE - Anaerobic digester for producing biogas from organic waste.    ADVANTAGE - The digester is provided with high and middle temperature tubs, thus effectively producing energy from organic waste. The digester is operated without a separate energy source input, thus reducing operational cost.    DETAILED DESCRIPTION - Volume ratio of the anaerobic digesters is 1:4 to 2:4. Mixing ratio of the organic waste and food category waste is 80:20 to 40:60.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an anaerobic digester.'(Drawing includes non-English language text)'    Anaerobic digester (400)    Solar cell (410)    Anaerobic digester parts (420, 430)    Controller (440)
NOVELTY - Synthesizing tetrahydropyridine medicament, involves (a) adding carbene catalyst 3-benzyl-5-(2-hydroxyethyl)-4-methylthiazole chlorate, triethylamine, cyanobenzene and solvent into a vessel, (b) agitating and reacting the mixture at normal temperature, adding acrylonitrile into the vessel, and (c) reacting the mixture by heating or microwave radiation, evaporating the solvent, and recrystallizing using ethanol to obtain tetrahydropyridine medicinal molecule.    USE - The method is useful for synthesizing tetrahydropyridine medicament (claimed).    ADVANTAGE - The tetrahydropyridine is produced at high yield using environmental-friendly and non-toxic carbene catalyst. The tetrahydropyridine is produced rapidly at low energy consumption using simple microwave radiating method, and the product can be purified easily.
NOVELTY - An improved three formatting septic tank comprises a pool tank (1) having two baffles (2) and divided into first chamber (3), second chamber and third chamber having an outlet tube; an inlet pipe at outer side wall of the first chamber; and a biological filter screen clapboard (5). The two baffles have an overflow pipe (4).    USE - An improved three formatting septic tank.    ADVANTAGE - The tank discharges sewage that meets environment-friendly standard.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an improved three formatting septic tank.    Pool tank (1)    Baffles (2)    First chamber (3)    Overflow pipe (4)    Biological filter screen clapboard (5)
NOVELTY - Pre-treatment system comprises a stirring tank, a settling channel and an anaerobic acidification tank. The bottom end of the stirring tank is connected to the settling channel through a valve. The settling channel is equipped with a grid and a baffle, and is connected to the anaerobic acidification tank.    USE - The pre-treatment system is useful for preparing biogas.    ADVANTAGE - The pre-treatment system is simple, easy to operate and economical, requires no maintenance, reduces use of pumps, ensures natural flowing, achieves stirring and thus prevents blockage in the pumps, and conserves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the pre-treatment system for preparing the biogas.
NOVELTY - A straw biogas reactor comprises a liquid stirring tank and reactor. The top of reactor is provided with pH and temperature detectors, horizontal opening, inclined port, manhole, negative pressure protection port, overflow weir, and positive pressure protection device. The reactor has a central pipe provided with a branch pipe which is connected with a discharge pipe of material liquid tank by switching valve. The bottom of reactor is provided with heating device, discharge device, and liquid distribution pipe connected with feed liquid circulation pump through a distributor.    USE - Straw biogas reactor.    ADVANTAGE - The reactor generates gas stably with high efficiency and is suitable for large continuous biogas production.    DETAILED DESCRIPTION - A straw biogas reactor comprises a liquid stirring tank and reactor. A discharge pipe of feed liquid tank is connected with feed pump of feeding pipe. The top of reactor is provided with pH and temperature detectors, horizontal opening, inclined port, manhole, negative pressure protection port, overflow weir, and positive pressure protection device which is connected with upper part of material liquid tank through a conveying pipe. The reactor has a central pipe provided with a branch pipe which is connected with a discharge pipe of material liquid tank by switching valve. The upper end of central pipe has scum collecting port and scum suction, and the lower end of central pipe has a flow guide cone. The bottom of reactor is provided with heating device, discharge device, and liquid distribution pipe connected with feed liquid circulation pump through a distributor. The distributor is connected with an inclined back opening through circulation pipe and horizontal back opening. The material circulation pump is connected with the suction part of upper part of reactor through suction pipe.
NOVELTY - Method for performing enrichment culture of ammonia oxidizing bacteria, involves adding activated sludge with nitrobacteria to culture medium using landfill leachate as raw material, culturing for 5 days as culture cycle for one generation, and carrying out culture process for four-generations.    USE - The method is useful for performing enrichment culture of ammonia oxidizing bacteria.    ADVANTAGE - The method improves ammonia oxidizing efficiency of the bacteria cultured by landfill leachate by 20.9% compared with that of bacteria not cultured by landfill leachate. Economic and effective high-concentration nitrobacteria can be obtained and added to wastewater biological denitrification to improve denitrification efficiency to reduce process time, unnecessary project cost and open up new denitrification concept for denitrification process of sewage treatment plant.
NOVELTY - Resource utilization and zero contaminant discharge of a livestock and poultry farm involves separating dried and cleared excrement, urine and flushing water of the farm, performing mixed fermentation to the dried and cleared excrement and bran; circulating the urine and the flushing water in a methane tank to generate methane and methane liquid, where a part of methane liquid is added with rape seed extract; and adding straw into the other part of methane liquid to ferment to prepare mycoprotein. The residual methane liquid serves as the flushing water of the colony house of the farm.    USE - Resource utilization and zero contaminant discharge of a livestock and poultry farm.    ADVANTAGE - The method achieves zero contaminant discharge and is a green technique with comprehensive resource utilization and sustainable development.    DETAILED DESCRIPTION - Resource utilization and zero contaminant discharge of a livestock and poultry farm comprises separating dried and cleared excrement, urine and flushing water of the farm, performing mixed fermentation to the dried and cleared excrement and bran, where leavening is used for producing aquatic feed and fermentation can generate methane; and circulating the urine and the flushing water in a methane tank to ferment to generate methane and methane liquid. Part of methane liquid is added with rape seed extract to ferment to achieve detoxification of the rape seed extract. Other part of methane liquid is added with straw to ferment to prepare mycoprotein. The two fermentation treatment processes generate the methane. Residual methane liquid serves as the flushing water of the colony house of the farm by exposure, deodorization and sterilization.
NOVELTY - Sewage processing biological suspended filler comprises tubular base body (1) set in partition board (2) crossly distributed and connected with two ends of base wall. The base body is covered with at least one outer layer with good hydrophilic surface layer (3).    USE - Sewage processing biological suspended filler.    ADVANTAGE - The sewage processing biological suspended filler attaches more organisms and good for different microorganism growth.    DETAILED DESCRIPTION - The separating plate is cross-shaped while base body is round tubular or elliptical tubular.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of sewage processing biological suspended filler.    Base body (1)    Partition board (2)    Hydrophilic surface layer (3)
NOVELTY - A furnace portion water jacket is arranged on outside of furnace fire-proof lining. A high temperature carbon dioxide inlet is arranged over jacket. A carbonizing chamber roof is arranged over jacket. A suction gas pipe port is arranged in middle of side face of roof. A seal charging pipe is arranged in middle of upper portion of roof. The rotating shaft is arranged in middle of seal charging pipe. The rotating gear is arranged over shaft. The carbon scraper is arranged below shaft. A seal charging port is arranged in middle of seal charging pipe.    USE - H-type carbonizing furnace.    ADVANTAGE - The high temperature heat-energy of the carriers of the generated gases is used to produce biomass active carbons by performing a dry distillation to save the energy sources and to improve the heat value of the biomass gases. The H-type carbonizing furnace collects the wood tar of the gases by employing a dry process purification process and uses wood vinegar as an industrial chemical raw materials to convert the agriculture waste resources to industrial chemical raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing biomass active carbon and carbonizing fuel using H-type carbonizing furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the H-type carbonizing furnace.
NOVELTY - Method for producing biofuel from biomass material, involves (a) pyrolysing a first fraction of the biomass material having a lower pyrolysis temperature relative to the pyrolysis temperature of a second fraction of the biomass material to obtain a primary volatile fraction, and (b) separating the primary volatile fraction from the biomass material before pyrolysing the second fraction.    USE - The method is useful for producing biofuel.    ADVANTAGE - The method increases yield of biofuel to 65 wt.% or more, and decreases yield of tar to 15 wt.% or less, and produces less quantity of secondary products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system, which comprises heating unit for heating the biomass material located in a pyrolysis zone, where the heating unit is configured to selectively heat the biomass material to sequentially pyrolyse the first fraction of the biomass material and then the second fraction of the biomass material, and vapor removal unit for removing volatile fraction of the pyrolysis from the pyrolysis zone, where the vapor removal unit is configured to remove the volatile fraction between sequential heating of the first and second fractions of the biomass material.
NOVELTY - A thiazole amino acid salt type ionic liquid (I) is new.    USE - Thiazole amino acid salt type ionic liquid (I) used in medical chemistry, organic chemistry and industrial chemistry.    ADVANTAGE - The compound (I) exhibits environmental conservation, diversity, strong dissolubility and biocompatibility. It is more friendly and greener to the environment.    DETAILED DESCRIPTION - Thiazole amino acid salt type ionic liquid of formula A+M- (I) is new.    A+=formula (a);    R1-R3=1-20C hydrocarbons;    M-=amino acid negative ions.    An INDEPENDENT CLAIM is included for preparation of the compound (I).
NOVELTY - Producing low-carbon olefin, aromatic hydrocarbon and gasoline comprises using carbinol as raw material by molecular sieve based catalysts through methanol alkylation reaction and aromatization reaction. The aromatization reaction is used for aromatizing the methanol alkylation product to obtain the mixture among olefin, aromatic hydrocarbon and alkane. The mixture is separated for obtaining the low-carbon olefin, the aromatic hydrocarbon and the gasoline. The low-carbon olefin comprises ethylene, propylene and butane.    USE - Method for producing low-carbon olefin, aromatic hydrocarbon and gasoline (claimed).    ADVANTAGE - The method has low discharge, low pollution, low power consumption, and low production cost.    DETAILED DESCRIPTION - Producing low-carbon olefin, aromatic hydrocarbon and gasoline comprises using carbinol as raw material for producing low-carbon olefin, aromatic hydrocarbon and the gasoline by molecular sieve based catalysts through methanol alkylation reaction and aromatization reaction. The aromatization reaction is used for aromatizing the methanol alkylation product to obtain the mixture among olefin, aromatic hydrocarbon and alkane. The mixture is separated for obtaining the low-carbon olefin, the aromatic hydrocarbon and the gasoline. The low-carbon olefin comprises ethylene, propylene and butane. The aromatic hydrocarbon comprises benzene, toluene and dimethylbenzene.
NOVELTY - The apparatus has heating unit (C1) that is formed into heat pipe structure. A collecting pipe is in connection with heat pipe of heating unit. A warm water introducing pipe is in connection with heat pipe. One end of heat medium pipe is inserted into one end of heat pipe, while other end of heat medium pipe is sealed.    USE - Apparatus for preparing biogas from liquid organic waste.    ADVANTAGE - The energy consumption of the device is reduced while yield and quality of biogas are increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing biogas from liquid organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for preparing biogas from liquid organic waste.    Heating unit (C1)    Solar collector (D)    Thermal storage tank (E)    Extractor (J)    Sludge (L)
NOVELTY - A solid base catalyst comprises a basic material dipped in a zeolite.    USE - Solid base catalyst for manufacturing biodiesel (claimed).    ADVANTAGE - The catalyst has high reactivity, and improves productivity of biodiesel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for manufacturing a solid base catalyst.
NOVELTY - Compost pretreatment of city restaurant wastes comprises grinding the restaurant wastes using Pressafiner (RTM: screw press); then putting ground restaurant wastes, water adjusting auxiliary materials and organism adjusting auxiliary materials into a stirred tank with an agitator; and crushing, grinding and uniformly stirring the mixed materials to obtain composting pretreated substances.    USE - Method for compost pretreatment of city restaurant wastes (claimed).    ADVANTAGE - The method can conduct real-time and high-quality pretreatment of the restaurant wastes, which is beneficial for efficiently composting city restaurant wastes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for implementing the pretreatment method, comprising the Pressafiner (RTM: screw press) having discharge hole arranged above the stirred tank, and a vertical agitator blade arranged on a vertical stirred shaft in the stirred tank. Outer side of the vertical agitator blade is an inclined plane matched with inner wall of the stirred tank.
NOVELTY - An ignition charcoal manufacturing method involves permeating charcoal in an alcoholic solution.    USE - Method for manufacturing ignition charcoal.    ADVANTAGE - The method enables manufacturing the ignition charcoal in a simple manner while preserving the properties of the charcoal.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating a method for manufacturing ignition charcoal. '(Drawing includes non-English language text)'
NOVELTY - A petroleum contaminated site remediation method involves growing Catalpa and Platycladus orientalis in the contaminated area and treating the polluted area with an oil processing reagent. Biomass recycling method is also claimed.    USE - Method for remediation of petroleum contaminated site and for recycling biomass.    ADVANTAGE - The method effectively purifying the petroleum contaminated sites and also enables production of biofuel using the grown plants as raw materials. The method is simple and eco-friendly in nature.
NOVELTY - Dehydration device comprises stirring container for stirring concentrated solution after adding medicament; gravity concentration device disposed under or at one side of stirring tank; and concentrated liquid filtering device for separating mud and discharging water from concentrated solution.    USE - Dehydration device used for sludge treatment.    ADVANTAGE - The dehydration device is easy to clean, convenient to maintain, and has high dehydration efficiency. It provides water content of 35-55% after dehydration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of dehydration device.
NOVELTY - The system has a mold unit that includes upper and lower mold units filled with composite powder of resin and graphite. A charge unit (100) charges the composite powder and heating portion (200) heats the charged powder. A compression molding unit (300) pressurizes the mold unit and a cooling unit (400) cools the compressed mold unit. An extraction portion (500) extracts a separator from the mold unit.    USE - System for manufacturing separator for fuel cell. Uses include but are not limited to molten carbonate fuel cell (MCFC), phosphoric acid fuel cell (PAFC), solid oxide fuel cell (SOFC) polymer electrolyte membrane fuel cell (PEMFC), direct methanol fuel cell (DEFC) and proton exchange membrane Fuel Cell.    ADVANTAGE - Manufacture of the separator can be automated and mass production of fuel cell can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the separator manufacturing system. (Drawing includes non-English language text)    Charge unit (100)    Heating portion (200)    Compression molding unit (300)    Cooling unit (400)    Extraction portion (500)
NOVELTY - Biomass-gasified raw material is stirred and heated to obtain high-temperature coke oil gas. Particle size of 80% primary particles of biomass-gasified raw material is less than 2 mm. Particle size of 30% primary particles of biomass-gasified raw material is less than 0.5 mm. The obtained high-temperature coke oil is subjected to high-temperature cracking-gasification process by heating in presence of steam to obtain carbon monoxide, hydrogen and methane. Resultant product filtered and condensing purification process is performed to obtain intermediate calorific value gas.    USE - Biomass airfloation flow state high-temperature heat exchange gasification method.    ADVANTAGE - The method efficiently and economically provides gasified product having high thermal efficiency, calorific value and productivity.    DETAILED DESCRIPTION - Biomass-gasified raw material is stirred and heated at 800-1400 degrees C to obtain high-temperature coke oil gas. Particle size of 80% primary particles of biomass-gasified raw material is less than 2 mm. Particle size of 30% primary particles of biomass-gasified raw material is less than 0.5 mm. The obtained high-temperature coke oil is subjected to high-temperature cracking-gasification process by heating at 1000-1800 degrees C in presence of steam to obtain carbon monoxide, hydrogen and methane. Resultant product filtered and condensing purification process is performed to obtain intermediate calorific value gas. An INDEPENDENT CLAIM is included for device for biomass airflow state high-temperature heat exchange gasification method.
NOVELTY - The device has a cylindrical shaped electric furnace which is provided with a storage unit (1) and reactor (2). A small air pipeline (6) is connected to storage unit. The storage device is provided with a combustion chamber (3). Outer air pipeline (7) and steam pipeline (4) are connected to combustion chamber. A controller is provided with an electronic valve (9).    USE - Intermittent gas reforming device.    ADVANTAGE - The temperature of the catalyst bed can be improved. The conversion efficiency of the gas can be improved and energy consumption can be reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of intermittent gas reforming device. (Drawing includes non-English language text)    Storage unit (1)    Reactor (2)    Combustion chamber (3)    Steam pipeline (4)    Small air pipeline (6)    Outer air pipeline (7)    Electronic valve (9)
NOVELTY - Harvester capable of taking air hydrogen as an energy source in a power plant comprises a hydrogen fuel container (8) set into an air hydrogen fuel cell harvester (9) in a reserved position. The container is connected with hydrogen fuel cell (11) via a hydrogen fuel conveying pipe (10) and hydrogen fuel cell is connected with a motor (13) via a conductive wire. The motor is connected with mechanical transmission device via a power output shaft and transmission device drives other mechanical components e.g. an eccentric reel and harvester arranged above a harvesting platform.    USE - Used as a harvester capable of taking air hydrogen as an energy source in a power plant.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the harvester capable of taking air hydrogen as an energy source in a power plant.    Hydrogen fuel container (8)    Air hydrogen fuel cell harvester (9)    Hydrogen fuel conveying pipe (10)    Hydrogen fuel cell (11)    Motor (13)
NOVELTY - Treating fecal sewage from city public latrines and digestion tanks comprises using compound enzyme product containing special proteins and bio-enzymes extracted from the natural plants, and mainly comprising protease, amylase, lipase, cellulose, glucanase, glucose oxidase, maltase, and pectinase.    USE - Method for treating fecal sewage from city public latrines and digestion tanks, which is highly concentrated organic wastewater, and has high content of organic matters and complicated components.    ADVANTAGE - The method uses special proteins and bio-enzymes having unique biodegradation function and which can promote propagation of beneficial strains. The special proteins and bio-enzymes can cause the beneficial microorganisms in the fecal sewage to grow in the best environment. The biochemical treatment effect can reach the peak value, and the chemical oxygen demand, biochemical oxygen demand, total suspended solids and hydrogen sulfide can be removed.
NOVELTY - A coal-containing mixture comprises coal-containing powder, low-grade alkanol, inorganic alkali and tackifier.    USE - Coal-containing mixture used in liquefied product (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a preparation of coal-containing mixture comprising mixing coal powder with first mixture-containing low-grade alkanol, inorganic alkali and tackifier;and    (2) liquefying coal comprising mixing to prepare coal-containing mixture comprising coal powder low-grade alkanol, inorganic alkali and tackifier, and irradiating the coal-containing mixture via radio-frequency irradiation.
NOVELTY - A biomass cleaning diesel oil comprises (mass%) biological methanol (45-60), fuel ethanol (20-30), plant oil (30-50), and n-ethane (2).    USE - A biomass cleaning diesel oil.    ADVANTAGE - The oil saves energy, reduces emission of carbon dioxide, and eliminates the dependence to petroleum.
NOVELTY - A cation exchange membrane is produced by carrying out radiation graft polymerization of a vinyl monomer, a polymer or sodium styrene sulfate on the surface of nanofiber with a single process.    USE - Cation exchange membrane is used for fuel cell, gas separation material, carbon dioxide absorbent material, air purification material and sensor material.    ADVANTAGE - The cation exchange membrane has improved hydrogen ion conductivity and water absorption rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of cation exchange membrane.
NOVELTY - Lipidase (RTM: lipase from fungal origin) biological promoter (C1) comprises lipase, surfactant, and metallic ions.    USE - Promoter (C1) used for treating oil-containing wastewater (claimed).    ADVANTAGE - The promoter (C1) is suitable for biochemical treatment units of different types.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of promoter (C1) for treating oil-containing wastewater comprising directly adding (C1) into biological processing unit for treating oil-containing wastewater, where amount of (C1) is 1-5 mg/L of water; and naturally mixing under hydraulic function.
NOVELTY - The composite oxygen-enriched biomass gasification furnace has a furnace case (1) which is provided with a split pipe (7) and a gasification chamber (G). The split pipe and a space between the gasification chambers form a combustion chamber (3). The gasification chamber is arranged at a bottom of a chamber spiral and crushing device (19), an oxygen inlet (15) and a steam inlet (16). The gasification chamber and split pipe are equipped with a dust collecting cover (5). The split pipe is arranged at a lower portion of a collection hood (6).    USE - Composite oxygen-enriched biomass gasification furnace.    ADVANTAGE - The temperature of the gasification chamber of the composite oxygen-enriched biomass gasification furnace can be improved by eliminating the gasification of residual carbon and oxygen. Hence the gasification efficiency is improved. The amount of the tar in the furnace can be reduced by improving the cracking through the coke oil, thus the production yield of the gas can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the composite oxygen-enriched biomass gasification furnace.    Furnace case (1)    Combustion chamber (3)    Dust collecting cover (5)    Collection hood (6)    Split pipe (7)    Oxygen inlet (15)    Steam inlet (16)    Chamber spiral and crushing device (19)
NOVELTY - Hydrogen of 2 equivalent with respect to total hydrogen of 3 equivalent from a hydrogen reservoir is discharged by providing a catalyst (c1) to ammonia borane or an ammonia borane derivative which is hydrogen reservoir. The catalyst (c1) comprises complex compound catalyst (I).    USE - Generation of hydrogen from hydrogen reservoir used for hydrogen-using device e.g. vehicle comprising fuel cell e.g. polymer electrolyte fuel cell (all claimed).    ADVANTAGE - The method enables generation of hydrogen within short of time.    DETAILED DESCRIPTION - Hydrogen of 2 equivalent with respect to total hydrogen of 3 equivalent from a hydrogen reservoir is discharged by providing a catalyst (c1) to ammonia borane or an ammonia borane derivative which is hydrogen reservoir. The catalyst (c1) comprises complex compound catalyst of formula (I).    M=metal;    R1-R4=H, or hydrocarbyl or heterohydrocarbyl (both optionally substituted);    R5,R6=hydrocarbyl or H;and    X=halo, 1-20C alkyl, 7-30C aryl alkyl, alkoxy substituted by 1-20C alkyl, 3-20C alkyl-substituted siloxy or amido substituted by 1-20C hydrocarbyl.    INDEPENDENT CLAIMS are included for the following:    (1) device for generating hydrogen from hydrogen reservoir;    (2) complex compound catalyst (I); and    (3) hydrogen-using device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen generator. (Drawing includes non-English language text)
NOVELTY - Gas station suitable for rural area comprises a centralized biogas generator, a biogas desulfurization and dehydration unit, a liquefied petroleum gas supply device, a mixer, a gas tank and a flame arrester. The centralized biogas generator and biogas desulfurization and dehydrating device are connected to the liquefied petroleum gas supply device. The mixer is connected with the gas tank, which is connected to the user through the flame arrester.    USE - Used as a gas station suitable for rural area.    ADVANTAGE - The device is reliable, environment-friendly and energy-saving and has stable gas volume.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the gas station suitable for rural area.
NOVELTY - Kitchen organic waste purification recovery unit comprises an organic waste inlet (1) of a waste grinding system (2), a water separating chamber (3), a fermentation vessel (4), and a drying and sterilizing operation room (5). The grinding system is connected with the water separating chamber through a first channel. The water separating chamber is connected with a sewer pipeline through a second channel.    USE - Used as a kitchen organic waste purification recovery unit.    ADVANTAGE - The kitchen organic waste purification recovery unit can ferment and process organic waste into powder or granular fertilizer, eliminates environment odor, and reduces environment pollution.    DETAILED DESCRIPTION - Kitchen organic waste purification recovery unit comprises an organic waste inlet (1) of a waste grinding system (2), a water separating chamber (3), a fermentation vessel (4), and a drying and sterilizing operation room (5). The grinding system is connected with the water separating chamber through a first channel. The water separating chamber is connected with a sewer pipeline through a second channel. The dehydrated material passes through a third channel connected with the bottom of the of the fermentation vessel. The outlet of the fermentation vessel is set at the bottom of the drying and sterilizing operation room. The drying and sterilizing operation room is provided with an organic fertilizer outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the kitchen organic waste purification recovery unit.    Organic waste inlet (1)    Waste grinding system (2)    Water separating chamber (3)    Fermentation vessel (4)    Drying and sterilizing operation room (5)
NOVELTY - A straw carbon, gas and by-product recycling device comprises a carbonization furnace (1), a purifier (2), a decoking device (3), condensation separators(s) (4), a blower (5), a cyclone separator, a gas-liquid separator, gas purifier(s), gas-phase separator(s), and an air storage tank.    USE - A straw carbon, gas and by-product recycling device.    ADVANTAGE - The device can generate high quality combustible gas; and can produce charcoal, wood tar, wood vinegar and other byproducts.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a straw carbon, gas and by-product recycling device.    Carbonization furnace (1)    Purifier (2)    Decoking device (3)    Condensation separator (4)    Blower (5)
NOVELTY - A compost bottom negative pressure fermentation tank comprises a fermenting slot (1) internally provided with a stirrer (2) installed on a stirring device guide rail (3); and comprising a barrier (4) having an air hole divided into upper and lower parts. The upper part is a compost ferment pool. The lower part is an air channel (5) connected with an exhaust fan and an outdoor exhaust passage.    USE - A compost bottom negative pressure fermentation tank.    ADVANTAGE - The tank solves long groove odor discharge during anaerobic microorganism activity.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a compost bottom negative pressure fermentation tank.    Fermenting slot (1)    Stirrer (2)    Stirring device guide rail (3)    Barrier (4)    Air channel (5)
NOVELTY - Gas supplying system comprises double-purpose fixing combustion furnace, relay movable dry distillation kettle, cooling and purifying system, and air storage tank of power transmission and distribution system. The movable dry distillation kettle is set on double-purpose fixing combustion furnace. The movable dry distillation kettle is connected with cooling and purifying system by pipe. The cooling purifying system is connected with power transmission and distribution system.    USE - Gas supplying system used for co-production of biomass dry distillation carbon, gas, oil, and liquid.    ADVANTAGE - The double-purpose fixing combustion furnace provides continuous operation, and realizes self-heating source. The system is not set with large gas storage cabinet device having high utilization rate, thus less construction investment, no sewage discharge, energy-saving, and environment friendly.    DETAILED DESCRIPTION - The double-purpose fixing combustion furnace is composed of furnace shell, flue, furnace door, and gas burner. The furnace door is set on front surface of furnace shell. The flue is connected with upper part of furnace shell back. The gas burner is set on oven shell bottom burner and enters into combustion furnace. The gas burner is connected with gas outlet pipe array cooler and cylinder by gas pipeline. The top of relay movable dry distillation kettle is set with dry distillation kettle cover. The gas outlet pipeline is provided with gate valve. The cooling purifying system is provided with three-stage cooling, primary washing, three-stage separating, and two-stage purifying device. The system adopts increasing transmission and distribution main pipe as air storage tank and pressure network transmission process, such that transmission and distribution pressure (P) is not greater than 0.09 MPa.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of gas supplying system.
NOVELTY - A roller type aerobic fermentation treatment device comprises bracket and shell arranged on the bracket. The shell is divided into upper and lower shells, which are hinged and fastened by a fastening piece. A porous roller in the shell is arranged horizontally. Two ends of the porous roller are connected with 2 ends of the lower shell by a roller shaft. The roller shaft on an end is fixedly connected with a roller handle.    USE - Roller type aerobic fermentation treatment device for kitchen waste (claimed) useful for cultivating flowers and vegetables.    ADVANTAGE - The device has porous roller arranged horizontally, thus the stirring blade stirs and ferments the organic waste fully; and has simple structure and convenient use.    DETAILED DESCRIPTION - Roller type aerobic fermentation treatment device comprises bracket and shell arranged on the bracket. The shell is divided into upper and lower shells, which are hinged and fastened by a fastening piece. A porous roller in the shell is arranged horizontally. Two ends of the porous roller are connected with 2 ends of the lower shell by a roller shaft. The roller shaft on an end is fixedly connected with a roller handle. An inner side of the porous roller is axially and fixedly connected with a stirring blade shaft. A water outlet pipe is below the lower shell. A heater is between an inner side of the shell and the porous roller.
NOVELTY - The device has lead screw (18) whose forward and backward movement is freely possible. The heating portion (20) of the screw case (12) is foldably installed to achieve plasticity and pyrolysis of the workpiece, while the thermal medium heated within screw using separate heater (26) is circulated. The driving unit (50) is equipped to move the piston to inner portion of screw case.    USE - Device for producing generative fuel from combustible waste in home or industry.    ADVANTAGE - Since the heating portion of the screw case is foldably installed to achieve plasticity and pyrolysis of the workpiece, the hopper is accurately guided to the helix of the screw without empty space. Thus the prevention of fault can be realized and the degradation of quality can be prevented. Hence the production efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for producing generative fuel.    Screw case (12)    Lead screw (18)    Heating portion (20)    Separate heater (26)    Driving unit (50)
NOVELTY - The sensor has a gas sensitive layer (106) formed on a passivation layer (105) of a miniature cantilever beam (108). The passivation layer is covered on a metal layer (110) and a silicon dioxide layer (104). Multiple exposed electrode wires (109) are formed on the silicon dioxide layer. A p+ resistor unit (103) is provided with two resistors, which are utilized as a set of cantilever beam resistors of a wheatstone electric bridge. Other two resistors are utilized as another set of cantilever beam resistors. The former set of cantilever beam resistors are placed inside the cantilever beam.    USE - Room-temperature gas sensor for a miniature cantilever beam (claimed).    ADVANTAGE - The gas sensitive layer absorbs or desorbs methane so as to cause stress change at root of the cantilever beam. The sensor has temperature compensation function, stable performance, prolonged service life, small volume and high definition, and consumes less power.    DETAILED DESCRIPTION - The passivation layer is a phosphorosilicate glass layer or silicon nitride layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a room-temperature gas sensor.'(Drawing includes non-English language text)'    P+ resistor unit (103)    Silicon dioxide layer (104)    Passivation layer (105)    Gas sensitive layer (106)    Miniature cantilever beam (108)    Exposed electrode wires (109)    Metal layer (110)
NOVELTY - A polyaromatic hydrocarbon polluted soil washed-out wastewater treatment system comprises a grid filter pool (1), a settling pool (2), a pump (3), an outlet water collecting pool (5), a cascaded plant biomass absorbing filter (4) connected with the outlet water collecting pool, a compost accessory storage, a mixing and stirring device connected with the compost accessory storage, and a compost reactor. The grid filter pool, settling pool, pump, cascaded plant biomass absorbing filter, mixing and stirring device, and compost reactor are orderly connected.    USE - A polyaromatic hydrocarbon polluted soil washed-out wastewater treatment system.    ADVANTAGE - The system not only degrades polyaromatic hydrocarbon but also uses plant biomass compost which can absorb the soil nutrition to improve the reaction efficiency and avoid loss of nutritional elements of the soil to realize biological circulated repair having low pollution and low nutrition loss during the soil washing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of treating a polyaromatic hydrocarbon polluted soil washed-out wastewater.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a polyaromatic hydrocarbon polluted soil washed-out wastewater treatment system.    Grid filter pool (1)    Settling pool (2)    Pump (3)    Cascaded plant biomass absorbing filter (4)    Outlet water collecting pool (5)
NOVELTY - High-density porous carrier comprises (in mass.%) fly ash (10-20), clay (40-50), coal gangue (5-20), pore-forming agent (2-10), adhesive (2-10) and water (15-20). The high-density porous carrier is obtained by mixing the above mentioned materials, pelleting, molding, drying, forging, milling, grinding, hole expansion by inorganic acid or alkali, drying, soaking in extracellular polysaccharides aqueous solution with concentration of 20-35% and drying under shade.    USE - The carrier is useful in biological fluidized bed reactor for treating wastewater e.g. domestic sewage, petrochemical wastewater, papermaking wastewater and coking wastewater (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the preparation of the high density porous carrier, comprising: (a) mixing (in mass.%) fly ash (10-20), clay (40-50), coal gangue (5-20) and pore-forming agent (2-10), and stirring them uniformly, adding water (15-20 mass.%) and adhesive (2-10 mass.%), stirring, aging the mixture for 3-5 days; (b) pelleting the mixture and molding it, drying the pelleted mixture for 4-5 hours at 80-100?OC, transferring the pelleted mixture to a muffle furnace to forge for 2-4 hours at high temperature of 1000-1100 degrees C, cooling the pelleted mixture, milling and grinding it, screening using a sieve of 20-40 meshes; and (c) placing the sieved granules in inorganic acid or alkali to expand the hole, drying, soaking the granules in the extracellular polysaccharides aqueous solution with concentration of 20-35%, and drying them in the shade to obtain the high-density porous carrier.
NOVELTY - An industrial breeding water purifying device comprises biofilter made of large algae, edible animal meat, and fish meat, organically combined together. The large algae comprise warm water macroalgae and cold water macroalgae. The edible animal meat is shellfish and fish. The shellfish is oyster, mussel and scallop. The fish is barracuda. The meat fish is weever, flounder, or black fuscescens.    USE - Industrial breeding water purifying device for sea fish wastewater (claimed).
NOVELTY - Complex enzyme comprises an enzyme preparation part and a microelement part. The enzyme preparation part includes solid monomer comprising (in %) 20000 mu /g xylanase (20-30), 20000 mu /g cellulase (20-30), 30000 mu /g lipase (5-10), 10000 mu /g pectinase (5-10), 30000 mu /g protease (5-10), 1000 mu /g amylase (5-10), 50000 mu /g glucoamylase (10-20) and 10000 mu /g glucanase (5-10). The microelement part comprises (in %) zinc sulfate (10-15), phosphate rock powder (20-30), steelmaking slag (10-20), calcium carbonate (12-16), furnace ash (20-25), active carbon (5-10) and non-ionic surfactant (4- 8).    USE - The complex enzyme is useful for methane fermentation and microelement supply.    ADVANTAGE - The complex enzyme: quickly degrades the raw materials in the methane fermentation, accelerates the gas generation, and increases gas yield; prolongs the fermentation time, reduces the residual energy and improves the utilization rate of the raw materials.    DETAILED DESCRIPTION - Complex enzyme comprises an enzyme preparation part and a microelement part. The enzyme preparation part includes a solid monomer raw material comprising (in %) 20000 mu /g xylanase (20-30), 20000 mu /g cellulase (20-30), 30000 mu /g lipase (5-10), 10000 mu /g pectinase (5-10), 30000 mu /g protease (5-10), 1000 mu /g amylase (5-10), 50000 mu /g glucoamylase (10-20) and 10000 mu /g glucanase (5-10). The microelement part comprises (in %) zinc sulfate (10-15), phosphate rock powder (20-30), steelmaking slag (10-20), calcium carbonate (12-16), furnace ash (20-25), active carbon (5-10) and non-ionic surfactant (4- 8). The weight ratio of the enzyme preparation part to the microelement part is 1:(1-2).
NOVELTY - An energy-saving methanol gasoline comprises methanol (85-95%), gasoline (1-3%), propionaldehyde (0.5-1.5%), acetone (5-7%) and benzene (0.5-1.5%). The methanol gasoline is produced by mixing above raw materials, uniformly stirring and filtering to obtain finished product.    USE - Energy-saving methanol gasoline.    ADVANTAGE - The methanol gasoline replaces conventional gasoline; and has high oxygen content, complete combustion, small exhaust gas, strong power, good commonality, energy preservation and exhaust reduction without changing engine and other components. It uses fuel taking methanol as main material and other materials as auxiliary material, thus reducing production cost; and has cooling and cleaning effect, reduces temperature of engine and prolongs service life of each component.
NOVELTY - A portable water electrolysis oxygen generator comprises water electrolyzer and water pot connected with electrolyzer. The generator further includes hydrogen fuel battery and storage battery. The hydrogen fuel battery charges storage battery. The storage battery provides power for electrolyzer. The electrolyzer is equipped with separating membrane. The separating membrane is polymer membrane having proton or hydroxy ion conduction ability. The oxygen produced by electrolyzer is output to outside. The hydrogen produced by electrolyzer is transferred to hydrogen fuel battery as fuel.    USE - Portable water electrolysis oxygen generator for special environment particularly plateau travel, emergent rescue, family, hospital, car, ship and office meeting or sealing place.    ADVANTAGE - The generator is light in weight, portable in carrying, continuous in making oxygen, high in oxygen yield and quick in speed. The oxygen purity is more than 99.9%. The cost is low.    DETAILED DESCRIPTION - A portable water electrolysis oxygen generator comprises water electrolyzer and water pot connected with electrolyzer. The generator further includes hydrogen fuel battery and storage battery. The hydrogen fuel battery charges storage battery. The storage battery provides power for electrolyzer. The electrolyzer is equipped with separating membrane. The separating membrane is polymer membrane having proton or hydroxy ion conduction ability. The oxygen produced by electrolyzer is output to outside. The hydrogen produced by electrolyzer is transferred to hydrogen fuel battery as fuel.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a portable water electrolysis oxygen generator.
NOVELTY - Refrigerant composition comprises (pts. wt.) difluoromethane (R32) (35-60), pentafluoroethane (R125) (35-60) and iso-butane (R600a) (1-10).    USE - Refrigerant composition for refrigeration air conditioning system, e.g. home air conditioning/heat pump.    ADVANTAGE - The refrigerant composition meets the environment protection demand. It has zero ozone depletion potential, low global warming potential, thermotechnical performance that is equal to or higher than that of R410A refrigerant. It is an ideal refrigerant in replace of hydroclorofluorocarbon-22 (R22).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing the refrigerant composition comprising physically mixing difluoromethane, pentafluoroethane and iso-butane in the liquid phase.
NOVELTY - A high clarity alcohol fuel oil comprises (pts.wt.) ferrocene (0.03-0.05), scrubbing oil (25-40), methanol (60-75), methylbenzene (1-2), acetone (2-3), and isobutanol (2).    USE - A high clarity alcohol fuel oil.    ADVANTAGE - The alcohol fuel oil has improved anti-detonating property and oxygen content, and reduced carbon deposition and discharge of carbon-oxygen composite, thus having improved heat value and protecting the environment.
NOVELTY - A micro-channel reactor comprises a reaction channel, a heat transfer channel, a substrate, and a pressure resistance machine wall. The reaction channel and the heat transfer channel are alternatively arranged in parallel. One side of the reaction channel is coated with boehmite sol and roasted to form gamma -alumina. The substrate on one side of the reaction channel is loaded with a nickel catalyst or a nickel-iron catalyst by soaking, roasting, and reducing. The reaction channel and the heat transfer channel are less than 1.5 mm high, 1-50 cm long, and 1-10 cm wide.    USE - A micro-channel reactor used for complete methanation of a synthetic gas, e.g. hydrogen and CO (claimed).    ADVANTAGE - The complete methanation achieves strong heat transfer capacity, has high space-time yield, requires low amount of metal catalyst, and uses a small volume of the device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for complete methanation of a synthetic gas, comprising:    (A) continuously circulating the synthetic gas comprising hydrogen gas and carbon monoxide (CO) in a reaction channel, where the volumetric ratio of hydrogen to CO is 3-3.1; and    (B) circulating cooling water or steam is circulated in a heat transfer channel to move the heat in the reaction channel; where the reaction system is at 2-5 MPa and 250-550 degrees C, and the volumetric air-speed of the synthetic gas is 1000-80000/hour.
NOVELTY - Method of recycling environment-friendly culture net, involves (a) immersing the net collected from sea, in tank filled with acid water, (b) heating the acid water at a specific temperature, (c) washing the net by maintaining the net in the acid water tank for a specific time, and (d) washing the net processed with the acid water using water, where the washing step involves washing the net with hot acid water by injecting microorganisms to the acid water tank and decomposing by the microorganisms.    USE - The method is useful for recycling environment-friendly culture net for breeding sea fish, and for producing organic fertilizer (claimed).    ADVANTAGE - The method is environmentally-friendly, reduces bad smell and contamination of seawater, and produces large quantities of organic fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of producing organic fertilizer, which involves performing the above-cited steps (a)-(d), precipitating the acid water using marine algae in the tank, collecting precipitate (fertilizer) in the tank, and drying and packaging the product.
NOVELTY - Methanol gasoline additive comprises (mass%) methanol (60-80), isopropanol (2.2-11.5), n-butanol (1.5-6), paraffin oil (0.2-0.8), ethyl acetate (1.5-6), methyl tert-butyl ether (10-20), and potassium nitrate (1-4).    USE - Methanol gasoline additive used for producing methanol gasoline fuel for vehicles, particularly large-sized engineering truck.    ADVANTAGE - The additive provides yellow transparent liquid methanol gasoline fuel, which has no phase separation when stored for a long time, octane value of 90-95, and no reduction of dynamic property when applied to large-sized engineering truck, in which torsion, power, and oil consumption for hundreds of kilometers can reach the national standard.
NOVELTY - A synthetic biodiesel comprises (wt.%): acid oil (50-70), methanol (10-20), desulfurated heavy benzol (10-38), light oil (1-5) and catalysis additive (0.3-0.8).    USE - Synthetic biodiesel.    ADVANTAGE - The biodiesel has high oxygen content, complete combustion, low sulfur content, small corrosivity, perfect flowing feature at low temperature and small tail gas drain pollutant. It cannot be frozen at below 4 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biodiesel which comprises pumping above raw materials in the container without pressure via a metering pump; circulating via electric heating mixer at 30-50 degrees C for 8 hours; and standing and filtering to obtain desired biodiesel.
NOVELTY - A methanol gasoline comprises (wt.%): methanol (10-50), gasoline (40-87), methyl tertbutyl ether (1-10), ethanol (1-35) and Tween 20 (RTM: polyoxyethylene (20) sorbitan monolaurate) or Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate) (0.3-1.8).    USE - Methanol gasoline.    ADVANTAGE - The gasoline has good stability, causticity-free and low manufacturing cost.
NOVELTY - Reactor comprises a water-cooled reaction portion, an air-cooled reaction portion and an air cooled shock portion. The water-cooled reaction portion is communicated with the air-cooled reaction portion through the air cooled shock portion. The water-cooled reaction portion, the air-cooled reaction portion and the air cooled shock portion all are integrated in a cylindrical closed container. The water-cooled reaction portion is mainly provided with a product outlet, at least one pair of cooling water inlet and cooling water outlet, and a number of tubular bodies to be filled with catalyst.    USE - The reactor is useful for gaseous phase exothermal reaction, preferably for the preparation of methane from synthesis gas.    ADVANTAGE - The reactor: has improved single-layer conversion rate; and has the capability of replacing the number of synthesis reactors when compared with the prior art with only one reactor, thus economical.    DETAILED DESCRIPTION - Reactor comprises a water-cooled reaction portion, an air-cooled reaction portion and an air cooled shock portion. The water-cooled reaction portion is communicated with the air-cooled reaction portion through the air cooled shock portion. The water-cooled reaction portion, the air-cooled reaction portion and the air cooled shock portion all are integrated in a cylindrical closed container. The water-cooled reaction portion is mainly provided with a product outlet, at least one pair of cooling water inlet and cooling water outlet, and a number of tubular bodies to be filled with catalyst. The air-cooled reaction portion is mainly provided with at least one reactant inlet and a number of tubular bodies to be filled with catalyst. The air cooled shock portion is mainly provided with at least one cold shock gas inlet and at least one gas mixer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the reactor for gaseous phase exothermal reaction.
NOVELTY - Additive composition comprises element (A) consisting of arylamine antioxidant and/or hindered phenol antioxidant, element (B) consisting of polyolefin amine, and element (C) consisting of metal passivator. The hindered antioxidant is biphenol antioxidant and/or polyphenol antioxidant with molecule containing at least three phenol hydroxyl radicals.    USE - Additive composition used in diesel composition    ADVANTAGE - The additive composition improves oxidization stability of biodiesel in diesel composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for diesel composition comprising basic diesel containing biodiesel, and additive composition.
NOVELTY - Glycerol conversion involves converting glycerol into synthesis gas at 225 degrees C with a platinum-based catalyst. The obtained synthesis gas is reacted with sodium hydroxide at 180 degrees C and 8 atmospheres pressure for obtaining sodium formate and hydrogen gas. The obtained sodium formate is thermally decomposed at 360 degrees C into hydrogen and sodium oxalate.    USE - Method for converting glycerol into methanol (claimed).    ADVANTAGE - The method provides methanol in an eco-friendly and cost-effective manner contentiously by using glycerol, which is a waste residue of biodiesel production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of glycerol conversion method. (Drawing includes non-English language text).
NOVELTY - Pyrolyzing furnace comprises a furnace, a fluidized bed installed in the furnace, and a feeding gas-solid nozzle installed on top of the furnace.    USE - Used as a pyrolysing furnace.    ADVANTAGE - The method increases the yield of biomass pyrolysing gas by completely pyrolysing the biomass raw material, and thus it increases the production rate of oil during condensation phase in the subsequent process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for pyrolyzing biomass comprising (i) spraying the biomass raw material and a carrier gas from top of the pyrolyzing furnace, mixing and preheating to obtain the mixture; and (ii) pyrolyzing the mixture at 500-800 degrees C, to obtain a biological semi-coke and a biomass pyrolysis gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the pyrolyzing furnace (Drawing includes non-English language text).
NOVELTY - A method for electro-oxidation of an organic compound involves providing an anion exchange membrane fuel cell having an electrolyte, a catalyst, an anode, and a cathode where the electrolyte comprises the organic compound and a metal co-catalyst dissolved in the electrolyte, the metal co-catalyst capable of forming oxidation states +2 and +4, both of which remain soluble in the electrolyte; and oxidizing the organic compound in the fuel cell, where a voltage is generated between an anode and a cathode of the fuel cell.    USE - For the electro-oxidation of an organic compound selected from methanol and ethanol (claimed).    ADVANTAGE - The metal co-catalyst, as enhancer vastly improves the rate of ethanol oxidation and promotes oxidation of the C-C bond to CO2. The progress improves the electro-oxidation of ethanol through the development of more efficient catalysts. Therefore improves the specific activity of dehydrogenation and C-C bond cleavage during the ethanol oxidation process. The process provides significant enhancements for direct-ethanol fuel cells.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel cell electrolyte (E1) comprising a soluble form of a metal co-catalyst capable of forming oxidation states +2 and +4 which remain soluble in the electrolyte;    (2) fuel cell comprising the electrolyte (E1); and    (3) preparing (P1) the electrolyte (E1) involving adding to a fuel cell electrolyte solution a salt of a metal capable of forming oxidation states II and IV which remain soluble in the electrolyte solution.
NOVELTY - The structure has a lower mold provided with a pressurization plate. A stepped pulley groove is formed at edge portion of the pressurization plate that pressurizes carbon-resin compound powder. A sealing surface is formed in inner side of the lower mold, and contacts with edge portion of an upper mold. The upper mold comprises a pressurization plate whose edge portion is formed with a stepped pulley part protrusion, where another sealing surface is formed in inner side of the upper mold.    USE - Mold structure for manufacturing a fuel cell separator.    ADVANTAGE - The structure has high electric conduction, and enables manufacturing a fuel cell separator with even density. The structure has excellent dimensional stability, and improves the quality of the fuel cell separator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a mold structure for manufacturing a fuel cell separator.    Stepped pulley part groove depth (Gh)    Stepped pulley part protrusion widths (Gw, Pw)    Stepped pulley part protrusion height (Ph)    Separator thickness (Sh)    Separator width (Sw)
NOVELTY - Method for extracting tea polyphenol, involves extracting tea by percolation method, concentrating the extract liquid, extracting the product using mixed solvent, recycling the extract agent, and freezing and drying the product.    USE - The method is useful for extracting tea polyphenol.    ADVANTAGE - The method is simple, inexpensive, environmentally-friendly and suitable for industrial production, has practical and safe process, and improved extraction rate and provides high purity of the tea polyphenol.
NOVELTY - A biomass pyrolyzing furnace comprises a furnace shell having a steam layer and inner wall, a furnace liner, an exhaust pipe, a tower, and a smoke pipe installed on the furnace shell and having an end having surrounding mesh screen.    USE - A biomass pyrolyzing furnace.    ADVANTAGE - The biomass pyrolyzing furnace has high efficiency and recycling rate, shortens pyrolysis, has high utilization rate of raw materials, reduces labor cost, and is safe.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a biomass pyrolyzing furnace.
NOVELTY - The generator has anode element and cathode element that are located in electrolytic tank. A water input pipeline is arranged in electrolytic cell. A slot is formed in electrolytic cell. The hydrogen gas is outputted by the hydrogen output pipeline. The hydrogen output pipeline is arranged in electrolytic cell. The surfaces of anode element and cathode element are provided with the metal layer. The nano powder is filled in metal layer. The material of the metal layer is selected from iron, cobalt, nickel, zinc, copper, aluminum, lithium, molybdenum or rare earth.    USE - Hydrogen generator.    ADVANTAGE - The usage of metal and graphite in the components of the hydrogen generator can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generator. (Drawing includes non-English language text)
NOVELTY - Non-grid type wind turbine generator set for producing hydrogen comprises at least one non-grid type wind power generator and at least one alternating current (AC)/direct current (DC) rectifier. The output end of the non-grid type wind generator is connected with the AC/DC input end of the rectifier. Each output ends of AC/DC rectifier are connected in parallel and connected with a hydrogen producing device.    USE - The non-grid type wind turbine generator set is useful for producing hydrogen.    ADVANTAGE - The device completely utilizes the wind source, produces hydrogen with high purity, can be used in the study of wind power generation.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the non-grid type wind turbine generator set for producing hydrogen.
NOVELTY - Preparing capecitabine, comprises reacting 1,1'-carbonyl-di(1,2,4-triazole) with hydroxy group protected cytidine compound (I) under aprotic solvent to obtain (2R,3R,4R,5R)-2-(5-fluoro-2-oxo-4-(1H-1,2,4-triazole-1-carboxamido)pyrimidin-1(2H)-yl)-5-methyltetrahydrofuran-3,4-bis(olate) compound (II), reacting (II) with n-amyl alcohol to obtain (2R,3R,4R,5R)-2-(5-fluoro-2-oxo-4-(pentyloxycarbonylamino)pyrimidin-1(2H)-yl)-5-methyltetrahydrofuran-3,4-bis(olate)compound (III), and removing the protective group of (III).    USE - The method is useful for preparing capecitabine.    ADVANTAGE - The method: avoids use of highly toxic chloroformate or phosgene acylating agent and utilizes easily available raw materials; has simple post treatment, high product yield and purity, and safe and environment-friendly operation; and is suitable for large scale production.    DETAILED DESCRIPTION - Preparing capecitabine, comprises reacting 1,1'-carbonyl-di(1,2,4-triazole) with hydroxy group protected cytidine compound of formula (I) under aprotic solvent to obtain (2R,3R,4R,5R)-2-(5-fluoro-2-oxo-4-(1H-1,2,4-triazole-1-carboxamido)pyrimidin-1(2H)-yl)-5-methyltetrahydrofuran-3,4-bis(olate) compound of formula (II), reacting (II) with n-amyl alcohol to obtain (2R,3R,4R,5R)-2-(5-fluoro-2-oxo-4-(pentyloxycarbonylamino)pyrimidin-1(2H)-yl)-5-methyltetrahydrofuran-3,4-bis(olate)compound of formula (III), and removing the protective group of (III).    either R3, R4 = acetyl, benzoyl (optionally substituted) or silyl protective group; or    R3+R4 = isopropylidene.
NOVELTY - An oil-saving device comprises electrolytic cell for electrolyzing water to generate hydrogen, oil-saving control board for controlling electric operation of electrolytic cell, and electric tube for connecting components. The two electrodes of electrolytic cell are connected with two output electrodes of accumulator. A gas discharge port is formed on side part of upper end of electrolytic cell. Processor chip unit, signal transmission interface, control signal output end and resistance circuit for regulating circuit are arranged on oil-saving control board.    USE - Oil-saving device of locomotive which is bridged among the engine, accumulator and electronic system of locomotive.    ADVANTAGE - The device can save more than 15% of the locomotive, thus reducing carbon and nitrogen of tail gas of locomotive. It is conveniently maintained.    DETAILED DESCRIPTION - Oil-saving device comprises electrolytic cell for electrolyzing water to generate hydrogen, oil-saving control board for controlling electric operation of electrolytic cell, and electric tube for connecting components. The two electrodes of electrolytic cell are connected with two output electrodes of accumulator. A gas discharge port is formed on side part of upper end of electrolytic cell and gas discharge port is connected with air inlet of an engine. Processor chip unit, signal transmission interface, a control signal output end and resistance circuit for regulating circuit are arranged on oil-saving control board. The signal transmission interface is connected with engine rotation speed output end of electronic system. The control signal output end is connected with switch of the accumulator.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating an oil-saving device. (Drawing includes non-English language texts)
NOVELTY - Heat supply system using straw as raw material in caustic soda processing, comprises e.g. a spiral conveyor, a dry distillation and gasification furnace, a gas-solid cyclone separator, a cooler, a gas-liquid separator, a Roots blower and an air storage cabinet. The input end of cooler is connected with a gas phase outlet of the gas-solid cyclone separator. The input end of the first-grade filter is connected with a gas phase outlet of the gas-liquid separator. The outlet of the gas storage cabinet accesses to a caustic soda pot stove through a fuel gas conveying distribution net.    USE - Used as a heat supply system using straw as raw material in caustic soda processing.    ADVANTAGE - The heat supply system: produces clean fuel gas through the distillation of the straw, therefore is environmental-friendly; consumes less energy; and prolongs the service life of the subsequent device.    DETAILED DESCRIPTION - Heat supply system using straw as raw material in caustic soda processing, comprises a spiral conveyor, a dry distillation and gasification furnace, a gas-solid cyclone separator, a cooler, a gas-liquid separator, a first-grate filter, a second-grade filter, a Roots blower and an air storage cabinet. The input end of cooler is connected with a gas phase outlet of the gas-solid cyclone separator. The input end of the first-grade filter is connected with a gas phase outlet of the gas-liquid separator. The outlet of the gas storage cabinet accesses to a caustic soda pot stove through a fuel gas conveying distribution net.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the heat supply system using straw as raw material in caustic soda processing (Drawing includes non-English language text).
NOVELTY - Ginkgolide is extracted and refined by grinding impurity-free ginkgo root bark until fineness is 30-50 meshes, soaking ground bark in aqueous saturated sodium acetate solution, filtering soaking liquid, leaching obtained filter slag with hot water, condensing the leaching liquid, dissolving the condensate in aqueous ethanol solution and filtering to obtain filtrate, condensing until the ethanol is completely recovered to obtain condensate, extracting with ethyl acetate, and condensing and drying obtained liquid to obtain high-content ginkgolide product.    USE - Method for extracting and refining ginkgolide (claimed).    ADVANTAGE - The method has low ginkgolide loss, improved solvent conservation, efficient macro-molecule impurity removal, low energy consumption, improved safety, simple operation, easy control and low production cost; and is pollution-free, thus environmentally friendly.    DETAILED DESCRIPTION - Extraction and refining of ginkgolide comprises grinding impurity-free ginkgo root bark until fineness is 30-50 meshes; soaking ground bark in aqueous saturated sodium acetate solution, filtering soaking liquid and discarding filtrate to obtain filter slag; leaching the filter slag with hot water and filtering to obtain leaching liquid; condensing the leaching liquid to obtain condensate; dissolving the condensate in aqueous ethanol solution, stirring, and filtering to obtain filtrate; condensing until the ethanol is completely recovered to obtain condensate; extracting with ethyl acetate to obtain extracting liquid; and condensing and drying the liquid to obtain high-content ginkgolide product.
NOVELTY - Improved demethanizer and deethanizer system of ethylene device comprises a pipeline (1) arranged at the bottom of a high-pressure demethanizing tower (6) and connected with an ethylene adding pipeline on the top of a low-pressure carbon rectifying tower (3) of the deethanizer system after being blocked to form a material circulating loop system between the demethanizer and the deethanizer system.    USE - Used as an improved demethanizer and deethanizer system of ethylene device.    ADVANTAGE - The system: comprises the material circulating loop between the demethanizer and deethanizer system, which ensures return of the material to the deethanizer system during the process of adjusting the demethanizer system; and reduces the ethylene dosage of deethanizer system by 15 t/hours, ethylene discharge by 50 t/hours, and reduces ethylene loss by 200 t each time during the ethylene driving process in comparison with the conventional systems.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the improved demethanizer and deethanizer system of ethylene device.    Pipeline (1)    Low-pressure carbon rectifying tower (3)    High-pressure demethanizing tower (6)
NOVELTY - The device has a condenser that is provided with a raw gas intake pipe, a condensed liquid outlet pipe, an uncondensed gas outlet pipe, a coolant medium inlet connecting pipe, and a coolant medium outlet connecting pipe. The uncondensed gas outlet pipe of condenser is connected with inlet end of film separator. The ventilated outlet pipe of film separator is connected with raw gas intake pipe through compressor. The film separator is provided with a rest ventilated gas outlet pipe and the condensed liquid outlet connected through with the de-ethanizing tower.    USE - Propylene recovery device of de-ethanizing tower installed in gas separation device.    ADVANTAGE - The device can separate the propylene without change the original parameter of the de-ethanizing tower. The utilization of the propylene and the economic benefit of the oil refinery are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the propylene recovery device. (Drawing includes non-English language text)
NOVELTY - A synthetic biofuel oil comprises which comprises (wt.%): acidified grease (30-50), methyl alcohol (10-30), desulfurized heavy benzol (30-59), and nano fuel oil additive (0.3-0.8).    USE - Synthetic biofuel oil.    ADVANTAGE - The biofuel oil has high oxygen content, low sulfur content, complete combustion, no accumulated charcoal, little hydrocarbon, carbon monoxide, nitrogen oxide (NOx), sulfur oxide (SOx) emission, low viscosity, good fluidity and high calorific value. It does not need to be heated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biofuel oil which comprises respectively measuring above ingredients, pumping ingredients in a container with normal pressure and normal temperature, and uniformly mixing; and circulating for 8 hours through electric heating static mixer, heating for 72 hours, and filtering to obtain desired biofuel oil.
NOVELTY - A methane catalyst is prepared by preparing catalyst body; and subjecting to pre-reduction comprising firing catalyst body, forming catalyst precursor having nickel aluminate, and pre-reducing the catalyst precursor.    USE - Method of preparing methane catalyst.    ADVANTAGE - The method has high temperature and high water to steam ratio, does not require high reducing temperature thus shorting heating period and minimizing high temperature risk, reduces high temperature resistance demand and investment cost of the methane synthesis device, has stable performance, and reduces power consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a synthesis methane catalyst precursor comprising nickel aluminate (5-75 mass%).    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of preparing methane catalyst. Drawing includes non-English language text.
NOVELTY - A solid catalyst comprises sodium-cobalt hydroxy ethylidene diphosphonate (94-99 wt.%) and sodium hydroxide (1-6 wt.%).    USE - Solid catalyst is used in normal-pressure transesterification process for preparing biodiesel.    ADVANTAGE - The solid catalyst has excellent catalytic activity, and enables formation of biodiesel with high productivity with reduced consumption of energy by simple method without affecting the environment.    DETAILED DESCRIPTION - A solid catalyst comprises sodium-cobalt hydroxy ethylidene diphosphonate (Na6Co6(OH)2(hedpH)6(H2O)10) (94-99 wt.%) and sodium hydroxide (1-6 wt.%).    INDEPENDENT CLAIMS are included for the following:    (1) manufacture of solid catalyst. Cobalt chloride and cobalt nitrate are dissolved in water, and hydroxyl ethylidene diphosphonate and pyrazine or 4,4'-bipyridyl as organic template agent are added and stirred. Sodium hydroxide is added to the resultant mixture, reacted at 120-160 degrees C or 24-72 hours, filtered and dried to obtain alkaline hydroxyl ethylidene cobalt sodium diphosphonate. The obtained alkaline hydroxyl ethylidene cobalt sodium diphosphonate is ground, sieved, and sodium hydroxide having concentration of 0.05-0.5 mol/L is added. The obtained mixture is stirred, soaped, and dried to obtain solid catalyst; and    (2) usage of solid catalyst used with normal-pressure transesterification reaction for preparing biodiesel. Soya-bean oil and methyl alcohol in the molar ratio of 3:1-10:1, are mixed with solid catalyst, and transesterification reaction is performed at 50-70 degrees C for 3-7 hours. The content of alkaline hydroxyl ethylidene cobalt sodium diphosphonate catalyst is 1-5 weight% with respect to content of soya-bean oil. The solid catalyst is separated from the resultant mixture to obtain biodiesel.
NOVELTY - Addition reaction of isobutenyl ketone and dimethyl(ethyoxycarbonyl methyl)sulfur ylide is carried out to obtain ethyl 3-acetyl-2,2-dimethylcyclopropane-1-carboxylate. The obtained ethyl 3-acetyl-2,2-dimethylcyclopropane-1-carboxylate is separated and oxydrolysis is performed in presence of oxidant, to obtain 3,3-dimethylcyclopropane-1,2-dicarboxylic acid. The obtained 3,3-dimethylcyclopropane-1,2-dicarboxylic acid is separated and linking reaction is performed, to obtain caronic anhydride.    USE - Manufacture of caronic anhydride.    ADVANTAGE - The method effectively and economically provides caronic anhydride with high safety without polluting the environment, by a simple method.
NOVELTY - The system has a hydrogen generator whose air outlet is connected with an air inlet of a fuel cell stack, where the fuel cell stack comprises acidic and alkaline batteries that are connected in series. Load circuits are respectively connected with two poles of the fuel cell stack. An upper cover of an electric generator is connected with an air outlet of a container. The container is filled with water and hydrogen-containing chemical substance. A membrane electrode assembly is formed by a carbon paper and a proton exchange membrane. The membrane is a perfluorinated sulfonic acid resin film.    USE - Acid alkali mixed water circulating structure fuel cell power generation system.    ADVANTAGE - The system saves dosage of platinum metal and material, saves resource, reduces energy consumption and reduces cost of an acid cell proton exchange membrane fuel cell. The acidic and alkaline batteries are connected in series so as to reduce volume and realize water self-circulation and self-humidifying functions. The system assembles the fuel cell stack in a convenient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an acid alkali mixed water circulating structure fuel cell power generation system.
NOVELTY - The gasifier has main portion with hearth and outlet at bottom of the hearth. The hearth is formed with dry section, cracking zone, oxidation zone and reduction zone from top to bottom. One end of air outlet pipe is connected with main portion of gasification furnace. Another end of air outlet pipe is connected with guide mechanism. The guide mechanism is connected with carbon monoxide gas pipeline. The portion of inner diameter of hearth corresponding to oxidation shrinks to hearth less than inner diameter of cracking zone and less than inner diameter of reducing zone.    USE - Downdraft biomass gasifier.    ADVANTAGE - The carbon monoxide can be fully restored to carbon dioxide gas. The back-fire caused by explosion of the gasification main portion of furnace can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the downdraft biomass gasifier.
NOVELTY - A biomass apparatus comprises an electrically-conductive primary conduit (3) having a first terminal; an electrically-conductive secondary conduit (5) having a second terminal; an electrical circuit or device electrically connected to the terminals; and a gravity-fed fluid flowed in between a space between the primary conduit and the secondary conduit.    USE - A biomass apparatus used for collecting hydrogen gas used as a source of fuel for a fuel cell, from a photosynthesis process (claimed).    ADVANTAGE - The apparatus alters dynamic properties of a fluid flowing by inducing turbulence while simultaneously generating an electrical charge which may be drawn and immediately utilized or stored.    DETAILED DESCRIPTION - A biomass apparatus comprises an electrically-conductive primary conduit (3) having a length and with a first terminal; an electrically-conductive secondary conduit (5) having a length similar to the length of the primary conduit, being disposed entirely in the primary conduit, and having a second terminal; an electrical circuit or device electrically connected to the terminals to capture energy from a voltage difference existing at the terminals; and a gravity-fed fluid flowed in between a space between the primary conduit and the secondary conduit, where an oxygen reduction potential of the fluid is altered and a residual voltage generated between the terminals.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of the biomass apparatus.    Reservoir (2)    Electrically-conductive primary conduit (3)    Cathode (4)    Electrically-conductive secondary conduit (5)    Anode (8)
NOVELTY - A methoxy group-containing compound (I) is reduced to obtain amine group-containing compound (II). The amino group of amine group-containing compound (II) is modified by protecting group to obtain 3-phenyl pyrazolo(5,1-b)thiazole compound (III).    USE - Manufacture of 3-phenyl pyrazolo(5,1-b)thiazole compound.    ADVANTAGE - The method enables manufacture of 3-phenyl pyrazolo(5,1-b)thiazole compound having high purity and high yield, without environmental pollution.    DETAILED DESCRIPTION - A methoxy group-containing compound of formula (I) is reduced to obtain amine group-containing compound of formula (II). The amine group-containing compound (II) is modified by protecting group of amino group to obtain 3-phenyl pyrazolo(5,1-b)thiazole compound of formula (III).    R3=methoxy, cyano, cyclobutyloxy methyl, methoxymethyl or ethoxymethyl;    R4=methoxy or chloro;and    Pr'=protecting group of amino.
NOVELTY - Degrading biomass involves using peroxide in presence of metal catalyst.    USE - For degrading biomass useful for building materials; and as a cofactor for enhancing activity of enzymes used to digest biomass. The method is useful to generate pressure used for mechanical work and electricity generation; gasify biomass to generate fuel gases, such as methane or hydrogen, where the fuel gases are used directly as a source of energy or for applications, e.g. fuel cells; for degradation and removal of solid biomass and/or organic waste; for extracting chemicals and biochemicals from the biomass waste; and in combination with UV light. The sugar extracted in the method is useful for feed stock (claimed).    ADVANTAGE - The method allows one to treat a starting biomass material to not only obtain glucose (for ethanol production), but also obtain heat (an additional source of energy) and pressure. This method can be used to gasify biomass very cheaply, under ambient conditions. Also, continuation of the same treatment can result in the removal of the remaining waste.
NOVELTY - A component-collecting system has a material (101) having surface (S1) and fibers, a medium (121) and component (a).    USE - System is used for collecting component e.g. algae, bacteria, ethane, hexanol, nitrate, phosphate, benzene, lead, mercury, cadmium, iron, aluminum and arsenic (claimed) in pharmaceutical, nutraceutical, cosmetics, biofuel, food product, crop fertilizer, animal feed and polymer.    ADVANTAGE - The system efficiently and economically collects the component, with reduced energy consumption and without environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for collection of component.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the system.    Material (101)    Medium (121)
NOVELTY - The device has a hydrogen sensor (100) for measuring the concentration of hydrogen and a controller (102) which generates the power control signal according to comparison result of set critical range and hydrogen density measurement value. A power supply unit (106) generates the electricity corresponding to the power control signal of the controller. A pressure driving unit (108) generates the air of pressurization state and ejects to the outside based on measured concentration value.    USE - Device for managing hydrogen energy for fuel cell of vehicle and ship.    ADVANTAGE - Hydrogen concentration is measured efficiently and safety of indoor hydrogen generation environment can be secured while increasing effectiveness of hydrogen management device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for membrane filter.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen management device. (Drawing includes non-English language text)    Hydrogen sensor (100)    Controller (102)    Power supply unit (106)    Pressure driving unit (108)    Fuel cell (204)
NOVELTY - The method involves producing hydrogen-containing-gas from the gas containing nitrogen gas and nitrogen compound by using hydrogen generator (2). The ammonia contained in the hydrogen-containing gas is removed. The temperature of hydrogen-containing-gas is detected after removing ammonia. The supply of hydrogen-containing-gas is started from the hydrogen generator to a fuel cell (7), when detected temperature exceeds the predetermined value.    USE - Operating method of fuel cell system for use as distribution type electric power generating apparatus.    ADVANTAGE - Sufficient electric power is obtained from the fuel cell. Absolute quantity of ammonia generated in fuel cell system can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the structure of fuel cell system. (Drawing includes non-English language text).    Hydrogen generator (2)    Combustor (3)    Ammonia removal device (5)    Fuel cell (7)    Fuel cell system (100)
NOVELTY - A process for the thermolysis of biomass containing lignin, comprises: mixing the biomass with a clay; and pyrolyzing the mixture.    USE - The process is useful for the thermolysis of biomass containing lignin; and for producing a pelletized carbonaceous product, where the pelletized carbonaceous product is useful as a soil improver, as a precursor for activated carbon, as a cracking catalyst, or as a carbon dioxide (CO2)-neutral fuel (all claimed).    ADVANTAGE - The process can be efficiently used in generating valuable materials such as char, activated charcoal, bio-oil, and combustible gasses.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a pelletized product obtainable by the process; and    (2) a pelletized carbonaceous product comprising pellets having mean dimensions in the range of 0.25-10 mm, where the pellets comprise carbon in an amount of 5-60 wt.%, and oxides of magnesium and silicon in an amount of 30-95 wt.%, relative to the total dry weight of the pellets.
NOVELTY - A recombinant host cell comprising (i) at least one deletion, mutation, substitution or their combinations in an endogenous gene encoding a polypeptide which converts pyruvate to acetaldehyde, acetyl phosphate or acetyl-CoA, or polypeptide having pyruvate decarboxylase activity, and (ii) a heterologous polynucleotide encoding a polypeptide having phosphoketolase activity, is new.    USE - The recombinant host cell is useful for producing 2,3-butanediol, 2-butanol, 2-butanone, valine, leucine, lactic acid, malic acid, alanine, fumaric acid, succinic acid, isoamyl alcohol or isobutanol, and reducing requirement for exogenous 2C substrate. The host cell is chosen from Clostridium, Zymomonas, Escherichia, Salmonella, Serratia, Erwinia, Klebsiella, Shigella, Rhodococcus, Pseudomonas, Bacillus, Lactobacillus, Enterococcus, Alcaligenes, Klebsiella, Paenibacillus, Arthrobacter, Corynebacterium, Brevibacterium, Schizosaccharomyces, Kluyveromyces, Yarrowia, Pichia, Candida, Hansenula, Saccharomyces and S.cerevisiae (all claimed). The obtained products are useful as fuel additive, feedstock and flavoring agent, and in plastic industry.    ADVANTAGE - The method is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for producing 2,3-butanediol, 2-butanol, 2-butanone, valine, leucine, lactic acid, malic acid, alanine, fumaric acid, succinic acid, isoamyl alcohol or isobutanol, involves growing the recombinant host cell under conditions where the product is produced, and optionally recovering the product;    (2) method (M2) for producing the recombinant host cell; and    (3) method (M3) for reducing requirement for an exogenous two-carbon substrate for growing the host cell, involves transforming the host cell with the heterologous polynucleotide.
NOVELTY - A proton exchange membrane comprises fluorine-containing polymer membrane having a microporous structure and ion exchange resin in the micropores of the fluorine-containing polymer membrane. Groups having an ion exchange function are grafted in the micropores of the fluorine-containing polymer membrane and bonded with the ion exchange resin by hydrogen bond or, alternatively, groups having an ion exchange function are grafted in the micropores of polymer membrane and modified by high valence metal ions which are bonded with the ion exchange resin by electrostatic force.    USE - Proton exchange membrane is used for manufacturing fuel cell (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of proton exchange membrane, which involves reacting fluorine-containing polymer membrane having microporous structure with substance having an ion exchange function to connect them through one or more methods chosen from thermal treatment, optical treatment, ionizing radiation, plasma, X ray and free radical initiator, generating ion exchange group on obtained film under the effect of acid or alkali, compounding ion exchange resin with prepared film, by extrusion, hot pressing, casting, tape casting, screen printing, spraying and/or impregnation, carrying out thermal treatment for 1-600 minutes at 30-300 degrees C, and optionally carrying out impregnation of the film in solution containing high valence metal ions between reacting and compounding.
NOVELTY - Microbial inoculum comprises (in parts by wt.): lactic acid bacteria (30-40), yeast (20-30), nitrobacteria (10-20), actinomycete (10-15) and mold (10-15).    USE - The microbial inoculum is useful for composting organic wastes.    ADVANTAGE - The microbial inoculum: degrades pollutants in organic waste and eliminates bad odor, reduces heavy metal poisoning, adjusts pH of the compacting material, accelerates hydrolysis of cellulose and prevents loss of ammonia nitrogen; and adjusts water content in high water containing sludge and in kitchen waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the microbial inoculum, comprising: (a) activating lactic acid bacteria by using a slant culture, inoculating in a liquid culture medium and culturing at 28-35 degrees C for 36-72 hours, activating yeast using slant culture, inoculating in liquid culture medium and culturing at 28-35 degrees C for 36-72 hours, activating nitrobacteria by using an inclined surface, inoculating in liquid culture medium and culturing at 28-35 degrees C for 36-72 hours, activating actinomycete by using slant culture, inoculating in liquid culture medium and culturing at 28-35 degrees C for 36-72 hours, activating mold by using slant culture, inoculating in liquid culture medium and culturing at 28-35 degrees C for 36-72 hours, calculating viable count, detecting lactic acid bacteria, yeast, nitrobacteria, actinomycete and mold counts, and mixing bacterial liquid based on a proportion, and (b) taking (in parts by wt.): wheat bran (30-50), chaff (20-30), sawdust (10-20) and bamboo charcoal (10-20) as adsorbing fermentation raw materials, crushing through 40 mesh sieve, sterilizing at 121 degrees C for 30 minutes, adding mixed bacteria liquid into the fermentation raw materials for adsorbing microbial inoculum, performing solid sealed fermentation at 25-35 degrees C for 3-5 days, drying at 30-35 degrees C, crushing and filtering in a 40 mesh sieve.
NOVELTY - Pollution control device comprises an underground bio-purification tank, where a temperature-controlled greenhouse is built above the purification tank. The greenhouse is installed with at least one shed frame.    USE - Used as a pollution control device.    ADVANTAGE - The device utilizes at least one shed frame installed in the greenhouse for soil less culture or cultivation of edible mushroom to reduce the cost of device. The greenhouse adapts sufficient space for the growth of mushrooms in temperature and moisture and the edible mushrooms directly increase profits for the sewage treatment companies, and reduces overall cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the pollution control device.
NOVELTY - The method involves packaging an edible fungi waste fungus bag that is covered by a plastic film adhesive, where the edible fungi waste fungus bag is crushed into small blocks by a crusher.    USE - Method for producing organic fertilizer.    ADVANTAGE - The method enables avoiding directly discarding of harmful material to the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing organic fertilizer.'(Drawing includes non-English language text)'
NOVELTY - The invention relates to Bacillus amyloliquefaciens strain B165, deposited under the number NCAIM(P) B0013603, as a bioinoculant for the treatment of vegetable wastes in complementarity with conservative agricultural technologies, having a broad antifungal spectrum against phytopathogenic soil fungi, plant growth stimulating activity and capacity of mineralization of vegetable material.
NOVELTY - Method for preparing cigarette residue bio-fertilizer, involves crushing cigarette residue or cigarette residue cylinders into particle having mesh size of 60, mixing strains of Candida tropicalis and Aspergillus oryzae with obtained product, heating the obtained product at 60 degrees C, fermenting the obtained product, adding bacterial strains of Bacillus subtilis and B.mucilaginosus to obtained product, cooling the product to 20-30 degrees C, culturing the product for 10 days, and transforming the product into bio-fertilizer.    USE - The method is useful for preparing cigarette residue bio-fertilizer useful for improving soil.    ADVANTAGE - The bio-fertilizer can be obtained simply, inexpensively, less labor intensively, and environmentally-friendly.
NOVELTY - Micro-emulsion diesel oil comprises (in parts by wt.) mineral diesel oil (30-60), biomass component (10-40), water (5-30), and composite emulsifier (5-20).    USE - Used as a micro-emulsion diesel oil.    ADVANTAGE - The diesel oil is economical, and environment friendly; utilizes unique physical and chemical properties of fusel oil for preparing cleaning fuel, and retaining high performance; and reduces the emission of particulate matter and nitrogen oxides.
NOVELTY - Preparing biomass fuel with edible fungi dregs comprises: (i) crushing edible fungi dregs and drying; (ii) screening mineral carbon; (iii) weighing calcium oxide, potassium nitrate and 11 kinds of raw materials based on ratio of chemical production procedure to obtain a powdery combustion improver; (iv) adding mineral carbon and a combustion improver, transferring the mixture into a mixing machine; (v) uniformly stirring the mixture for naturally cooling, sealing and packing directly in a plastic bag; and (vi) directly using in a wood burning stove and suspended combustion.    USE - The method is useful for preparing biomass fuel with edible fungi dregs.    ADVANTAGE - The method: is simple, economical, produces an alternate form of energy, and solves the disposal problem and the pollution caused by the fungal residue. The biomass fuel: is odorless, non-toxic, and releases no smoke when used and is environment friendly.    DETAILED DESCRIPTION - Preparing biomass fuel with edible fungi dregs comprises: (i) crushing edible fungi dregs, drying the crushed edible fungi dregs to maintain a moisture content of not less than 25%; (ii) screening mineral carbon of diameter not less than 1 mm, where the carbon content in the mineral carbon is not greater than 65%; (iii) weighing calcium oxide, potassium nitrate and 11 kinds of raw materials based on ratio of the chemical production procedure to obtain a powdery combustion improver; (iv) adding 3-8% of mineral carbon to the pre-treated edible fungi dregs, simultaneously adding 1-2% of the combustion improver, transferring the mixture into a mixing machine with a heating device and stirring uniformly without adding water, maintaining the mixture in a loose form and drying; (v) uniformly stirring the mixture and spreading out for naturally cooling, sealing and packing directly in a plastic bag after the temperature is normal; and (vi) directly using in a wood burning stove and suspended combustion.
NOVELTY - A biomass fuel comprises stillage, bacteria bract, camphor leaf and/or dairy manure. The components are uniformly mixed.    USE - Biomass fuel.    ADVANTAGE - The fuel has high heat value, is environment-friendly and energy-saving, has simple preparation method, and good economic benefit and recycling usage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biomass fuel which comprises separately preparing above raw material or mixed preparing; adding coal catalyst to coal gasification process, adding coal catalyst and coal, and processing for 8-10 hour and drying until or aqueous is 10-25%, and rolling forming.
NOVELTY - A large plastic biogas fermenting tank comprises a main body made of plastic material. The main structure is composed of a tank body, an air storage chamber, a protective cover, and a base of four parts.    USE - A large plastic biogas fermenting tank.    ADVANTAGE - The fermenting tank is resistant to corrosion, acids, and alkalis. It has high intensity and long service life, reduces device cost, saves investment, and reduces biogas production cost.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of a large plastic biogas fermenting tank.
NOVELTY - A sealed joint mode is used when excrement enters the integrated solid-liquid separating equipment.    USE - Sealed joint mode is used when excrement enter integrated solid-liquid separating equipment.    ADVANTAGE - The use of sealed joint mode radically solves the pollution problem of dejection and sewage.
NOVELTY - Chemically processing plagued animal carcass, comprises performing alkaline hydrolysis reaction to infectious microorganism and animal body in sterile aqueous solution under high temperature so as to transform proteins, nucleic acids and lipids of all cells and tissues into small peptides, amino acids, sugar, soap and electrolytes.    USE - The method is useful for chemically processing plagued animal carcass.
NOVELTY - The method involves using vegetable oils or animal fats.    USE - Method for obtaining biodiesel for use in diesel engine or for use as substitute fuel oil for boilers.    ADVANTAGE - The method involves using vegetable oils or animal fats, and hence enables to provide efficient way without using biodiesel washing and low-temperature processes.
NOVELTY - An immobilized microsphere comprises sodium alginate used as embedding material, attapulgite as absorbent absorbed petroleum hydrocarbon degrading bacteria and nutrient elements. The diameter of immobilized microsphere is 2.5-3.0 mm.    USE - Immobilized microsphere for repairing petroleum polluted soil, particularly for degrading petroleum hydrocarbon (claimed).    ADVANTAGE - The microsphere is spherical and has improved hole clearances and absorption capability, thus improving loading capability. It also has improved internal survival environment, thus reinforcing resistance to environmental impact, and has environmental protection safety and good biocompatibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the microsphere which comprises:    (A) culturing and preparing suspension liquid of petroleum hydrocarbon degrading bacteria used for repairing petroleum polluted soil;    (B) uniformly mixing sodium alginate and attapulgite and placing into deionized water, processing wet heat sterilization at high temperature and keeping at 40-60 degrees C to obtain sodium alginate-attapulgite gelatin;    (C) adding obtained suspension liquid into obtained gelatin, and uniformly mixing, where bacterial concentration in mixture is 0.01-0.04 (preferably 0.04) g/mL, sodium alginate concentration is 0.01-0.06 (preferably 0.035) g/mL, attapulgite concentration is 0.005-0.03 (preferably 0.01) g/mL;    (D) dropping obtained mixture into calcium chloride solution, fastly and uniformly mixing to obtain immobilized particles, reacting calcium chloride solution into which immobilized particles are being soaked at 4 degrees C, where concentration of calcium chloride solution is 0.02-0.08 (preferably 0.03) g/mL; and    (E) washing obtained particles and transferring into proliferation culture medium, culturing by shaker bed, and washing to obtain desired microsphere.
NOVELTY - A two-stage gasification furnace comprises a hole type cylindrical furnace body. The interior of furnace body is divided into two stages of reactors having calabash structure. Nozzles having cylindrical passageway are arranged under two furnace rows. An upper high-temperature vapor inlet and a lower high-temperature vapor and air inlet are opened at nozzle side. A solid feed inlet is arranged on upper end of first-stage reactor and a synthesis gas outlet is arranged at the side. A liquid and particulate feed injection port is arranged at the side of second-stage reactor.    USE - Two-stage gasification furnace used for processing biomass.    ADVANTAGE - The furnace is energy saving and environment friendly; and has high gasification efficiency, high gas quality, high calorific value, fast gasification speed, complete reaction, and high utilization ratio of raw material.    DETAILED DESCRIPTION - A two-stage gasification furnace comprises a hole type cylindrical furnace body. The interior of furnace body is divided into two stages of reactors having calabash structure. The dip angle of side furnace wall at contraction part is 45-60 degrees , and the middle narrow part is separated by a furnace row. A furnace row is also arranged under a second stage reactor. A slag collecting room is arranged under the furnace row structure, and a slag discharging port is arranged on the slag collecting room. Nozzles having cylindrical passageway are arranged under the two furnace rows. An upper high-temperature vapor inlet and a lower high-temperature vapor and air inlet are opened at nozzle side. A solid feed inlet is arranged on upper end of first stage reactor and a synthesis gas outlet is arranged at the side. A liquid and particulate feed injection port is arranged at the side of second stage reactor.
NOVELTY - Preparation of a microalgae oil biodiesel comprises providing an algae powder formed by drying microalgae; extracting microalgae oil from the algae powder; representing physicochemical constants of the microalgae oil, and obtaining saponification value for determining quantity of needed methyl alcohol; and using ionic liquid comprising 1-butyl-3-methylimidazolium hexafluorophosphate or tertiary butanol as a reaction medium, adding methyl alcohol with alcohol-oil at a molar ratio of (1:2)-(5:1) to the microalgae oil, and adding 50-400 mg expanding mold lipase.    USE - Method for the preparation of a microalgae oil biodiesel (claimed).
NOVELTY - A hydrogen oxygen separating generating device comprises first shell formed with clapboard having vent holes and first chamber, partition board extends from center of clapboard towards inner wall surface of first shell; second shell formed with first chamber having corresponding grooves formed at two sides of second chamber; pole plates respectively inserted in grooves; and partition boards respectively inserted in grooves, located between pole plates and adjacent to clapboards.    USE - Hydrogen oxygen separating generating device.    ADVANTAGE - The hydrogen and oxygen are separated easily and are output independently. The number of electrolyzing device is increased randomly according to use requirement.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating hydrogen oxygen separating generating device.
NOVELTY - The generator has electrolysis reactor that is connected with anode and cathode of storage battery for vehicle. The electrolysis reactor is provided with anode terminal and cathode terminal. A water inlet above the water tank is connected with an exhaust gas tube. The exhaust gas tube is connected with gas inlet of vehicle engine.    USE - Power source generator for petrol-diesel oil vehicle.    ADVANTAGE - The fuel consumption and emission of harmful gases can be reduced so that service life of the engine is prolonged. The accelerating performance of the engine is improved and vehicle can be started easily. The generator reduces the temperatures of exhaust gas tube and engine cooling water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the power source generator for petrol-diesel oil vehicle.
NOVELTY - The machine has water electrolyzing hydrogen producing device (4) that is interconnected with hydrogen fuel storing container manufacturing workshop (6) by hydrogen transmitting pipeline (5). The hydrogen fuel storing container is interconnected with hydrogen fuel battery (9) by hydrogen fuel transmitting pipe (8). A hydraulic lift (15) is installed behind rod cutting device (14) to adjust height of cutting device. The threshing roller (21) is installed below drying device (19). The niblet storing box (23) is installed below threshing roller.    USE - Corn harvesting machine.    ADVANTAGE - The corn can be dried easily, since threshing roller is installed below drying device, and niblet storing box is installed below threshing roller.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the corn harvesting machine.    Water electrolyzing hydrogen producing device (4)    Hydrogen transmitting pipeline (5)    Hydrogen fuel storing container manufacturing workshop (6)    Hydrogen fuel transmitting pipe (8)    Hydrogen fuel battery (9)    Rod cutting device (14)    Hydraulic lift (15)    Drying device (19)    Threshing roller (21)    Niblet storing box (23)
NOVELTY - The device has an infrared ray source (1) generating infrared radiation. A gas pool (9) to be detected absorbs infrared energy of an absorbing spectral line corresponding to gas to be detected. A gas measuring pool (2) with a gas outlet and a gas inlet fills gas to be detected. An infrared sensor measures infrared energy penetrating a nitrogen pool (8) and gas to be detected. Another infrared sensor measures another infrared energy penetrating the gas pool and gas to be detected.    USE - Device for absorbing and detecting gas infrared ray.    ADVANTAGE - The device realizes precise band filtering property, improves gas infrared ray absorbing and detecting precision and lowest detection concentration, and improves sensitivity and consistency of detection device, and can efficiently filter interference factors. The device has better selectivity for carbon hydrogen explode gas.    DETAILED DESCRIPTION - The gas to be detected is combustible gas. The gas pool to be detected is a carbon hydrogen gas pool. The infrared ray source is made of nickel-chromium electrothermal alloy wire.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for absorbing and detecting gas infrared ray.    Infrared ray source (1)    Gas measuring pool (2)    Infrared sensors (7)    Nitrogen pool (8)    Gas pool (9)
NOVELTY - Method for manufacturing organic fertilizer using waste gypsum, involves mixing waste gypsum, wool and microbial culture in waste food substance in a ratio of 70:10:20, and aging the obtained mixture at 20 degrees C for 15-20 days.    USE - The method is useful for manufacturing organic fertilizer which is used in agriculture and forestry. Can also be used as pesticide in livestock shed for preventing pests, preferably maggot.    ADVANTAGE - The method recycles waste products and thus reduces wastes in environment. The fertilizer is environmentally-friendly and has excellent quality.
NOVELTY - Special biological organic fertilizer comprises (in %): sodium humate (15-16), sheep manure (25-40), furfural slag (25-40), urea (4-5), superphosphate (8-10) and potassium sulfate (4-8), where urea contains 46% of nitrogen, superphosphate contains 12% of phosphorus pentoxide, and potassium sulfate contains 50% of potassium oxide.    USE - The special biological organic fertilizer is useful as base fertilizer (claimed) in agricultural land of watermelon.    ADVANTAGE - The fertilizer improves yield of watermelon, disease resistant and overcomes fertilizer burn in seedlings and strengthens fertilizer effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for preparing the special biological organic fertilizer involves (a) (i) adding bacterial liquid which expands effective microorganism (EM) to the sheep manure and the furfural slag, (ii) sealing and fermenting the mixture for 10-15 days, when the mixture attains wine cube smell in fermented product, sheep manure and fufural salg are fermented fully, and (b) (i) adding the sodium humate, the urea, the superphosphate, the potassium sulfate and soil restoring agent to the fermented product to obtain mixture, where amount of the microorganism soil restoring agent is 3-4 l/ton, (ii) adding the mixture to the organic material in spraying and turning manners using sprayer, and (iii) drying the organic fertilizer to reduce water content of organic fertilizer to be less than 30% through turning; and    (2) method (M2) for fertilizing land of watermelon using biological organic fertilizer, involves (a) digging the sand layer on the above-mentioned land, (b) forming a socket having length of 25-30 cm and width of 10-15 cm, (c) planting the watermelon at an end, (b) digging a small cavity at other end, and (e) covering the sand layer after uniformly mixing the soil with the biological organic fertilizer.
NOVELTY - Preparation of fertilizer involves mixing edible mushroom residue with agricultural waste, and composting the mixture.    USE - Method for preparing fertilizer used for vegetable, particularly tomato, seeding (claimed).    ADVANTAGE - The matrix containing the fertilizer improves growth index of tomato seedling, and solves the problem of peat resource shortage. Edible mushroom residue is recycled as fertilizer, thus, reducing environment pressure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vegetable plug seeding matrix comprising fertilizer, peat and vermiculite.
NOVELTY - A drought-resistant synergistic conditioner comprises (wt.%) polymer (0-3), natural mineral (20-30), and agricultural organic waste (67-77).    USE - Conditioner used for crop culturing, seeding, flower planting, city and garden afforesting, and as soil additive for tobacco or garden pot flower (claimed).    ADVANTAGE - The conditioner regulates water and nutrient in the soil, retains water and fertilizer, modifies soil, improves microenvironment for growing seed or plant, increases efficiency and output of crop, and protects environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of conditioner by respectively preparing polymer and fermenting agricultural organic waste; preprocessing and mixing fermented organic waste and natural mineral, mixing with polymer, and further adding natural mineral; and preparing into grains and checking.
NOVELTY - A glucosamine sulfate potassium chloride complex salt is prepared by mixing anion resin and 10% sulfuric acid solution to obtain saturated sulfate radical; passing glucosamine hydrochloride solution having a concentration of 10 wt.% through a column at rate of 500 ml/hour; adding slowly potassium chloride to the obtained solution at a mole ratio of 2:1, refluxing heating at 45-65 degrees C for 24 hours, and distilling obtained product at 50-60 degrees C; and centrifuging the distillate, filtering, washing the filter cake with 95% ethanol, drying the filter cake at 40-50 degrees C, checking quality, and packing.    USE - Method of preparing a glucosamine sulfate potassium chloride complex salt.    ADVANTAGE - The method is fast, efficient and environment-friendly; reduces operation cost; prepares product having content of 98-102, pH value of 3-5, optical rotation of 50-52, ignition residue of 27-29%, and density of 0.92 that meets American FDA standard; and does not require organic solvent for freeze drying.
NOVELTY - A soil conditioning agent comprises (wt.%): mineral glaucophane powder (40-60), diatomite (10-30), photosynthetic bacteria (3.5-7.5), Saccharomycetes (3-8), nitrogen-fixing bacteria (3-8), lactic acid bacteria (3.5-8.5), growth bacteria (3-8%) and phosphorus-solubilizing bacteria (3-8%).    USE - Soil conditioning agent used for improvement of soil for planting crops.    ADVANTAGE - The agent has small usage amount and exhibits improvement effect. The long-term use of the agent changes soil structure, improves ventilation property, makes heavy metals and pesticide residues in soil completely absorbed and adjusts pH value of soil, thus making soil in neutral state and contributing to normal growth of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the soil conditioning agent which comprises taking glaucophane as raw material, grinding by grinding machine, calcining at 1400 degrees C to remove impurities to form active compound state; extracting oxygen, silicon, phosphorus, sulfur, chlorine, aluminum, calcium, magnesium, sodium, potassium, iron, manganese, titanium, chromium, zinc, copper, lanthanum, cerium, cobalt, nickel, vanadium, molybdenum, scandinavium, gallium, germanium and selenium natural mineral elements from rock by electrolytic process; and finely grinding to obtain powders, and adding diatomite, photosynthetic bacteria, Saccharomycetes, nitrogen-fixing bacteria, lactic acid bacteria, growth bacteria and phosphorus-solubilizing bacteria, mixing to obtain desired soil conditioning agent.
NOVELTY - A heat supply system comprises spiral conveyor, destructive distillation gasification furnace, gas-solid cyclone separator, cooler, gas-liquid separator, filters, Roots blower and gas storage cabinet. An input end of cooler is connected with gaseous phase outlet of cyclone separator. An input end of first-level filter is connected with gaseous phase outlet of gas-liquid separator. An outlet of gas storage cabinet is connected with kiln oven of sodium hydroxide boiler via gas conveying and distributing pipeline. The system takes straw as raw material in sodium hydroxide processing.    USE - Heat supply system.    ADVANTAGE - The system has environmental-friendly production, thus energy source is saved, and service life of device is prolonged.
NOVELTY - Device comprises structure frame (200) forming a cover (210) in upper side of the device, an excrement inlet valve (300), a blower (410), an air inlet (400) connected to the blower, diffuser (420), water level sensor (500), injection nozzle (870), inlet port, outlet port, cavitation pipe, polarity column, peripheral magnet, central magnet and automatic control unit.    USE - The device is useful for preparing liquefied fertilizer.    ADVANTAGE - The device prepares fertilizer rapidly within 24-48 hours.    DETAILED DESCRIPTION - Device comprises structure frame (200) forming a cover (210) in upper side of the device, an excrement inlet valve (300) formed on the upper side of the device for supplying livestock excretion, a blower (410) for supplying air into the device, an air inlet (400) connected to the blower, diffuser (420) having minute holes for diffusing gas into device, water level sensor (500) provided on the side wall of the device for monitoring water level, injection nozzle (870) for removing bubbles during supply of livestock excretion, inlet port, outlet port, cavitation pipe, polarity column, peripheral magnet, central magnet and automatic control unit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device.    Structure frame (200)    Cover (210)    Excrement inlet valve (300)    Air inlet (400)    Blower (410)    Diffuser (420)    Water level sensor (500)    Injection nozzle (870)
NOVELTY - Tar catalyzing and converting agent comprises (in wt.%): sodium carbonate (0.1-0.3), potassium carbonate (0.1-0.3), iron oxide (0.1-1), sodium chloride (0.5-0.8), potassium chloride (0.5-0.8), potassium hydroxide (0.3-0.5), sodium hydroxide (0.3-0.5), nickel nitrate hexahydrate (0.1-1), potassium nitrate (0.1-1), cerium nitrate (0.1-0.5), attapulgite dry powder (20-46) and dolomite dry powder (46-75).    USE - The tar catalyzing and converting agent is useful in gas for biomass boiler.    ADVANTAGE - The tar in gas of biomass boiler can be converted into flammable micromolecule with catalyzer and thus reduces danger caused by tar to large extent.    DETAILED DESCRIPTION - Tar catalyzing and converting agent comprises (in wt.%): sodium carbonate (0.1-0.3), potassium carbonate (0.1-0.3), iron oxide (0.1-1), sodium chloride (0.5-0.8), potassium chloride (0.5-0.8), potassium hydroxide (0.3-0.5), sodium hydroxide (0.3-0.5), nickel nitrate hexahydrate (0.1-1), potassium nitrate (0.1-1), cerium nitrate (0.1-0.5), attapulgite dry powder (20-46) and dolomite dry powder (46-75), where the dolomite dry powder has particle size of 325 mesh size or more, water content of 1% or less and calcium carbonate and magnesium carbonate content of 1-1.5. The attapulgite dry powder has particle size of 325 meshes or more, water content of 1% or less, and magnesium oxide content of 23% or less and silicon dioxide content of 56% or less.
NOVELTY - Submerged membrane bioreactor comprises membrane filter (630) installed in an aerobic bath or a membrane filtering bath (610) in order to separate overlaying water. A membrane cleaning diffuser (640) cleans the membrane of the membrane filter installed at the lower side of the membrane filter. A cover (650) is installed at the upper side of the membrane filter. A gas circulating pipe (660) connects the cover and the entrance of a membrane cleaning blower (620). An air pipe connects the membrane cleaning diffuser and the exit of the membrane cleaning blower.    USE - The submerged membrane bioreactor is useful for processing sewage (claimed).    ADVANTAGE - The bioreactor separately controls dissolved oxygen concentration and air volume of sewage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of processing sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of submerged membrane bioreactor.    Membrane filtering bath (610)    Membrane cleaning blower (620)    Membrane filter (630)    Membrane cleaning diffuser (640)    Cover (650)    Gas circulating pipe (660)
NOVELTY - Preparing organic substrate involves composting vine and mixing chitin as an adjunct during the thermophilic phase of composting and then inoculating Trichoderma harzianum T78 strain in the end of the thermophilic phase of composting.    USE - Method for preparing organic substrate used for controlling plant disease such as vascular diseases in plants, Fusarium wilt in field crops and scab in melon during soilless culture and cultivation of melon and inducing resistance against pathogenic microorganism, and used in fertilizer for stimulating plant growth (all claimed).
NOVELTY - Sandy soil is modified by adding straw modified material into soil and uniformly mixing with surface soil; when ratio of soil is 85% more than 0.02 mm of sand, adding 1400-1750 kg/acre of straw modified material; when ratio of soil is 55-85% more than 0.02 mm of sand, adding 750-1000 kg/acre of straw modified material; and when ratio of soil is 50% less than 0.02 mm of sand, adding 300-500 kg/acre of straw modified material. The straw modified material is obtained by uniformly mixing corroded crop straw, calcium-based bentonite and anionic polyacrylamide at mass ratio of 900-1000:100-120:5-30.    USE - Method for modifying sandy soil (claimed).    ADVANTAGE - The method has no secondary pollution, low cost and no hardened soil; and does not need to do any modifying on a sandy land or cultivated land and does not need subsequent management. The straw modified material has characters of soil modifying agent of an organic fertilizer.
NOVELTY - Preparing organic fertilizer, by (a) mixing livestock excrement and human excrement, pulverizing mixture, and storing mixture, (b) mixing pulverized mixture with other raw materials e.g. briquet and sewage sludge in mixing tank, (c) heating mixture, (d) fermenting mixture with potassium permanganate solution and sodium hypochlorite solution, (e) adding potassium permanganate and inorganic activator to mixture, and drying mixture, (f) supplying moisture to dried product, (g) molding mixture, (h) drying obtained product, and (i) packaging product.    USE - The method and system are useful for preparing organic fertilizer (claimed).    ADVANTAGE - The prepared fertilizer is environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing organic fertilizer, involves (a) mixing livestock excrement and human excrement in the weight ratio of 6:4, agitating the mixture, pulverizing the mixture, and storing the mixture in a storing tank, (b) mixing the pulverized mixture with other raw materials chosen from briquet, shell powder, husk powder, sawdust and sewage sludge in a mixing tank, (c) heating the mixture in a heat exchanger, (d) fermenting the mixture in a fermenting tank with potassium permanganate solution and sodium hypochlorite solution at 25-30 degrees C, (e) adding potassium permanganate and inorganic activator to the fermented mixture, and drying the mixture using a drier, (f) supplying moisture to the dried product using a moisture supplier, (g) molding the mixture into fertilizer form using a fertilizer molder, (h) drying the obtained product, and (i) packaging the obtained product. An INDEPENDENT CLAIM is included for system for preparing the fertilizer.
NOVELTY - A continuous biodiesel-producing system comprises liquid alcohol storage groove, continuous extracting module having extracting grooves, tube-type trans-esterification reactor, and gas and liquid separating groove used for separating trans-esterification product to obtain biodiesel. The extracting grooves are used for receiving liquid alcohol and extracting oil raw material in extracting grooves to obtain extracting product. The trans-esterification reactor is used for receiving the extracting product.    USE - A continuous biodiesel-producing system.    ADVANTAGE - The system simplifies the preparation of the biodiesel, reduces manpower, and reduces usage of energy source since the same alcohol is used for extraction reaction and trans-esterification reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biodiesel comprising pressing and heating liquid alcohol to supercritical state or high pressure liquid state, extracting the supercritical state or high pressure liquid state alcohol, performing trans-esterification reaction, and separating the trans-esterification product.
NOVELTY - Method of improving saline-alkali soil, involves biologically composting garbage, remains of dead animal and plant, sludge and kitchen garbage for protecting ecological equilibrium and increasing crop yield.    USE - The method is useful for improving saline-alkali soil for producing strong seeds and promoting high yield of crops.    ADVANTAGE - The method reduces garbage processing problem, changes waste material into valuable products and saves resources. The biological fertilizer degrades farm chemical fertilizer residue, increases sugar degree, improves quality of soil, and produces green product without any harmness to soil. The method reinforces root activity, increases absorbing area of soil, increases crop stress resistance, overcomes continuous cropping disease and reduces soil disease as it forms mycorrhizal fungi.
NOVELTY - Fumaric acid tiamulin is refined by adding acetone to crude fumaric acid tiamulin at a mass ratio of 1:3-4 at 55-57 degrees C while stirring at 35-45 rpm, refluxing for 3-5 hours, reducing to 8-10 degrees C/hour, adjusting stirring speed to 18-22 rpm to crystallize backflow, adding fumaric acid tiamulin seed crystal at 48 degrees C, keeping the temperature for 2-3 hours when it is reduced to 1 degrees C to crystallize, filtering, adding cold acetone, removing impurities, filtering to obtain fumaric acid tiamulin refined powder, and vacuum drying at 55-65 degrees C and 6 degrees C/hour and - (0.07-0.09)MPa for 2-4 hours.    USE - Method for refining fumaric acid tiamulin (claimed).    ADVANTAGE - By using the property that the fumaric acid tiamulin is slightly soluble in the acetone, the method can reduce the dosage of refining solvent, reduce the consumption of solvent, save the production cost, reduce impurities in the product, and improve the product quality.    DETAILED DESCRIPTION - Refining fumaric acid tiamulin involves taking crude fumaric acid tiamulin, adding acetone at a mass ratio of 1:3-4, raising the temperature to 55-57 degrees C while stirring at 35-45 rpm, and refluxing and keeping the temperature for 3-5 hours. The temperature is reduced at 8-10 degrees C/hour. The stirring speed is adjusted to 18-22 rpm to crystallize the backflow. Fumaric acid tiamulin seed crystal is added at 48 degrees C. The temperature is kept for 2-3 hours when it is reduced to 1 degrees C to crystallize the product. The product is filtered. Cold acetone is added to clean the product twice. Impurities are removed. The product is filtered to obtain fumaric acid tiamulin refined powder. The powder is placed into a vacuum drying oven at 55-65 degrees C and 6 degrees C/hour. The degree of vacuum is - (0.07-0.09) MPa. Refined fumaric acid tiamulin raw powder is obtained after drying the refined powder for 2-4 hours.
NOVELTY - Synthesis of 2-cyano-7-azaspiro(3,5)nonane derivative includes using piperidine formaldehyde as initial raw material and benzyltrimethylammonium hydroxide as an alkali; reacting the raw materials with acrylonitrile; in ethanol solution, reacting the obtained product with sodium borohydride to reduce aldehyde into alcohol; reacting the reduced alcohol and p-methylbenzene sulfonyl chloride at room temperature using 4-dimethylaminopyridine as catalyst, to protect the hydroxy group; and subjecting the obtained product and lithium hexamethylsilylamine to ring-closing reaction.    USE - Synthesis of 2-cyano-7-azaspiro(3,5)nonane derivative (claimed) useful as intermediate for synthesis of medicines or useful product.    ADVANTAGE - The method solves the prior art problems of using metal catalyst that causes unstable yield, heavy pollution, difficult purification, and low yield.    DETAILED DESCRIPTION - Synthesis of 2-cyano-7-azaspiro(3,5)nonane derivative includes:    (A) using piperidine formaldehyde as initial raw material and benzyltrimethylammonium hydroxide as an alkali; and reacting the raw materials with acrylonitrile to obtain 4-propionitrile-4-formaldehyde piperidine derivative;    (B) in ethanol solution, reacting the obtained product with sodium borohydride to reduce aldehyde into alcohol;    (C) using 4-dimethylaminopyridine as catalyst; at room temperature, reacting the reduced alcohol and p-methylbenzene sulfonyl chloride to protect the hydroxy group; and    (D) at - 78 degrees C to room temperature, subjecting the obtained product and lithium hexamethylsilylamine to ring-closing reaction to obtain 2-cyano-7-azaspiro(3,5)nonane derivative.
NOVELTY - The method involves mixing solid citrus residue with water with contaminants, where amount of the water with contaminants is equal to amount of fresh water free from contaminants. Aqueous slurry is hydrolyzed in atmospheric pressure in a hydrolysis reactor (2) heated by direct injection of steam. Pressure of the hydrolysis reactor is lowered suddenly to the atmospheric pressure. Limonene is extracted by condensing vapor-limonene. Limonen tarmat hydrolysat is collected. Pectin is extracted. Ethanol, biogas and/or bio fertilizer is produced.    USE - Method for producing multifarious products of citrus residues.    ADVANTAGE - The ethanol, the biogas and/or the bio fertilizer is produced in a simple and inexpensive manner without virtually generating waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a hornbeam device.    Hydrolysis reactor (2)    Water inlet line (2a)    Inlet line (2b)    Steam inlet line (2c)    Hydrolysates outlet pipe (2d)
NOVELTY - The invention relates to an antagonist Trichoderma viridae strain Td50, deposited under number (P) 001158 to NCAIM Budapest, presenting a strong antagonistic character related to a series of phytopathogenic fungi and to a process for using the same for the bioconversion of marc resulting from ethanol manufacturing into a an antifungal biopreparation, by passing the marc resulting from ethanol manufacturing into a mixer to which 0.4...0.5% of potassium superphosphate is added for normalizing the potassium content, inoculating with 0.1% hydrogellified biopreparation based on Trichoderma viridae obtained by drying granules of Td50 fungi formed after having been cultured onto an agarized Weidling medium and then inoculated on a hydrogellified medium for industrial multiplication, for 7 days and maintaining the resulting composition for 7...8 days while stirring with 1 rot/h frequency for aerating the substrate, to result a highly efficient biopreparation for the phytosanitary management of vegetable waste.
NOVELTY - Organic fertilizer is obtained by mixing soil microorganism with other microorganisms e.g. yeast, cellulose degrading bacterium, nitrogen-fixing bacteria, fungi, Lactobacillus, Bacillus subtilis, Aspergillus oryzae, methanoic acid bacteria, iron-oxidizing bacteria, photosynthetic bacterium, soil actinomycetes, and organic waste, fermenting the mixture, mixing the fermented mixture and organic fertilizer raw material with nutritious raw materials, and again fermenting the mixture.    USE - As organic fertilizer.    DETAILED DESCRIPTION - Organic fertilizer is obtained by mixing soil microorganisms (0.1-0.5 wt.%) with other microorganisms including yeast, cellulose degrading bacterium, nitrogen-fixing bacteria, fungi, Lactobacillus, Bacillus subtilis, Aspergillus oryzae, methanoic acid bacteria, white rot fungus, iron-oxidizing bacteria, iron reducing bacteria, sulfate-reducing bacteria, thiophilic bacteria, nitrobacter, manganese oxidizing bacteria, nitrifying bacteria, heterotrophic bacteria, manganese reducing bacteria, photosynthetic bacterium, soil actinomycetes, beneficial bacteria and organic waste (99.5-99.9 wt.%) chosen from rice bran and bean-curd refuse, subjecting the mixture to superheat fermenter, fermenting the mixture at 60-200 degrees C for 20-30 hours to produce soil microorganism group, mixing the fermented mixture (0.01-0.05 wt.%) and organic fertilizer raw material (99.95-99.99 wt.%) with nutritious raw materials, subjecting the mixture to superheat fermenter, and fermenting the mixture at 100-200 degrees C for 20-50 hours. An INDEPENDENT CLAIM is included for method for preparing the above-cited organic fertilizer.
NOVELTY - The biomass gasification system (1) has gasifier (2) for producing combustible gas known as producer gas or synthesis gas (3) by gasifying biomass in presence of oxidizer. The synthesis gas is received by gas engine (4) which generates energy using the synthesis gas, and the gas storage (5) which stores synthesis gas and provides stored synthesis gas to the gas engine based on availability of the synthesis gas from the gasifier to the gas engine.    USE - Biomass gasification system.    ADVANTAGE - Starts system in a self-sustainable way without depending on external power source. Conserves gas for other utilities by providing flow control mechanism. Reduces start time for biomass gasification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass gasification system.    Biomass gasification system (1)    Gasifier (2)    Synthesis gas (3)    Gas engine (4)    Gas storage (5)
NOVELTY - The structure has a gasification furnace comprising a gas burner connected with a gas outlet pipeline, where the burner is set with wind inlet. An outer surface of the furnace is equipped with a blower. A pipe wall of a gas pipe is provided with a hollow interlayer, whose two ends are respectively connected with an outlet and burner wind inlet. The outlet is provided with a temperature collecting device, which is connected with a control unit, where the control unit receives a signal of the temperature collecting device and controls a fan according to the signal.    USE - Biomass gas transmission pipeline prevent tar cohesion structure.    ADVANTAGE - The structure avoids gas pipe thermal insulating and high temperature burner air distribution problem by setting special distribution and gas transmission pipeline so as to improve heat transfer efficiency of a gasification generation oil burning system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gas transmission pipeline prevent tar cohesion structure.
NOVELTY - The purifier has a cylindrical casing (1) whose wall portion is provided with an air inlet (2) and an air outlet (3). A filter (4) is fixed on the top of casing. An opening of air inlet and air outlet is provided with a baffle plate (5). The bottom portion of casing is connected with an impurity storage tank (6).    USE - Gas purifier for straw gasification device.    ADVANTAGE - The tar and impurity in fuel gas cam be effectively removed by fuel gas cleaner. The environmental protection effect of gas purifier can be improved. The corrosion of combustion equipment can be avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gas purifier.    Cylindrical casing (1)    Air inlet (2)    Air outlet (3)    Filter (4)    Baffle plate (5)    Impurity storage tank (6)
NOVELTY - A hydrogen oxygen gas-evolution combustion apparatus (34) has an electrolysis tank which electrolyzes water, a gas-liquid separation tank which separates liquid moisture content mixed with gas emitted by electrolysis, a burner (53) which burns the gas, a cooler (38) which cools gas provided from gas-liquid separation tank and provided between gas-liquid separation tank and burner, and a heater (51) which heats gas discharged from cooler and provided downstream the burner.    USE - Hydrogen oxygen gas-evolution combustion apparatus. Uses include but are not limited to welding machine, metal cutting and disassembling apparatus, combustion furnace, combustion apparatus of thermal power station, turbine plant, combustion apparatus of garbage incineration system, engine and boiler combustion apparatus.    ADVANTAGE - The hydrogen oxygen gas-evolution combustion apparatus is safe, and suppresses backfire or explosion. The generation of mist of water is prevented. The water vapor volume in gas is reduced. The gas has high combustion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of hydrogen oxygen gas-evolution combustion apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the hydrogen oxygen gas-evolution combustion apparatus.    Hydrogen oxygen gas-evolution combustion apparatus (34)    Cooler (38)    Heater (51)    Burner (53)    Flame (54)
NOVELTY - Producing biodiesel fuel includes preparing vegetable oil by heating the oil up to 80 degrees C, and performing alkaline ethanolysis by potassium hydroxide in ethanol of a molar concentration of 2 mole/dm3, where before heating, the vegetable oil is mixed with 1% aqueous solution of an eco-friend preparation, and the vegetable oil is maintained in mixture for 24 hours at 23-27 degrees C.    USE - The process is useful for producing biodiesel fuel.
NOVELTY - Combination of compost receptacle (10) (defines opening (12) having two side walls (14) join together at two wall angles on opposite ends forming flattened cone shape, and side walls tapers into a point) and removable newspaper liner (arranged complementary to shape of opening with side surfaces that tapers into closed point, to receive newspaper liner when opening, the point of opening receives closed point of liner, and newspaper liner forms disposable compost collector (collects and retains household food waste to compost and then be removed when full) out of newspaper liner), is claimed.    USE - The combination is useful for capturing and storing compostable material before transferring to the green bin outside or other external disposal.    ADVANTAGE - The combination provides proper ventilation thus reducing the food waste and avoiding cleaning the green bin or municipal collection vehicle and thus reducing the fuel cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the compost receptacle, comprising the opening, where the opening is in the form of a cone shape and is sized to receive a paper based liner that has been arranged into a complementary cone shape, and the food waste can be collected and retained within the cone shaped liner during use; and    (2) collecting household compost for recycling, comprising: using the compost receptacle having a cone shaped opening; constructing a paper based liner into a cone shape that complements the shape of the opening; placing the paper based liner in the opening to form a removable compost collector; placing household compost in the compost collector; and removing the compost collector when full of compost.    DESCRIPTION OF DRAWING(S) - The figure shows the schematic view of the compost receptacle and the lid.    Compost receptacle (10)    Opening (12)    Side wall (14)    Lid (50)
NOVELTY - The method involves obtaining gasification medium by pure vapor. The vapor is heated by more than 900 degrees Celsius. A constant current injection fixed bed gasification reactor (7) is connected with a biomass gasification steam part in high temperature of 900 to 1050 degrees Celsius to obtain hydrogen-rich gas. Volume of hydrogen in hydrogen-rich gas fraction is from 45 to 51 percent, reaction time is 30 min and a gasifier is 11 to 14MJ/Nm3. Biomass is saw dust or rice hull.    USE - Biomass high temperature steam method for producing gas by gasification hydrogen-rich gas.    ADVANTAGE - The method enables avoiding catalyst properties and obtaining high hydrogen-rich gas. The method enables improving utilization energy rate. The method enables converting the biomass of low quality into hydrogen with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass high temperature steam device for producing gas by gasification hydrogen-rich gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass high temperature steam device.    Constant flow metering pump (4)    Steam generator (5)    Tubular furnace (6)    Constant current injection fixed bed gasification reactor (7)    Condensing pipe (8)
NOVELTY - The system has a top cover arranged on top of a water interlayer and provided with a material position power device. Bottom of the interlayer is connected with an ash bin. An air outlet is arranged on a side part of the ash bin. An upper part of the ash bin is provided with a fire grate. The power device is in transmission connection with a fixing plate that is connected with a distributing motor. An output shaft of the motor is extended downward in the top cover, and includes a material rake. A discharging pipe of a feeding lifting machine passes via the top cover, and extends into a hearth.    USE - Large biomass forming fuel fixed bed gasification power generating system.    ADVANTAGE - The system takes biomass forming fuel as raw material, ensures continuous operation of a large-scale gasification furnace, and avoids limitation of generating power of 1 megawatt.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a large biomass forming fuel fixed bed gasification power generating system.
NOVELTY - The method involves conveying municipal solid waste comprising inorganic material and organic material into pre-conditioner unit. The waste in pre-conditioner unit is treated to sterilize majority of waste. The ferrous and non-ferrous materials are separated. The inorganic materials are separated from organic materials, in an environment of saturated steam. The environment of saturated steam containing organic matter is heated to a temperature of 160 degrees C. A gaseous by-product is produced by heating the organic material in an environment of depleted oxygen at about 7000 C.    USE - Method for converting municipal solid waste into fuel for gas powered turbine engines.    ADVANTAGE - The municipal waste is effectively treated and used for generation of electric power. Uniform pyrolysis is carried out along with reduced retention time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pyrolysis apparatus for treating municipal waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pyrolysis unit within a waste processing facility.    Fiber (103)    Dryer (104)    External manifold (106)    Gas powered turbine engine (107)    Gas storage unit (108)
NOVELTY - Hydrogen production comprises: providing a gas mixture comprising methanol and oxygen; conducting gas mixture to flow through a catalyst at an ambient temperature lower than 100 degrees C, where the catalyst is a member comprising e.g. manganese/zinc oxide and copper/manganese oxide catalysts; catalyzing and initiating a partial oxidization of methanol (POM) process, where the POM process supplies heat energy itself; and generating a hydrogen rich gas (HRG) at less than or equal to 200 degrees C, where HRG contains less than or equal to 4 vol.% carbon monoxide, and the POM process generates greater than or equal to 1.8 moles hydrogen per 1 mole methanol consumed.    USE - The process is useful in petroleum industry and fuel cell technology.    ADVANTAGE - The process: eliminates the need of external heat for initiating the POM process; provides high hydrogen yield; and is economic.    DETAILED DESCRIPTION - Hydrogen production comprises: providing a gas mixture comprising methanol and oxygen; conducting the gas mixture to flow through a catalyst at an ambient temperature lower than 100Q, where the catalyst is a member comprising manganese/zinc oxide, copper/manganese oxide, copper/cerium oxide, copper-cerium/zinc oxide and copper-manganese/zinc oxide catalysts; catalyzing and initiating a partial oxidization of methanol (POM) process, where the POM process supplies heat energy itself; and generating a hydrogen rich gas (HRG) at less than or equal to 200 degrees C, where the HRG contains less than or equal to 4 vol.% carbon monoxide, and the POM process generates greater than or equal to 1.8 moles hydrogen per 1 mole methanol consumed.    DESCRIPTION OF DRAWING(S) - The figure shows a diagram schematically illustrating a POM process.    Reactants (100)    Reduced catalyst (200)    Fixed bed reactor (201)    Mixing chamber (202)    Reaction products (300)
NOVELTY - An integrated device comprises chain grate and kiln. The chain grate is arranged in the kiln. A material inlet is arranged at one end of chain grate. The kiln is divided into coking chamber, burnout chamber and de-dusting chamber. The coking chamber is arranged at upper part of chain grate and is divided into as burnout chamber and de-dusting chamber via the rear arch located above coking chamber and isolating wall with holes. The burnout chamber is located at one side of material inlet. The de-dusting chamber is connected with a hot air outlet.    USE - Integrated device for continuously making charcoal by using biomass fuel and utilizing hot air.    ADVANTAGE - The device solves the problem that biomass fuel cannot be used for continuously producing and heat cannot be effectively used in charcoal making process. It controls output and quality of charcoal via adjusting the operating speed of chain grate, thus avoiding generation of waste product.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating an integrated device.
NOVELTY - Manufacture of butanol gasoline blend involves blending biologically-sourced butanol isomer(s) with gasoline. The butanol gasoline blend has high-butanol driveability index (HBDIa) which satisfies specific relation.    USE - Manufacture of butanol gasoline blend (claimed) used for spark-ignition engine for vehicle.    ADVANTAGE - The butanol gasoline blend is manufactured efficiently with excellent cold-start and warm-up driveability characteristics.    DETAILED DESCRIPTION - Manufacture of butanol gasoline blend involves blending biologically-sourced butanol isomer(s) with gasoline. The butanol gasoline blend has high-butanol driveability index (HBDIa) which satisfies relation of formula: HBDIa=BuOH(A1+A2E200+A3RVP) which is below the maximum limit of driveability index (DI) of gasoline measured based on ASTM D 4814, where BuOH is concentration in volume percent of the biologically-sourced butanol isomer in butanol gasoline blend, E200 is volume percent of butanol gasoline blend which distills at 200 degrees F or less, RVP is Reid Vapor Pressure in psi, and A1-A3 are coefficients selected to give a linear relationship between the values of the linear combination of butanol gasoline blend and logarithms of the mean corrected measured total weighted demerits of blends, at concentrations of the at least one biologically-sourced butanol isomer of 80 volume% or less, and total weighted demerits of butanol gasoline blend of less than 40. INDEPENDENT CLAIMS are included for the following:    (1) butanol gasoline blend; and    (2) method for identifying butanol gasoline blend.
NOVELTY - Method and a device for optimal use of all energy sources during the production of bio-coal by a pyrolysis process in a reactor (10), are claimed.    USE - The energy sources obtained during the production of bio-coal is useful for producing heat, electricity and liquefied petroleum gas (claimed).    ADVANTAGE - The reactor has a space-saving design, a large volume capacity, is capable of quick production of the product, is suitable for different organic matters, biomasses for the production the final product, has a equipment for automatic filling up and emptying after the termination of processes, where the final product is automatically ejected outside of the reactor, is operated with an external energy source and then further operated with the energy-rich gas, is filled with gas and/or oil, thus it has a reduced pollutant emissions. The heat between the air layers is sucked off thus the reactor can be cooled in rapid manner, which enables the multiple fillings.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the overall system with a reactor.    Reactor (10)    Lower building (20)    Motor house (30)
NOVELTY - The method involves stopping water electrolysis process of water electrolysis apparatus (10). The pressure of hydrogen generated in cathode side electrolysis chamber is set based on concentration of hydrogen with respect to oxygen. The operation of water electrolysis apparatus is stopped when set hydrogen pressure is below than atmospheric pressure. The hydrogen is leaked to anode side when pressure of hydrogen exceeds atmospheric pressure.    USE - Method for shutting down water electrolysis apparatus.    ADVANTAGE - The operation of water electrolysis apparatus is stopped when set hydrogen pressure is below than atmospheric pressure so as to prevent expansion of hydrogen in electrolytic membrane during shut down period, so that damage of electrolytic membrane is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of water electrolysis apparatus.(Drawing includes non-English language text)    Water electrolysis apparatus (10)    Water electrolysis mechanism (12)    Pure-water supply structure (14)    Water circulation mechanism (16)    Controller (18)
NOVELTY - Rural household biogas digesters deslagging hand screw comprises an outer cylinder, a screw, a gear, and a hand lever. The outer cylinder is installed with a slag inlet (1) and a slag outlet. The screw is axially installed in the outer cylinder. The screw on one end of the slag outlet is extended into the outer cylinder. The extended screw is installed on a gear C (5). The gear C is installed with a gear B (4) on the outer cylinder. The gear B is installed with a gear A (3) on the outer cylinder, and the outer end surface of the gear A is installed with a hand lever (2).    USE - Used as a rural household biogas digesters deslagging hand screw.    ADVANTAGE - The device has simple structure and convenient usage; removes the slag in the biogas digester, thus increases the yield of the biogas; is safe; and ensures long-term service life of the biogas digester.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the rural household biogas digesters deslagging hand screw.    Slag inlet (1)    Handle lever (2)    Gear A (3)    Gear B (4)    Gear C (5)
NOVELTY - A hydrogen storage material (1) comprises hydrogen storage alloy (10), and carbon nanotube (20) which is coupled with surface of hydrogen storage alloy.    USE - Hydrogen storage material for hydrogen fueled engine motor vehicle.    ADVANTAGE - The hydrogen storage material is excellent in heat conductivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a manufacturing method of hydrogen storage material involving supplying carbon source gas while arranging hydrogen storage alloy in heating atmosphere, making carbon nanotube grow from surface of hydrogen storage alloy with chemical gaseous phase synthesis method, bonding end of length direction of carbon nanotube with surface of hydrogen storage alloy and obtaining hydrogen storage material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen storage material.    Hydrogen storage material (1)    Hydrogen storage alloy (10)    Carbon nanotube (20)
NOVELTY - Method for producing saccharolytic enzyme from Porodisculus pendulus, involves culturing P.pendulus in culture medium having pH of 5.5-6.0 at 25-30 degrees C, and separating saccharolytic enzyme from the culture medium, where the culture medium comprises cellulose as carbon source, and corn powder, peptone and/or yeast extract as nitrogen source.    USE - The method is useful for producing saccharolytic enzyme which is used for producing biofuel (claimed).    ADVANTAGE - The method produces biofuel cost-effectively in large amounts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing biofuel, which involves using biomass chosen from cellulose and rice straw.
NOVELTY - Carbonization furnace for fine particles of biomass raw material comprises a furnace body of high temperature resistant stainless steel or inner and outer surface with heat-resistant steel for enamel treatment.    USE - Used as a carbonization furnace for fine particles of biomass raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the carbonization furnace for fine particles of biomass raw material.
NOVELTY - A fluidized bed reactor system comprises vacuum feeder, fluidized bed, cyclone separator, and condenser. An outer wall of the fluidized bed has electric heating device having wall provided with heat medium layer. A bottom of fluidized bed is connected with a preheating carrier gas inlet pipe. The fluidized bed through a gas conveying pipe is connected to the cyclone separator, gas pipe and condenser.    USE - A fluidized bed reactor system.    ADVANTAGE - The reactor system does not use oxygen, has high temperature heating rate (1000-10000 K/s) and has short reaction time (less than 2 seconds). It is capable of providing short chain low molecular substance product and improves yield and quality of biological oil.
NOVELTY - Recycling system of waste iodine in the production of diosmin comprises a main reaction system connected with the iodine waste solution tank, and iodine waste solution storing tank via first plate frame filter connected with iodine waste solution acidification tank, which is connected with reaction precipitation tank via second plate frame filter. The reaction precipitation tank is connected with centrifuge. The iodine waste solution acidification tank is connected with sulfuric acid measuring tank. The reaction precipitation tank is further connected with hydrogen peroxide storage tank.    USE - Used as a recycling system of waste iodine in the production of diosmin.    ADVANTAGE - The system utilizes simple equipment; can achieve the quality standard that can be recycled and the recycling rate is more than 95%; reduces the consumption of iodine and production cost of diosmin; operates under normal temperature with less volatility; and is environmental friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the recycling system.
NOVELTY - Methane generation involves grinding crop straw and exploding with gas, adding microorganisms (0.1-0.2 wt.%, based on weight of crop straw), applying water and stacking, mixing with animal excrement until carbon and nitrogen ratio is 20-30:1, and inoculating with biogas slurry; and anaerobically fermenting at 25-35 degrees C.    USE - Method for generating methane (claimed).    ADVANTAGE - The method reduces cellulose, hemicellulose and lignin of straw to obtain high yield; prevents organic acid from accumulating excessively; and ensures balance temperature in anaerobic reactor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methane generation system comprising an excrement storage tank connected with a mixing tank through a pipe; a first conveying pump between the excrement storage tank and mixing tank; an anaerobic reactor connected with the mixing tank through a pipe; a second conveying pump between the mixing tank and reactor; a circulated water heating boiler outside the reactor; a backflow liquid outlet arranged on bottom end of reactor and connected with a material feeding port through a backflow pump; a biogas residue discharge port arranged on bottom end of reactor and connected with a biogas residue storage pool; a plate frame press respectively connected with biogas residue storage pool and mixing tank through conveying pipes; a third conveying pump between the biogas residue storage pool and plate frame press; and a fourth conveying pump between the plate frame press and mixing tank. The mixing tank, second conveying pump, anaerobic reactor, biogas residue storage pool, third conveying pump, plate frame press and fourth conveying pump form a closed loop.
NOVELTY - Biodiesel production involves adding lipase to fermentation liquid containing thallus of wall-cracked petroliferous microorganism and hydrolyzing to remove aqueous phase and obtain oil phase; and adding lipase and short chain alcohol to oil phase and esterifying.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method reduces energy consumption, avoids reversible reaction during converting to esterification reaction from hydrolysis, and improves conversion ratio of biodiesel.
NOVELTY - Preparation of bio-oil with low acidity and low oxygen content in two-section conversion method comprises using biomass particles as raw materials; and conducting first-phase fluidized bed pyrolysis at 400-450 degrees C and 0.01-0.1 MPa and second-phase microwave pyrolysis at 450-600 degrees C and atmospheric pressure, where microwave frequency is 2400-2500 MHz, initial power is 0.9-1.1 kW, nitrogen flow rate is 0.10-0.20 m3/hour, and after the temperature of the material to be reacted reaches the predetermined temperature of 400-600 degrees C, the power is reduced to 0.25-0.35 kW.    USE - Preparation of bio-oil with low acidity and low oxygen content in two-section conversion method (claimed).    ADVANTAGE - The product steam can continuously flow out and the raw material biomass particles can be circulated in the bed, where the particles residence time in the reactor is 0.1-3 seconds. The large particles are fully cracked until the particles become small; and then the particles are discharged from the bed layer by gas. The bio-oil steam cracked by the first-phase fluidized bed is catalyzed and upgraded in a microwave field to reduce energy consumption and improve the quality of bio-oil.
NOVELTY - An LED lighting system comprises a wind driven generator and/or solar energy photovoltaic panel, a hydrogen energy brine electrolysis hydrogen generator with output end connected with a hydrogen storage, a hydrogen energy generating set with load for LED lighting, and an electrical control system. The loads of the wind driven generator and/or solar energy photovoltaic panel are two supplying sub-circuits for LED lighting directly and for hydrogen energy brine electrolysis hydrogen generator, respectively. The output end of the hydrogen storage is connected with the generating set.    USE - An LED lighting system for wind energy, solar energy, and wind-light complementary hydrogen energy electricity-generating, storing, and supplying (claimed).    ADVANTAGE - The lighting system can solve the problem of storage and synchronization of solar electrical energy generation and wind power generation. It can form the independent out-of-net power-supply system, namely the distribution type micro-power grid system.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of a LED lighting system.
NOVELTY - A substitution reaction is carried out between an aryl borate compound (II) and metal nitride (III) in presence of a cuprous catalyst and aqueous ammonia, to obtain trinitride compound (I).    USE - Synthesis of trinitride compound is used for medicines, polymers and natural products.    ADVANTAGE - The method effectively provides trinitride compound with high yield and tolerance without polluting the environment.    DETAILED DESCRIPTION - A substitution reaction is carried out between an aryl boric compound of formula (II) and metal nitride of formula: MN3 (III) in presence of a cuprous catalyst and aqueous ammonia, to obtain trinitride compound of formula (I).    M=lithium, sodium, potassium, cesium or rubidium;    R=H, 1-20C alkyl, 2-20C vinyl, 2-20C alkynyl, 6-20C aryl, halo, -OH, -NO2, -NH2, -NHR', -C(=O)OR', -NHC(=O)R', -OR' or -C(=O)R';    R'=H, 1-6C alkyl, 2-6C vinyl, 2-6C alkynyl, phenyl or benzyl, or    R+benzene ring=fused ring, and    n=1-5.
NOVELTY - Controlling fermentation in biomass microenvironment, involves crushing biomass, mixing biomass and nitrogen source ingredients, stirring the contents to obtain mixture, and adjusting pH of the mixture at 6-9.5 and controlling water content of mixture to 40-75% to obtain nutritional material, and filling the nutrition material into artificial fermentation device, fermenting nutritional material at 65-85 degrees C for 48 hours by specific bacterial colony, 55-65 degrees C for 48 hours by fungal colony and 30-55 degrees C for 48 hours by Actinomycetes colony to decompose biomass.    USE - The method and device are useful for controlling fermentation in biomass microenvironment (claimed).    ADVANTAGE - The method ferments waste materials into useful products, hence reduces environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device, which has simulated rumen, reticulum and omasum, where the stimulated rumen comprises air inlet and air outlet, the reticulum is placed into the stimulated rumen and is a basket containing ventilating holes, the omasum is placed into the reticulum comprising hollow cylinder and pressing gasket, the pressing gasket is arranged on the hollow cylinder, heat-dissipating oxygen flowing holes are opened on the pressing gasket, and walls of the heat-dissipating oxygen flowing holes are extended to heat-dissipating oxygen flowing pipes in downward position and the heat-dissipating oxygen flowing pipes are inserted in the hollow cylinder.    DESCRIPTION OF DRAWING(S) - The drawing shows perspective view of device for controlling fermentation in biomass microenvironment.
NOVELTY - Integrated machine comprises water electrolysis hydrogen production air-liquid separation unit. The separation unit is provided with a hydrogen outlet and an oxygen inlet. The separation unit further comprises oxygen purification unit. The pure oxygen inlet of the oxygen purification unit is connected to the oxygen outlet of the water electrolysis hydrogen production air-liquid separation unit. The pure oxygen outlet of the oxygen purification unit is externally connected to an oxygen recycling device.    USE - The integrated machine is useful for electrolyzing water.    ADVANTAGE - The machine is simple and suitable for industrial use, and saves cost, space and social resource.    DESCRIPTION OF DRAWING(S) - The figure shows schematic view of integrated machine.
NOVELTY - An integrated system of biomass pyrolysis coal gas comprises crushing molding device (1); a pre-processing device (2); a high-temperature pyrolysis device (3); a gas-liquid separating system(4); a gas purifying system (5); a high-purity combustible gas; an ecological charcoal; an active carbon; a collecting liquid; a processing liquid; and related control system and device.    USE - An integrated system of biomass pyrolysis coal gas.    ADVANTAGE - The system is automatic and operated continuously, requires fewer operators, and has low energy consumption.    DETAILED DESCRIPTION - An integrated system of biomass pyrolysis coal gas comprises:    (A) crushing molding device (1);    (B) a pre-processing device (2);    (C) a high-temperature pyrolysis device (3);    (D) a gas-liquid separating system(4);    (E) a gas purifying system(5);    (F) a high-purity combustible gas;    (G) an ecological charcoal;    (H) an active carbon;    (I) a collecting liquid;    (J) a processing liquid; and    (K) related control system and device.    The biomass is pyrolyzed into activated carbon by crushing, molding and pre-processing; and extracting combustible gas (preferably hydrogen and carbon dioxide) and liquid into a biopesticide product for environment protection, bioenergy and biopesticide.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an integrated system of biomass pyrolysis coal gas. Drawing includes non-English language text.    Crushing molding device (1)    Pre-processing device (2)    High-temperature pyrolysis device (3)    Gas-liquid separating system (4)    Gas purifying system (5)
NOVELTY - Quinazoline derivative (Ic) is prepared by reacting quinazoline-containing compound (II) and 1-amino-3-chloro-4-fluorobenzene compound (III) in the presence of alkaline and polypeptide condensing agent in organic solvent    USE - Method for preparing quinazoline derivative (claimed) used in preparing gefitinib medicine.    ADVANTAGE - The method has cheap raw material, is easy to obtain, has little side reaction, high yield coefficient, and has little pollution environment compared with prior art.    DETAILED DESCRIPTION - Quinazoline derivative of formula (Ic) is prepared by reacting quinazoline-containing compound of formula (II) and 1-amino-3-chloro-4-fluorobenzene compound (III) in the presence of alkaline and polypeptide condensing agent in organic solvent.    R1=Ra or C(O)Ra; and    Ra=optionally substituted linear chain 1-8C alkyl, optionally substituted linear chain 2-8C alkenyl, optionally substituted linear chain 52-8C alkynyl , 3-8C cycloalkyl, or optionally substituted saturated 2-8C heterocyclic; optionally substituted 6-12C aryl; or optionally substituted 3-12C heteroaryl, where above substituents are one or more of 186 group of compounds e.g. F, protected hydroxy, carbonyl, -NH-(2-8C alkenyl) and bi(4-12C heteroaryl) substituted azyl.
NOVELTY - A hydrogen production system comprises a shell (5); a fluid tank (6) and a reaction tank (7) located in the shell; and a micro pump (1) and a pressure switch (2) connected to the fluid tank and reaction tank. The outlet of the fluid tank is connected with the inlet of the reaction tank. The micro pump can be a peristaltic pump, a pressure ceramic pump or a diaphragm pump. The system may further include a buffer tank (8) into which a hydrogen filter reagent is added. The buffer tank has an inlet connected with the outlet of the reaction tank.    USE - Hydrogen production system used in fuel cell (9) (claimed).    ADVANTAGE - The hydrogen production system utilizes the pressure switch for controlling the micro pump so as to control the flow speed of the fluid from the fluid tank to the reaction tank so that the generated hydrogen volume is more stable. When employed in fuel cell, the power and voltage generated by the power generation of the fuel cell are stable and the life of the fuel cell is long.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic sectional view illustrating the hydrogen production system connected to a fuel cell.    Micro pump (1)    Pressure switch (2)    Shell (5)    Fluid tank (6)    Reaction tank (7)    Buffer tank (8)    Fuel cell (9)
NOVELTY - Integrated apparatus comprises a hydrogen production and a gas and liquid separation unit provided with a hydrogen outlet and an oxygen outlet and an oxygen purification unit, where the pure oxygen inlet of the oxygen purification unit is connected with the oxygen outlet of the hydrogen production and the gas and liquid separation unit and the pure oxygen outlet is connected with a pure oxygen recovery apparatus.    USE - The device is useful for hydrogen production and gas and liquid separation and oxygen purification by water electrolysis.    ADVANTAGE - The device: is simple and carries out a simplified process, saves cost, space and resources.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the integrated apparatus.
NOVELTY - The corn harvester has power device that is arranged in corn harvester, and hydrogen fuel container (12) is connected with hydrogen fuel cell (14) through hydrogen fuel conveying pipe (13). The hydrogen fuel cell is connected with motor (16) through conductor wire (15). The motor is connected with mechanical transmission device (18) through power output shaft (17). The mechanical transmission device is connected with each portions of corn harvesting device through each related mechanism portions.    USE - Device for harvesting corn using hydrogen fuel cell energy applied by power device.    ADVANTAGE - The current can be generated in high efficiency by applying hydrogen fuel directly in electrochemical reaction with oxygen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for harvesting corn.    Hydrogen fuel container (12)    Hydrogen fuel conveying pipe (13)    Hydrogen fuel cell (14)    Conductor wire (15)    Motor (16)    Power output shaft (17)    Mechanical transmission device (18)
NOVELTY - A lycopene oleoresin is refined by performing supercritical fluid extraction on lycopene oleoresin with lycopene content of 2.1-12.3 wt.% at extracting pressure of 10-50 MPa and extracting temperature of 32-70 degrees C, where ratio of flow rate of fluid to volume of extraction kettle is 1-10/hour; obtaining refined lycopene oleoresin with lycopene content as 8.7-20.6%; and filling carbon dioxide (CO2) or nitrogen to protect, and storing in dark place at 0-20 degrees C.    USE - Method for refining lycopene oleoresin (claimed).    ADVANTAGE - The method has simple technique, low energy consumption, and cheap extracting agent, is non-toxic and has easy recovery. The acid value and peroxide value of the oleoresin are reduced. The purity of lycopene is improved, peculiar smell is removed, and product quality is improved.
NOVELTY - A solar low-carbon fuel gas device comprises solar battery panel, electrolysis tank, gas storing bottle and ceramic stove; solar battery panel located outdoor and for receiving solar energy, converting solar energy into electric energy and supplying power to the electrolysis tank; output pipe of electrolysis tank connected with gas storing bottle; and hydrogen outlet pipe of gas storing bottle connected to ceramic stove.    USE - Solar low-carbon fuel gas device.    ADVANTAGE - The solar low-carbon fuel gas device electrolyzes hydrogen gas by solar energy, uses hydrogen gas as fuel with stove having highest heat value; and the hydrogen gas is burned and generates the water without the harmful substance, thus saving energy and reducing exhaust.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the solar low-carbon fuel gas device.
NOVELTY - Manufacturing partially biologically-derived alkylate (m1) involves obtaining ethanol from biological source; converting ethanol into ethylene by alcohol dehydration process; obtaining petroleum-derived hydrocarbons selected from cycloparaffins and/or isoparaffins; alkylating ethylene with petroleum-derived hydrocarbons to form effluent; and recovering partially biologically-derived alkylate from effluent.    USE - For manufacture of a partially biologically-derived alkylate (claimed) used as a gasoline or distillate fuel blending component.    ADVANTAGE - The method provides partially biologically-derived alkylate having percent Modern Carbon (pMC) (1-40 preferably 2-20, especially 5-10). The process enables the blending of volatile products from the saturation of benzene into gasoline. The process also enables the incorporation of other volatile compounds from petroleum such as isopentane into the biofuel composition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biofuel composition comprising partially biologically-derived alkylate having a percent Modern Carbon (pMC) of 1-40, where the partially biologically-derived alkylate is made by the method (m1).
NOVELTY - Multi-stage reaction system comprises: a fluidized bed (115) reactor that includes a partial oxidation zone (112), in which a gas and many char particles are created in the partial oxidation zone; and an entrained flow partial oxidation reactor positioned downstream from the fluidized bed reactor.    USE - The system is useful for producing low-tar combustible gas, preferably for converting feed stocks such as biomass and waste to combustible gases with low tar levels. The system is useful for the gasification of other higher volatile matter solid fuels e.g. various low rank coals, brown coal, peat, and lignite; and in high efficiency gas-to-power system for the synthesis of biofuels (ethanol, mixed alcohols, and Fischer-Tropsch liquids) and chemicals e.g. hydrogen and ammonia.    ADVANTAGE - The system is feasible, operable in an industrial setting, and provides high quality gases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for controlling an operating pressure of a two-stage gasification system, comprising: performing a partial oxidation of a portion of biomass in a fluidized bed reactor, where the partial oxidation creates a gas and the char particles; elutriating at least a portion of the char particles and gas from the fluidized bed reactor, where the elutriating includes removing a mixture of gas and char particles from the fluidized bed reactor; receiving the mixture into an entrained flow reactor, where the entrained flow reactor includes a moving granular bed of filtering media; allowing the mixture to flow through the moving granular bed; and capturing a portion of the char particles in the filtering media.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of a multi-stage reaction system.    First reactor (101)    Freeboard (110)    Partial oxidation zone (112)    Fluidized bed (114)    Blast inlet (118)
NOVELTY - Method (M1) to remove precipitates in biofuel involves subjecting the biofuel to ultrasonic energy.    USE - To remove or prevent formation of precipitates in biofuel such as plant based biofuel; animal-fat based fuel; vegetable oil fuel such as waste vegetable oil, straight vegetable oil and/or pure plant oil; biodiesel such as plant based biodiesel, animal-fat based biodiesel (claimed). Also alcohol biofuels such as methanol, propanol, ethanol, butanol, cellulose-based and/or lignocellulose-based plant matter such as switch grass, corn stalks, wheat stalks, agricultural, municipal, paper industry, and forestry waste products.    ADVANTAGE - Sonication effectively reduces filtration time. Therefore, the thermoviscous effects associated with the application of acoustic energy were responsible to improve filtration times. The ultrasonic energy can remove up to 90% of the precipitates (that generally clog a filter) from the biofuel.
NOVELTY - The device has diversified reaction chamber which is placed at the upper portion of the sealed liquid tank. The mixed gas inlet (4) is set at the right lower portion outside the diversified reaction chamber. The water supply pipe is located at the upper portion of the multi-functional reaction chamber. The water supply pipe is connected with the upper end of the reaction chamber different types of nozzle (7). The mixed gas outlet is located at the left upper portion reaction chamber.    USE - Purifying device for preparing high purity fuel gas by biomass.    ADVANTAGE - The cost of the device can be reduced. The stable and reliable production can be obtained.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the purifying device for preparing high purity fuel gas by biomass.    Water reverse reaction chamber (2)    Mixed gas inlet (4)    Pressure water reaction chamber (6)    Nozzle (7)    High pressure spraying reaction chamber (8)
NOVELTY - Degrading a prion protein in a specified risk material (SRM) comprises: (a) feeding the SRM to a sequencing batch reactor (SBR) containing a layer of acclimatized anaerobic sludge; and (b) allowing the SRM to react with the sludge at a temperature below 25 degrees C so as to allow degradation of the prion protein.    USE - The processes are useful for degrading prion protein in SRM; and for measuring efficacy of SBR to degrade prion proteins in SRM (all claimed).    ADVANTAGE - The invention provides process that eliminates prion protein in SRM from animal that is low in cost, is very stable, simple, and easy to operate and which does not interfere with regular farm operations.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process of measuring efficacy of SBR to degrade prion proteins in a SRM comprising: (a) feeding the SRM to the SBR containing a layer of acclimatized anaerobic sludge; (b) adding a model protein to the SBR; and (b) allowing the SRM and model protein to react with the sludge at a temperature between 5 degrees C to 25 degrees C, where degradation of the model protein is indicative of the efficiency of the SBR to degrade prion proteins in the SRM.
NOVELTY - Natural seasoning liquid comprises single or several garlic powder and instant coffee and shell powder. The raw materials are immersed and extracted using vinegar and packed using cloth, nonwoven fabric and net.    USE - The natural seasoning liquid is useful for cooking unpolished-rice and preparing liquid manure and fermented fertilizer.    ADVANTAGE - The liquid recycles waste material and highly preserves nutritional value of the unpolished-rice. The unpolished-rice provides excellent texture and taste to food and is easily absorbed by human body.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) of preparing the above-mentioned liquid, involves performing the above-mentioned process, and sealing and marking the product in a plastic bag; and    (2) method (M2) of preparing liquid manure and fermented fertilizer, involves mixing lees with several crab shell fine granule, fish fertilizer and animal fertilizer, subjecting the mixture to natural fermentation, immersing the mixture in vinegar, wood vinegar, bamboo vinegar and water, extracting the solution as liquid manure, and adding and mixing the lees of the liquid manure with crab shell fine granule, fish fertilizer, and animal fertilizer to obtain fermented fertilizer.
NOVELTY - A sending mechanism (35) separately sends out spherical/cylindrical shaped metal particles (31) into water (32). The sending mechanism includes an elastic delivery pipe (41) for sending out the particles, and the pipe dimension is set such that the particles closely contact the pipe interior. A feeder (42) supplies the particles one by one to the delivery pipe. The feeder has a feed mechanism with rollers rotating in opposite directions on either side of particles for feeding the particles.    USE - Hydrogen producing apparatus used in fuel cell system of vehicles such as electric vehicle.    ADVANTAGE - The amount of metal particles injected in water can be accurately controlled by sending out the metal particles separately into water irrespective of influence of external factors such as vibration. Hydrogen can be generated stably. The particles can be replenished safely without any leakage of hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of fuel cell system employing hydrogen producing apparatus. (Drawing includes non-English language text)    Fuel cell apparatus (2)    Metal particles (31)    Water (32)    Sending mechanism (35)    Delivery pipe (41)    Feeder (42)
NOVELTY - The portable prefabricated system for generating biogas/bio energy from the bio degradable organic waste materials/household waste materials comprises an anaerobic digester for processing the bio degradable waste materials and supplying the generated biogas to the gas collector placed movably on the top part of the digester. For the easily lifting of the gas collector from the digester, two projections are fixed on the top center of the gas collector. The processed liquid and the bio waste are fermented by the organic microbes in the anaerobic digester for the production of biogas. The pressure controller controls the pressure of the gas generated inside the gas collector. The digester comprises an inlet means for the introduction of the waste into the digester where inlet means comprises a hygienic cover and an inbuilt lock system for holding the inlet means and the inlet means is provided without any bends and curvature to prevent the chance of blockage in the inlet means. Accordingly the digester is provided with a projection for the receipt of the bend less and straight inlet means. The digester is provided with ribs at predetermined locations for improving the structural strength and additional space at the bottom edge of the outlet means for the block less delivery of the slurry. Image 0/0
NOVELTY - Nucleotide sequence encoding SEQ ID NO. 1 from Aspergillus nidulans, where the amino acid sequence comprises amino acid substitutions by threonine at amino acid position 92, serine at amino acid position 100, aspartic acid or asparagine at position 102, and alanine at position 195, is new. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The nucleotide sequence, expression vector, or cell is useful for obtaining enzymatic product with endoxylanase activity using a heterologous expression system. The expression product is useful as an enzyme with endoxylanase, for obtaining xylose oligomers from plant material; and for obtaining bioethanol (all claimed).    ADVANTAGE - The invention provides endoxylanase that has greater thermal stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) an expression vector comprising the nucleotide sequence;    (2) an expression product of the nucleotide sequence or the expression vector;    (3) cell comprising the nucleotide sequence, the expression vector, the expression product, or its combination;    (4) a method for obtaining enzymatic product with endoxylanase activity comprising: (a) inserting at least one nucleotide sequence in expression vector capable of expressing the nucleotide sequence in a microorganism; (b) transforming at least one cell of the organism with the product obtained in step (a); and (c) culturing the cell obtained in step (b) in a culture medium; and    (5) a method for obtaining bioethanol comprising: (a) contacting, in vitro, expression product, where the expression product is an enzyme with endoxylanase, and vegetable matter; and (b) incubating the mixture with ethanol-producing microorganisms at 30-60 degrees C.
NOVELTY - Gasifying fuel, such as wood chips, with a co-current gasifier, which has a combustion chamber and a liquid channel for circulating cooling liquid, such as water, comprises leading the cooling liquid from the liquid channel to the bottom of the combustion chamber below a grate and from the bottom of the combustion chamber out of the combustion chamber.    USE - The method is useful for gasifying fuel, such as wood chips, with co-current gasifier, which has combustion chamber and liquid channel for circulating cooling liquid, such as water (claimed).    ADVANTAGE - The invention provides improved method and apparatus for gasifying biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is an apparatus for gasifying fuel, such as wood chips, where apparatus has a co-current gasifier, comprising a combustion chamber and a liquid channel for circulating cooling liquid, such as water, where the co-current gasifier further comprises a first flow duct leading from the liquid channel to the bottom of the combustion chamber and a second flow duct leading out of the combustion chamber.
NOVELTY - A liquid bio-fuel mixture comprises: a liquid condensate product of biomass fast pyrolysis a bio-diesel component; an ethanol component, where the liquid bio-fuel mixture is macroscopically single phase.    USE - The liquid bio-fuel mixture is useful in a combustion process for the generation of electrical power, mechanical power, and for the generation of heat (claimed).    ADVANTAGE - The liquid bio-fuel mixture is highly improved and can be efficiently used in the generation of electrical power, mechanical power, and heat.
NOVELTY - The system (100) has controller (20) that instructs fuel cell (10) to perform reference operation, acquire required amount of cathode gas supplied to fuel cell, detect characteristic value, and acquire supply amount reference value. The difference between supply amount reference value and amount of supplied gas measured by gas delivery amount sensor is obtained. The amount of supplied cathode gas is adjusted by controller such that error is compensated for supplying cathode gas to fuel cell, on basis of value measured by gas delivery amount measurement sensor.    USE - Fuel cell system installed in vehicle, used for supplying reactant gases to fuel cell for generating electricity.    ADVANTAGE - The correlation between amounts of supplied cathode gas during the performance of reference operation can be easily controlled, and the characteristic value can be easily acquired. Thus, the amount of supplied cathode gas can be more accurately acquired on basis of detected characteristic value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of controlling fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system.    Fuel cell (10)    Controller (20)    Cathode gas supply portion (30)    Cathode gas discharge portion (40)    Fuel cell system (100)
NOVELTY - Treating (M1) oil-containing seeds involves contacting the seeds with an enzyme, which is capable of hydrolyzing chlorophyll or its derivative.    USE - For treating oil-containing seeds e.g. soya beans, peanuts, cotton seeds, sunflower seeds and rapeseeds, preferably soya or rapeseed, and for producing crude or refined plant oil (claimed).    ADVANTAGE - The reaction product such as chlorophyllide, pheophorbide and/or pyropheophorbide is simply and easily removed from the oil by acid treatment/caustic neutralization. Thus chlorophyll or its derivatives can be removed from the oil without the need for further processing steps such as clay and/or silica treatment and deodorization. The method does not involve a clay treatment step. Avoiding the use of clay is advantageous as this reduces cost, reduces losses of oil through adherence to the clay and increases retention of useful compounds such as carotenoids and tocopherol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) obtaining (M2) oil from plant seeds involving treating the seeds by the method (M1); pressing the treated seeds; and recovering oil from the pressed seeds; and    (2) producing a refined plant oil involving obtaining a crude oil by the method (M2); and refining the crude oil.
NOVELTY - The device has a display controller, a garbage storing feeding device, an oil-water separating tank and an oil-water product recovery device that are jointly operated. The garbage storing feeding device is provided with a shell, two sealing cover plate and filter tanks. The oil water separation tank is provided with a feed channel, gravity oil separating tank, an aerobic reaction tank and a biological reaction pool. A membrane bioreactor is provided with a membrane module and a filtering film. A tube and a container are provided in oil-water product recovery device.    USE - Oil-water separating device for restaurant-kitchen garbage.    ADVANTAGE - The oil-water separation of waste can be realized, the kitchen waste can be reliably recycled, and the waste can be processed safely.
NOVELTY - The apparatus has screw feeder (28) that inserts the screw shaft (27) in the cylindrical casing (26). The material supply direction downstream end of the cylindrical casing of the screw feeder is attached to the furnace wall (23) of a fluidized-bed gasifier (1). The solid raw material (5) is supplied to the inner portion of the fluidized-bed (4) formed in the fluidized-bed gasifier by the screw feeder. The gas injection unit injects the gas (36) for protection from the furnace wall side towards the screw feeder front portion of the fluidized-bed.    USE - Apparatus for supplying raw materials such as coal and biomass to gasification furnace.    ADVANTAGE - The abrasion of the front-end portion of a screw can be suppressed and the in-service of the screw shaft can be extended reliably. The filling rate of the solid raw material in that portion can be increased, and the material seal can be improved, since the internal diameter of the edge portion at the side of the material supply direction downstream of the casing is assigned to the fluidized-bed gasifier and gradually-reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of the gasification furnace raw materials supply apparatus.    Fluidized-bed gasifier (1)    Fluidized-bed (4)    Solid raw material (5)    Furnace wall (23)    Cylindrical casing (26)    Screw shaft (27)    Screw feeder (28)    Protection gas (36)
NOVELTY - The device has a temperature control device for controlling a heating furnace (6) and a temperature adjusting device (14). A high pressure liquid phase pump (12) and a liquid storage tank (11) are connected via a valve (V6). A mass flow meter (2), another valve (V1) and an air storage tank are connected with the high temperature gas-liquid reactor (16) via a third valve (V4). The high temperature gas-liquid reactor is connected with a fourth valve (V9), a gas-liquid separator (18), a pressure controller (19), a fifth valve (V13) and a data collection device (22).    USE - Biological oil and derivative catalytic hydrogenation device for use in a petrochemical industry.    ADVANTAGE - The device realizes economic efficiency of biologic oil and derivatives that are stable containing compounds to prepare a petrochemical product. The device improves effectively relieving petroleum shortage. The device is simple in structure, easy to operate and suitable for industrial application.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biological oil and derivative catalytic hydrogenation device.    Valves (V1,V6,V4,V9,V13)    Mass flow meter (2)    Heating furnace (6)    Liquid storage tank (11)    High pressure liquid phase pump (12)    Temperature adjusting device (14)    High temperature gas-liquid reactor (16)    Gas-liquid separator (18)    Pressure controller (19)    Data collection device (22)
NOVELTY - The device has dry distillation cracking and the main radiation chambers (15,16) that are equipped with a cracking pipe inside. The cracking pipes are connected with each other through a gas buffer (11). The output end of the cracking pipe inside the main radiation chamber is connected with the water washing cooling device outside the furnace (1). The water washing cooling device is connected with an air inlet pipe (9) through a spraying pipe (6). The dewatering filtering device is connected with a gas output pipe (10).    USE - Gas reaction device for biomass vehicle engine.    ADVANTAGE - The device can ensure cleanness and environmental protection. The heat efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biomass vehicle engine gas reaction device.    Furnace (1)    Spraying pipe (6)    Air inlet pipe (9)    Gas outlet pipe (10)    Gas buffer (11)    Dry distillation and main radiation chambers (15,16)
NOVELTY - The device has a first spiral feeding machine (1) and a second spiral feeding machine (3) that are provided with a first grade spiral feeder and a second grade spiral feeder, respectively. The second spiral feeding machine is provided with a gasification furnace feeding port and arranged on a hearth of a biomass fuel boiler. An upper end of the first spiral feeding machine is provided with a feeding port with a discharge hole that is connected to an input end of the second grade spiral feeder.    USE - Biomass fuel two-grade material plug spiral positive pressure continuous feeding device.    ADVANTAGE - The device is convenient to operate with reduced failure rate. The device ensures safe and stable burning of load.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass fuel two-grade material plug spiral positive pressure continuous feeding device.    Spiral feeding machines (1, 3)
NOVELTY - An operating method of hydrogen generating apparatus or fuel cell system comprises supplying source gas to modifier through first path while heating modifier by combustion operation of combustor at time of starting, and performing circulating movement which returns part of gas discharged from carbon monoxide reduction device to first path through second path.    USE - An operating method of hydrogen generating apparatus or fuel cell system.    ADVANTAGE - The temperature difference between modifier and carbon monoxide reduction device can be reduced in temperature rising operation at the time of starting.    DETAILED DESCRIPTION - An operating method of hydrogen generating apparatus or fuel cell system comprises supplying source gas to modifier through first path while heating modifier by combustion operation of combustor at time of starting, and performing circulating movement which returns part of gas discharged from carbon monoxide reduction device to first path through second path. The hydrogen generating apparatus (100) comprises first path (21) into which source gas flows, modifier which produces hydrogen containing gas using source gas supplied from first path, carbon monoxide reduction device which reduces carbon monoxide in hydrogen containing gas, second path (22) which returns gas discharged from carbon monoxide reduction device to first path, and combustor (2) which heats modifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of hydrogen generating apparatus. (Drawing includes non-English language text).    Combustor (2)    Combustion fan (5)    First path (21)    Second path (22)    Hydrogen generating apparatus (100)
NOVELTY - Fuel containing sulfur is contacted with nickel or nickel-containing desulfurizing agent at desulfurization temperature of 100 degrees C or less and at hydrogen/raw material flow volume of 0.001 L/cc or more to obtain desulfurized fuel. The desulfurizing agent contains metal chosen from lanthanum, nickel, manganese, chromium, vanadium, iron, cobalt, copper, zinc, molybdenum, tungsten, bismuth, aluminum and cerium.    USE - Desulfurization of fuel e.g. hydrocarbon fuel or oxygen-containing fuel such as kerosene, light oil, jet fuel, naphtha, gasoline, cracked gasoline, biofuel, liquefied nitrogen gas, liquefied petroleum gas, natural gas, town gas, dimethyl ether, methanol and ethanol (all claimed).    ADVANTAGE - The desulfurization process efficiently removes the sulfur compound from the fuel under mild conditions.
NOVELTY - A film catalyst unit (7) comprises one surface of electron and ion mixed conductivity film as electronic conductor and solid ion conductor, or ion-conductive film as solid ion conductor which is made to laminate oxidation catalyst film, and other surface which is made to laminate reduction catalyst film. A part of oxidation-catalyst films and/or reduction catalyst films are opening.    USE - Film catalyst unit for manufacturing compound e.g. hydrogen peroxide (claimed).    ADVANTAGE - The highly purified hydrogen peroxide can be simply manufactured with the reaction apparatus using the film catalyst unit.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacture of compound involving introducing reducing substance into oxidation-catalyst film using film catalyst unit, introducing oxidizing substance into reduction catalyst film, and producing compound by oxidation-reduction reaction; and    (2) manufacture of hydrogen peroxide involving introducing hydrogen donor into oxidation catalyst film using film catalyst unit, introducing oxygen into reduction catalyst film, and producing hydrogen peroxide by oxidation reduction reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the hydrogen peroxide manufacturing apparatus.    Film catalyst unit (7)    Reduction chamber (11)    Oxidizing chamber (12)    Inlet port of oxidizing substance (15)    Exit of oxidizing substance (16)
NOVELTY - Apparatus for producing biogas comprises a composter inside a Biogas Digester.    USE - The apparatus is useful for producing biogas (claimed).    ADVANTAGE - The heat generated by the hot composting process is transferred to the feedstock in the anaerobic digester tank via the composter's high thermal conductivity walls thus raising its temperature to assist anaerobic digestion which produces biogas. Advantageously, the biogas produced in the process is then fed to a storage tank from where it is further fed to a biogas consumption system. The apparatus uses the Hot Composting process and the Biogas production process to achieve an eco-friendly process for the production of Biogas in low temperatures.
NOVELTY - A chlorine-containing waste material is subjected to decomposition-desalination at high temperature and dried. When the amount of alkali in waste material is 3 molar equivalents or less in reaction container with respect to chlorine content, the superheated steam is supplied and discharged to the reaction container. The vaporized chlorine in the reaction container is derived by the superheated steam, and using regenerated solid fuel solid content which remained in the reaction container.    USE - Processing of chlorine-containing waste material e.g. organic refuse, foodstuffs waste material, agricultural waste material, forest-product waste material, plastic waste material, building waste material, motor-vehicle shredder dust material, and municipal waste material, and used as solid fuel.    ADVANTAGE - The method provides processed material having favorable grindability. The chlorine-containing waste material is economically processed, by simple method. The chlorine is efficiently recovered from the waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the superheated steam apparatus. (Drawing includes non-English language text)
NOVELTY - An antioxidant contains diphenylamine compound (I).    USE - Antioxidant is used for biodiesel fuel for diesel engine.    ADVANTAGE - The antioxidant has excellent antioxidant performance and oxidation stability, and replaces light oil, which is fossil fuel.    DETAILED DESCRIPTION - An antioxidant contains diphenylamine compound of formula (I).    R=H or 1-18C alkyl (optionally branched and substituted);    m,n=0-2;and    m+n=1 or 2.    An INDEPENDENT CLAIM is included for biodiesel fuel containing the antioxidant.
NOVELTY - Nickel sulfate, magnesium oxide and tungsten salt, cobalt salt and/or molybdenum salt are mixed and subjected to conjugation reaction. The conjugated mixture is dehydrated and washed. The washed mixture is mixed with calcium raw material, dried and baked to obtain gasification catalyst.    USE - Manufacture of catalyst used for gasification processing system (claimed) for gasifying biomass and air.    ADVANTAGE - The method enables manufacture of gasification catalyst having excellent activity, caulking-proof property and sulfur-proof property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for gasification processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the gasification processing system. (Drawing includes non-English language text)    Gasifier (1)    Catalyst recovery apparatus (2)    Dust collector (3)    Tar decomposition installation (4)    Catalyst portion (4a)
NOVELTY - Preparing organic fermented feed, obtaining organic waste material, adding Saccharomyces cerevisiae Kakegawa strain (FERM P-18964) to the organic waste material, maintaining the mixture, subjecting the mixture to fermentation using lactic acid bacteria, activating the S.cerevisiae Kakegawa, sterilizing the obtained product, proliferating lactic acid bacteria as a nutrient, and fermenting product by S.cerevisiae to obtain feed.    USE - The method is useful for preparing organic fermented feed for livestocks, cultures, and pet for promoting growth and stimulating appetite.    ADVANTAGE - The method sterilizes various microorganisms from product, is carried out at optimum environmental condition suitable for propagation of yeast, and stimulates disassembly of organic waste material. The feed has few alcohol odor with improved palatability, is easy to absorb and digest, increases weight of pig by 40%, and unsaturated fatty acid in muscles, and changes linoleoic acid to healthy meat quality by 5%.    DETAILED DESCRIPTION - Method of preparing organic fermented feed, involves obtaining organic waste material emitted from a general household, foodstuff associated business, agriculture-and-forestry and fishing, adding fermentation yeast, preferably Saccharomyces cerevisiae Kakegawa strain (FERM P-18964) to the organic waste material, maintaining the mixture at predetermined temperature for predetermined period of time, subjecting the mixture to fermentation using lactic acid bacteria, activating the S.cerevisiae Kakegawa, sterilizing the obtained product for removing various microorganism for the predetermined time, proliferating lactic acid bacteria as a nutrient after the activating S.cerevisiae Kakegawa strain, decreasing number of lactic acid bacteria, and fermenting the obtained product by S.cerevisiae to obtain feed.
NOVELTY - Stirring and turning device for purifying waste gas comprises a machine frame, a motor, a roller, a primary sprayer, a purifying medium, a filtering net, a filtrate collector, a suction fan, and a second cover. The filtrate collector comprises a filter screen. The air outlet of the filtrate collector is set below the filter screen. The purifying medium is set at the upper surface of the filter screen. The sprayer is set at the top of the purifying medium within the filtrate collector. The bottom of the filtrate collector is connected to a secondary spraying hole set on the filtrate collector.    USE - The device is useful for purifying waste gas.    ADVANTAGE - The device: reduces the discharge of waste gas into the atmosphere; is energy-saving and ecofriendly.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the stirring and turning device.
NOVELTY - The stove has a separating ring connected with hearth and furnace feet of table. A smoke channel is provided in the isolation ring. The isolation ring is assembled with sealing door and flame ring. The upper grate is provided with insulating pipe. The fire tube is provided with furnace cover. The gas ring is provided with a row of uniformly distributed air outlet holes.    USE - Biomass fuel gasification combustion stove.    ADVANTAGE - The heating performance of the fire tube can be improved. The heat consumption of fire pipe can be reduced. The temperature of the furnace can be controlled. The adjusting flame, closed flame, flame guide and flue gas flow functions of the stove can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the biomass fuel gasification combustion stove.
NOVELTY - The method involves forming the insulating layer (11) on the top of the electrolyte layer (10). The electrode (13) is formed at the lead line (12) of the temperature measuring junction. The thermocouple is formed on the top of the insulating layer. The electrode and lead line are covered by the insulation layer. The fuel anode is formed on the top of the insulating layer. The air electrode (15) is formed in the lower portion of the electrolyte layer.    USE - Fuel cell manufacturing method.    ADVANTAGE - The composition and supply quantity of the feed gas are controlled during the driving of the fuel cell. The thermocouple is surrounded with the insulating layer so that the reliability of the thermocouple is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional diagrams of the fuel cell.    Electrolyte layer (10)    Insulating layer (11)    Lead line (12)    Electrode (13)    Air electrode (15)
NOVELTY - The device has a solution application module including a solution application unit coating solution in top of a material to form a coating layer on a surface of the material. A blade module is installed in a rear side of the solution application unit, and a blade pad is installed at a lower part of the blade module. A dry heating chamber and a drying module include an aluminum heater, so that an ion exchange film is continuously applied with heat.    USE - Ion exchange film manufacturing device for a fuel cell.    ADVANTAGE - The device can mass-produce different ion exchange films.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an ion exchange film manufacturing device.
NOVELTY - Treating a flue gas (410), comprises burning an elemental magnesium in the flue gas.    USE - The process is useful for treating the flue gas for producing methane gas, which is useful in the direct carbon fuel cell to generate electrical energy (all claimed).    ADVANTAGE - The process: facilitates the removal of harmful or other undesirable chemicals from the flue gases and improves the electrical efficiency of the system; is capable of producing excess thermal energy, hence does not require external energy for the recovery of elemental magnesium; facilitates the regeneration of and recycling of elemental magnesium; and increases the production of thermal and electrical energy.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of the process for the regeneration of elemental magnesium.    Flue gas (410)    Magnesium oxide stream/fraction (414)    Magnesium iodide stream/fraction (424)    Vessel (430)    Elemental magnesium stream/fraction (434)
NOVELTY - The cover has a feeding device (2) for continuous feeding and provided with a cover body (1). The feeding device is provided with a feed port (3) and a hollow inside housing (4) that is connected to a furnace reaction chamber through the cover body. A U-shaped hopper (5) conveys biomass material from a feed port to the furnace reaction chamber through a circumlocutory overturning part that is equipped in the housing. A lower part of the cover body is provided with a circumlocutory and a filtering path (6). An end of the filtering path is connected with the furnace reaction chamber.    USE - Multifunctional furnace cover for a biomass gasification furnace.    ADVANTAGE - The cover realizes sealing state of the furnace reaction chamber in filtering and continuous feeding conditions. The cover is simple in structure and smart in design. The cover has tar filtering channel to filter tar materials so as to provide a high thermal state to the furnace reaction chamber. The cover improves cleaning of the filtering channel and provides guaranteed smooth filtering channels.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a multifunctional furnace cover.    Cover body (1)    Feeding device (2)    Feed port (3)    Housing (4)    Hopper (5)    Filtering path (6)
NOVELTY - Wet desulfurization tower comprises a reservoir located at the lower part of tower. The reservoir lower part includes a gas inlet pipe. The gas inlet pipe is inserted into the desulfurization tower and a wind inlet. The upper cap is provided with a liquid distributing pipe provided with atomizing spraying device. The desulfurization tower is provided with demister, a biogas outlet pipe, where the demister of the liquid storing tank and the water pump inlet are connected by a pipeline and its outlet is connected with a water pump spraying opening pipe.    USE - The wet desulfurization tower is useful for desulfurizing biogas.    ADVANTAGE - The tower provides enhanced efficiency of gas desulfurization without filler, thus is economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the wet desulfurization tower for desulfurizing biogas.
NOVELTY - The boiler has a gasification furnace (1) provided with a main water jacket (8) that comprises a flame path (9). An upper part of the flame path is provided with a smoke pipe (10). A lower part of the flame path formed with an air inlet hole is connected with a gas collecting chamber (6) by a pipeline (11) and provided with an ignition controller. The pipeline is provided with a fan (12). The flame path is provided with a preheating jacket (13). A grate (5) is provided with hollow steel tubes. Two ends of each steel tube are connected with an outer wall of the main water jacket.    USE - Biomass gasification steam boiler for use in a factory, a dining hall and a toilet.    ADVANTAGE - The boiler has simple structure, convenient operation, high heat efficiency and better combustion rate, and saves energy and reduces pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification steam boiler.    Gasification furnace (1)    Grate (5)    Gas collecting chamber (6)    Main water jacket (8)    Flame path (9)    Smoke pipe (10)    Pipeline (11)    Fan (12)    Preheating jacket (13)
NOVELTY - Producing ethanol from biomass, comprises either converting the biomass into a first stream comprising syngas, catalytically converting at least some of the syngas into a second stream comprising methanol, separating some of the syngas into hydrogen and carbon monoxide, catalytically converting at least some of the methanol with some of the carbon monoxide into a third stream comprising acetic acid, and reducing at least some of the acetic acid with some of the hydrogen into a fourth stream comprising ethanol.    USE - The process is useful for producing ethanol from biomass (claimed), which is useful as fuel additive and feedstock for industrial products.    ADVANTAGE - The improved process provides ethanol with high yield and reduced by-products in an economical manner.    DETAILED DESCRIPTION - Producing ethanol from biomass, comprises: either converting the biomass into a first stream comprising syngas, catalytically converting at least some of the syngas into a second stream comprising methanol, separating some of the syngas into hydrogen and carbon monoxide, catalytically converting at least some of the methanol with some of the carbon monoxide into a third stream comprising acetic acid, and reducing at least some of the acetic acid with some of the hydrogen into a fourth stream comprising ethanol; or converting the biomass into syngas, reacting the syngas in the presence of a catalyst to form methanol, supplying part of the syngas to a separator unit to recover carbon monoxide and hydrogen, carbonylating the methanol with the carbon monoxide to form acetic acid, and reducing at least some of the acetic acid with the hydrogen to form the ethanol.
NOVELTY - An ultrasonic wave is used in dehydration of biomass tar by sampling, weighing and packaging biomass tar, placing tar container in ultrasonic wave generation device in axial direction vertically, and starting ultrasonic wave at 50-100 KHz, 0.5 W/cm2, and 20-55 degrees C for 10-60 minutes; and post layering completely, standing, cooling and separating, and performing post recycling treatment to separated moisture and dehydrated tar.    USE - Ultrasonic wave used in dehydration of biomass tar (claimed).    ADVANTAGE - The use of ultrasonic wave breaks the emulsion state of water in tar by penetrability cavitation effect of the ultrasonic wave, so moisture and organic ingredient of the tar are layered effectively and distinctly. Water content of the biomass tar is reduced from 20-50% to less than or equal to 10%. The used ultrasonic wave instrument and other devices are all devices with low power and low energy consumption.
NOVELTY - The device has an oil tar purifier (4) whose outlet is connected with an inlet of a gas-water separator (5). An outlet of the gas-water separator is connected with a buffer tank (6). The buffer tank is connected with a pipeline between a gas pressure drum draught fan (7) and a grate. The grate is double layers, where each layers is provided with a fire grate and a movable fire grate controlled by hydraulic pressure control.    USE - Device for continuously producing/preparing combustible gas by using biomass fuel.    ADVANTAGE - The device can continuously generate gas, ensure the requirement of continuous production, and obtains the biomass gasification fuel gas by removing the dust, tar and moisture. The device has high purity and yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a device for continuously producing/preparing combustible gas by using biomass fuel.    Cooling dedust spray tower (3)    Oil tar purifier (4)    Gas-water separator (5)    Buffer tank (6)    Gas pressure drum draught fan (7)
NOVELTY - The device has a barrel type gasification furnace attached to a plasma generator and an oxygen-enriched combustion-supporting device of a pyrolysis zone. The supporting device is attached with a vapor heating reaction zone and a cracking area attached plasma generator. The device is provided with a biomass feeding device, a cyclone separating and conveying device, a steam production supply device, an air blowing device and a slag processing device. Working gas of a plasma generating device 2b is hydrogen or carbon monoxide gas or methane or ethylene.    USE - Device for producing combustible gas by a plasma pyrolysis and oxygen enriched combustion support material.    ADVANTAGE - The device improves gasification efficiency and quality of the product, reduces energy consumption, and prolongs the service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a device for producing combustible gas by plasma pyrolysis and oxygen enriched combustion support material.
NOVELTY - The method involves cutting and hammering a herbaceous plant to a thick filament, and inoculating anaerobic microorganism fermentation in a fermenting tank, where the herbaceous plant is one of straw, wheat straw and rush. Methane, residual cellulose and lignin are added in fermentation liquor at fermentation temperature of 20 degrees Celsius to 30 degrees celsius for fermentation time of 7 to 12 days. The filament is filtered and cleaned to obtain a natural fiber material.    USE - Method for extracting a natural plant fiber e.g. straw, wheat straw and rush (all claimed).    ADVANTAGE - The method enables saving investment and energy consumption. The method enables extracting a natural plant fiber in an easy manner without pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view illustrating a method for extracting a natural plant fiber.
NOVELTY - Thermophilic microbial consortium for conversion of cellulosic or lignocellulosic biomass to methane, comprises a) a cellulolytic thermophile; b) an acetate-oxidizing thermophile effective to oxidize acetate to carbon dioxide and hydrogen; and c) a hydrogen-utilizing thermophilic methanogen.    USE - For conversion of cellulosic or lignocellulosic biomass to methane (claimed) used as fuel.    ADVANTAGE - The composition converts biomass to methane with minimal waste; and reduces the national dependence on imported fossil fuels, and mitigates the threat of global warming.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a system for the conversion of cellulosic or lignocellulosic biomass to methane comprising a thermophilic microbial consortium comprising a cellulolytic thermophile, an acetate-oxidizing thermophile effective to oxidize acetate to carbon dioxide and hydrogen, and a hydrogen-utilizing thermophilic methanogen; and an electromethanogenic electrochemical cell; and    (2) converting lignocellulosic biomass to methane, involving exposing the lignocellulosic biomass to a thermophilic microbial consortium comprising a cellulolytic thermophile, an acetate-oxidizing thermophile effective to oxidize acetate to carbon dioxide and hydrogen, and a hydrogen-utilizing thermophilic methanogen, under conditions effective for microbial action on the lignocellulosic biomass to produce lignin, carbon dioxide (CO2) and methane.
NOVELTY - The method involves making an anode (102) to contact with an anode electrolyte (104), and making a cathode (106) to contact with a cathode electrolyte (108), where the anode electrolyte is separated from the cathode electrolyte by a cation exchange membrane (116). Acid e.g. hydrochloric acid, is produced in the anode electrolyte without generating gas at the anode, and a mineral e.g. mafic mineral, is made to contact with the acid. Hydrogen gas at the anode is oxidized to form hydrogen ions. Hydrogen gas produced at the cathode is transferred from the cathode to the anode.    USE - Method for electrochemically producing alkaline solution used in chemical processes to achieve chemical i.e. neutralize acid such as hydrochloric acid (claimed), buffer pH of a solution, precipitate an insoluble hydroxide, carbonate and bicarbonate from a solution, and to dissolve materials e.g. biomass materials.    ADVANTAGE - The method ensures that relatively low voltage is utilized across the anode and the cathode to produce the alkaline solution, and the hydrogen generated at the cathode is utilized at the anode, so as to eliminate the need for external supply of hydrogen, thus ensuring that relatively low amount of energy is utilized to produce the alkaline solution. The method ensures that carbon dioxide from industrial waste gases can be utilized to produce the alkaline solution, thus reducing carbon dioxide emissions into atmosphere.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system for electrochemically producing alkaline solution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for electrochemically producing alkaline solution.    Anode (102)    Anode electrolyte (104)    Cathode (106)    Cathode electrolyte (108)    Cation exchange membranes (116, 122)
NOVELTY - The device has a position adjusting mechanism (3) installed on a solar stirling engine bracket (1a) and a burner (2). A fuel soft tube (7) is connected with the burner. The burner is installed on a flexible output end of a telescopic mechanism or output end of a bending connecting bar mechanism of the position adjusting mechanism. A fuel supplying system (4) is provided with a pipeline connected with an air storage tank, a pump (4b), a main switch valve (4c), a branch switch valve (5), a flow regulating valve (6) and a flexible guide pipe.    USE - Disk-type solar stirling engine power generation device.    ADVANTAGE - The device can run continuously at day and night and continuously generate power during cloudy days, and is stable.    DETAILED DESCRIPTION - The fuel supplying system is a fuel gas supplying system, a biomass gasification supply system, a liquid fuel supply system or biomass liquid supply system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a disk-type solar stirling engine power generation device.    Solar stirling engine bracket (1a)    Burner (2)    Position adjusting mechanism (3)    Fuel supplying system (4)    Pump (4b)    Main switch valve (4c)    Branch switch valve (5)    Flow regulating valve (6)    Fuel soft tube (7)
NOVELTY - Biogas digester comprises tank body (1) at one side, feed tank (3), overflow chamber (5), discharging tank (4) and top cover (2). The tank body is equipped with the feed tank. The lower part of the tank body is equipped with the outlet of the feed tank. The tank body is provided with the other side of discharging tank. The discharging tank and the lower part of the tank body are similar. The discharging tank is provided with overflow outlet at the top. The tank body in the middle part of the tank wall is provided with storage air bag. The storage air bag is provided with air outlet pipe.    USE - Used as a biogas digester.    DETAILED DESCRIPTION - Biogas digester comprises a tank body (1) at one side, a feed tank (3), an overflow chamber (5), a discharging tank (4) and a top cover (2). The tank body is equipped with the feed tank. The lower part of the tank body is equipped with the outlet of the feed tank. The tank body is provided with the other side of the discharging tank. The discharging tank and the lower part of the tank body are similar. The discharging tank is provided with an overflow outlet at the top. The tank body in the middle part of the tank wall is provided with a storage bag. The storage air bag is provided with an air outlet pipe. The air outlet pipe from the top cover extends out the tank body. The storage air bag is expanded while producing the methane gas. The inner walls of the bag walls are connected to the tank body after the expansion of the storage air bags.    DESCRIPTION OF DRAWING(S) - The drawing illustrates a schematic representation of the biogas digester.    Tank body (1)    Top cover (2)    Feed tank (3)    Discharging tank (4)    Overflow chamber (5)
NOVELTY - A recombinant cell (C1) for synthesis of n-butanol is new. The cell comprises recombinant sequences encoding the enzymes that convert: (A) acetaldehyde to acetyl-coenzyme A (acetyl-CoA); (B) acetyl-CoA to acetoacetyl-CoA; (C) acetoacetyl-CoA to 3-hydroxybutyryl-CoA; (D) 3-hydroxybutyryl-CoA to crotonyl-CoA; (E) crotonyl-CoA to butyryl-CoA; and (F) butyryl-CoA to n-butanol.    USE - For the enzyme catalyzed synthesis of n-butanol from acetaldehyde (claimed), n-butanol is useful as biofuel.    ADVANTAGE - The recombinant cell produces elevated levels of n-butanol and ethanol compared to a wild-type cell.    DETAILED DESCRIPTION - A recombinant cell (C1) for the synthesis of n-butanol is new. The cell comprises a recombinant sequence encoding:    (A) an acylating aldehyde dehydrogenase catalyzing the conversion of acetaldehyde to acetyl-CoA, or a pyruvate:flavodoxin/ferredoxin-oxidoreductase catalyzing the conversion of pyruvate to acetyl-CoA;    (B) a keto-thiolase or acetyl-CoA acetyltransferase catalyzing the conversion of acetyl-CoA to acetoacetyl-CoA;    (C) an acetoacetyl-CoA reductase or hydroxybutyryl-CoA dehydrogenase catalyzing the conversion of acetoacetyl-CoA to 3-hydroxybutyryl-CoA;    (D) a crotonase catalyzing the conversion of 3-hydroxybutyryl-CoA to crotonyl-CoA;    (E) a crotonyl-CoA reductase, butyryl-CoA dehydrogenase or trans-enoyl-CoA reductase catalyzing the conversion of crotonyl-CoA to butyryl-CoA; and    (F) a butyraldehyde/butanol dehydrogenase catalyzing the conversion of butyryl-CoA to n-butanol.    An INDEPENDENT CLAIM is included for production (M1) of n-butanol, involving growing the recombinant cell (C1) in the presence of a suitable carbon source.
NOVELTY - Bio-fuel oil energy-saving agent comprises alkanes, cycloalkanes, aromatic hydrocarbons, chitosan, auxiliary enzymes and yeast. The auxiliary enzyme is dextranase or yeast powder.    USE - Used as a bio-fuel oil energy-saving agent.    ADVANTAGE - The product: prevents incomplete combustion of fuel; saves fuel oil; reduces decomposition of carbon in fuel; cleans the pressure adjusting system of engines, thus it prolongs the service life of engines; and reduces the discharge of harmful gases through incomplete combustion, thus it is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-fuel oil energy-saving agent, comprising: extracting chitin from marine organisms, extracting the chitosan derivatives from chitin and degrading the chitosan to obtain micro molecular chitosan, dissolved the obtained chitosan in an organic acid to obtain a chitosan solution, fermenting, adding petroleum, mixing, fermenting and filtering.
NOVELTY - A strain of acid-resistant heterotrophic Pichia spartinae D13 applied to sludge biological leaching treatment and deposited as CGMCC No. 3035, is new.    USE - The P. spartinae D13 strain is used for sludge biological leaching treatment (claimed).    ADVANTAGE - The strain improves the biological efficiency and stability of leaching method.
NOVELTY - An Acinetobacter baumannii (CGMCC 4728) for degrading imazamox is new.    USE - Acinetobacter baumannii used for degrading imazamox (claimed).
NOVELTY - A Pseudoxanthomonas japonensis (CGMCC 4797) is new.    USE - Pseudoxanthomonas japonensis used in microorganism agent for degrading petroleum hydrocarbon, preferably in bioremediation of soil polluted by petroleum (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a microorganism agent for degrading petroleum hydrocarbon, comprising P. japonensis as active component.
NOVELTY - Microbial agent comprises a culture medium and a bacterial strain, where the bacterial strain is Pseudoxanthomonas japonensis with the preservation number of CGMCC No.4797, Pseudomonas with the preservation number of CGMCC No.4793, Gordonia amicalis with the preservation number of CGMCC No.4794 and/or Gordonia alkanivorans with the preservation number of CGMCC No.4796.    USE - The microbial agent is useful for: degrading petroleum hydrocarbon; and bioremediation of petroleum polluted- soil and water body (all claimed).    DETAILED DESCRIPTION - An INDEPNEDENT CLAIM is also included for preparing the microbial agent, comprising inoculating at least any two of the bacterial strains into the culture medium for culturing.
NOVELTY - The material has a branch section that is provided with a water retaining property. The thickness of an upper fermenting padding is 70-80cm. The upper and a bottom fermenting paddings are mixed with biological fermentation. The padding is comprised with 80-100 kg of sawdust, 60-80kg of rice, 60-80kg of straw mushroom residue and alcohol, 10-15kg of rice bran or bran, 50-100kg of water, 50-100kg of soil and stone dust, 0.5-0.8kg of biological fermentation and 0.5-0.8kg of salt.    USE - Padding material used for preparing microorganism fermentation for raising collection and reusage of pig excrement.    ADVANTAGE - Since the padding material can be used as the fertilizer, the amount of wastage released is reduced. Hence the pollution is avoided and the fermentation process is ecological and environment-friendly. Since the moisture environment is protected, the fermentation process can be used in southern high temperature regions. The fermentation is done in a simple and easy way, so that the cost is reduced.    DETAILED DESCRIPTION - An independent claim is included for preparation method of microbial fermentation using padding material.
NOVELTY - The instrument has circuit unit provided with pH value measuring circuit (6), methane concentration measuring circuit (7), methane LEL concentration measuring alarm circuit (8) and hydrogen sulphide gas concentration measuring circuit (9) are used as gas for parameter measurement signals. The respective measuring circuits are connected with signal output end of A/D conversion and interface circuit (11). A/D conversion and control signal output end of interface circuit is connected with CPU (1) input and output (I/O) port.    USE - Biogas preparing parameter combination instrument.    ADVANTAGE - The cost of the instrument can be saved, and the convenience of the instrument can be improved. The reliability and stability of the instrument can be improved. The local area network can be controlled for data communication effectively. The technology parameter in the marsh gas preparing process can be measured intermittently.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of biogas preparing parameter combination instrument. (Drawing includes non-English language text)    CPU I/O port (1)    PH value measuring circuit (6)    Methane concentration measuring circuit (7)    Methane LEL concentration measuring alarm circuit (8)    Hydrogen sulphide gas concentration measuring circuit (9)    Interface circuit (11)
NOVELTY - Kitchen waste anaerobic digestion, comprises (i) sorting kitchen waste, crushing, and centrifugal dehydrating, (ii) conveying into a hydrogen fermentation tank, (iii) discharging hydrogen from tank, conveying into methane tank (simultaneous fermentation of mixed sludge), and fermenting to produce biogas, and (iv) using gas internal-combustion generating set, lithium bromide absorption type cold/hot water unit, and heat exchanger to obtain methane fuel gas and converting synchronously into electric and heat energy.    USE - The method is useful for hydrogen production and methane power generation technology.    ADVANTAGE - The process can produce hydrogen with high calorific value to improve the efficiency of gas-powered electricity generation; and can carry on harmless treatment and resourceful utilization of the kitchen waste.
NOVELTY - Methylamine pump combination valve comprises a drainage valve comprising a cover, an O shaped ring I, a space ring I, a discharging spring, a discharging valve core, an O shaped ring II, a valve seat which is connected to a bolt, an O shaped ring III, a ring II, an O shaped ring IV, a liquid inlet valve plate, a liquid inlet valve cover, and a liquid inlet spring, where the drainage valve core structure is composed of a mushroom type four jaw guide type drainage valve core. The liquid discharging valve core friction surface is composed of an annular friction surface of four frictional line.    USE - The methylamine pump combination valve is useful for producing urea.    ADVANTAGE - The valve comprises drainage valve core sealing surface, which extends the life cycle of the combination valve, reinforces the production continuity, and improves the process stability; is environmental-friendly; and consumes less energy.    DETAILED DESCRIPTION - Methylamine pump combination valve comprises a drainage valve comprising a cover, an O shaped ring I, a space ring I, a discharging spring, a discharging valve core, an O shaped ring II, a valve seat which is connected to a bolt, an O shaped ring III, a ring II, an O-shaped ring IV, a liquid inlet valve plate, a liquid inlet valve cover, and a liquid inlet spring. The drainage valve core structure is composed of a mushroom type four-jaw guide type drainage valve core. The liquid discharging valve core friction surface is composed of an annular friction surface into four friction line, at the liquid discharging valve cover with a valve seat connected with the bolt of a hexagon nut edge of a through hole, with a stainless steel wire one ring bolt series.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the methylamine pump combination valve.
NOVELTY - The processor has a sewage separating device (2) that is provided with sewage inlet and sewage outlet in the upper portion. The outlet of sewage separating device is connected with a medicine mixing device (4). A liquid medicine box (5) is connected with the medicine mixing device. The input end of a screw compressor (6) is connected with the medicine mixing device.    USE - Processor for hardening filth in septic tank.    ADVANTAGE - The dirt in the sewage tank can be collected, compressed, deslagged, sterilized, filtered and classified into residue automatically by the filth hardening processor for recycling, thus the environment is prevented from pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the filth hardening processor.    Rectangular frame (1)    Sewage separating device (2)    Medicine mixing device (4)    Liquid medicine box (5)    Screw compressor (6)
NOVELTY - Ecological water processing system comprises a sewage tank, a water tank, mountaintop tank with water pump, water pipe, and water purifying tank.    USE - Ecological system used for water processing.    ADVANTAGE - The system intensively removes nitrogen, utilizes original landform during constructing, and realizes ecological treatment without adding chemical agent, thus reducing secondary pollution.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of the ecological water processing system.
NOVELTY - The fermentation bed has fermentation bed main portion (6) that is set with main air distribution duct (1). The main air distribution passage is provided vertical to the main air distribution channel on both sides of the main air distribution duct. The main air channel and the side air cover are covered with cover board (5). One end of automatic control system is connected with main air distribution passage by the blower, and the other end is connected with multifunctional probe. The multifunctional probe is set on the fermenting bed organic solid waste.    USE - Organic solid waste fermentation bed.    ADVANTAGE - The infrastructure of the fermentation bed can be saved. The production of the organic fertilizer can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of organic solid waste fermentation bed.    Main air distribution duct (1)    Retaining wall (3)    Side air cover are covered with cover board (5)    Fermentation bed main portion (6)
NOVELTY - The method involves processing a base under high pressure into a sterile and protein-free substance through anaerobic digestion to form into composed biogas. Treatment of organic components is performed with sodium or potassium hydroxide. Waste is mixed with sodium or potassium hydroxide in water. An amount of sodium or potassium hydroxide is required to saponify polymers in the waste, where the treatment is performed with temperature of 200 to 250 degree Celsius. The treatment is performed in a vessel.    USE - Method for producing biogas from organic compound waste such as household waste of vegetables and fruits, plastic waste, cardboard waste, catering waste in restaurants and hotels, hospital waste, wastes from nursing homes, airplanes, trains, boats, airports, agricultural field, horticulture, livestock processing, trade and logistic industry, and pharmaceutical industry.    ADVANTAGE - The organic compound waste is pretreated with sodium hydroxide followed by anaerobic digestion to produce biogas of 368 cubic meters per ton, so that yield from the organic compound waste can be increased while reducing costs for processing waste.
NOVELTY - The biodegradation system uses a strain of microorganism of Pseudomonadales, where the system utilizes water contaminated with residues components. An airlift reactor is provided in the system to provide optimal conditions for growth of bacteria. Pollutant as carbon source is generated by metabolizm of microorganisms.    USE - Biodegradation system for volatile organic compounds, gasoline and phenolic residues in aqueous solution.
NOVELTY - Hydrogen is added into bio-oil to prepare biodiesel by using catalyst comprising copper oxide as active component, silicon dioxide and/or aluminum oxide as carrier, and providing bio-oil and hydrogen as reaction objects. The mass ratio of copper oxide to catalyst is 22-70:100. The reaction temperature in reactor is controlled at 180-260 degrees C. The reaction pressure is 4-8 MPa. The biodiesel is prepared by adding hydrogen for the reaction.    USE - Method for adding hydrogen in bio-oil to prepare biodiesel (claimed).    ADVANTAGE - The conversion rate of bio-oil and selectivity of biodiesel component are greater than 90%.
NOVELTY - A simple anaerobic biogas preparing device comprises reaction container with adjustable volume and plug matched with opening of reaction container tightly. A through hole is opened on plug. A hard pipe is sleeved inside through hole. The plug has sealing match with hard pipe. Two open ends of hard pipe are arranged inside and outside cavity of reaction container. The hard pipe outside cavity of reaction container is sleeved to flexible pipe. The length of flexible pipe is greater than that of hard pipe outside cavity of reaction container.    USE - Simple anaerobic device for preparing biogas (claimed).    ADVANTAGE - The device makes evaluation with low cost for biogas generating ability of biomass product such as straw. The oxygen in reaction is discharged simply nearly with zero cost.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a simple anaerobic biogas generating device.
NOVELTY - Solar assisted methane fermentation device comprises temperature sensor, water inlet pipe, heat collector circulating pump, heat storage water tank, electric heating coil, switch, vacuum-pipe solar collector, angle regulator, and solar storage battery. The electric heating coil is arranged inside heat storage water tank and is connected with solar storage battery through first conductor and switch. The vacuum-pipe solar collector generates heat and transmits to solar storage battery through battery connecting panel.    USE - Solar assisted methane fermentation device.    ADVANTAGE - The device performs methane fermentation in highlands with strong solar radiation and large temperature difference between day and night.    DETAILED DESCRIPTION - Solar assisted methane fermentation device comprises temperature sensor, water inlet pipe, heat collector circulating pump, heat storage water tank, electric heating coil, switch, vacuum-pipe solar collector, angle regulator, and solar storage battery. The water storage water tank is connected with vacuum-pipe solar collector. The electric heating coil is arranged inside heat storage water tank and is connected with solar storage battery through first conductor and switch. The vacuum-pipe solar collector generates heat and transmits to solar storage battery through battery connecting panel. The angle regulator is arranged at lower end of battery connecting panel. The heat collector circulating pump is arranged on water inlet pipe, such that one end of water inlet pipe is connected with heat storage water tank, while other end is connected with water outlet through helical radiating pipe. The heat collector circulating pump is connected with temperature through second conductor. An INDEPENDENT CLAIM is included for solar assisted methane fermentation using solar assisted methane fermentation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of solar assisted methane fermentation device.
NOVELTY - Saccharomyces cerevisiae T43 (CGMCC 4642) is new.    USE - S. cerevisiae used for alcoholic fermentation; for preparing seed liquid; or for producing alcohol (claimed). Specifically, it can be used for efficiently converting glucose in maize straw hydrolyzate to ethanol and can be used to current fuel ethanol productive technology and lignocellulose new process.    ADVANTAGE - The S. cerevisiae strain has multi-stress resistance and has wide thermal adaptability (i.e. S. cerevisiae can be used for reducing cooling and heating cost in fermentation process). It has relative high tolerance to suppressant in cellulose hydrolyzate, thus simplifying production technology while shortening fermentation time. It is conducive to starting saccharomycetes cellulose hydrolyzate to produce ethanol under relative high temperature at low energy consumption, and ethanol high yield of yeast fermenting layer.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fermentation medium of Saccharomyces cerevisiae comprising (g/l) yeast powder (5-10), urea (2-6), monopotassium phosphate (0.5-1), magnesium sulfate heptahydrate (1.5), and calcium chloride and maize straw hydrolyzate whose total reducing sugar content is 100-200 g (0.50);    (2) preparation of seed liquid of Saccharomyces cerevisiae by carrying out shake culture to Saccharomyces cerevisiae at 28-37 degrees C for 14-20 hours to obtain liquid strain; carrying out shake culture to converted liquid strain at 28-37 degrees C for 14-20 hours to obtain first level seed culture liquid; and culturing converted first level seed culture liquid at 28-37 degrees C for 14-20 hours to obtain seed liquid by controlling dissolved oxygen at 3-4 mg/l; and    (3) production of ethanol by fermenting Saccharomyces cerevisiae.
NOVELTY - Ethanol production involves extracting sugars present in coffee grounds with acid solution, where the acid solution is dilute sulfuric acid. The reaction is carried out in presence of Saccharomyces cerevisiae.    USE - Method for producing c from coffee grounds.    ADVANTAGE - The method produces ethanol with high yield.
NOVELTY - Bio-jet fuels obtaining involves reacting a mixture of glycerides material, 1-5C alcohol and homogeneous and heterogeneous catalyst. Ester and glycerin phase is separated from the mixture.    USE - Method for obtaining bio-jet fuels.    ADVANTAGE - The bio-jet fuel has reduced cost.
NOVELTY - The method involves preparing a molding material by polyphenyl sulfone resin and a carbon-type electroconductive material. A composition volume ratio of the polyphenyl sulfone resin is less than or equal to 10-40 volume percent. A composition volume ratio of the electroconductive material is less than or equal to 60-90 volume percent. A phosphoric acid fuel is utilized at temperature of 150-200 degree Celsius along with phosphoric acid. Average particle diameter of the carbon-type electroconductive material is less than or equal to 1-500 micrometers.    USE - Method for manufacturing a separator of a fuel cell i.e. phosphoric acid fuel cell (claimed).    ADVANTAGE - The method enables preparing the molding material by the polyphenyl sulfone resin and the carbon-type electroconductive material, where the composition volume ratio of the electroconductive material is less than or equal to 60-90 volume percent, thus manufacturing the separator with an electrical property, a mechanical capability and high corrosion resistance in a simple and inexpensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a separator of a fuel cell.
NOVELTY - A substitution reaction is carried out between an aryl boric compound (II) and metal hydroxide (III) in presence of a cuprous catalyst and aqueous ammonia, to obtain phenolic compound (I).    USE - Synthesis of phenolic compound is used for medicines, polymers and natural products.    ADVANTAGE - The method effectively provides phenolic compound with high yield and tolerance without polluting the environment.    DETAILED DESCRIPTION - A substitution reaction is carried out between an aryl boric compound of formula (II) and metal hydroxide of formula: MOH (III) in presence of a cuprous catalyst and aqueous ammonia, to obtain phenolic compound of formula (I).    M=lithium, sodium, potassium, cesium or rubidium;    R=H, 1-20C alkyl, 2-20C alkenyl, 2-20C alkynyl, 6-20C aryl, halo, -OH, -NO2, -NH2, -NHR', -C(=O)OR', -NHC(=O)R', -OR' or -C(=O)R';    R'=H, 1-6C alkyl, 2-6C alkenyl, 2-6C alkynyl, phenyl or benzyl;and    or R+benzene ring=fused ring.
NOVELTY - A substitution reaction is carried out between an aryl boric acid compound (II) and metal nitrate (III) in presence of cuprous catalyst and aqueous ammonia, to obtain nitrobenzene compound (I).    USE - Synthesis of nitrobenzene compound is used for medicines, polymers and natural products.    ADVANTAGE - The method effectively provides nitrobenzene compound with high yield without polluting the environment.    DETAILED DESCRIPTION - A substitution reaction is carried out between an aryl boric acid compound of formula (II) and metal nitrate (III) of formula: MNO2 (III), in presence of cuprous catalyst and aqueous ammonia, to obtain nitrobenzene compound of formula (I).    M=lithium, sodium, potassium, cesium or rubidium;    R=H, 1-20C alkyl, 2-20C alkenyl, 2-20C alkynyl, 6-20C aryl, halo, -OH, -NO2, -NH2, -NHR', -C(=O)OR', -NHC(=O)R', -OR' or -C(=O)R';    R'=H, 1-6C alkyl, 2-6C alkenyl, 2-6C alkynyl, phenyl or benzyl;and    or R+benzene ring=fused ring.
NOVELTY - The apparatus has cathode-and-anode resin exchanger connected with a water channel (2) for purifying water, and a rechargeable storage battery. A hydrogen opening of an electrolytic channel, a gas-water separator and a hydrogen drier are connected through a hydrogen pipeline. A solar heater is located between the cathode-and-anode resin exchanger and the water channel. A circulating pump is mounted with a temperature control rotate speed demodulator, and the rotation speed of the circulating pump is controlled to maintain the temperature of electrolyte in the electrolyte channel.    USE - Safe environmental-friendliness hydrogen generating apparatus used for metal powder reduction and fuel battery.    ADVANTAGE - Goals of energy conservation, low carbon and environment friendliness are achieved, by pressurizing the hydrogen and storing in the gas accumulation tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the safe environmental-friendliness hydrogen generation apparatus.    Water channel (2)    Condensation return pipe (12)
NOVELTY - Continuously processing dye waste water by using fixed Phanerochaete chrysosporium and Pseudomonas putida, comprises (a) preparing bacterial cellulose film fixed P. chrysosporium; (b) preparing bacterial membrane cellulose film fixed P. putida; (c) preparing dye waste water; and (d) continuously treating dye waste water by using fixed P. chrysosporium and P. putida.    USE - The method and device are used for continuously processing dye waste water by using fixed P. chrysosporium and P. putida (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a processing device for continuously processing the dye waste water by using the fixed P. chrysosporium and P. putida, comprising P. chrysosporium reactors I and II and a P. putida reactor I at the constant-temperature water bath, where the outlet of the peristaltic pump is connected with the water inlet at the lower side of the P. chrysosporium reactor I through a pipeline with a valve on it; the water outlet at the upside of the P. chrysosporium reactor I is connected with the water inlet of the following P. chrysosporium reactor II through the pipeline having the valve on it; the P. chrysosporium reactor II is connected with the water inlet of the P. putida reactor through the pipeline with a valve on it; the water outlet of the P. putida reactor is lower than the water inlet; the water inlet of the P. putida reactor is lower than the water outlet of the P. chrysosporium reactor II in front so that the position difference is formed; an exposure pump is respectively connected with the three processors through the bottom inserted exposure pipe; and the inlet pipe of the exposure pump is provided with a rotor flow meter.
NOVELTY - Hydrogen delivery system of an electrolytic cell comprises a first hydrogen delivering device, a second hydrogen delivering device and a total buffer tank. The first hydrogen delivering device comprises e.g. a low-current-density electrolytic cell, first hydrogen washing tower, a first hydrogen cooler, a first steam-water separator and a first distribution table. The second hydrogen delivering device comprises e.g. a high-current-density electrolytic cell, a hydrogen compressor, a second hydrogen cooler, a second steam-water separator, a water fog collector and a second distribution table.    USE - Used as a hydrogen delivery system of an electrolytic cell.    ADVANTAGE - The system: satisfies the requirement of hydrogen by meeting the production scale, reduces hydrogen discharge and waste, and ensures safe and stable delivery of hydrogen.    DETAILED DESCRIPTION - Hydrogen delivery system of an electrolytic cell comprises a first hydrogen delivering device, a second hydrogen delivering device and a total buffer tank. The first hydrogen delivering device comprises a low-current-density electrolytic cell, a first hydrogen washing tower, a first buffer tank, a first hydrogen cooler, a first steam-water separator and a first distribution table which are connected in turn. The second hydrogen delivering device comprises a high-current-density electrolytic cell, a second hydrogen washing tower, a hydrogen compressor, a second hydrogen cooler, a second steam-water separator, a water fog collector and a second distribution table which are connected in turn. The first distribution table and second distribution table are connected with the total buffer tank by the pipe with an automatic emptying valve.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hydrogen delivery system of electrolytic cell.
NOVELTY - A glucosamine hydrochloride is prepared by heating hydrochloric acid having a mass concentration of 30-35% at 60-70 degrees C using steam, adding citric acid waste residue, and hydrolyzing at 95-105 degrees C for 2-5.5 hours; filtering, washing the filter cake with water (2-3 times filter cake quantity), washing with a hydroxide containing solution having a mass concentration of 1-3%, and washing with water; and drying until water content is 80%, and cooling to 25-35 degrees C. The weight ratio of citric acid waste residue and hydrochloric acid is 1:1.6-2.5    USE - Method of preparing glucosamine hydrochloride.    ADVANTAGE - The method reduces utilizes waste thus reducing pollution, is environment-friendly and low cost, prepares product that is free of fishlike smell and heavy metal pollution, has high yield and improved efficiency, prepares product having high purity, and shortens the time for hydrolysis reaction.
NOVELTY - Method of treating night soil and food waste, involves mixing culture medium and to-be-processed object in the ratio of 1:1-1:2, injecting the 50-65 vol.% of mixture into processing tank, injecting 0.1-0.15 wt/% of microorganism including Actinomycete, and Bacillus mycoides to obtained product, and processing the obtained product at 30-60 degrees C.    USE - The method is useful for treating night soil and food waste.    ADVANTAGE - The method is rapid and environmentally-friendly and reduces bad smell during process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for excrements and food garbage disposal apparatus.
NOVELTY - Neotame is prepared by using sodium acetate borohydride as reducing agent to reduce reactant of aspartame and 3,3-dimethyl butyraldehyde.    USE - Method of preparing neotame.    ADVANTAGE - The method is simple and environment-friendly, has high yield, and prepares product having high purity.
NOVELTY - Reforming reaction kettle for biomass power generation system, comprises e.g. a cylindrical main body with a thermal insulating wall, where one end of the cylindrical main body is a tapered cone-shaped end cover while its other end is a kettle section with a purified biogas outlet, and center of the end cover is a primary gas inlet. Plasma electrode jacks are uniformly distributed on the tapered cone surface around the primary gas inlet along the circumference, where air distribution holes are distributed on the tapered cone surface around the plasma electrode jacks along the circumference.    USE - Useful as a reforming reaction kettle for biomass power generation system.    ADVANTAGE - The reaction kettle mixes air and primary gas uniformly, and thus it stabilizes electric arc flame, protects insulating wall, completes reforming reaction and improves heat value of output gas.    DETAILED DESCRIPTION - Reforming reaction kettle for biomass power generation system, comprises a cylindrical main body with a thermal insulating wall, where the cylindrical main body is installed horizontally and its one end is a tapered cone-shaped end cover while other end is a kettle section with a purified biogas outlet, and center of the end cover is a primary gas inlet. Plasma electrode jacks are uniformly distributed on the tapered cone surface around the primary gas inlet along the circumference, where axial lines of the plasma electrode jacks are crossed and air distribution holes are uniformly distributed on the tapered cone surface around the plasma electrode jacks along the circumference. An inner end outlet of the air distribution hole is distributed along an insulating wall of the end cover, and a preset helix angle is formed along the outlet direction.
NOVELTY - Power supply system for base station of cell phone signal emitting tower, comprises e.g. a vertical wind generator, hydrogen generator, a hydrogen storage unit and a hydrogen fuel battery, where the vertical wind generator is located on top end of the cell phone signal emitting tower and an electric energy output is connected with a hydrogen generator. A hydrogen output end of the hydrogen generator is connected with a hydrogen storage unit, which is connected with a hydrogen fuel battery, and an electric energy output of the hydrogen fuel battery is connected to a power consumption unit.    USE - Used as the power supply system for base station of cell phone signal emitting tower.    ADVANTAGE - The system: utilizes the vertical wind generator, which generates the electric energy for charging the base station to generate the hydrogen gas; utilizes the hydrogen fuel battery for charging the base station when the vertical wind generator has insufficient wind power or cannot work normally; and utilizes wind energy and solar energy to generate the power and thus reduces the power supply cost.    DETAILED DESCRIPTION - Power supply system for base station of cell phone signal emitting tower, comprises a vertical wind generator, a hydrogen generator, a hydrogen storage unit and a hydrogen fuel battery, where the vertical wind generator is located on top end of the cell phone signal emitting tower and an electric energy output end is connected with a hydrogen generator by an inverter. A rectifier and a current stabilizer are connected to the power consumption unit of the base station by the inverter, and a hydrogen output end of the hydrogen generator is connected with the hydrogen storage unit which is connected with a hydrogen fuel battery, the electric energy output end of the hydrogen fuel battery is connected with a power consumption unit of the base station.
NOVELTY - The pile is formed by serially connecting top plate (1), bottom plate (7) and flat-type solid oxide electrolytic cell units which are composed of metal double-electrode plates (6), metal sealing frame (4), flat-type solid oxide electrolytic cell sheet and current collecting net. The electrolytic cell sheet is embedded in metal sealing frame, and is sealed and insulated by sealing bar. An outer sealer is located in each of four edges of metal sealing frame. The two sides of region of hydrogen flow channel are provided with outer sealer parallel to hydrogen flow channel.    USE - Flat slant-type solid oxide electrolytic cell pile.    ADVANTAGE - The outer sealer and inner sealer can be separated efficiently through improved sealing structure of the pile. The contact area of the electrolytic cell sheet and the neighbor assembly can be reduced effectively. The heat stress caused by the difference of the thermal expansion coefficients of different assemblies can be reduced. The stability of the electrolytic cell sheet can be improved. The sealing effect and the heat circulation stability of the cell pile can be improved. The cell pile can be used for the large-scale high-temperature water vapor to electrolyze the hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the flat slant-type solid oxide electrolytic cell pile.    Top plate (1)    Metal sealing frame (4)    Metal double-electrode plates (6)    Bottom plate (7)    Outlet holes (12)
NOVELTY - A Phoma sp. (KCTC No: 11825BP) capable of producing cellulase of fibrous cell biomass derived from Rhodophyta, is new.    USE - The Phoma sp. (KCTC No: 11825BP) is useful in composition for decomposing cellulose, and producing beta -glucosidase and bioethanol (all claimed).    ADVANTAGE - The cellulose efficiently hydrolyzes fibers remaining after acid saccharification.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) fiber biomass-derived composition comprising supernatant of culture liquid obtained by culturing the Phoma sp. as an active ingredient; (2) method (M1) of decomposing cellulase, involves culturing the Phoma sp. in a culture medium, filtering the culture medium to obtain culture supernatant and adding the supernatant to the fibrous cell biomass; (3) method (M2) of producing bioethanol, involves performing the above-mentioned method (M1), and separating the bioethanol; (4) purified beta -glucosidase obtained by culturing the above-mentioned strain; and (5) nucleic acid molecule encoding the beta -glucosidase.
NOVELTY - Method for preparing lipid and specific fatty acid from microalgae, involves irradiating light of long wavelength and culturing microalgae, and irradiating light of long wavelength using light emitting diode.    USE - The method is useful for preparing lipid and specific fatty acid for reducing linoleic acid content and enhancing oleic acid content, and manufacturing raw material for biodiesel (all claimed).    ADVANTAGE - The microalgae improve quality and yield of raw material of biodiesel. The biodiesel has high oxidation stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for diversifying fatty acid composition of microalgae, which involves culturing the microalgae and irradiating light of long wavelength.
NOVELTY - A 2C fraction is enabled from deethanization tower of an ethylene unit to enter into a fixed bed catalytic hydrogenation reactor through hydrogen for selective hydrogenation and acetylene is removed. The 2C fraction is performed with selective hydrogenation reaction as polymerization reaction in the multi-section fixed bed catalytic hydrogenation reactor. The fixed bed catalytic hydrogenation reactor is a multi-section fixed bed catalytic hydrogenation reactor.    USE - Hydrogenation of 2C fraction.    ADVANTAGE - The hydrogenation of 2C fraction is effectively enabled.
NOVELTY - An electronic control unit (3) is connected with an internal combustion engine generator (2) to obtain a voltage signal of generator. The control unit is connected with storage battery and oxy-hydrogen machine coil relays (4,5). The control unit is connected with hydrogen and oxygen pressure sensors (9,7) to obtain pressure signals of hydrogen and oxygen storage tanks respectively. The control unit is connected with a storage battery (6) to obtain a voltage signal of storage battery. The generator is connected with an internal combustion engine main portion.    USE - Device for preparing oxygen and hydrogen by internal combustion engine residual power supplying vehicle-mounted oxy-hydrogen machine.    ADVANTAGE - The electronic control unit controls the operation of oxy-hydrogen machine based on the relationship between voltages of generator and the storage battery and the pressures of hydrogen and oxygen in the storage tank. Hence the storage tank is achieved with priority level for charging. The oxy-hydrogen machine can be stopped from operating when the gas in hydrogen tank and oxygen tank is in overpressure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for controlling internal combustion discharging control device based on vehicle-mounted oxy-hydrogen machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for preparing oxygen and hydrogen machine.    Internal combustion engine generator (2)    Electronic control unit (3)    Storage battery coil relay (4)    Oxy-hydrogen machine coil relay (5)    Storage battery (6)    Oxygen pressure sensors (7)    Hydrogen pressure sensor (9)
NOVELTY - An emulsifier comprises (wt.%) high grade vegetable oil fatty acid (70-74), polyalcohol ester fatty acid (12-13), fatty alcohol polyoxyethylene ether (4-5), alkyl alcohol amide (5-6), and fatty amine (5-6).    USE - An emulsifier for a biological emulsion diesel oil (claimed).    ADVANTAGE - The biological diesel oil has high stability with energy saving reaching to greater than or equal to 20%, and has an average exhaust gas emission reduction of greater than 50%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the emulsifier, comprising under an ice and water cooling condition, preparing high grade vegetable oil fatty acid and fatty amine, mixing, adding polyalcohol ester fatty acid, fatty alcohol polyoxyethylene ether, and alkyl alcohol amide, and uniformly agitating; and    (2) a biological emulsion diesel oil, comprising an emulsifier, water, and biomass fuel.
NOVELTY - Producing enantiomerically enriched isomer of 3-(1-amino-ethyl)phenyl compound (I), comprises: reacting 3-(1-amino-ethyl)-phenol compounds (II) with a protecting agent (i); resolving the racemic compound of (I) to obtain diastereomeric salt of (S)-3-(1-amino-ethyl)-phenyl compound (III) and (R)-3-(1-amino-ethyl)-phenyl compound (IV); reacting (IV) with a base in a solvent; reacting the (R)-3-(1-amino-ethyl)-phenyl derivative (V) with an aldehyde (ii); treating the substituted phenol compounds (VI) with a base; and converting the racemic substituted phenol compound (VII) with an acid.    USE - The process is useful for producing enantiomerically enriched isomer of (I) for preparing rivastigmine (claimed), which is useful in the treatment of Alzheimer's disease. No biological data given.    ADVANTAGE - The process is economic, cost effective and environment friendly.    DETAILED DESCRIPTION - Producing enantiomerically enriched isomer of 3-(1-aminoethyl)phenyl derivative of formula (I), comprises: (a) reacting 3-(1-amino-ethyl)-phenol compounds of formula (II) with a protecting agent of formula (RX) (i) to obtain a racemic compound (I); (b) resolving (I) by employing a resolving agent of an optically active acid (HA) in a solvent to obtain diastereomeric salt of desired (S)-3-(1-amino-ethyl)-phenyl derivative of formula (III) and diastereomeric salt of undesired (R)-3-(1-amino-ethyl)-phenyl derivative of formula (IV); (c) reacting (IV) with a base in a solvent to obtain (R)-3-(1-amino-ethyl)-phenyl derivative of formula (V); (d) reacting (V) with an aldehyde of formula (R1aCHO) (ii) in the presence of an acid in an organic solvent to obtain substituted phenol compound of formula (VI); (e) treating (VI) with a base in an organic solvent to obtain a racemic substituted phenol compound of formula (VII); and (f) converting (VII) with an acid or by hydrogenolysis in a solvent to obtain racemic compound (I).    R = substituted sulfonyl; and    X = leaving group.
NOVELTY - The reaction tank has a tank main portion (1) that is connected with a color steel plate (2). The tank main portion is positioned on the outer surface that is provided with an insulating layer (3). The outer surface of the tank main portion is coated with insulating layer. The insulation layer is made of polyurethane. The length of the insulating layer is of 100mm.    USE - Biogas reaction tank.    ADVANTAGE - The stability of the biogas reaction tank is strong. The tank has improved waterproof effect. The durability of the tank is improved. The working efficiency of the tank is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biogas reaction tank.    Tank main portion (1)    Color steel plate (2)    Insulating layer (3)
NOVELTY - A porous polymer material having a specific surface area of 1-2000 m2/g, is obtained by taking aromatic compound as raw material; dissolving into organic solvent; and using crosslinking agent to crosslink the aromatic compound in the presence of Lewis acid as catalyst. The aromatic compound is aromatic compound used for carrying out Friedel-Crafts reaction.    USE - Porous polymer material used as catalyst carrier, separation membrane, air storage material, carbon dioxide storing material, methane storing material or ion adsorbent (claimed).    ADVANTAGE - The preparation method is simple, and uses raw material that is cheap and easy to obtain. The kind of aromatic compound can be flexibly selected according to different application requirements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of porous polymer material comprising:    (A) adding aromatic compound, crosslinking agent and organic solvent into a reactor under normal temperature, where the concentration after the aromatic compound is dissolved in organic solvent is 0.1-30 mol/L, and the molar ratio of crosslinking agent and aromatic compound is 0.1:1-20:1;    (B) magnetically stirring for 0.1-2 hours, and then adding Lewis acid as catalyst, where the molar ratio of catalyst and crosslinking agent is 0.1:1-10:1; then keeping magnetically stir, and then heating up to 30-60 degrees C, and reacting for 2-12 hours, then heating up to 70-120 degrees C, and reacting under the temperature for 10-72 hours, and obtaining brown turbid liquid or extreme thick solid-liquid mixture;    (C) filtering the turbid liquid or mixture, and obtaining brown solid crude product; using diethyl ether or carbinol to wash the solid product for 3 times to remove the remaining crosslinking agent, solvent and catalyst; and    (D) then using carbinol to extract for 24 hours to remove trace catalyst; and then decompressing and drying, and obtaining the multi-hole polymer material.
NOVELTY - Supercritical carbon dioxide is used as solvent to extract and separate statin hyphae synthesized by microorganisms. An entrainer chosen from alcohol, acetone, ethyl acetate and butyl acetate is used in the extraction process.    USE - Method for using supercritical carbon dioxide for extracting and separating statin.    ADVANTAGE - The extraction is carried out economically by an environmentally-friendly process using reduced amount of solvent. The statin with high quality is extracted.
NOVELTY - Method of producing compressed compost, involves mixing animal nature compost, vegetable nature compost, vegetable additives and mineral additives. The animal nature compost is livestock feces. The vegetable nature compost is sawdust, rice bran, fallen leaves, weeds or rice straws. The vegetable additives are amylose or amylopectin. The mineral additives are formed with mixed material of yellow soil and magnesium. The mixing ratio of the animal nature compost and vegetable nature is 80-90.    USE - The method is useful for producing compost.    ADVANTAGE - The bad smell of compost is removed, and viscosity is increased as vegetable additives are added to compost. The compost has improved strength as it contains mineral additives.    DETAILED DESCRIPTION - Method of producing compressed compost, involves mixing animal nature compost, vegetable nature compost, vegetable additives and mineral additives. The animal nature compost is livestock feces. The vegetable nature compost is sawdust, rice bran, fallen leaves, weeds or rice straws. The vegetable additives are amylose or amylopectin. The mineral additives are formed with mixed material of yellow soil and magnesium. The mixing ratio of the animal nature compost and vegetable nature is 80-90. The product gets stuck in farmland with shape given in figures 1-6 provided in the patent specification. An INDEPENDENT CLAIM is included for apparatus for performing above-cited method.
NOVELTY - The device has solid-liquid separating and drying device, crushing device and fermentation equipment. The solid-liquid separating, drying device, crushing device and ferment device are connected in turn from up and down. The baffle plate (5) is connected with the baffle motor (10). The stirring motor (1) and garbage inlet (2) are set on the top cover (16). The stirring box portion is provided with connecting rod (14). The connecting rod is connected with the mixing rod. The stirring device (12) is arranged on the stirring rod.    USE - Kitchen waste processing device.    ADVANTAGE - The environment pollution can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the kitchen waste processing device.    Stirring motor (1)    Garbage inlet (2)    Baffle plate (5)    Baffle motor (10)    Stirring device (12)    Connecting rod (14)    Top cover (16)
NOVELTY - The method involves subjecting whey to a hydroxylation in presence of enzymes. Resulting hydrolyzed whey are added to mixture of hydrolyzed whey and carrier materials that are added to excipients, which is selected from a group of minerals, nitrogen-rich compounds, stabilizers, carbon-containing compounds and zeolites. Weight of the hydrolyzed whey content is 10-95 weight percent of total weight of organic manure. Weight of carrier substance content is in the range of 25-80 weight percent of the total weight of the organic manure.    USE - Method for processing whey into an organic fertilizer (claimed) for use as a soil improver and a nutrient in an agricultural field.    ADVANTAGE - The method enables obtaining nitrogen content of the mixture with weight of 5-20 weight percent of the total weight of organic manure, so that the material obtained can be used to replace synthetic fertilizer and stored for multiple years without reduction in fertilizer's organic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an organic fertilizer.
NOVELTY - Synthesizing 6-ethyl-5-fluoro-4-hydroxy pyrimidine and intermediate 2-fluoro-3-oxo-pentanoic acid ethyl ester thereof, comprises: (a) generating condensation reaction by the ethyl fluoroacetate with the propionyl chloride at the reaction temperature, obtaining 2-fluoro-3-oxo-pentanoic acid ethyl ester after finishing the reaction; and (b) reacting the 2-fluoro-3-oxo-pentanoic acid ethyl ester with the acetic acid carbonamidine at the reaction temperature, and obtaining the 6-ethyl-5-fluoro-4-hydroxy pyrimidine after finishing the reaction.    USE - The process is useful for synthesizing 6-ethyl-5-fluoro-4-hydroxy pyrimidine and intermediate 2-fluoro-3-oxo-pentanoic acid ethyl ester thereof (claimed).    ADVANTAGE - The process is safe, environment-friendly, simple, and efficient.
NOVELTY - The tower (27) is connected to re-boiler (29) to provide heat. The inlet of re-boiler is connected to outlet of gas compressor (9), while outlet is connected to inlet of tower backflow tank (19). The inlet in bottom of absorption/de-sorption tower (12) is connected to outlet of over-heater (11) and compressor. The loop structure is formed by outlet on top of absorption/de-sorption tower with reproducible alcohol vapor over-heater (13). The outlet in bottom of absorption/de-sorption tower is connected to alcohol vapor condense structure (14) and coarse alcohol tank (15).    USE - Distillation and dehydration device for producing fuel ethyl alcohol and ordinary edible alcohol.    ADVANTAGE - The device can concurrently produce fuel ethyl alcohol and ordinary edible alcohol, can employ multi-effect energy coupling, and can greatly reduce the energy consumption. The vapor consumption can be reduced effectively, so that the high quality vapor can be saved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing fuel ethyl alcohol and ordinary edible alcohol.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the distillation and dehydration device. (Drawing includes non-English language text)    Gas compressor (9)    Over-heater (11)    Molecular sieve absorption/de-sorption tower (12)    Reproducible alcohol vapor over-heater (13)    Weak alcohol vapor condense structure (14)    Coarse alcohol tank (15)    Tower backflow tank (19)    Alcohol tower (27)    Re-boiler (29)
NOVELTY - Flammable gas conversion catalyst comprises (in %): cerium nitrate hexahydrate (Ce(NO3)3.6H2O) (4-9), nickelous nitrate hexahydrate (Ni(NO3)2.6H2O) (0.1-2), magnetite (Fe3O4) (0.1-2), potassium nitrate (KNO3) (0.1-2) and attapulgite powder (85-90). The grain size of the attapulgite powder is 325 meshes or more. The water content is 1% or less. The magnesium oxide (MgO) content is 23% or more. The silicon dioxide (SiO2) content is 56% or less.    USE - The flammable gas conversion catalyst is useful for biomass (e.g. straws) boiler for generating gas.    ADVANTAGE - The catalyst reduces flammable substances in residue and stove ash, and improves conversion efficiency and burning speed of biomass materials.
NOVELTY - Chemical process comprises providing municipal solid waste or feedstock comprising a carbon containing biology based feed; subjecting the municipal solid waste or the feedstock to plasma pyrolysis to form an intermediate for chemical production, where the intermediate comprises carbon monoxide and hydrogen; and transferring the intermediate from the plasma pyrolysis to a chemical or liquid fuel production process.    USE - The process is useful for the production of syngas, which is useful as a fuel source or as an intermediate for the production of other chemicals.    ADVANTAGE - The process reduces the volume of waste entering landfills and reduces the carbon dioxide footprint by utilizing renewable feedstocks.
NOVELTY - The method involves filling raw material in cracking tower. The oil is circulated through the connecting pipe. The circulation of oil through the circulating loop is started. The temperature of the heating oven is controlled. The control valve of the gas-liquid separating tank is closed. The raw material is sprayed to the stack layer distributor. The oil is entered into gas-liquid separating tank. The oil gas in the fractionating tower is distributed through the discharge hole. The product tank region is cooled.    USE - Method for cracking biomass such as waste plastic, waste rubber and the organic matter of oil.    ADVANTAGE - The cracking process can be performed at low cost. The energy need for the cracking process can be saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the cracking tower.
NOVELTY - The device has heating chambers (3,12) that are located in the centeral gasification chamber (4) and the peripheral gasifying chamber (2). A residual carbon reflowing room (9) and the central gasification chamber are separated. The upper portion and the lower portion of the annular heating chamber are provided with the fuel gas outlet (10) and the fuel gas inlet (5) respectively. The fuel gas outlet of the annular heating chamber is connected with the gasification chamber.    USE - Gasification device for organic waste and agricultural-forestry waste in city.    ADVANTAGE - The heat utilization rate of the gasification device can be improved. High heat transfer efficiency of the gasification device can be achieved. The gasification efficiency of the gasification device can be improved, since the residual carbon is passed into the gasification chamber. The efficient combustion of heating chamber can be achieved, since the biomass fuel is passed into the heating chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the gasification device.    Peripheral gasifying chamber (2)    Heating chambers (3,12)    Centeral gasification chamber (4)    Fuel gas inlet (5)    Residual carbon reflowing room (9)    Fuel gas oulet (10)
NOVELTY - The method involves drying and crushing a carbon material and optional gasification catalyst, and obtaining solution containing carbon particles. Some of the particles are made to enter into a gasifier from bottom and remaining carbon particles are made to enter into a vaporizer. Gaseous products are generated from synthesis gas ash mixture after recycling the synthesis gas ash in the gasifier or with carbon.    USE - Method for preparing synthesis gas.    ADVANTAGE - The method enables strong adaptability of raw material, carbon content to be between 1 to 100 weight percent of any carbon material, optimized control, faster combustion reaction and gasification reaction coupling slowly, and enables preparation of synthesis gas with high yield.    DETAILED DESCRIPTION - The carbon-containing material is selected from a group consisting of asphalt powder coal, petroleum coke, biomass, oil solvent degreasing, water-coal-slurry, highly organic waste, municipal solid waste, or petroleum catalytic. The gasification catalyst is selected from one of alkali metal, alkaline earth metal, group VIII metal or one of carbonate, sulfate, oxide or chloride of the metal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an environment in which a synthesis gas preparing method is performed.
NOVELTY - The device has a furnace cover (6) mounted at top of a domestic biomass gasification furnace. A middle part of the furnace is provided with a blanking device (5). A bottom part of the furnace is provided with a burning area (3) and a gas-supply pipe (8). A side of the furnace is provided with a gas incoming pipe (7). A lower part of a shell of the furnace is provided with an annular coke treating device. The treating device comprises a drying layer, a dolomite catalytic pyrolysis layer (2) and a wood carbon pyrolysis layer (1) from top to bottom. An ash outlet (4) is located under the area.    USE - Decoking device for domestic biomass gasification furnace.    ADVANTAGE - The device integrates the gasification with pyrolysis and makes the produced gas to pass through the catalytic pyrolysis layer circularly so as to decompose the coke into permanent gas that reduces the coke content generated in the biomass gasification course effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a decoking device for domestic biomass gasification furnace.    Wood carbon pyrolysis layer (1)    Dolomite catalytic pyrolysis layer (2)    Burning area (3)    Ash outlet (4)    Blanking device (5)    Furnace cover (6)    Gas incoming pipe (7)    Gas-supply pipe (8)
NOVELTY - The furnace has a tar cracking device and a feeder (7) installed on an outer layer on a bottom part and an upper part of a fuel barrel, respectively. A combustion area (2) and an air supply pipe (19) are arranged on the bottom part of the barrel. A soot door (1) is arranged below the combustion area, and an outer layer at the upper part of the barrel is connected with a high temperature cracking furnace head. A water tank is arranged at back of the barrel. A water outlet is arranged at an upper side of the water tank, and a water inlet is arranged at a lower side of the water tank.    USE - Tar-free straw gas heating furnace.    ADVANTAGE - The furnace effectively improves the utility ratio of heat, and meets the demand of outdoor heating.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a tar-free straw gas heating furnace.    Soot door (1)    Combustion area (2)    Feeder (7)    Blower (17)    Air supply pipe (19)
NOVELTY - A wastewater treatment system comprises an activated sludge system, a trickling filter system, a light-emitting device which irradiates light to tanks, a carbon dioxide (CO2) collecting unit which collects CO2 emitted by microorganisms in each tank, a vent pipe which releases nitrogen gas (N2) to air, a dissolved oxygen auxiliary device and a small air blower. The wastewater treatment system does not have an opening part.    USE - A wastewater treatment system (claimed).    ADVANTAGE - Photosynthesis is continuously activated, food chain of microorganisms is maintained, scattering of water droplets is prevented, the wastewater treatment system is easily installed, treatment of wastewater is efficiently carried out, filter apparatuses are not required, maintenance costs are reduced, toxic gases are not produced, and biological oxygen demand (BOD) load factor is high.
NOVELTY - The method involves introducing sludge mixed with waste plastics or tires into a reaction kettle for mixing purpose by a fully closed equipment.    USE - Method for turning municipal sludge into storable gas, fuel oil and solid fuel.    ADVANTAGE - The method enables preventing carbon, exhaust gas, dioxin gas and heavy metals in fly ash from discharging during pollution treatment. The method enables treating and recycling municipal sludge in an environmental friendly manner without secondary pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of a system for turning municipal sludge into storable gas, fuel oil and solid fuel.
NOVELTY - Extracting (M1) carbon-based molecule from a cell involves contacting the cell with a biphasic solution having a solvent layer, where the biphasic solution contains cyclodextrin.    USE - For extracting a carbon-based molecule e.g. alkane, alkene, and fatty acid ester; 1-nonadecene, pentadecane, a hexadecane from a cell such as prokaryotic cell (preferably photosynthetic cell, which is cyanobacterium having genetic modification, which reduces the S-layer of the cyanobacterium or reduces the percent composition of glycocalyx of the cyanobacterium) (claimed), used in biofuel production.    ADVANTAGE - The presence of the cyclodextrin in the biphasic solution increases the transfer rate of the carbon-based products to solvent phase of the biphasic solution relative to the transfer rate observed using an otherwise identical biphasic solution lacking the cyclodextrin.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for culturing a cell for production of a carbon-based molecule involving culturing the prokaryotic cell in a biphasic solution comprising a non-polar phase and a polar phase, and further comprising at least one cyclodextrin, where the cell releases the carbon-based molecule; and collecting the carbon-based molecule from the non-polar phase of the biphasic solution; and    (2) a composition for producing carbon-based products comprising a cell, and a biphasic system containing at least one cyclodextrin.
NOVELTY - Reducing ash content from a biomass feedstock or a biomass fraction of an aquatic species comprises providing the biomass; lysing the biomass to generate a lysed biomass; treating the biomass with an alcohol and a catalyst to generate a reaction mixture; separating the reaction mixture into a solid phase and a liquid phase; and recovering reagents by collecting the solids and distillating the liquids, where the ash content of the biomass is reduced by at least 40%.    USE - The process is useful for reducing ash content from biomass feedstock or biomass fraction of aquatic species (claimed).    ADVANTAGE - In the process for reducing ash content from biomass feedstock or biomass fraction of aquatic species, use of a prewash to remove minerals before acidifying the biomass can additionally improve acid pretreatment efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a system of reducing the ash content from a biomass feedstock or of a biomass fraction of an aquatic species comprising a reaction chamber suitable to facilitate a reaction among the biomass feedstock, an alcohol, and a catalyst; a vessel connected to the reaction chamber via a closable fluid connection; a lysing unit for lysing the biomass to generate a lysed biomass; a separating unit for separating the lysed biomass to generate a juice and a solid phase; and a separator adapted to separate the unreacted alcohol from the reaction product; where processing the biomass in the system results in at least 40% reduction of the ash content of the biomass.
NOVELTY - Method for recovering nutrient, involves (a) heating anaerobic digester (10) effluent containing fibrous solids and suspended solids to 160 degrees F, (b) separating fibrous solids from suspended solids in effluent, (c) heating and aerating the effluent in aeration reactor (320) to convert soluble ammonium to gaseous ammonia (162), (d) providing the ammonia from the aeration reactor to a stripping tower (190), where the stripping tower provides controlled amounts of acid to react with ammonia, and (e) recovering ammonium salt produced from the reaction in stripping tower.    USE - The method and the system are useful for recovering nutrients e.g. phosphorus and nitrogen by processing waste materials e.g. animal waste from livestock, and for increasing quantity of biogas recovery from anaerobic digester.    ADVANTAGE - The method enables recovery of nutrients at higher recovery rates, with ease of operation, flexibility, minimized chemical usage, reduced energy sources, and capital investments. The method can be altered based on desired outcome of products, and recovery of one specific nutrient or more than one nutrient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for nutrient recovery system, which comprises an aeration reactor for heating and aerating anaerobic digester effluent, a stripping tower for mixing controlled amounts of acid with gaseous ammonia from the aeration reactor, and a vessel for collecting an ammonium salt produced from the reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of nutrient recovery system.    Anaerobic digester (10)    Effluent pit (110)    Solid-liquid separator (130)    Separated solids (135)    Separator liquid stream (137)    Ammonia gas (162)    Heat exchanger (180,322)    Stripping tower (190)    Biogas (200)    Two-chamber air tight vessel (310)    Aeration reactor (320)    Nozzle (324)    Two tower system (360)    Tank 2 (370)    Tank 1 (380)
NOVELTY - The method involves controlling temperature of a reaction kettle at 100-500 degrees centigrade. Plant distillate by catalyzing a reaction distillation raw material pump is mixed with hydrogen after exchanging heat from a heat exchanger into a hydrogenation reactor. A carrier is separated to obtain a gasoline component at 180 degrees centigrade and diesel component at 180-360 degrees. The hydrogenation diesel component is condensed for heating hydrogenation heterogeneous and a reactor. A metal catalyst is provided with nickel, platinum, ruthenium, palladium and cobalt.    USE - Method for producing reproducible petrol and diesel oil.    ADVANTAGE - The method enables using the metal catalyst to select the carrier according to composition and property of cracking vegetable oil through a liquid phase deposition method in a simple manner. The method enables reducing hydrogen consumption and avoiding consumption of low carbon alcohol.    DETAILED DESCRIPTION - The carrier is molecular sieve or amorphous aluminum silicon.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a reproducible petrol and diesel oil producing method. '(Drawing includes non-English language text)'
NOVELTY - The device has a grate (13) set on air pipe, and fixed on a pan (15). A head adjusting mechanism has a sleeve rod slidingly connected to a guide sleeve supported by a sleeve bracket. The guide sleeve is fixed on a blast pipe (14). A vertical bracket whose upper end is connected with fan-shaped wheel is fixed in the blast pipe. An eccentric wheel is connected to lower end of a rotating shaft, which is connected to the fan-shaped wheel. A middle rod is connected with the fan-shaped wheel and the lower end of the eccentric wheel.    USE - Temperature measuring device for residual slag of gasification furnace.    ADVANTAGE - The device can be installed easily and has convenient measurement. The accuracy and timeliness of the deslagging are improved along with improvement in garbage processing efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the temperature measuring device.    Furnace housing (12)    Grate (13)    Blast pipe (14)    Pan (15)    Furnace housing fixing frame (16)
NOVELTY - Rhodococcus ruber (CGMCC 4795) is new.    USE - R. ruber (CGMCC 4795) used in microbial agent for degrading petroleum hydrocarbon and bioremediation of petroleum pollutants, petroleum-polluted soil, and petroleum-polluted water (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for microbial agent for degrading petroleum hydrocarbon comprising R. ruber (CGMCC 4795) as active component.
NOVELTY - Pseudomonas (CGMCC 4793) is new.    USE - Pseudomonas (CGMCC 4793) used in microbial agent for degrading petroleum hydrocarbon and bioremediation of petroleum pollutants, petroleum-polluted soil, and petroleum-polluted water (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for microbial agent for degrading petroleum hydrocarbon containing Pseudomonas (CGMCC 4793) as an active component.
NOVELTY - The device has a connecting pipe extending into a filtering bottle. Bottom of the filtering bottle is provided with a clapboard. The filtering bottle is divided into left and right adjacent collecting areas. Two sides of bottom of the collecting areas are respectively provided with liquid outlet pipes. Each liquid outlet pipe is provided with a flow control valve or switch valve. Bottom of a filter is provided with two connecting pipes respectively extending into the collecting areas. The connecting pipes of the filter are respectively provided with flow rate control valves or switch valves.    USE - Device for filtering and separating high and low radioactive waste liquids.    ADVANTAGE - The device adopts different types of filters to simultaneously filter samples obtained from a culture flask, a culture dish and a test tube body. The device is provided with two filter drain pipes matched with the collecting areas of the filtering bottle for collecting high and low radioactive waste liquids.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a device for filtering and separating high and low radioactive waste liquids.
NOVELTY - The device has oxygen chamber (12), anaerobic chamber (14), contact aeration chamber (15), settling chamber (17) and sewage inlet (11). The sewage inlet is arranged at the upper portion of oxygen chamber. The settling chamber is opened with water outlet (24). The anoxic chamber is connected with biogas recycling pipe (13), oxygen chamber, anaerobic chamber and contact aeration chamber. The upper portion of guide hole is connected with contact aeration chamber and settling chamber.    USE - Rural domestic sewage processing device.    ADVANTAGE - The rural domestic sewage-processing device is simple in structure. The energy consumption of processing device is reduced. The pollutant removal rate of processing device is improved. The sewage treatment effect of processing device is improved. The gas can be recycled effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of rural domestic sewage processing device.    Sewage inlet (11)    Oxygen chamber (12)    Biogas recycling pipe (13)    Anaerobic chamber (14)    Contact aeration chamber (15)    Settling chamber (17)    Water outlet (24)
NOVELTY - The reactor has four reaction chambers (12-15), in which each chamber is provided with three-phase separator (5), air seal (6) and baffle plate (8) respectively. A gas lifting pipe (4) is provided at the top of each reaction chamber. The gas generated in the reactor is collected by a gas collecting device (2). The reaction chamber (15) is provided with bundle fiber filler (3) and micro-aeration device (9). A water inlet pipe (1) is arranged on the reaction chamber (12). A water outlet pipe (10) is provided in the tail portion of the reaction chamber (15).    USE - Multi-level multi phase anaerobic micro-oxygen baffling plate reactor.    ADVANTAGE - The shock resistance of the multi-level multi phase anaerobic micro-oxygen baffling plate reactor is improved. The loading capability of the reactor is improved. The water quality of the reactor is enhanced. The processing efficiency of the reactor is enhanced. The reaction time of the reactor is increased. The production of methane is improved by the reactor. The energy consumption of the reactor is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-level multi phase anaerobic micro-oxygen baffling plate reactor.    Water inlet pipe (1)    Gas collecting device (2)    Bundle fiber filler (3)    Gas lifting pipe (4)    Three-phase separator (5)    Air seal (6)    Baffle plate (8)    Micro-aeration device (9)    Water outlet pipe (10)    Reaction chambers (12-15)
NOVELTY - Heating device comprises device main body (1), an internal hollow pipe (2), connector (3), connecting pipe (4) and a thermostat bath (5). The internal hollow pipe is located within the device main body and the connectors are placed above the device main body. The connectors are separately connected with the internal hollow pipe and the connecting pipe as an enclosed connection. The connecting pipe is placed in the thermostat bath to form hollow pipeline loop with the main body.    USE - The heating device is useful for composting.    ADVANTAGE - The device: is simple in structure, easy to manufacture and provides heat efficiently at low temperature for composting.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the heating device for composting.    Device main body (1)    Internal hollow pipe (2)    Connector (3)    Connecting pipe (4)    Thermostat bath. (5)
NOVELTY - The device has a biomass gasification furnace (1) that is provided with the spiral tubes (7). An exhaust branch pipe is provided with the flow exhaust control valve (20). The biomass gasification furnace is arranged inside the filtering room (4) and the catalytic cracking chamber (5). The outlet of the gasification furnace is connected with the heat exchanger (11). The spiral tubes are arranged in the inner cylinder wall of the gasification furnace.    USE - Biomass gasification device for dual fuel engine.    ADVANTAGE - The tar content in the fuel gas can be reduced, since the biomass gasification furnace is arranged inside the filtering room and the catalytic cracking chamber. The structure of the biomass gasification device can be simplified. The flow resistance of the biomass gasification device can be made small. The gasification process of the biomass gasification device can be performed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass gasification device.    Biomass gasification furnace (1)    Filtering room (4)    Catalytic cracking chamber (5)    Spiral tubes (7)    Heat exchanger (11)    Flow exhaust control valve (20)
NOVELTY - The furnace has a furnace body (1) provided with a fire grate (2) of a gas outlet (3) and a feed port (8). A gas channel is provided with the fire grate and located on a lower part of a gasification agent inlet (4), a dust outlet (5) and an ignition port (6). A gas passage is connected with the gas outlet and the furnace body. The gas passage is provided with a methanation catalyst (16). The dust outlet is provided with a liquid seal (7). The gas outlet is fixed on the furnace body.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has high gas quality, high energy utilization rate and high gas tar content. The furnace saves production time, and can be utilized for continuous feeding.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification furnace.    Furnace body (1)    Fire grate (2)    Gas outlet (3)    Gasification agent inlet (4)    Dust outlet (5)    Ignition port (6)    Liquid seal (7)    Feed port (8)    Methanation catalyst (16)
NOVELTY - Constant temperature fiberglass biogas digester comprises a gas storage chamber (1) and a fermentation chamber (2), where the gas storage chamber is connected to a feed pipe (3) and an air outlet pipe (4). The fermentation chamber is provided with a thermostat (5) with the thermostat settings at the bottom of the chamber fixedly connected to the inner wall of the fermentation chamber. The thermostat comprises a constant temperature groove, a thermostatic liquid medium, a temperature sensor, a temperature controller and a thermostat cooling device, which are electrically connected.    USE - Used as constant temperature fiberglass biogas digester.    ADVANTAGE - The digester: maintains a constant temperature, has stable biogas production and controls the gas concentration easily.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the constant temperature fiberglass biogas digester.    Gas storage chamber (1)    Fermentation chamber (2)    Feed pipe (3)    Air outlet pipe (4)    Thermostat (5)
NOVELTY - An integrated biogas pool comprises an anaerobic reaction tank having a hard top cover on its upper part, and a double film structure gas storage cabinet. The top cover has a gas hole connected with the gas storage cabinet, and having double heat preservation or insulating layers on the top part.    USE - An integrated biogas pool.    ADVANTAGE - The pool has simple structure and heat preservation effect, eliminates integration of methane tank thus reducing energy consumption, reduces labor operation, ensures low temperature condition during winter, and can perform vigorous breeding of anaerobic bacteria without losing activity.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of an integrated biogas pool.
NOVELTY - The apparatus (100) has a microelectromechanical system (MEMS) micro-mirror (102) arranged in an optical path (150) of light from a light source (101) e.g. LED, that has passed through a sample to direct selected wavelengths of the light to a single detection point. A detector i.e. indium gallium arsenide (InGaAs) single point detection device (103), is arranged at the single detection point to convert incident light into electrical signals. A processor (106) is programmed to determine gas concentration of gases in the sample based on the electrical signals.    USE - Gas monitoring apparatus for monitoring gas concentrations in a gas sample i.e. methane (claimed) for industrial applications and research applications. Can also be used for hydrogen gas.    ADVANTAGE - The MEMS micro-mirror can be precisely rotated or positioned in response to a control signal. The apparatus allows desired wavelength of the light from absorption spectrum of the gas sample to be selectively directed to a light sensor, thus enabling full- spectrum acquisition of the absorption spectrum of the gas sample with a single light sensor, and hence allowing for accurate monitoring of the gases contained in the gas sample with the single light sensor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for determining gas concentration in a gas sample    (2) an alarm system for protecting from high concentration of certain gases.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas monitoring apparatus with an optical path.    Gas monitoring apparatus (100)    Light source (101)    MEMS micro-mirror (102)    InGaAs single point detection device (103)    Processor (106)    Optical path (150)
NOVELTY - Treating plant biomass comprises immersing plant biomass in a solution that contains a polar solvent and an imidazolium salt that has a melting point of at least 100 degrees C.    USE - The methods are useful for treating plant biomass; producing saccharide from plant biomass; and for producing biofuel (all claimed).    ADVANTAGE - Reacting the immersed plant biomass with a cellulase produces saccharide at high conversion efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of producing a saccharide from plant biomass comprising obtaining a saccharide by subjecting plant biomass to treatment by the treatment method above and to the action of a cellulase; and    (2) a method of producing a biofuel comprising producing a saccharide using the production method above; and further subjecting the obtained saccharide to fermentation.
NOVELTY - Preparing total saponin of Chinese Pulsatilla root comprises e.g. crushing the Pulsatilla root and extracting to obtain an extract solution; adding diatomaceous earth, filtering, vacuum extracting and concentrating to obtain concentrated extract solution; extracting using water saturated n-butanol and recovering to obtain n-butanol extract; passing the alcohol extract through polyamide resin column, adding distilled water and aqueous alcohol as eluent and collecting the eluents; and passing the eluents through neutral alumina column, recovering and drying the extract.    USE - The method is useful for preparing total saponin of Chinese Pulsatilla root.    ADVANTAGE - The method: is economical; produces total saponin having less impurity; and cause less environmental pollution.    DETAILED DESCRIPTION - Preparing total saponin of Chinese Pulsatilla root comprises: (i) crushing the Pulsatilla root into crude powder and extracting through microwave technique using water or methanol to obtain an extract solution; (ii) adding diatomaceous earth to agitate, filtering, vacuum extracting and concentrating the filtrate to obtain concentrated extract solution of Chinese Pulsatilla root; (iii) extracting the concentrated solution using water saturated n-butanol and recovering to obtain n-butanol extract; (iv) passing the n-butanol extract through polyamide resin column, adding distilled water and aqueous alcohol as eluent and collecting the eluents; and (v) passing the eluents through neutral alumina column, recovering and vacuum drying the extract.
NOVELTY - Treating organic residues from anaerobic processes, preferably fluid residues, comprises concentrating the organic residues by evaporation, and producing an ammonia-containing condensate in addition to the concentrated organic residues, where the condensate is subjected to an after-treatment, in which the ammonia is stripped from the condensate, and a dissipative, low ammonia effluent is produced.    USE - The method is useful for treating organic residues derived from anaerobic processes.    ADVANTAGE - The method: exhibits treatment of the resulting condensate so that, it is not discarded, and forms a dissipative effluent; exhibits significantly reduced amount of fluid to be disposed; and produces low ammonia water, which is conductive as a major part of the resulting fluid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow diagram of the after-treatment process.    System for organic residue treatment (1)    Condensate input (2)    Condensate container (3)    First heat exchanger (5)    First stripping column (6)
NOVELTY - The method involves securing a frame element (7.1) in a bottom portion of a front end of a bipolar plate (6) in a fluid tight manner. Another frame element (7.2) enclosing a membrane electrode unit (8) is secured in fluid tight manner, where frame elements are welded with one another. The latter frame is secured in an upper area of the front end of the bipolar plate. The membrane electrode unit is secured at a top face of the latter frame element for manufacturing a fuel cell (2) in a fluid tight manner.    USE - Method for manufacturing a fuel cell stack of fuel cells (claimed).    ADVANTAGE - The bipolar plate is provided with the circulating frame and the membrane electrode unit, so that the fuel cells are stacked in the fuel cell stack effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fuel cell comprising a circulating frame.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a fuel cell stack with several fuel cells.    Fuel cell stack (1)    Fuel cells (2-4)    Bipolar plate (6)    Frame elements (7.1, 7.2)    Membrane electrode unit (8)
NOVELTY - An organic hydride dehydrogenation system (100) has a thermoelectric feeder device (8) for generating heat and electricity, and a water electrolysis apparatus (12) for electrolyzing water and producing hydrogen. The heat is supplied by the feeder device for dehydrogenation of organic hydride, and electric supply is performed with respect to water electrolysis apparatus.    USE - Organic hydride dehydrogenation system.    ADVANTAGE - The organic hydride dehydrogenation system effectively utilizes electricity produced in thermoelectric feeder device.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of thermoelectric supply type organic hydride station.    Hydrogen purification device (3)    Thermoelectric feeder device (8)    Control unit (11)    Water electrolysis apparatus (12)    Organic hydride dehydrogenation system (100)
NOVELTY - The invention relates to an exciter for under atomic particles of fossil and nuclear fuels. According to the invention, the exciter comprises 4 overlapped layers of which one layer (2) is a support layer of expanded polyvinyl, one layer (3) of expanded polyvinyl wherein there were embedded 50...150 g/m2 of aluminium shots of 0.1...0.3 mm, one layer (4) of expanded polyvinyl wherein there were embedded 200...600 g/m2 of magnetized barium hexaferrite having a grain size of 0.1...0.3 mm and one layer (5) of expanded polyvinyl wherein there were embedded 100...300g/m2 SiO2 of 98% purity, with a grain size of 0.1...0.3 mm, one bioadhesive layer (6) and one layer (7) for the protection of the bioadhesive layer being applied on tanks, supply pipes and engines working with fossil and nuclear fuels, leading to a reduction of 10...15% of the fuel consumption.
NOVELTY - The system has a separating material processing system that separates decay processed organic waste. The degradable biological comprehensive treatment system performs anaerobic digestion treatment. An artificial wetland integrated treatment system purifies liquid. The material processing system, biological integrated processing system and artificial wetland integrated treatment system are provided with observing and controlling spot. A control system is connected with monitoring point for detecting and controlling operating state of processing system.    USE - Comprehensive processing system for processing urban organic garbage.    ADVANTAGE - The city organic waste can be processed in circular manner. The organic garbage can avoid secondary pollution to the environment. The processing integration system using the organic natural biomass can be provided for processing city organic waste and forming ecological economic circulation processing chain.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the comprehensive processing system for processing urban organic garbage. (Drawing includes non-English language text)
NOVELTY - Large wrap-around multi-stage mixing biogas fermentation device comprises an inner chamber and an outer chamber. The outer chamber is provided with multiple inner grading stirrers and a surrounding plate. The inner cavity is equipped with a stirrer. The entire wall on the inner chamber is provided with multiple secondary fermentation feed inlet and a slag door is located at the bottom. The inner and outer chamber is connected with a gas-guide tube. The outer chamber is equipped with a water inlet and feeding port.    USE - Used as a large wrap-around multi-stage mixing biogas fermentation device.    ADVANTAGE - The device completely digests the organic material; has raw material utilization rate of 75% and gas production rate of 20%; prevents the hardening of raw materials; aids in complete mixing of raw materials which enhances the function of killing pathogenic bacteria, and reduces the secondary pollution; has simple operation; is safe and reduces the operating costs by 20%; and is utilized for digesting various organic matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the large wrap-around multi-stage mixing biogas fermentation device.
NOVELTY - Large bent plastic pipe of anaerobic digester, where the pipe is tubular in shape, is claimed.    USE - Used as a large bent plastic pipe of anaerobic digester.    ADVANTAGE - The device is safe and economical; has high strength and long service life; has good heat insulating performance; and has corrosion resistance, and acid and alkali resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the large pipe type plastic anaerobic digester.
NOVELTY - The furnace has a vent hole (4), a gas pipe (5), a grate (6), a fuel board (7), a back counter heating board (8), a cover (9), a steel pipe (10), a super-conduction heat tube (12), a chimney (13), a combustion chamber furnace cover (14), a chamber cover (15), a hopper (16), and a furnace body divided into a storage area (1), a burning area (2) and a flue (11). The storage area and burning area are separated from a front counter heating board (3). The flue gas channel area is provided with a combustion area for supplying oxygen to middle flame and outer flame for complete burning.    USE - Three-pass counter heating biomass superconducting heat semi-gasification furnace.    ADVANTAGE - The furnace has better heating effect, simple and rapid operation, and environment-friendly and energy-saving effects. The furnace effectively absorbs residual heat, and reduces the waste of heat energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a three-pass counter heating biomass superconducting heat semi-gasification furnace.    Storage area (1)    Burning area (2)    Front counter heating board (3)    Vent hole (4)    Gas pipe (5)    Grate (6)    Fuel board (7)    Back counter heating board (8)    Cover (9)    Steel pipe (10)    Flue (11)    Super-conduction heat tube (12)    Chimney (13)    Combustion chamber furnace cover (14)    Chamber cover (15)    Hopper (16)
NOVELTY - The method involves allowing platinum ion to adsorb cation exchange resin by carrying out ion exchange reaction of a mixture. Hydrogen in the platinum ion of the mixture is reduced. A cation of transition metal is chosen from sulfate ion, nitrate ion, cobalt, nickel and iron. The cation of the metal is allowed to adsorb the cation exchange resin contained in the mixture. Hydrogen in the cation of the metal in the mixture is reduced. The metal is obtained by dissolving a transition metal compound in a solvent, and anion is produced by the transition metal compound.    USE - Method for producing a catalyst i.e. platinum, for a fuel cell i.e. polymer electrolyte fuel cell, of an electric power generation system.    ADVANTAGE - The method enables providing high content rate of transition metal alloy with respect to alloying degree.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating relationship between count of carrying of cobalt and alloying degree of a platinum-cobalt alloy and relationship between count of carrying of cobalt, catalyst and content rate of alloyed cobalt. '(Drawing includes non-English language text)'
NOVELTY - Preparing a composition (A) of alcohol esters of 6-26C linear monocarboxylic acids and glycerin, comprises reacting vegetable or animal oil, neutral or acidic, virgin or recycled, with 1-18C aliphatic monoalcohol in the presence of a heterogeneous acid-base catalyst based on nitrogen metallophosphate (I).    USE - (A) is useful in diesel fuels, heating oil, ecological solvents, base compounds for the manufacture of sulfonates of fatty alcohol, amides, esters, and dimers.    ADVANTAGE - The process is economical to produce (A) and provides the composition with high purity. The process reduces operating costs. (A) can be easily purified.    DETAILED DESCRIPTION - Preparing a composition (A) of alcohol esters of 6-26C linear monocarboxylic acids and glycerin, comprises reacting vegetable or animal oil, neutral or acidic, virgin or recycled, with 1-18C aliphatic monoalcohol in the presence of a heterogeneous acid-base catalyst based on nitrogen metallophosphate of formula (M(m)P(1-y)O(m+5(1-y)3x)/2Nx) (I).    M = a metal cation of at least one element comprising metals of groups 4 and 13 of the periodic classification;    m = the degree of oxidation of the cation M;    y = 0-1; and    x = more than 0 to up to 2.67, where m+5(1-y)-3x is greater than or equal to 0.
NOVELTY - Preparing polyazoles, comprises: (a) treating at least one polyazole having at least one amino group in a repeat unit with a solution comprising (i) at least one strong acid and (ii) at least one stabilizing reagent, where the total content of stabilizing reagents in the solution is 0.01-30 wt.%; and (b) performing the stabilization reaction directly and/or in a subsequent processing step by heating to a temperature of greater than 25 degrees C, where the process is carried out using at least one high-functionality polyether as the stabilizing reagent.    USE - The polyazoles are useful in a membrane, where the membrane is useful for producing a membrane electrode unit which is useful for producing a fuel cell (all claimed).    ADVANTAGE - The process provides polyazoles in a simple, economical, environmentally friendly and industrial manner. The polyazoles has improved conductivity, mechanical stability such as elasticity and elongation stability, and long term durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a membrane comprising at least one polyazole obtained by the process.
NOVELTY - Kitchen waste processing device comprises a solid-liquid separating and drying device, a crushing device and a fermentation equipment. The solid-liquid separating and drying device, crushing device and fermentation device are sequentially connected from top to bottom and provided with programmable logic controller.    USE - Used as a kitchen waste processing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the kitchen waste processing device.    Stirring motor (1)    Waste inlet (2)    Baffle (5)    Funnel (15)    Top cover (16)
NOVELTY - The device has a percolate recharging system comprising a percolate collecting pool, a water pump and several water inlet pipes and water outlet pipes. A landfill reactor is provided with an acid buffer layer, and the domestic garbage landfill layers located on the acid buffer layer. The acid buffer layer is provided with the burned remains of the domestic garbage.    USE - Biological reaction device for accelerating landfill stabilization process of domestic garbage.    ADVANTAGE - The garbage filling humidity is recharged by the percolation liquid, the pH environment in the garbage main portion is adjusted through acid buffer layer, and a better living environment is created for garbage degradation microorganism, so as to realize acceleration of the degradation of garbage. The device investment cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biological reaction device.
NOVELTY - Digester for improving rural household biogas comprises a marsh gas tank (1), hydraulic pressure room (2), discharging pool (4), fertilizer storage tank (5), drain tube (3), feed pipe, dreg pipe and return pipe. The tank includes a wall body on the ground wall body, and the hydraulic pressure room of the marsh gas tank is installed southwest 60-62 degrees .    USE - Used as a digester for improving rural household biogas.    ADVANTAGE - The digester: improves the circulation of material solution in the biogas pool so as to fully ferment and smoothly feed; reduces the circulating dead angle area; and occupies little space.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the digester.    Marsh gas tank (1)    Hydraulic pressure room (2)    Drain tube (3)    Discharging pool (4)    Fertilizer storage tank (5)
NOVELTY - The device has channels that are connected orderly with the electronic display and controller of a garbage centrifugal separator, waste fermentation tank, integrated waste synthesis device and solid product mixed recycling device. The electronic display and controller is used for real-time monitoring of garbage centrifugal separator, waste fermentation tank, integrated waste synthesis device and solid product feeding and discharging device.    USE - Device for dry fermentation of organic garbage.    ADVANTAGE - A safe and high-efficient mixing of organic garbage is performed efficiently so as to realize recycling of garbage reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of organic garbage dry fermentation device. (Drawing includes non-English language text)
NOVELTY - The electrolysis electrode has a porous membrane for transmitting generated gas to the gas passage side without transmitting the electrolyte solution. The electrolyte solution flow path making the gap to impregnate the electrolyte solution is provided by inducing the electrolyte solution to the gap. The gap is formed such that the emitted gas in wetted surface in bubble form contacts the porous membrane. Insulating membrane includes fluorine. Hydrogen and fluorine gas are emitted be electrolyzer.    USE - Electrolysis electrode used in electrolysis of electrolyte solution (claimed).    ADVANTAGE - The porous membrane transmits generated gas to the gas passage without transmitting it to the electrolyte solution. Gas passage is completely isolated in stable state so that the stagnation of the generated gas is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolyser.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the electrolysis electrode. (Drawing includes non-English language text)    Bubble (4)    Spacer (5)    Porous membrane (6)    Gap (7)    Electrolyte solution (18)
NOVELTY - An energy generation system (1) comprises electric power generation unit to produce electric power and hot exhaust gas, hydrogen generation unit (30) to produce hydrogen by dehydrogenating hydrogen storage medium using heat of hot exhaust gas of electric power generation unit, and electrolysis unit to electrolyze water and produce hydrogen and oxygen using electric power from electric power generation unit.    USE - An energy generation system for hydrogen-fueled car, polymer electrolyte fuel cell, and solid oxide fuel cell.    ADVANTAGE - Energy generation system is small in size and produces electric power and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an energy generation system. (Drawing includes non-English language text).    Energy generation system (1)    Engine (11)    Generator (13)    Hydrogen generation unit (30)    Electric power distribution apparatus (51)
NOVELTY - The method involves uniting a porous body member with a metallic bond, where the porous body member consists of spherical metal powder. Shape of the porous body member is naturally obtained by the effect of surface tension. Size of a hole is matched with a particle size of the spherical metal powder. Optimal sintering temperature is changed corresponding to the particle size of the spherical metal powder.    USE - Method for manufacturing a fuel cell separator.    ADVANTAGE - The porous body member consisting of metal powder is mutually united by the metallic bond, thus improving freedom degree of flow-path design with precision, supply characteristics and emission characteristic, and reducing contact resistance.
NOVELTY - A composition comprises an ignition accelerator selected from normal propyl nitrate, di-tert.-butyl peroxide, acetone peroxide, m-nitrobenzotadecylamide di or triethylene glycol dinitrate, and alkyl or cycloalkyl nitrates having 10 carbon atoms selected from allyl nitrate, heptyl nitrate, 2-ethylhexyl nitrate, butyl nitrate, ethyl nitrate, amyl nitrate or isopropyl nitrate. Another component is selected from propylene glycol monoalkyl ether, butylene glycol monoalkyl ether, methyloxyalcohol, ethyloxyalcohol, propoxyalcohol, butoxyalcohol or 1-4C alcohols.    USE - Composition for improving combustion performance of hydrocarbon or alcohol based fuels used as fuel component in a standard non-modified gasoline or diesel engine (claimed).    ADVANTAGE - The composition has adjustable fuel power booster component and generates lower amounts of toxic gas emission and provides more power.    DETAILED DESCRIPTION - A composition comprises an ignition accelerator selected from normal propyl nitrate, di-tert.-butyl peroxide, acetone peroxide, m-nitrobenzotadecylamide di or triethylene glycol dinitrate, and alkyl or cycloalkyl nitrates having 10 carbon atoms selected from allyl nitrate, heptyl nitrate, 2-ethylhexyl nitrate, butyl nitrate, ethyl nitrate, amyl nitrate or isopropyl nitrate. Another component is selected from propylene glycol monoalkyl ether, butylene glycol monoalkyl ether, methyloxyalcohol, ethyloxyalcohol, propoxyalcohol, butoxyalcohol, 1-4C alcohols, polyoxypropylene glycol monoalkyl ether or polyoxybutylene glycol monoalkyl ether. A third component is selected from methyl carbonate, ethyl carbonate, propyl carbonate, butyl carbonate with dimethoxymethane or diethoxymethane.
NOVELTY - The generator main portion is set on the top side of a material inlet (1). A gas filling layer (2) filled with dislocation type material (5) is formed in back layer of material inlet. A sedimentation slot (3) is provided at the lower side of main portion.    USE - Biogas generator.    ADVANTAGE - The biogas is generated by anaerobic fermentation of waste material of the cattle efficiently so as to achieve effective utilization of energy and environment protection effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas generator.    Material inlet (1)    Gas filling layer (2)    Sedimentation slot (3)    Dislocation type material (5)    Heat exchanger (10)
NOVELTY - The apparatus has a compression chamber (1) that is provided with a feeding port. The lower end of feeding port is provided with a discharge opening (3). The compression chamber is set on the ground through the triangular bracket (4). The feeding port is connected with a feeding pipe (5).    USE - Apparatus for manufacturing combustion rod device by using manure mixture.    ADVANTAGE - The cow dung and other mixture can be provided into the feed inlet through feeding pipe. The compression chamber is suspended to collect and package the carbon rod efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for manufacturing combustion rod device by using manure mixture.    Compression chamber (1)    Discharge port (2)    Discharge opening (3)    Triangular bracket (4)    Feeding pipe (5)
NOVELTY - The processing system has water-adjusting tank whose water outlet is connected with biogas generating pool. The biogas generating pool is connected with discharging pipe. The greenhouse house water pipe is paved under soil layer which is provided on bottom of chamber. The chamber is provided with water outlet.    USE - System for processing domestic sewage used for generating combustible gas product.    ADVANTAGE - The sewage is treated without using chemicals, so that cost for treating sewage is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of domestic sewage processing system.
NOVELTY - The machine has a movable carriage that is provided on the machine main portion. A tractor is provided on the power output shaft. The input shaft of the universal joint is connected with speed reducer. The crusher is connected with the power input shaft of the belt.    USE - Machine for manufacturing biomass fuel.    ADVANTAGE - The efficiency, operability, and reliability of the machine for manufacturing biomass fuel can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the machine for manufacturing biomass fuel.
NOVELTY - A household organic garbage biogas generating device comprises a soft marsh gas bag (3) in a detachable shell, and a feeding flange interface or feeding device on the detachable shell, capable of moving up and down the material pipe (10) on the detachable shell.    USE - A household organic garbage biogas generating device.    ADVANTAGE - The device can be disassembled to move, and is convenient to use, economical, and practical.    DESCRIPTION OF DRAWING(S) - The drawing is a sectional view of a household organic garbage biogas generating device.    Soft marsh gas bag (3)    Connection plate (5-1)    Frame (8)    Bottom (9)    Material pipe (10)
NOVELTY - Disclosed is a method of obtaining a dry form of a biopreparation based on Pseudomonas or Rhodococcus oil-decomposing microorganism for cleaning territories from oil and oil products. Pseudomonas or Rhodococcus bacteria are cultured in a liquid culture medium. The bacteria suspension is them mixed with a protective medium. The protective medium is prepared based on 0.05 M sodium-potassium phosphate buffer with pH 6.8, with the following ratio of components: 4% polyglucin, 10% saccharose, 4% thiourea, 2% ascorbic acid, followed by titration with 45% sodium hydroxide solution to pH 6.8-7.2. The obtained mixture is added to a sorbent - expanded pearlite sand. The preparation then undergoes contact drying at t=37 degrees C until constant mass.    USE - Chemistry.    ADVANTAGE - Method increases survival rate of bacterial cells of oil-decomposing microorganisms Pseudomonas and Rhodococcus. 1 dwg, 2 tbl, 3 ex
NOVELTY - The device has ferment tank divided into upper portion of solid phase biogas fermentation area and lower portion of liquid phase biogas fermentation area. The sludge is mixed marsh liquid in liquid phase area. The solid phase biogas fermentation area is set in two layer breaking cutting arm. The solid phase baseplate is installed at solid phase biogas fermentation area. The biogas residue and biogas liquid is discharged by sieve plate. The biogas sludge from bottom drain valve outlet is passed into feeding slot through connecting valve.    USE - Biogas ferment device.    ADVANTAGE - The biogas ferment device is simple in structure. The biogas ferment device can be operated conveniently and continuously. The biogas residue and biogas liquid are capable of realizing power-free two phase separation. The liquid can be circulated easily so as to reduce pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas ferment device.
NOVELTY - The tank has tension net (19) that is provided on gas storage cabinet (6). A tank portion (3) is provided with constant pressure explosion-proof fan (20). A liquid circulate loop tube (12) is provided on pH value monitoring port (13). A biogas outlet pipe (9) is provided on methane concentration monitoring port (10) which is provided on biogas flow monitoring port (11). A stirrer (4) is mounted on the blade shaft. A heating device (17) that is provided in tank portion is arranged on middle of the base of external spiral heating tube.    USE - Anaerobic fermentation tank.    ADVANTAGE - The biogas fermentation process can be monitored effectively. The dynamic change of the microorganism can be monitored. The utilization efficiency of the fermentation tank can be improved. The performance of the fermentation tank can be controlled effectively. The production efficiency can be improved. The energy loss and cost can be reduced. The fermentation tank can be maintained effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic fermentation tank.    Tank portion (3)    Stirrer (4)    Gas storage cabinet (6)    Biogas outlet pipe (9)    Methane concentration monitoring port (10)    Biogas flow monitoring port (11)    Liquid circulate loop tube (12)    Monitoring port (13)    Heating device (17)    Tension net (19)    Constant pressure explosion-proof fan (20)
NOVELTY - The system has an overflow tube (2) whose lower end is provided with an overflow opening (1). An upper portion of tube is provided into overflow tank. An overflow box (6) is provided with a liquid pipe (7). The overflow box is provided with a maintenance hole (5) and gas-guide hole (4).    USE - Overflow system of anaerobic biogas tank.    ADVANTAGE - The blockage of biogas slurry pipe in self-propelled marsh liquid can be prevented. The pressure of biogas tank can be kept constant. The sunk in reaction device can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the overflow system of anaerobic biogas tank.    Overflow opening (1)    Overflow tube (2)    Gas-guide hole (4)    Maintenance hole (5)    Overflow box (6)    Liquid pipe (7)
NOVELTY - Mixed fuel of biodiesel and non-standard diesel, is claimed. The mixed fuel is prepared by mixing a non-standard diesel with a mixture A containing biodiesel and denatured methanol in a volume ratio of 9:1-1:9, where the mixture A is prepared by adding denatured methanol to biodiesel in a volume ratio of 15%, and the denatured methanol is prepared by adding auxiliary materials comprising (vol. %) isopropyl alcohol (15-45), isobutyl alcohol (15-45), isooctane (15-25), oleic acid (5-10), polyether (2-4) and Tween 80 (RTM: Polysorbate 80) (2-5%) into methanol in a volume ratio of 10-20%.    USE - The mixed fuel is useful for diesel engine.    ADVANTAGE - The method allows complete combustion of biodiesel, and prevents layering of the fuel after long-time storage. The mixed fuel is transparent and is can be used in a diesel engine, prevents the smell of tail gas, and is a good fuel for vehicle.
NOVELTY - Candida versatilis is used for removing aflatoxin B1 (AFB1) in traditional seasoning, high-salt liquid material system, and high-salt semi-solid material system by culturing activated strain in malt juice liquid culture medium, where concentration of initial strain is 1.0x 106-3.0x 106 colony forming units/g (ml).    USE - The C. versatilis is used for removing AFB1 in traditional seasoning, high-salt liquid material system, and high-salt semi-solid material system by culturing activated strain in malt juice liquid culture medium. It is for use in each traditional brewing product, such as pomegranate fruit juice, fermented bean curd, and fermented soya beans; and is inoculated in AFB1 polluted soy sauce, soybean paste, or thick broad bean sauce. (all claimed)    ADVANTAGE - The C. versatilis has AFB1 removing rate of 20.15%.
NOVELTY - Composition is obtained by using roots, seeds, buds, leaves, stems, heartwood, fruit, pulp and/or peel of terrestrial and/or aquatic plants, subjecting obtained product for drying process chosen from drum drying and freeze drying, subjecting obtained product for solvent extraction process using carbon dioxide, ethanol, water, glycol, and steam, and subjecting obtained product for cold pressing, or glycerine suspension and/or other type of extraction process chosen from hydrogenation, hydrolysis, esterification, etherification, sulfatation, and fermentation process.    USE - The composition is used in pharmaceutical and cosmetic formulation for performing transfollicular oxyfusion process for treating hair loss, androgenic alopecia, alopecia, telogen effluvium, senile hair greying, premature hair graying, actinic keratosis, lipofuscin, skin pigmentation disorders, glycated tissues, acne, rosacea, eczema, psoriasis, scar healing, wound healing, stretch mark, wrinkles, fine lines in skin, scalp sagging, skin sagging, and UV radiation damage, and promoting vascular circulation, and lymphatic circulation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) meristematic stem cell derived by subjecting terrestrial and/or aquatic plant to hydroponic techniques, and subjecting obtained product for incubation and/or mass cultivation;    (2) synthetic components obtained by using the above-cited composition, and subjecting the composition for common laboratory practices; and    (3) use of above-cited composition and/or solution for transfollicular oxyfusion process, by administering the above-cited composition to the human scalp skin, face skin, neck skin, arm skin, or body skin.
NOVELTY - The device has anaerobic reactor (2) that is provided with slant stirrer and inner heat pipe (1). The heat pipe is connected with wall of the annular tube of anaerobic reactor tank wall. The anaerobic reactor is provided outside built house. The solar heat collecting bottom of solar heat supply pipeline (8) is connected with heat pipe in anaerobic reactor water inlet end. The heat taking pipelines in anaerobic reactor water outlet and water inlet is connected with solar collector of anaerobic reactor. The anaerobic reactor is connected with methane gas outlet pipe.    USE - Processing device for resource utilization of edible fungi.    ADVANTAGE - The absorptivity, anti-corrosion, antiultraviolet and aging of resource utilization of edible fungi can be obtained. The processing device for resource utilization of edible fungi can used to fully absorb the solar energy, high temperature anaerobic fermentation, biogas large gas yield, commercial product with multiple specifications. The fungal drug with corn straw and cattle excrement in the anaerobic reactor can be combined for fermentation. The crust of feeding and discharging of fungal drug raw material can be avoided. The organic fertilizer residue can be generated. The biogas can be generated to prepare fruit or vegetable fertilizer. The residues can be processed to obtain the energy biogas and organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing device for resource utilization of edible fungi.    Heat pipe (1)    Anaerobic reactor (2)    Plastic cover (3)    Solar heat supply pipeline (8)    Biogas outlet pipe (9)
NOVELTY - The system has discharging port that is provided with gas-guide tube and slag. A connecting seat is connected with lower end of sullage pipe. The lower end of connecting seat is connected with a base through a flange. The upper end of discharging pipe is connected with an elbow welded with a support on upper end flange set on the base. The base is connected with a support fixed with a motor. The micro lock switch is arranged to bear larger current and pressure generated by self-lock mechanism through the pressure pipe and switches the micro-switch to ON or OFF state.    USE - Biogas garbage processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biogas garbage processing system.
NOVELTY - The device has a methane tank (1) whose upper and lower portions are provided with a fixing bump (7). A screw (6), fixing bump and methane tank are connected with a material inlet (2) and material outlet (3). The opening of the methane tank is provided with a flange cover (4) inserted in the methane tank and air outlet pipe (5).    USE - Marsh gas generating device for generating methane.    ADVANTAGE - The marsh gas generating device is convenient to use and install, environment-friendly and energy saving.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the marsh gas generating device.    Methane tank (1)    Material inlet (2)    Material outlet (3)    Flange cover (4)    Air outlet pipe (5)    Screw (6)    Fixing bump (7)
NOVELTY - The device has marsh gas collecting shell (1) is fixed on the base plate by a pin (2) and center of methane collecting shell is connected with a marsh gas gas-guide tube (5). The marsh gas gas-guide pipe is equipped with a gas outlet valve. One end of the marsh gas gas-guide tube is provided with a water vapor filter.    USE - Biogas collecting device.    ADVANTAGE - The device has simple structure, low manufacturing cost. The device greatly reduces the collection cost of the biogas and reduces the pollution of the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas collecting device.    Marsh gas collecting shell (1)    Pin (2)    Chassis (3)    Gas valve (4)    Marsh gas gas-guide tube (5)
NOVELTY - The device has a fermenting unit and storage unit and lighting unit that are located on one end of device. The storage unit and the fermenting unit are connected with each other. The upper end of a fermenting tank is provided with a feeding port and the lower end is provided with a discharge port.    USE - Biogas device e.g. marsh gas generator.    ADVANTAGE - The device is featured with simple structure, high production efficiency, stable reaction, convenient use and low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas device.
NOVELTY - The system has a bounding wall (3) on which transparent heat concentrating shed is arranged. A furnace grate is installed between air inlet and feed inlet. The air inlet is connected with methane tank (2) through pipeline, and decomposed manure kiln is set as an elongated groove which is arranged underground. The multiple fixed cover plates with charging opening, are arranged on groove at intervals and movable cover plate (4) is arranged between two fixed cover plates. The drying field (1) has charging opening (85) that matches with methane tank.    USE - Garbage treatment system for village.    ADVANTAGE - The garbage treatment system has simple structure and low manufacturing cost, protects ecological environment and is capable of realizing effects of sanitation, harmless disposal, resource utilization, convenience and feasibility.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the garbage treatment system.    Drying field (1)    Methane tank (2)    Bounding wall (3)    Movable cover plate (4)    Charging opening (85)
NOVELTY - The material has a material body containing opal-bottom sediment in an amount of 10-50 percent by weight. A combustible material is obtained in an amount of 50-90 percent by weight and moisture content of 2-15 percent. Rapeseed meal, rapeseed pollution, Chopper, fine coal, coal waste, bone meal, sawdust, wood chips are mixed with each other and utilized as a technological addition of quicklime. The combustible material is freely formed and dried to obtain adequate moisture about 10 percent.    USE - Fuel material for producing combustion in a fireplace and a furnace that is utilized in power plants.    ADVANTAGE - The material is high in calorific value, inexpensive and environmentally friendly.
NOVELTY - Method involves introduction of a consortium of microorganisms and mineral culture medium into the medium to be cleaned. The microorganisms used are the yeast strain Candida maltosa VKPM Y-3446 and the bacterial strain Dietzia mans VKPM Ac-1824 in ratio (1-99):(99-1)%, respectively.    USE - Chemistry.    ADVANTAGE - Invention increases efficiency of cleaning the environment from hydrocarbon pollutants. 2 tbl
NOVELTY - A biological gas is produced from methane by removing solid impurities in methane through a filter, desulfurizing through drying, compressing to 0.8-1.5MPa through a compressor, feeding the pressurized methane into an absorbing tower from the lower part of the absorbing tower to spray and wash by water, and adsorbing, drying and dewatering through a molecular sieve.    USE - Process for producing biological gas from methane (claimed).    ADVANTAGE - The process uses methane to produce biological gas, and is simple, safe in operation, high in gas product recovery ratio, and free in pollution to environment. It also meets the national standards.
NOVELTY - An Aspergillus niger strain J4 (CGMCC 4219) is new.    USE - Aspergillus niger strain J4 (CGMCC 4219) used as fungicide for degrading organophosphorus insecticide (claimed).    ADVANTAGE - The fungal strain provides degradation enzyme system that can effectively degrade thiophosphate (P=S bond) and phosphate (P=O bond), and has broad application spectrum, high degrading rate and short degrading time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fungicide for degrading organophosphorus insecticide, where the fungicide is prepared by respectively inoculating Aspergillus niger strain J4 (CGMCC 4219) and Aspergillus niger strain J6 (CGMCC 4220) to a potato dextrose agar (PDA) inclined face to prepare inclined-face strain, cultivating through a PDA substrate until spore is matured, respectively adding to a glucose base salt substrate, cultivating until the spore is sprouted into spore seed liquid, and preparing two seed liquids at volume ratio of 0.3-3:1.
NOVELTY - A microalgae strain, preferably Mychonastes sp. HS0-3-1 (CGMCC No: 4654), is new.    USE - The microalgae strain, preferably Mychonastes sp. HS0-3-1 is useful for producing grease, biodiesel, algae protein, fatty acid and/or biomass components. The grease is chosen from 3-18C unsaturated fatty acid linolenic acid and 1-24C nervonic acid (all claimed).    ADVANTAGE - The microalgae strain produces high value products inexpensively and environmentally-friendly.
NOVELTY - A middle electrode plate (6) is equipped between front and back end titanium electrode plates (3). Two sides of middle electrode plate are equipped with a groove symmetrical to front and back end electrode plates. A film electrode is equipped between middle electrode plate and front end electrode plate and between middle plate and back end electrode plate. The film electrode is equipped with a water inlet and an outlet. The film electrode is sealed with front end electrode plate and inside of back end electrode plate and sealed with side of middle electrode plate.    USE - Hydrogen production device based on solid electrolytic cell.    ADVANTAGE - The middle electrode plate is used to form several groups of electrolytic cells such that hydrogen production efficiency of the hydrogen production device can be improved. The number of the electrolytic cells is increased or decreased freely according to the required quantity of hydrogen production. The heat dissipation holes are formed on the middle electrode plate such that the heat dissipating performance of the solid electrolyte electrolytic cell can be improved with prolonged service life of products.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the hydrogen production device.    Front end plate (1)    Back end plate (2)    Front end electrode plate (3)    Middle electrode plate (6)
NOVELTY - A hydrogen-oxygen source pre-cracking device is composed of a super-gravity cutter, a supersonic atomizer, an electromagnetic radiation generator, a channel and a spray.    USE - Device is used for predetermined-cracking hydrogen-oxygen source.    ADVANTAGE - The device efficiently and economically cracks hydrogen-oxygen source.
NOVELTY - Preparation of aryl ring propionaldehyde derivative (I) comprises reacting phenyl-containing compound (II) with magnesium to obtain magnesium-phenyl-containing compound (III), hydrolyzing compound (III) with boron-containing compound to obtain phenyl-borodihydroxy compound (IV); and reacting compound (IV) with acrolein and alkali in the presence of catalyst to obtain compound (I).    USE - Preparation of aryl ring propionaldehyde derivative (I) used in medicine and daily chemicals.    ADVANTAGE - The method uses easy to obtain raw materials, and low cost. It is carried out without oxidation and reduction reactions, simple route, mild reaction condition, low requirement of production device, and small three wastes discharging amount. It is environment-friendly and produces aryl ring propionaldehyde derivative in high yield and easy industrial production.    DETAILED DESCRIPTION - Preparation of aryl ring propionaldehyde derivative of formula (I) comprises reacting phenyl-containing compound of formula (II) with magnesium to obtain magnesium-phenyl-containing compound of formula (III), hydrolyzing compound (III) with boron-containing compound of formula (B(OR6)3) to obtain phenyl-borodihydroxy compound of formula (IV); and reacting compound (IV) with acrolein and alkali in the presence of catalyst to obtain compound (I).    R1-R5=H, 1-4C alkyl, 1-4C alkoxy, F, Cl, halo, or NO;    R6=H or 1-4C alkyl;and    X=F, Cl, Br, or I.
NOVELTY - The device has a solar battery (1) that is installed at an upper portion of support bracket (2), and linked with a brine electrolysis type hydrogen producing device (4) through conductive wire (3). The hydrogen producing device is connected with hydrogen fuel storing container manufacturing workshop (6) through hydrogen input pipe (5). A hydrogen fuel storing container (7) is linked through hydrogen fuel conveying pipe (8), with hydrogen fuel battery (9) which is linked with electric motor through conductive wire. The electric motor is connected to rape harvester.    USE - Power device for supplying solar hydrogen energy source to rape harvester.    ADVANTAGE - Since the power energy can be released effectively via the electrochemistry reaction and the power energy in the electric motor can be transformed into mechanical energy supplied to the rape harvester, the harvesting and threshing operations of rape can be performed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the power device for supplying solar hydrogen energy source to rape harvester.    Solar battery (1)    Support bracket (2)    Conductive wire (3)    Brine electrolysis type hydrogen producing device (4)    Hydrogen input pipe (5)    Hydrogen fuel storing container manufacturing workshop (6)    Hydrogen fuel storing container (7)    Hydrogen fuel conveying pipe (8)    Hydrogen fuel battery (9)
NOVELTY - The device has an anaerobic digester (110) making organic waste using anaerobic digestion. A microorganism concentration device (120) uses anaerobic digestive fluid as mixed liquid and biogas generated in the anaerobic digester as pressurized gas, and separates the anaerobic digestive fluid ejected from the anaerobic digester into processing water and solid material. The microorganism concentration device comprises a floating detachment tank (121) storing the solid material. A coagulant feeding unit (124) supplies coagulant to a mixing unit (123).    USE - Anaerobe concentration device.    ADVANTAGE - The device has high biogas production efficiency, and improves flotation separation efficiency of solid content included within the anaerobic digestive fluid. The device prevents influence of anaerobic digestion process. The device has low organic component and solid material concentration, and removes microorganism thickened sludge. The device can discharge waste water economically.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an anaerobe concentration device. '(Drawing includes non-English language text)'    Anaerobic digester (110)    Microorganism concentration device (120)    Floating detachment tank (121)    Mixing unit (123)    Coagulant feeding unit (124)
NOVELTY - Nano rare-earth additive comprises lanthanum compound, cerium compound, manganese compound, or their salts, which account for 60% of quality component. Their single compound accounts for 10-25% of proportion; and remaining 3-5 components comprise dysprosium compound, lutetium compound, erbium compound, scandium compound, praseodymium compound, neodymium compound, and yttrium compound, or their salts.    USE - Nanometer rare-earth additive used for dimethyl ether fuel gas and methyl alcohol fuel; or for liquid-phase dimethyl ether or methyl alcohol (claimed).    ADVANTAGE - The additive improves heat utilization rate of fuel, solves defect that oxygen-containing fuel including dimethyl ether fuel gas and methyl alcohol fuel has low heat value. It produces oxygen-containing fuel that is better than petroleum liquefied gas and totally replaces traditional fuel including petroleum liquefied gas and diesel oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of nano rare-earth additive by preparing compounds of nano rare-earth elements or their salts into raw material of nano rare-earth additive according to proportion; and processing raw material to solution with mass concentration of 5-30% using water or low carbon alcohol as solvent.
NOVELTY - An organic semiconductor visible light photochemical catalyst with membrane-shaped structure consists of layer (I) comprising 10-30 nm thick perylene amide biomembrane layer, layer (II) comprising 24-45 nm thick mixed membrane layer of perylene amide derivative and (6,6)-phenyl-61C methyl butyrate in the mol ratio of 4:1-11.6:1, and layer (III) comprising 3-15 nm thick (6,6)-phenyl-61C methyl butyrate membrane layer. The photochemical catalyst can be initiated in visible light region, in the presence of electric field, and decomposes water to produce hydrogen and oxygen.    USE - Organic semiconductor visible light photochemical catalyst used for decomposing water into hydrogen and oxygen (claimed).    ADVANTAGE - The organic semiconductor visible light photochemical catalyst produces clean hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of the photochemical catalyst, which involves placing two quartz containers containing the perylene amide derivative and (6,6)-phenyl-61C methyl butyrate into two crucibles of an vacuum evaporation instrument, placing indium tin oxide conductive glass in the hollow cavity of the vacuum evaporation instrument, vacuumizing until 1x 10-5-4x 10-5, regulating the current for heating up the crucible containing the perylene amide derivative to be 1.5-1.8A, evaporating the derivative on the conductive glass to form the layer (I), consequently, regulating the current for heating up the crucible containing the perylene amide derivative to be 1.5-1.8A for evaporating the perylene amide derivative, at the same time, regulating the current for heating up the crucible containing (6,6)-phenyl-61C methyl butyrate to be 1.3-1.6A, at the same time, evaporating onto layer (I) to form layer (II), consequently, regulating the current for heating the crucible containing (6,6)-phenyl-61C methyl butyrate on and evaporating the (6,6)-phenyl-61C methyl butyrate on layer (II) to form layer (III).
NOVELTY - A pre-treatment apparatus has a dipping tank which removes soluble material from biomass, a supplier which mixes the biomass without the soluble material, water, acid, alkali, and ionic liquid, a reactor, a saccharifying reactor, and a rotary explosive valve which maintains the pressure inside the reactor.    USE - Pre-treatment apparatus is used for preparing biofuel and bio-chemicals (both claimed).    ADVANTAGE - The pre-treatment apparatus effectively manufactures biofuel and bio-chemicals with reduced generation of wastewater.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of biofuel; and    (2) manufacture of bio-chemicals.
NOVELTY - Method for preparing pore-type structure, involves preparing aqueous acid solution containing dual template, structure-directing agent and monodispersible polymeric particle, allowing the particle to assemble, and reacting the obtained product with silica precursor in aerosol reactor.    USE - The method is useful for preparing pore-type structure used for preparing enzyme immobilized catalyst for producing biodiesel (all claimed).    ADVANTAGE - The enzyme immobilized catalyst is stable for prolonged period of time and increases yield of biodiesel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) pore-type structure obtained by the above-cited method; and    (2) enzyme immobilization catalyst obtained by immersing the structure into enzyme.
NOVELTY - Stabilizing and transferring fungal biomass involves culturing Trametes versicolor on a Petri dish for 7 days. Filtrate is added slowly with the cultured Trametes versicolor for 28 days at 280 degrees C at 180 revolutions per minute in a shaker in a liquid medium containing potato broth, glucose and water. The obtained materials are cultured on 10 Petri dishes for 28 days at 280 degrees C at 180 revolutions per minute in a shaker. 25mlof sterilized culture solution is added to the Petri dishes after every 7 days.    USE - Method for stabilizing and transferring fungal biomass by slow filtration.    ADVANTAGE - The method enables to stabilize and transfer fungal biomass by degrading toxic chemical.
NOVELTY - Use of microfibrous cellulose (MFC) as a suspension aid in polymer suspensions that are useful for many applications including cementitious mixtures, liquid laundry detergents and agricultural chemical concentrates, is claimed.    USE - The MFC is useful as a suspension aid in polymer suspensions that are useful for many applications including cementitious mixtures, liquid laundry detergents and agricultural chemical concentrates.    ADVANTAGE - The MFC is insoluble, much less sensitive to compatibility issues such as high ionic strength, high surfactant levels or low water activity. The MFC can be used in its wet-cake form and when properly incorporated and used at proper levels in the carrier fluid for liquid formulation, the MFC creates a 3-dimensional network that provides suspension of gum particles. The MFC will function in most water-miscible solvents, even with little or no water present, and provide a true yield stress that can provide good suspension of solids such as dispersed polymers.
NOVELTY - A high concentration biogas and oil manufacturing method involves introducing organic waste into a cylindrical rotary drum (80) supported by a support stand (10), where the drum is vertically mounted on a floor at intervals by rotating a motor, and a rotary shaft (100) is horizontally installed on both sides of the lateral center axis of the rotating drum. The organic waste in the drum is biodegraded using biodegradable materials.    USE - Method for manufacturing high concentration biogas and oil.    ADVANTAGE - The method enables manufacturing high concentration biogas and oil in a simple, rapid, economical and eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view illustrating a method for manufacturing high concentration biogas and oil. '(Drawing includes non-English language text)'    Support stand (10)    Motor gear box (20)    Motor bearing (30)    Motor belt (40)    Cylindrical rotary drum (80)    Rotary shaft (100)
NOVELTY - Isolating biomass, preferably algal biomass from an aqueous medium comprising cellular material, preferably algae, comprises: providing the aqueous medium comprising the cellular material; subjecting the cellular material to lysis, thus forming a first fraction comprising liquids and a second fraction comprising solid material, where the fractions are dispersed in the aqueous medium; and separating at least part of the liquid fraction and solid fraction from the aqueous medium, where the subjecting and separating steps are performed in a single apparatus (1).    USE - The method is useful for: isolating biomass (algal biomass) from the aqueous medium, which is useful for the preparation of medicines and/or biofuel (all claimed); and lysing other cellular (organic) material e.g. orange peels, palm oil hulls and yeast.    ADVANTAGE - The method: utilizes less energy, less processing steps, apparatus which is energy efficient and/or has high selectivity, thus isolates the algal biomass with high sensitivity; and does not require preprocessing of the harvested stream.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) apparatus for isolating cell content from cellular material comprised in the aqueous medium, comprising a centrifugal separator (2), a lysis device (10) arranged upstream of the centrifugal separator in an aqueous medium supply stream for lysing the cellular material;    (2) the lysis device for use in the apparatus;    (3) algal biomass obtainable by the method; and    (4) use of a rotational separator in the processing of an algae containing slurry.    DESCRIPTION OF DRAWING(S) - The figure shows cross sectional view of the apparatus.    Apparatus (1)    Centrifugal separator (2)    Inner element (3)    Outer element (4)    Lysis device (10)
NOVELTY - Component composition of reformed gas obtained by thermally decomposing carbonaceous complex waste and modifying, is analyzed with time interval of t1, and emitted heat amount (Qt1) is computed at instant. The average emitted amount (Qt2) at time interval of t2 which is more than t1, is computed at instant based on emitted heat amount (Qt1). The operating condition of reforming furnace is changed based on variation of emitted heat amount.    USE - Control method of emitted heat amount of gas discharged during thermal decomposition of carbonaceous waste material e.g. municipal solid waste, woody biomass including construction waste material, coppiced timber, and wood land surplus material, waste plastics, waste tire, sewage sludge, etc.    ADVANTAGE - The emitted heat amount of reformed gas is stably controlled.    DETAILED DESCRIPTION - Component composition of reformed gas obtained by thermally decomposing carbonaceous complex waste and modifying, is analyzed with time interval of t1, and emitted heat amount (Qt1) is computed at instant. The average emitted amount (Qt2) at time interval of t2 which is more than t1, is computed at instant based on emitted heat amount (Qt1). The operating condition of reforming furnace is changed based on variation of emitted heat amount from relation: Modulus of ( Delta Qt12) greater than or equal to Qt2x (a/100), where a is 1-3 and Delta Qt12 is difference of Qt1 and Qt2.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating control method of emitted heat amount. (Drawing includes non-English language text)
NOVELTY - A fuel cell system (100) consists of a desulfurizer (2), a hydrogen generator (3), a fuel cell (4), a gas supply device (9), and a controller (50). The desulfurizer carries out adsorption-desulfurization of source gas. The hydrogen generator produces hydrogen-containing gas by reforming the raw material. The fuel cell produces electric power using the hydrogen-containing gas. The gas supply device supplies a gas for desorption which disconnects a preset adsorbate from desulfurizer. The controller operates the gas supply device before removal of desulfurizer.    USE - Fuel cell system is used in cogeneration systems.    ADVANTAGE - The fuel cell system suppresses exchange of desulfurizer and odor from desulfurizer.    DETAILED DESCRIPTION - A fuel cell system consists of a desulfurizer, a hydrogen generator, a fuel cell, a gas supply device, and a controller. The desulfurizer carries out adsorption-desulfurization of sulfur compound contained in a source gas. The hydrogen generator has a modifier which produces hydrogen-containing gas by reforming reaction using the raw material after passing through the desulfurizer. The fuel cell produces electric power using the hydrogen-containing gas. The gas supply device supplies a gas for desorption which disconnects a preset adsorbate from the desulfurizer among the substances adsorbed by the desulfurizer. The controller operates the gas supply device before removal of desulfurizer. An INDEPENDENT CLAIM is included for operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel cell system, and adsorbate desorption process of desulfurizer.    Desulfurizer (2)    Hydrogen generator (3)    Fuel cell (4)    Gas supply device (9)    Controller (50)    Fuel cell system (100)
NOVELTY - The furnace has a purifier barrel (4) whose outlet is connected with a suction port (501) of a purification cylinder (5) via a gas pipeline. A wet purifier (2) of an upper part of a barrel body is arranged on a side surface with an overflow port. The wet purifier is provided with a sewage port. A top part of the wet purifier is provided with a water inlet. A suction opening (201) of the gas pipeline is extended into a cavity water deep position. A suction inlet of an air supplying device (3) i.e. air pump, liquid pump, or fan is connected with a purification cylinder (401) by the gas pipeline.    USE - Straw gasification furnace.    ADVANTAGE - The furnace avoids combustible gas in the hearth of the material to escape from the inlet. The furnace ensures energy consumption and prevents environment pollution, and has high stove gas work efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a straw gasification furnace.    Wet purifier (2)    Air supplying device (3)    Purifier barrel (4)    Purification cylinder (5)    Suction opening (201)    Purification cylinder (401)    Suction port (501)
NOVELTY - The invention relates to a process for treating the mud resulting from waste water purification by anaerobic fermentation with a selective culture medium consisting of a main medium comprising 0.75 g of KH2PO4, 1.45 g of K2HPO4 x 3 H2O, 0.9 g of HN4Cl, 0.2 g of MgCl2 x H2O, 0.5 g of Na2S x 9 H2O, 1 ml of 0.2% resazurine, 1 g of agar, 1000 ml of distilled water, said medium being enriched in a ratio of 1.5...2%, as compared with the main medium, with a solution of 0.1 mol/l tetrahydrated nickel acetate and then the so enriched medium is seeded with decimal dilutions of fermented mud and the samples are incubated under mesophilic conditions, an increase by 17.2% in the activity of methane-generating microorganisms involved in biogas preparation being registered upon determination by the statistic method, in comparison with the initial sample.
NOVELTY - The invention relates to a non-destructive method and to a device for determining a new property of the briquettes made of lignocellulosic materials, namely the compaction coefficient Kc. According to the invention, the method consists of the following succession of operations: there are taken over at least eight briquettes immediately after coming out of the press and are brought to the humidity of the wood chips, the briquettes being numbered by applying some dots with figures 1, 2...n, each briquette is weighed thereby determining the mass mb where b=1,2...n, each briquette is introduced into the device for determining the compaction coefficient Kc and the height h1 of each briquette is measured, the device is successively loaded with the amount of chips corresponding to the mass of each briquette, the device being placed on vibratory table and the chips are arranged inside the cylinder determining the height of each amount of chips h2, the compaction coefficient of each briquette is calculated by the relation Kc= mb/ma x h2/h1, the relation being simplified to Kc=h2/h1 if the mass of the chips ma is equal to the mass mb of the briquette and finally the arithmetic average of these values is calculated and an average compaction coefficient Kmc is obtained. The device claimed by the invention consists of a cylinder (7) positioned on a support base (9) provided with an orifice (10) closed by a lower cover (11), the upper side of the cylinder (7) is closed by a threaded cover (3) wherethrough there penetrates the rod (1) guided by a spring (2), the rod (1) being provided at the lower end with a plateau (4) for determining the height h2 of the chips whose value is read on a graded dial (5) of the cylinder (7).
NOVELTY - The furnace has a base (1) provided with an ash box (2), where a furnace body (3) is arranged on the base. The furnace body is provided with a hearth (5). A feeding port (4) is arranged at a side of the furnace body. A combustion chamber (6) is arranged on the hearth. A burner (7) is arranged at top of the furnace body. A side of the burner is equipped with a hearth clapboard that is provided with a stove chamber (9). An upper side of the stove chamber is provided with a table surface (10). A side of the stove chamber is connected with a flue pipe (11) that is connected to a smoke pipe (12).    USE - Low-emission biomass semi-gasification furnace.    ADVANTAGE - The furnace improves heat efficiency and reduces discharge of smoke dust.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a low-emission biomass semi-gasification furnace.    Base (1)    Ash box (2)    Furnace body (3)    Feeding port (4)    Hearth (5)    Combustion chamber (6)    Burner (7)    Stove chamber (9)    Table surface (10)    Flue pipe (11)    Smoke pipe (12)
NOVELTY - A manufacturing apparatus of mixed biomass fuel (S1) comprises main fuel pipe (L1, L1') equipped with diameter reducing part (103), throat part (104) where main fuel fluid passes through, and enlarged diameter part (105), mixing acceleration part (100) which accelerates mixing of waste edible oil supplied to throat part from waste edible oil pipe (L2, L2'), and vertical eddy generation part (200) which makes composite fuel fluid produce a vertical eddy.    USE - A manufacturing apparatus of mixed biomass fuel for agricultural heating machine and agricultural boiler.    ADVANTAGE - High quality mixed biomass fuel is manufactured efficiently and at a low cost without passing through a complicated process, combustion efficiency is improved, malfunction of combustion defect and soot production are eliminated, and recovery and reuse of waste edible oil is promoted.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) manufacturing method of mixed biomass fuel which involves performing accelerated mixing of waste edible oil, producing primary composite fuel fluid, expanding primary composite fuel fluid within the enlarged diameter part (105), producing vertical eddy, and obtaining secondary composite fuel fluid; and    (2) agricultural combustion apparatus comprising nozzle part (405) which ejects mixed biomass fuel and mixing acceleration part (100) which makes an airflow in a rotational flow sheet and an airflow discharged by nozzle part simultaneously produce a vertical eddy.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the manufacturing apparatus of mixed biomass fuel. (Drawing includes non-English language text).    Mixing acceleration part (100)    Vertical eddy generation part (200)    Main fuel pipe (L1, L1')    Waste edible oil pipe (L2, L2')    Manufacturing apparatus of a mixed biomass fuel (S1)
NOVELTY - Producing carbon dioxide, comprises: feeding an enriched oxygen air gas stream and a carbon rich fuel gas stream to an auto-thermal reformation/partial oxidation process, where the enriched oxygen air gas stream is a waste gas stream from an air separation unit; recovering the synthesis gas formed by the auto-thermal reformation process and feeding the synthesis gas to a shift reactor to produce hydrogen and carbon dioxide; and feeding the hydrogen and carbon dioxide to a carbon dioxide removal unit to recover carbon dioxide.    USE - The method is useful for the production of carbon dioxide. The carbon dioxide and the nitrogen are used in enhanced oil recovery process. The hydrogen is fed to a combined cycle power plant as fuel, where the power plant is a gas turbine generator and heat recovery steam generator (all claimed).    ADVANTAGE - The method: maximizes the amount of carbon dioxide and nitrogen; provides the carbon dioxide with minimal changes to the existing plant and decreased carbon dioxide emissions; and utilizes the oxygen waste stream from an air separation unit.
NOVELTY - The furnace has a bracket (2) fixed on a furnace shell (1) that is provided with a furnace outer wall (3) and a furnace inner wall. The furnace outer wall is formed at an outer side of the furnace inner wall that is formed with a heating gasification layer. A furnace layer (4) is formed between the furnace outer and inner walls. Bottoms of the furnace inner wall and the furnace outer wall form a combustion heating section. The furnace outer wall is equipped with a stirring device, steam inlet and a rich oxygen air inlet (14). The furnace outer wall is provided with an insulating layer (15).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace prevents a mass of gasification volatile from being burnt, and improves the final generated gas yield and gasification efficiency. The furnace allows the steam from the steam inlet to react with the residual carbon to generate combustible gas, avoids biomass waste of energy and increases production of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Furnace shell (1)    Bracket (2)    Furnace outer wall (3)    Furnace layer (4)    Rich oxygen air inlet (14)    Insulating layer (15)
NOVELTY - The electrode (10) has a solid metallic substrate (101) that is provided with primary coating (102) of metal nanoparticles and secondary nanoparticle coating (103). The primary coating is configured to promote adhesion of other coating by creating a direct metal-to-metal bond between the nanoparticles of coatings.    USE - Electrode for electrolyzer and fuel cell device (all claimed) used in electrochemical and catalytic application.    ADVANTAGE - The secondary layer can act as the most active layer of the electrode so as to increase the rate of electrochemical reaction, so that the efficiency of the electrode for generating energy can be improved at low cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) electrolyzer;    (2) fuel cell; and    (3) method of preparing nanoparticle coated electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the layers formed on the surface of the solid metallic substrate.    High-surface area electrode (10)    Solid metallic substrate (101)    Primary coating (102)    Secondary nanoparticle coating (103)
NOVELTY - Method for devulcanizing rubber by microbial or enzymatic process, involves providing a particulate vulcanized rubber compound, swelling the particulate vulcanized rubber compound in a solvent, and introducing microorganism or enzyme into the solvent containing the particulate vulcanized rubber compound to devulcanize the compound.    USE - The method is useful for devulcanizing rubber for producing a product useful in tire manufacturing industries (al claimed).    ADVANTAGE - The method is safe as the method involves biologic agents for devulcanization, simple, effective, and inexpensive, exposes all portions of the ground rubber particles to bio-agent, utilizes specific bio-agent, enables to use larger ground rubber particles, ensures compatible rate of degradation of sulfur-sulfur (S-S) and sulfur-carbon (S-C) bonds in terms of commercialism, and degrades all the essential S-S and S-C bonds, thus the method produces rubber composition that can be easily combined in large quantities with fresh rubber compounds with uniform dispersion without any significant loss in product performance. The devulcanized product is capable of replacing 1-40% of fresh rubber compounds in tire manufacturing process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for product which is produced by performing the above-cited method.
NOVELTY - A hydrogen separation alloy has metal structure having hydrogen-permeable phase containing niobium and hydrogen-embrittlement resistant phase which is transition metal phase. The hydrogen-permeable phase and hydrogen-embrittlement resistant phase have dilated structure formed from rolling. The ratio of hydrogen-permeable phase in 10x 10 mu m region in 50x 50 mu m observation plane by an electron microscope of cross-section in a direction which is the direction of thickness thinned by rolling, is 35-70%.    USE - Hydrogen separation alloy is used for manufacturing highly-pure hydrogen for fuel cell.    ADVANTAGE - The hydrogen separation alloy has excellent hydrogen brittleness resistance and hydrogen-permeation performance, and can be applied to large surface area products on the side where hydrogen passes through. The hydrogen separation alloy is manufactured economically.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of hydrogen separation alloy.
NOVELTY - The apparatus (1) has an inner tube (13) is provided with internal peripheral surface and outer peripheral surface such that the helical convex unit and recessed unit is closely united. The internal peripheral surface is provided with convex unit whose upper surface is contacted with the outer peripheral surface. The outer peripheral surface is provided with convex unit whose upper surface is contacted with the internal peripheral surface.    USE - Apparatus for generating hydrogen used in fuel cell system such as domestic-use cogeneration system.    ADVANTAGE - The reformation water in the hydrogen generating apparatus can be heated so as to evaporate water at constant speed. The flow volume and temperature of water vapor are generated so that the supply of hydrogen from the apparatus can be obtained stably.    DESCRIPTION OF DRAWING(S) - The drawing shows the cross-sectional view of the hydrogen generation apparatus.    Hydrogen generating apparatus (1)    Modifier (2)    Transformer (3)    Inner cylinder (11)    Inside tube (13)
NOVELTY - The method involves containing methane and carbon dioxide in the gas (200). The gas is processed by a spirally constructed coil pump (20) together with a liquid (65) by alternating dosing in such a manner. The coil pump is alternately supplied with liquid and gas that leave the coil pump after a building up of pressure and are conducted to a gas separator (30) from which the gas is conducted as required to a liquid scrubber (40) for a continued purification before the gas is transported to a usage site.    USE - Method for purifying gas or biogas for vehicle.    ADVANTAGE - The biogas can be upgraded so the vehicle quality or natural-gas quality can be improved. The carbon dioxide content is separated off or reduced to raise the energy content of the biogas during upgrading. The occurrence of hydrogen sulphide and other by-products are normally reduced in the gas. The purification process can be performed efficiently and the manufacturing cost for the motor fuel can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for arrangement for purification of gas or biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating purification process.    Coil pump (20)    Gas separator (30)    Liquid scrubber (40)    Liquid (65)    Gas (200)
NOVELTY - The apparatus has a hydrogen-producing unit (10) that generates hydrogen by electrolysis reaction and self-reaction of an electrode (11). A fuel cell (20) generates electric power by supplying generated hydrogen. A voltage application circuit (30) applies a voltage to hydrogen-producing unit directly or indirectly using electric power from the fuel cell. An output unit (40) outputs the excessive electric power generated by fuel cell. The electric power of initial stage supplied to hydrogen-producing unit is large than electric power in steady state.    USE - Electric-power generating apparatus.    ADVANTAGE - The electric-power generating apparatus can be enabled to supply the generated hydrogen to the fuel cell, and to output the surplus electric power from the outside.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of the electric-power generating apparatus.    Hydrogen-producing unit (10)    Electrode (11)    Fuel cell (20)    Voltage application unit (30)    Output unit (40)
NOVELTY - Degrading sludge from pulp and/or paper manufacturing, comprises: applying (i) at least one enzyme having cellulase activity, and (ii) at least one non-ionic surfactant that is a difunctional block copolymer having an hydrophilic lipophilic balance (HLB) value of at least 7, or a composition comprising (i) and (ii) to the sludge; and de-watering the sludge.    USE - The method is useful for degrading sludge from pulp and/or paper manufacturing, forming sugar which in turn is fermented to form ethanol (all claimed).    ADVANTAGE - The method: utilizes the enzyme and the non-ionic surfactant, or the composition, thus results in higher sludge solid reduction (10 wt.% greater than the method using the enzyme alone); and reduces the amount of the sludge that needs to be disposed to a landfill, thus provides cost savings and an environmentally friendly solution to the company or person in possession of the sludge.
NOVELTY - Fuel blend, comprises hydrocarbon-containing fuel component and ethyl acetate.    USE - The fuel blend is useful in: road diesel motor transport vehicles; private or commercial diesel passenger vehicles; marine diesel engines; diesel-electric train engines; diesel powered construction equipment; portable or stationary diesel powered electric generators; a marine application including jet skis, outboard motors or inboard motors; recreational application including snowmobiles, mopeds or motorcycles; and residential application including lawnmowers, string trimmers or chain saws (all claimed).    ADVANTAGE - The fuel blend utilizes ethyl acetate, which when added to mixtures of diesel fuel and biodiesel, or biodiesel and mixtures of biodiesel, reduces the cloud point and improves winter operation and performance of the fuel blend, and adjusts the viscosity of the fuel blend.
NOVELTY - The hopper has a feeding port located on top of a storage bin main body. Bottom part of the storage bin main body is provided with a discharging port. The storage bin main body comprises an upper cylinder body and a lower cone part. The storage bin main body is provided with multiple rotating shafts. Each rotating shaft is provided with multiple helical blades. A main body of a storage hopper is fixed in the rotating shafts. Friction angle of a wall with inclined angle of a lower cone is about 14 to 16 degrees.    USE - Biomass hopper for a biomass gasification reaction system (claimed).    ADVANTAGE - The system balances damage force caused by external disturbances, and prevents stacking of angle material when the material is in an arch portion. The system enlarges a biomass gasification furnace by utilizing a raw material bin.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification reaction system comprising a fluidized bed gasification reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass gasification reaction system.
NOVELTY - The boiler has a boiler main body (2) placed in a furnace wall. A furnace part is provided with a feeding port and an air-adjusting door. Semi gasification combustion is performed from an upper level to a lower level by utilizing a reverse burning method.    USE - Biomass semi-gasification combustion boiler.    ADVANTAGE - The boiler performs semi-gasification combustion by utilizing a straw, sawdust, dry cow manure, biomass waste in agricultural, forest and a pasturing area as fuel, so that the boiler has high utilization rate, prolonged service life and high working efficiency. The boiler saves energy and prevents environment from being polluted, and is convenient to operate.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass semi-gasification combustion boiler.    Boiler main body (2)    Biomass fuel (7)    Lower ash lighting door (10)
NOVELTY - Micro-emulsified methanol diesel oil, comprises (in %): diesel oil (50-70), methanol (10-25), ethyl acetate (4.9-6), isobutyl alcohol (2.7-9.4), oleic acid (6.8-8.6) and soybean oil (1-5.6).    USE - Micro-emulsified methanol diesel oil.    ADVANTAGE - The methanol diesel oil satisfies commercial diesel oil national standard, is inexpensive, can be prepared simply, generates no pollution, and has wide and commercial application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the above-mentioned methanol diesel oil, which involves mixing methanol with diesel oil at normal temperature and pressure, adding alcohol, ethyl acetate, oleic acid and soybean oil to the mixture sequentially, stirring the obtained mixture uniformly and emulsifying the obtained mixture.
NOVELTY - The heated medium cable has a hose line (1) for medium transport and a resistance heating wire (2) for heating the medium, where the resistance heating wire is connected at an electrical power source. The resistance heating wire is partially arranged in inner hollow space of the hose line.    USE - Heated medium cable, particularly for process medium of a fuel cell system (Claimed).    ADVANTAGE - The heated medium cable has a hose line for medium transport and a resistance heating wire for heating the medium, where the resistance heating wire is connected at an electrical power source, and thus ensures simple and cost-effective design of the heated medium cable.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a heated medium cable.    Hose line (1)    Resistance heating wire (2)    Coupling (3)    Straps (10,10')    Strap leg (12)
NOVELTY - Biocidal composition comprises silver, at least one pyrithione, and at least one l,2-benzisothiazolin-3-one derivatives as microbicidal active components.    USE - The biocidal composition is useful: for container preservation of coating materials, preferably paints, varnishes, plasters, polymer dispersions, emulsions, latices and adhesives; and in preserved product comprising paints, lacquers, glazes, plasters, latices, polymer dispersions, adhesives, cleaning agents, lignosulfonates, chalk slurries, minerals slurries, ceramic masses, sealants, casein-containing products, starch products, bitumen emulsions, surfactant solutions, fuels, cleaning agents, pigment pastes and pigment dispersions, inks, lithographic liquids, thickeners, cosmetic products, toiletries, water circulation system, liquids in paper processing, liquids in leather production, liquids in textile production, drilling oils, cutting oils, hydraulic fluids or coolants (all claimed).    ADVANTAGE - The biocidal composition: used in a lower concentration, exhibits a synergistic effect for controlling microorganisms, thus it reduces the cost and effort for controlling harmful/unwanted organisms; is in the form of a liquid preparation, which can be easily adjusted to avoid discoloration or graying of the products comprising biocidal composition during its application; exhibits long-term stability and long-term efficiency and improved light-insensitive property, which protects the composition from light radiation; and comprises emission free biocides for preserving container of coating material.
NOVELTY - Producing lipids for biofuel or lubricant comprises cultivating bacterial cells of the genus Streptomyces in a medium comprising organic waste(s) or residue(s) or their mixtures as carbon and/or nutrient source(s); and recovering the lipids from the cells or from the culture medium.    USE - The method and Streptomyces culture are used for producing lipids for biofuel or lubricant. The lipids or lipid composition or a fraction of the lipids or lipid composition is used as biofuel and/or lubricant, or as a starting material for biofuel and/or lubricant production. The lipids or lipid composition or a fraction of the lipids or lipid composition is used for the production of biodiesel or renewable diesel (all claimed).    ADVANTAGE - The present invention provides new cost-effective processes and new microorganisms for lipid production for biofuel production.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are: (1) a Streptomyces culture for lipid production, which comprises (a) a population of bacteria of the genus Streptomyces; and (b) a culture medium comprising organic waste(s) or residue(s) or their mixtures as carbon and/or nutrient source(s); (2) a Streptomyces host genetically modified to express an endogenous or exogenous gene encoding diacylglycerol acyltransferase (DGAT) activity (EC 2.3.1.20) and/or 3-ketoacyl-acyl carrier protein synthase III (FabH) (EC: 2.3.1.41 ), or a nucleotide sequence causing the same or an equivalent function as gene products ID 101096381 or ID 101101330 have; (3) a lipid composition produced according to the method above; (4) biofuel which comprises the lipids or lipid composition or a fraction of lipids or lipid composition, and optionally suitable additives for biofuel use; and (5) lubricant which comprises the lipids or lipid composition, or a fraction of lipids or lipid composition, and optionally suitable additives for lubricant use.
NOVELTY - The fuel cell has bipolar plates (1) or a stack of bipolar plates provided with lateral cooling fins (2) in which cooling passages (9) are arranged in an s-shaped structure. A seal is arranged between the bipolar plates. The cooling passages, the cooling fins and/or the seal exhibit a stability-increasing design adapted to heat distribution within the bipolar plates and/or within the stack. A flat seal is provided on the bipolar plates with seal tongues laterally projected from the plates. A diaphragm is arranged in a flow direction of a cooling flow before and/or after the stack.    USE - Fuel cell for producing electricity by chemical reaction of reaction media e.g. liquid media and gaseous media such as hydrogen and methanol.    ADVANTAGE - The cooling passages, the cooling fins and/or the seal exhibit the stability-increasing design adapted to heat distribution within the bipolar plates and/or within the stack of bipolar plates, thus improving cooling of the fuel cell stack with optimal temperature distribution and stability of the cooling fins, and hence increasing service life of the fuel cell. The cooling passages are arranged in the cooling fins in the s-structure, thus increasing stability of the bipolar plates with respect to vibrations while reducing susceptibility to damage of the bipolar plates with respect to vibrations.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a bipolar plate with s-shaped cooling passages.    Bipolar plates (1)    Lateral cooling fins (2)    Cooling passages (9)
NOVELTY - The method involves subjecting animal fat to trans-esterification and melting processes. The animal fat is broken into smaller pieces and mixed with primary aliphatic alcohol and carbon atoms. Strong inorganic acid is added to the smaller pieces and heated to temperature of about 50 to 95 degree Celsius. Residues in the aliphatic alcohol are subjected to a distillation process. The aliphatic alcohol is subjected to neutral reaction. An aqueous extract is utilized to separate glycerol. An organic phase is obtained after drying a biofuel.    USE - Method for producing an animal fat based biofuel.
NOVELTY - The fuel contains 20 to 80 percent of recycled or residual fabric, biomass, 20 percent of water content, combustible agents, binder and additives.    USE - Biomass fuel.
NOVELTY - The fuel contains compressed mixtures in a form of residue, 15 percent of water content, combustible ingredients and non-combustible additives.    USE - Sorghum sugar based fuel.
NOVELTY - A cellulose decomposition promoting agent contains polypeptide derived from microorganisms belonging to Rhizopus genus or Mucor genus.    USE - A cellulose decomposition promoting agent for manufacturing ethanol (claimed), processing waste materials and foodstuffs and modifying cellulose fiber.    ADVANTAGE - A cellulose material is efficiently processed, and an increase in cellulose decomposing activity due to synergistic effect between polypeptide contained in the cellulose decomposition promoting agent and cellulase is observed.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a manufacturing method of the cellulose decomposition promoting agent which involves culturing Rhizopus or Mucor microorganisms which produce polypeptide exhibiting cellulose decomposing activity and recovering polypeptide from culture product;    (2) a cellulose decomposition method which involves processing a cellulose material in the presence of the cellulose decomposition promoting agent and cellulase; and    (3) a manufacturing method of ethanol which involves using sugar produced by cellulose decomposition method to produce ethanol.
NOVELTY - Biomass pyrolysis gas purification system comprises a pyrolysis furnace (1) arranged inside retorting kettle (2) provided with a two-stage heat exchanger (4). One end of a first-stage heat exchanger is connected with a high level voltage electrostatic detarrer. The system further comprises a water sealing device (3) with secondary high voltage electrostatic detarrer. One end of water sealer is connected with retorting kettle, and other end with two-stage heat exchanger. One end of high level voltage electrostatic detarrer is connected with secondary high level voltage electrostatic detarrer.    USE - Used as a biomass pyrolysis gas purification system.    ADVANTAGE - The system has good delignification effect; is simple in structure and consumes less energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass pyrolysis gas purification system.    Pyrolysis furnace (1)    Retorting kettle (2)    Water sealing device (3)    Two-stage heat exchanger (4)    Secondary heat exchanger (5)
NOVELTY - A desulfurizing agent consists of sponge nickel having a BET specific surface area of 65-200 m2/g and a volume average particle diameter of 80-300 mu m as measured by laser diffraction scattering method.    USE - Desulfurizing agent is used for removing sulfur compound from hydrocarbon containing sulfur compound, and/or oxygen-containing organic compound (claimed) in liquefied petroleum gas, lamp oil, gasoline, or light oil used in distribution type fuel cells e.g. polymer electrolyte fuel cell used in household applications, small-scale business applications, and motor vehicles.    ADVANTAGE - The desulfurizing agent has excellent desulfurization performance and durability, and efficiently removes even trace amount of sulfur compound, at normal pressure and temperature. The desulfurizing agent can be manufactured by a simple and economical method. Since a pressure-resistant container is not required, a desulfurization apparatus can be made compact. Since desulfurization performance is maintained over a long period of time, exchange of desulfurization unit and regeneration of desulfurization agent are reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for desulfurization method.
NOVELTY - Crab compost is composed of organic compounds of waste crab. Fermentation of organic matter is done quickly in some days to make it biocompatible. Crab compost has lots of nutrients like as cattle dung, where the compost contains calcium and magnesium. The compost has equivalent percentage of organic matters, where calcium content is higher than found in cow manure (more than 20 times of their chemical composition and structure).    USE - Crab compost used as compost or organic fertilizer for agricultural purpose (claimed).    ADVANTAGE - The crab compost has high nutritional value and produced basic fertilizer.
NOVELTY - Compound comprising a polyamidoamine (PAMAM) dendrimer (I) having many terminal amino groups bonded with porphyrins, porphyrin like compounds or their derivatives, is new.    USE - (I) is useful for the treatment of HIV infection (claimed). No biological data given.    ADVANTAGE - (I) is eco-friendly, due to having non-immunogenic, water soluble, biocompatible and biodegradable properties. (I) is very effective in controlling the release of a variety of chemical or medicinal compounds to the targeted site. (I) has high potential of commercialization due to its lower cost of controlled-release systems compared to traditional pharmaceutical formulations and facile manufacturing route.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the preparation of (I).
NOVELTY - The system has a fuel cell system producing electric power by supplying hydrogen, where a combustion part burns the hydrogen. A restoration part restores oxide of a negative electrode metal of an air cell (17) with the hydrogen. Electric power supplied by discharge of the air cell is required at time of starting/stopping of the fuel cell system. A supply tank supplies the hydrogen to a fuel cell stack (3). The air cell is charged by restoring oxide of the negative electrode metal.    USE - Hybrid power source system.    ADVANTAGE - The restoration part restores oxide of the negative electrode metal of the air cell with the hydrogen, and the electric power is required at time of starting/stopping the fuel cell system supplied by discharge of the air cell, so that the hybrid power source system can start and stop the fuel cell system reliably in any environments.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a hybrid power supply operating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a hybrid power source system.'(Drawing includes non-English language text)'    Housing (1)    Hydrogen cylinder (2)    Fuel cell stack (3)    Pure water pump (7)    Air cell (17)
NOVELTY - Preparing biomass coal includes crushing the raw coal and biomass and sieving; mixing and heating; pressurizing and molding the mixture of the raw coal and biomass; and cooling the molded coal and de-molding to obtain the biomass product containing lignin.    USE - Method for preparing biomass coal (claimed).    ADVANTAGE - The method can produce high-strength biomass compound coal without adhesive.    DETAILED DESCRIPTION - Preparing biomass coal comprises: (a) crushing the raw coal and biomass and sieving; mixing and heating by (b1) mixing the raw coal and biomass uniformly to obtain the mixture; (c1) heating the mixture to a predetermined temperature and selectively maintaining for a predetermined time; or by (b2) heating the raw coal to the first temperature and heating the biomass to the second temperature; (c2) uniformly mixing the heated raw coal and biomass in step (b2) to obtain the mixture of the raw coal and biomass and maintaining the mixture for predetermined time selectively; (d) pressurizing and molding the mixture of the raw coal and biomass obtained in step (c1) or (c2); and (e) cooling the molded coal and de-molding to obtain the biomass product containing lignin; where the predetermined temperature is the temperature for softening or liquefying the biomass; the first temperature is lower than the second temperature; and the second temperature is greater than the predetermined temperature.
NOVELTY - A biomass molded coal comprises (pts.wt.) raw coal (50-90) and biomass (10-50). The raw coal is low metamorphic grade coal and/or middle metamorphic grade coal. The biomass is grass family plant, agricultural wastes, forestry biomass, aquatic plant, and/or energy plant.    USE - A biomass molded coal.    ADVANTAGE - The biomass molded coal does not add extract adhesive; has simple preparation, high strength, and good waterproof; and can satisfy the demand of long-distance transport and stored in open air.    DETAILED DESCRIPTION - A biomass molded coal comprises (pts.wt.) raw coal (50-90) and biomass (10-50). The raw coal is low metamorphic grade coal and/or middle metamorphic grade coal. The biomass is grass family plant, agricultural wastes, forestry biomass, aquatic plant, and/or energy plant. The biomass molded coal is made by breaking (pts.wt.) raw coal (50-90) and biomass (10-50), and screening the powder coal and biomass of predetermined granularity via a sieving device. The powder coal and biomass are raised to predetermined temperature, then a pressurizing molding die or a pressurizing molding machine is used for pressurizing and molding the powder coal and biomass under predetermined pressure, and then the molded coal is cooled and demolded, and the biomass molded coal product can be obtained.
NOVELTY - Producing biomass coal comprises crushing the raw coal and biomass and sieving; mixing and heating; pressurizing and molding the mixture of the raw coal and biomass; and cooling the molded coal and demolding to obtain the biomass product. The biomass contains lignin.    USE - Method for producing biomass coal (claimed).    ADVANTAGE - The method can produce high-strength biomass compound coal without using adhesive.    DETAILED DESCRIPTION - Producing biomass coal comprises: (a) crushing the raw coal and biomass and sieving; mixing and heating by (b1) mixing the raw coal and biomass uniformly to obtain the mixture; and (c1) heating the mixture from step (b1) to a predetermined temperature and selectively maintaining for a predetermined time; or (b2) heating the raw coal to the first temperature and heating the biomass to the second temperature; and (c2) uniformly mixing the heated raw coal and biomass from step (b2) to obtain the mixture of the raw coal and biomass and maintaining the mixture for the predetermined time selectively; (d) pressurizing and molding the mixture of the raw coal and biomass obtained in the step (c1) or (c2); and (d) cooling the molded coal and demolding to obtain the biomass product; the biomass contains the lignin. The predetermined temperature is the temperature for softening or liquefying the biomass. The first temperature is lower than the second temperature. The second temperature is greater than the predetermined temperature.
NOVELTY - Preparing biomass coal comprises crushing the raw coal and sieving; crushing biomass and sieving; uniformly mixing the sieved raw coal and biomass based on a predetermined ratio and uniformly mixing to obtain a mixture of the raw coal and biomass; heating the mixture to a predetermined temperature and selectively maintaining for a predetermined time; pressurizing and molding the mixture by a mold by a molding pressure; and cooling the molded coal and demolding to obtain the biomass coal product.    USE - Method for preparing biomass coal (claimed).    DETAILED DESCRIPTION - Preparing biomass coal comprises crushing the raw coal and sieving; crushing biomass and sieving; uniformly mixing the sieved raw coal and biomass based on a predetermined ratio and uniformly mixing to obtain a mixture of the raw coal and biomass; heating the mixture to a predetermined temperature and selectively maintaining for a predetermined time; pressurizing and molding the mixture by a mold by a molding pressure; and cooling the molded coal and demolding to obtain the biomass coal product. The biomass contains the lignin. The predetermined temperature is the temperature for softening or liquefying the biomass.
NOVELTY - A biomass molded coal comprises (pts.wt.) raw coal (50-90) and biomass (10-50). The molded coal is prepared by breaking raw coal and biomass. The powdered coal and biomass of predetermined granularity are screened, and the powdered coal and biomass are raised to predetermined temperature, and the temperature is kept for a predetermined time, pressurizing and molding the powdered coal and biomass under predetermined pressure, and the molded coal is cooled and de-molded to obtain the biomass molded coal without adhesive.    USE - A biomass molded coal.    ADVANTAGE - The biomass molded coal does not add binder and removes the steps of binder preparation, uniform mixing of binder and powdered coal, drying and curing biomass molded coal. The biomass molded coal has high intensity and good waterproof property, which can satisfy the demand of long-distance transport and storage in open air, and can save raw coal.
NOVELTY - A bio-briquette comprises 50-90 pts.wt. raw coal and 10-50 pts.wt. biomass. The biomass is grass, agricultural waste, forestry biomass, aquatic plant, and/or energy plant. The bio-briquette is prepared by crushing the raw coal and the biomass; sieving; increasing temperature of the powder coal and the biomass to predetermined temperature; keeping the temperature for the predetermined time; pressing the powder coal and the biomass by pressurizing mold or pressurizing machine; and cooling and de-molding the formed coal so as to obtain the non-adhesive bio-briquette product.    USE - Bio-briquette.    ADVANTAGE - The bio-briquette has simple structure without extra binding agent, high intensity and good waterproof capacity for satisfying the demand of long-distance transport and outdoor storage.
NOVELTY - Producing biomass coal comprises crushing the raw coal and sieving; crushing biomass and sieving; heating the sieved raw coal to a first temperature and the sieved biomass to a second temperature; uniformly mixing the heated raw coal and biomass based on a predetermined ratio and selectively maintaining for a predetermined time; pressurizing and molding the mixture by a mold by a molding pressure; and cooling and demolding to obtain the biomass coal product. The biomass contains lignin. The predetermined temperature is the temperature for softening or liquefying the biomass.    USE - Method for producing biomass coal.    ADVANTAGE - Additional adhesive is not added to the production of the biomass coal.    DESCRIPTION OF DRAWING(S) - The drawing is a flow diagram illustrating the method for producing biomass coal (Drawing includes non-English language text).
NOVELTY - A Pistia stratiotes biological coal has volatile (Vdaf) content of 50-65%, quantity of heat Q(net,ar) of 3500-5000 KJ/kg, ash content Ad of not greater than 10%, and whole water content Mt of not greater than 20%/M.    USE - Pistia stratiotes biological coal.    ADVANTAGE - The biological coal has high crude fiber content, good burning effect and less burned ash. The burned powder can be used as plant fertilizer without polluting the environment. The coal not only has standard production so that the process of using P. stratiotes as main raw material to prepare biological coal is controllable, but also fully utilizes the P. stratiotes. Problem that P. stratiotes pollute environment is solved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the P. stratiotes biological coal comprising (A) pressing and dewatering the P. stratiotes until the water content is 40-50%; dewatering straw until the water content is less than 20%; (B) crushing the dewatered P. stratiotes and straw by using a sieve with 50-155 meshes; (C) drying the mixed material at 80-120 degrees C; drying until the water content is 80-90%; (D) adding the crushed straw into the crushed P. stratiotes, where weight ratio of the added straw to the P. stratiotes is 3-5:7-5; uniformly stirring and forming as mixed material; (E) pressing the mixed material as biological coal under a pressure greater than 15 t, where the pressing volume ratio is 30:1.
NOVELTY - A biodiesel is prepared by using quaternary ammonium II type base ion exchange resin to catalyze plant oil and low carbon alcohol to process transesterification and performing separation reaction to obtain biodiesel.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method is environment-friendly; and has high reaction activity, fast reaction speed, and mild reaction condition. It does not cause saponification reaction and does not cause device corrosion. After-processing steps to the products are simple and convenient. The used catalyst can be used repeatedly to lower production cost.
NOVELTY - An organic fertilizer comprises (pts. wt.): wormcast (20-30), broken corn straw (25-35), rice chaff (25-35) and roseite (10-15).    USE - Organic fertilizer for preventing tomato continuous cropping obstacles (claimed).    ADVANTAGE - The fertilizer has improved content of organic material. It can modify soil, restrict pathogenic bacteria breeding, improve tomato yield and increase tomato quality. The tomato disease incidence is reduced at 80% as compared with not-used organic fertilizer. The tomato yield is improved at 20%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer which comprises providing above raw materials; completely mixing broken corn straw, rice chaff and roseite, watering so that the water content of compost is 50-60%, piling mixed material in greenhouse or plastic shed to form trapezoidal pile having narrow upper part and wide lower part, and aerobically fermenting at natural state or fermenting via fermenting fungus; and completely mixing completely fermented mixture of broken corn straw, rice chaff and roseite and wormcast to prepare desired fertilizer.
NOVELTY - A butanol is produced by separating kitchen wastes in liquid-solid way by centrifugal dehydrator; exploding dehydrated kitchen wastes in the gas; adding saccharifying enzyme to processed kitchen wastes and adding cellulose to continuous solid-state ferment reactor; continuously vaccinating culture medium to cultured Clostridium acetobutylicum seed liquid; rectifying condensed solvent to obtain purified products of acetone, alcohol and butanol and further drying fermented residue by continuous dryer so that water content is less than 14% as organic fertilizer.    USE - Method for producing butanol.    ADVANTAGE - The method uses continuous solid-state ferment process, thus avoiding processing wastewater. It converts waste materials into useful products. The processing efficiency is increased. The energy consumption is reduced and production cost of the butanol is decreased.    DETAILED DESCRIPTION - Butanol is produced by (A) separating kitchen wastes in liquid-solid way by centrifugal dehydrator; (B) exploding dehydrated kitchen wastes in the gas; (C) adding saccharifying enzyme to processed kitchen wastes and adding cellulose to continuous solid-state ferment reactor; (D) continuously vaccinating culture medium to cultured Clostridium acetobutylicum seed liquid; (E) continuously inputting raw material to reactor to continuously ferment and extract butanol under predetermining conditions; (F) rectifying condensed solvent to obtain purified products of acetone, alcohol and butanol; and (G) further drying fermented residue by continuous dryer so that water content is less than 14% as organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a method for producing butanol.
NOVELTY - Anaerobic methane production involves taking biogas produced from storage site or from digester output and bubbling biogas within digester effluent through a distributor below. The biogas bubbles are captured after reducing concentration of hydrogen sulfide.    USE - Method for producing anaerobic methane in anaerobic digesters (claimed).    ADVANTAGE - The method produces anaerobic methane in a cost-effective manner by using biogas as an acidifying agent of residual brewery, where carbon dioxide bubbling from hydrocarbon combustion engines increases biogas production and reduces emissions of carbon dioxide into atmosphere.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the method. (Drawing includes non-English language text).
NOVELTY - The apparatus has a blasting unit (131) mounted on a pipe (102), and a deodorizing part (130) in which a pre-filter (133) is mounted. A cooling part (120) is provided with a cooling room, and another blasting unit (155) is mounted on the former blasting unit. Partition walls are provided in the cooling part. Fire holes are formed in an edge of the deodorizing part. Crossbars are intersected with each other.    USE - Food waste disposal apparatus.    ADVANTAGE - The apparatus reduces electric energy consumption and effectively and dually heats and cools the food waste. The apparatus is hard to damage. The apparatus reduces waste and environmental contamination and prevents bad smell.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a food waste disposal apparatus.    Pipe (102)    Cooling part (120)    Deodorizing part (130)    Blasting units (131, 155)    Pre-filter (133)
NOVELTY - A load-applying mechanism (45) is arranged between cathode-side feeder (42) and cathode-side separator (36), while an anode-side feeder (40) is set with smaller contact area. The feeders are set with a larger contact area range than an anode electrode catalyst layer (40a) and cathode electrode catalyst layer (42a). A contact surface (40b) that touches a solid polymer electrolyte membrane (38) on anode-side feeder is arranged projecting farther to the side of electrolyte membrane than a contact surface (34a) on anode-side separator and contact surface (43a) on frame (43).    USE - Water electrolysis device for manufacturing hydrogen gas for fuel cell used for power generation.    ADVANTAGE - The desired contact pressure is provided reliably with respect to catalysts provided in both sides of electrolytic membrane such that electrolysis capability is improved by simple structure with anode-side feeder and cathode-side feeder.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the unit cell.    Contact surface of anode-side separator (34a)    Cathode-side separator (36)    Solid polymer electrolyte membrane (38)    Anode-side feeder (40)    Anode electrode catalyst layer (40a)    Contact surface of anode-side feeder (40b)    Cathode-side feeder (42)    Cathode electrode catalyst layer (42a)    Frame (43)    Contact surface of frame (43a)    Load-applying mechanism (45)
NOVELTY - Method for generating hydrogen, involves adding liquid ammonia to electrolyte, and electrolyzing the liquid to obtain the final product.    USE - The method is useful for generating hydrogen used for producing electric power (claimed). Can also be used in petroleum refining, chemical industry, automobile industry, fuel cell, fuel cell electric vehicle, hydrogen fueled engine motor vehicle, electric power generating apparatus and hydrogen fueled engine.    ADVANTAGE - The method utilizes less power source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electric power generation system.
NOVELTY - Human waste sewage disposal system of rural toilet comprises a processing pool (6) set at toilet sewer connected with a water inlet pipe (1) and the other end provided with a water outlet pipe (4). The processing pool provided with a sedimentation septic area and a processing area. The sedimentation septic area and the processing area separated between the clapboard (5) and installing clapboard side water hole in the filter plate (3). The water inlet pipe is connected with precipitation septic area, water outlet pipe and the processing area. The water outlet pipe connected with the water tank.    USE - Used as a human waste sewage disposal system of rural toilet.    ADVANTAGE - The human waste sewage disposal system: prevents pathophoresis; is environmental friendly; and improves the human waste sewage disposal system of the existing rural toilet.    DETAILED DESCRIPTION - Human waste sewage disposal system of rural toilet comprises a processing pool (6) set at one end of the toilet sewer connected with a water inlet pipe (1) and the other end provided with a water outlet pipe (4). The processing pool is provided with a sedimentation septic area and a processing area. The sedimentation septic area and the processing area are separated between the clapboard (5) and install at clapboard side water hole in the filter plate (3). The water inlet pipe is connected with precipitation septic area, water outlet pipe and the processing area. The water outlet pipe is connected with the other end of the water tank. The reservoir of the overflow port is connected with a water discharge pipe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the human waste sewage disposal system of rural toilet.    Water inlet pipe (1)    Filter plate (3)    Water outlet pipe (4)    Clapboard (5)    Processing pool (6)
NOVELTY - Device comprises a degrading tank (1), a heating device (2), an agitator (3), an air purifying device (4), a power system (5), a delivery device and a control panel. The degrading tank top cover is provided with an air inlet and an exhaust port. The exhaust port is connected with the air purifying device, and the tank body of the degrading tank is equipped with a discharging port. A stirring device is arranged in the tank. The power system arranged at external side of the tank body, and the power system is connected with the agitator. The heating device is arranged on the top cover.    USE - The device is useful for degrading organic wastes.    ADVANTAGE - The device quickly degrades organic wastes; is safe; converts organic wastes into high-efficiency fertilizer; and has short degradation period (24-48 hours).    DETAILED DESCRIPTION - Device comprises a degrading tank (1), a heating device (2), an agitator (3), an air purifying device (4), a power system (5), a delivery device and a control panel. The degrading tank top cover is provided with an air inlet and an exhaust port. The exhaust port is connected with the air purifying device, and the tank body of the degrading tank is equipped with a discharging port. A stirring device is arranged in the tank. The power system arranged at external side of the tank body, and the power system is connected with the agitator. The heating device is arranged on the top cover. The delivery device is arranged at one side of the degrading tank. The control panel device is arranged at the outer wall of the degrading tank. The control panel respectively controls the heating device, the air purifying device, the power system and the delivery device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for degrading organic wastes.    Degrading tank (1)    Heating device (2)    Agitator (3)    Air purifying device (4)    Power system (5)
NOVELTY - Organic fertilizer fermentation distributing device, comprises a mixing machine, a discharging telescopic belt machine, a reversible cloth belt machine, a material distributing trolley, and a support. The mixing machine and the discharging telescopic belt machine are fixed on the support. The discharging telescopic belt machine is set in the mixing machine below the discharging port. The reversible cloth belt machine is set in the material distributing trolley. The reversible cloth belt machine is located at the discharging telescopic belt machine.    USE - Used as an organic fertilizer fermentation distributing device.    ADVANTAGE - The device: greatly reduces forklift fuel consumed by large number of fabric, and reduces the pollution caused by tail gas of the forklift in the working environment; guarantees the cloth continuity, and automation; reduces the workers labor intensity, and deducts the working staff in the organic fertilizer fermenting area; eliminates the hazardous tail gas ferment from harming the human body, and achieves cloth in an unmanned operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the organic fertilizer fermentation distributing device. (Drawing includes non-English language text)
NOVELTY - Method for manufacturing dioxin decomposer from Stevia plant, involves drying the leaves of S.rebaudiana Bertoni, until water content of the leaves reaches 8%, pulverizing the dried leaves, extracting the pulverized product using water for 5-7 times, culturing the obtained extract in 5-20 l of liquid medium containing wood-decay fungus, and concentrating the obtained product.    USE - The method is useful for manufacturing dioxin decomposer used in agent for treating inorganic matter and sludge.    ADVANTAGE - The method is environmentally-friendly, as it efficiently removes heavy metals from sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for preparing a dioxin decomposition agent, which involves culturing wood-decay fungus capable of producing dioxygenase and lignin peroxidase (LiP) enzyme in liquid medium and extracting the obtained product with Stevia under vacuum.
NOVELTY - Carbonizing device comprises a shell, a cover, a heating device and an inner container. The cover is equipped with a one-way air valve of the inner container.    USE - The carbonizing device is useful for processing the organic waste in homes and at other small units.    ADVANTAGE - The carbonization device avoids spoilage; is suitable for processing all types of organic wastes; ensures short processing time; reutilizes the resources after processing the organic waste; and reduces the quantization effect.    DETAILED DESCRIPTION - An INDEPENDENT claim is also included for a method of using the carbonizing device for processing an organic waste, comprising (i) introducing the organic waste into the inner container, covering with the cover, which is equipped with the one-way gas valve of the inner container, (ii) heating using the heating device, and (iii) turning-off the device when the pressure inside the enclosed space stops increasing, placing it in a cooling device for a suitable period of time and opening the one-way air valve for discharging the internal gas, then opening the cover, and taking out the solid residue.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the carbonizing device.
NOVELTY - The device has an absorption tower i.e. stainless steel filling material tower, and regeneration tower i.e. stainless steel filling material tower, where absorption and regeneration towers are provided with four stages of flower-type liquid redistributing apparatuses. An outer side of the regeneration tower is provided with an insulating layer. Temperature in the absorption tower is controlled stable through relay control. Bottom of the regeneration tower is provided with an electric heating device. A top part of the regeneration tower is provided with a condensing device.    USE - Device for removing biogas, carbon dioxide and hydrogen sulfide in a gas source.    ADVANTAGE - The device has high utilization ratio. The inner side of the absorption tower to a regeneration tower is provided with a flower-type liquid redistributing apparatus, so as to improve effect of removing the carbon dioxide and hydrogen sulfide and regeneration efficiency of waste liquid. The preheating device is used to improve regeneration effect of a chemical absorption reagent. The content of methane in the biogas is improved after the processing through the device reaches 97-100 percent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for removing biogas, carbon dioxide and hydrogen sulfide in a gas source.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for removing biogas, carbon dioxide and hydrogen sulfide in a gas source.
NOVELTY - Method of producing biodiesel and fermentation product by culturing microalgae, involves culturing microalgae, dissolving cultured product in support extraction solvent, fractionating the mixture using lipid extraction solvent, obtaining lipid-solvent fraction, re-culturing some of the fractioned microalgae, fermenting the remaining fractioned microalgae using one of ethanol, butanol, or organic acid, extracting lipid from the fraction, extracting biodiesel from the product, and obtaining one of ethanol, butanol, or organic acid from the product.    USE - The method and apparatus are useful for producing biodiesel and fermentation product chosen from ethanol, butanol, and organic acid (claimed).    ADVANTAGE - The apparatus simultaneously produces biodiesel and other fermentation products.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus, which comprises culture tub (10) for culturing microalgae, solvent tank (20) for storing lipid extraction solvent, mixed tub (30) for dissolving cultured product in support extraction solvent, fractionating tub (40) for fractionating the mixture using lipid extraction solvent, fermentor (50) for fermenting the fractioned microalgae, cycling tank (60) for cycling remaining microalgae, distillation bath (70) for extracting lipid from the fraction, and diesel tank (80) for collecting biodiesel.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of apparatus.    Culture tub (10)    Solvent tank (20)    Mixed tub (30)    Fractionating tub (40)    Fermentor (50)    Cycling tank (60)    Distillation bath (70)    Diesel tank (80)
NOVELTY - The device has a two-position three-way valve whose one outlet port is connected to a sampling analysis pipeline while other outlet port is connected to a micro-metering valve. The micro-metering valve is connected to one inlet end of a two-position four-way valve. One outlet end of four-way valve is connected to an analysis meter connected to other inlet end of four-way valve. The other outlet end of four-way valve is connected to an air flow meter. The inlet end of a dryer connected to outlet end of air flow meter has a pressure-relieving pipeline with a micro safety valve.    USE - Multifunctional preprocessing device for water electrolysis hydrogen preparation analysis meter.    ADVANTAGE - The probe of the analysis meter is prevented from being damaged by working in air and unqualified gas for a long time. By switching the valve of the two-position four-way valve, the analysis meter is avoided from being damaged and the maintenance cost of the multifunctional preprocessing device is saved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional preprocessing device for water electrolysis hydrogen preparation analysis meter.
NOVELTY - Biogas dehydration device comprises condenser having condenser inlet and condenser outlet; steam trap having steam inlet and steam outlet, where steam inlet is connected with the condenser outlet; and gas and water separator having inlet, biogas outlet, and water outlet, where separator inlet is connected with the steam outlet.    USE - Device for biogas dehydration (claimed).    ADVANTAGE - The device uses two-stage dehydration, i.e. two-stage condensation dehydration and secondary centrifugal dehydration, thus, achieving good dehydration effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biogas dehydration method.
NOVELTY - A garbage processing agent comprises (pts. wt.) Bacillus cereus (60-118), and spherical red Pseudomonas (100-200).    USE - A garbage processing agent.    ADVANTAGE - The agent does not need require addition of chemical reagent, is environment-friendly, and does not produce secondary pollution to the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the garbage processing agent comprising subjecting B. cereus to slant activation, inoculating in liquid culture medium, cultivating at 35 degrees C for 36-72 hours, subjecting Pseudomonas to slant activation, inoculating in liquid culture medium, cultivating at 35 degrees C for 28-72 hours, calculating active bacteria, detecting bacteria count of B. cereus and spherical red Pseudomonas, mixing the bacteria liquid, fermenting at 25-35 degrees C for 36-75 hours, drying at 30 degrees C, crushing, and screening using 40 mesh sieve.
NOVELTY - The device has wind driven generator (2) and blade (1) that are installed on top end of hollow strut (3) of wind driven generator. Wind driven generator is connected with electrolytic hydrogen generating device (5) connected with manufacturing workshop (7) of hydrogen fuel storage container via hydrogen conveying pipe (6). Hydrogen fuel storage container (8) is connected with hydrogen fuel battery (10) via hydrogen fuel conveying pipe (9). Fuel battery is connected with motor (11) which is connected with mechanical driving device (14) via power output shaft (12).    USE - Power device for supplying wind and hydrogen energy source to rape harvesting machine.    ADVANTAGE - Since the electric energy is connected into mechanical energy in the motor to drive the rape harvesting machine, the rape can be harvested and threshed easily.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a power device.    Blade (1)    Wind driven generator (2)    Hollow strut (3)    Electrolytic hydrogen generating device (5)    Hydrogen conveying pipe (6)    Manufacturing workshop (7)    Hydrogen fuel storage container (8)    Hydrogen fuel conveying pipe (9)    Hydrogen fuel battery (10)    Motor (11)    Power output shaft (12)    Mechanical driving device (14)
NOVELTY - The device has engine (1), direct-current generator (3), water electrolyzing device (6), hydrogen delivery pipeline (13), and oxygen delivery tube (12). The engine is connected with the direct-current generator in transmission manner. The anode and cathode (5,4) at output end of generator are respectively connected with electrolyzing anode plate (8) and electrolyzing cathode plate (8') in electrolyzing device. A closed container of electrolyzing device is provided with oxygen collecting chamber (11) and hydrogen collecting chamber (9).    USE - Device for economizing fuel of automobile.    ADVANTAGE - Since the engine is connected with the direct-current generator in transmission manner, the rest power of the automobile in low-speed running can be transformed into hydrogen fuel used for operating the engine. Hence fuel storage can be improved and waste gas exhaust can be reduced. The simple structure of the fuel economizing device can be achieved.    DETAILED DESCRIPTION - One end of oxygen delivery pipeline is connected with oxygen collecting chamber and other end is connected with air inlet pipeline (14) of engine. One end of hydrogen delivery pipeline is connected with hydrogen collecting chamber and other end is connected with air inlet pipeline of engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for economizing fuel of automobile.    Engine (1)    Direct-current generator (3)    Cathode (4)    Anode (5)    Water electrolyzing device (6)    Anode plate (8)    Cathode plate (8')    Hydrogen collecting chamber (9)    Oxygen collecting chamber (11)    Oxygen delivery tube (12)    Hydrogen delivery pipeline (13)    Air inlet pipeline (14)
NOVELTY - A propoxur is synthesized by adding o-iso-propoxyphenol and catalyst, stirring and cooling, slowly dropping methyl isocyanate (MIC) and carrying out reaction for 0.5-3 hours at 60-110 degrees C after dropping. The ratio of n(phenol) to n(catalyst) is 1:0.001-0.05. The ratio of the n(phenol) to n(MIC) is 1/1-1/1.2.    USE - Method for synthesizing propoxur (claimed).    ADVANTAGE - The method has simple process, small pollution and high yield.
NOVELTY - Microbial organic fertilizer comprises (in wt.%): microorganism composite bacterial suspension (0.5-5), strontium carbonate (5-20), humic acid (40-80) and drying agent (5-40).    USE - The microbial organic fertilizer is useful for vegetables and fruit trees.    ADVANTAGE - The microbial organic fertilizer increases soil fertility and yield of crops, has high organic content and improves flora.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-cited microbial organic fertilizer, which involves (a) inoculating strains of Bacillus, Actinomycetes and Acinetobacter into strain activation culture medium, culturing the strain under sealing condition at 24-35 degrees C, separately conducting active culturing for 10-15 hours, separately conducting fermentation rapid propagation of the cultured strains for 12-60 hours in production fermentation culture medium and oscillating the culture medium every 2 hours during the active culturing and fermentation rapid propagation process to separately obtain microorganism bacterial suspensions of Bacillus, Actinomycetes and Acinetobacter, and (b) mixing microorganism bacterial suspensions of Bacillus, Actinomycetes and Acinetobacter in the volume ratio of 5:2:3 to obtain composite bacterial suspension, pulverizing raw material humic acid, strontium carbonate and bentonite, uniformly mixing the pulverized mixture, spraying the composite bacterial suspension on surface of the mixed raw materials, and mixing the mixture uniformly, prilling the mixture and drying the mixture to obtain fertilizer.
NOVELTY - Method of preparing biocarbon using Triarrhena lutarioriparia plant and capturing and storing carbon of air, involves cultivating, harvesting and pretreating the T.lutarioriparia plant and producing the biocarbon. The pretreatment involves airing the harvested T.lutarioriparia stem, cutting the stem into length suitable for smoke-less coking process, and subjecting the preferably-treated cut pieces to smoke-less coking process at 450-550 degrees C without oxygen.    USE - The method is useful for preparing biocarbon for capturing and storing carbon dioxide from air, and generating electricity directly.    ADVANTAGE - The method is economic and environmentally-friendly. The method improves soil structure, improves soil fertility, increases yield of crops, and reduces influence of energy crisis for national economy and production.
NOVELTY - Conditioning dewatered sludge and preparing slow release fertilizer, involves (a) adding hygroscopic clay mineral (20-100 kg) and plant residues (100-300 kg) to dewatered sludge (m3), (b) fermenting the mixture for 10-15 days to obtain fermented product, (c) adding substance containing phosphate radicals and ammonium ions (50-100 kg) to the fermented product, (d) uniformly mixing the mixture, (e) allowing the mixture to stand for 2-3 days, (f) adding magnesium-containing alkaline substance (5-20 kg) to the uniform mixture, and (g) repeating the steps (d) and (e).    USE - The method is useful for conditioning dewatered sludge and preparing slow release fertilizer.    ADVANTAGE - The method is suitable for large scale application and provides highly nutritious raw material for preparing slow release fertilizer.
NOVELTY - Method for preparing biological control microbial organic fertilizer, involves (a) mixing hydrolysis residue powder with powdered lime and reacting mixture, (b) fermenting Bacillus subtilis strain HL259, B.mucilaginosus Krassilnikov, and Streptomyces sp. strain YL04, and (c) mixing the hydrolysis residue with the microorganism, and pulverizing the mixture to obtain powdered microbial organic fertilizer, where the quality of the composite microbial organic fertilizer is 4-6% of finished product of organic fertilizer.    USE - The method is useful for preparing biological control microbial organic fertilizer for preventing diseases of crops and reducing seedling disease rate.    ADVANTAGE - The fertilizer improves nutrient required for growth of crops and increases crop yield.    DETAILED DESCRIPTION - Method for preparing biological control microbial organic fertilizer, involves (a) pulverizing big block of hydrolysis residue into powder or small particle, mixing the powder with powdered lime, and stacking the mixture and completely reacting the mixture to obtain pH of 5-8, (b) separately fermenting Bacillus subtilis strain HL259, B.mucilaginosus Krassilnikov, and Streptomyces sp. strain YL04, using absorbing medium to absorb the fermented mixture, and mixing and crushing the microorganisms in the ratio of 4.5-5:3-3.5:1.5-2, and (c) mixing the hydrolysis residue obtained in step (a) with the microorganism obtained in step (b), uniformly stirring the mixture and pulverizing the mixture to obtain powdered microbial organic fertilizer, where the quality of the composite microbial organic fertilizer is 4-6% of finished product of organic fertilizer.
NOVELTY - The device has a casing whose upper end is provided with storage cabinet (1) and controller (2). A fuel gas output port (8) is connected with cyclone dust collector (18). An outlet of dust collector is connected with filter screen extraction component (19) of heat exchanger (20). A gasification air inlet of heat exchanger (22) is connected with air flow adjusting valve (24) and air fan (25). A fuel gas outlet of heat exchanger is connected with fuel gas online detector (27).    USE - Poly-generation device for backing fire, coking and preparing fuel gas for engine using coal and biomass such as wood, bamboo, straw, rice husk, and rubbish bar.    ADVANTAGE - The discharging of the polluted wastewater to the surrounding, during the generation of the fuel gas can be prevented effectively. The fuel gas can be prepared effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the poly-generation device.    Storage cabinet (1)    Controller (2)    Fuel gas output port (8)    Cyclone dust collector (18)    Filter screen extraction component (19)    Heat exchangers (20,22)    Air flow adjusting valve (24)    Fuel gas online detector (27)
NOVELTY - The method involves discharging a low molecular weight substance to outside of a reactor. A bio-chip is injected from organic waste and an aerobic microorganism. The organic waste and the bio-chip are mixed with a polymer through a stirring part. A reaction condition of a reaction bath is controlled by the stirring part. The mixer of the organic waste and the bio-chip is circulated in an upper and a lower part of a reaction bath that is equipped with the stirring part. Temperature of a reaction container down part is maintained in a range of 70 to 95 degree Celsius.    USE - Method for extracting biodiesel raw material from organic wastes such as food waste and livestock industry garbage.    ADVANTAGE - The method enables providing easy extraction of fat ingredients, and avoids separate cost of equipment or operating cost for the extraction of the fat ingredients, and has reduced installation expense.    DESCRIPTION OF DRAWING(S) - The drawing shows a photographic representation of a method for extracting biodiesel raw material from organic waste.
NOVELTY - A biological organic compound fertilizer preparation process using sludge and straws, involves preparation of fertilizer raw materials, high-temperature aerobic fermentation, curing treatment, and compound fertilizer preparation. Also claimed is, a device for producing biological organic compound fertilizer.    USE - Process for producing biological organic compound fertilizer using sludge and straw.    ADVANTAGE - The method provides a complete and integral technical route for economically producing biological organic compound fertilizer.
NOVELTY - The method involves transferring plastic to sludge rotary feeder (40) and mixing the biomass fuel with plastic. The sludge generated after the mixing process is transferred through scale conveyor belt (19) and sludge is cut through cutter (18). The remaining portions of the sludge are stored in lower portion of sludge mixture repository (17).    USE - Method for transferring biomass fuel to biomass fuel bunker sludge.    ADVANTAGE - The transfer amount of the biomass fuel is maintained in constant rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for transferring biomass fuel.    Selection conveyor belt (10)    Sludge mixture repository (17)    Cutter (18)    Scale conveyor belt (19)    Sludge rotary feeder (40)
NOVELTY - Organic agricultural product comprises 0.004-0.005 wt.% of azadirachtin (40-500 ppm), 1-30 wt.% of leaf tobacco, 35-90 wt.% of organic materials, and 2-35 wt.% of soil pest preventing ingredients.    USE - The organic agricultural product is useful for preventing pest, preferably root-knot nematode of melon, preferably water melon and Momordica charantia, ginseng, tomato, carrot, Chinese cabbage, red pepper or peanut (claimed).    ADVANTAGE - The product enhances fertility of seed, and is environmentally-friendly.
NOVELTY - Method of preparing microbial nutrient, involves preparing first medium by mixing (in parts weight) mixed solution (800-1200), glucose (40-60), and amino acid (1-5), preparing second medium by mixing mixed solution (90-94), glucose (3-7), and amino acid (1-5), mixing first medium (800000-1200000) and second medium (80-120), and culturing Lactobacillus in the obtained medium at 25-30 degrees C for 9-11 hours.    USE - The method is useful for preparing microbial nutrient (claimed), which is used for improving growth of plant, preferably rice, and controlling pest and virus.    ADVANTAGE - The nutrient reduces use of agricultural composition, and improves soil fertility.    DETAILED DESCRIPTION - Method of preparing microbial nutrient, involves preparing first medium by mixing (in parts weight) mixed solution (800-1200), glucose (40-60), and amino acid (1-5), preparing second medium by mixing mixed solution (90-94), glucose (3-7), and amino acid (1-5), mixing first medium (800000-1200000) and second medium (80-120), and culturing Lactobacillus in the obtained medium at 25-30 degrees C for 9-11 hours. The mixed solution is prepared by mixing wasted milk, wasted soybean milk, rice water, and wasted yogurt in a ratio of 35-45:3-7:50-60:0.5-1.5 to obtain mixed solution. An INDEPENDENT CLAIM is included for microbial nutrient, which is prepared by performing the above-mentioned method.
NOVELTY - The waste is separated into general purpose garbage and combustible waste. The general purpose garbage is cut, and the foreign substance and metal in the general purpose garbage are selected by the process of agitating. The PVC in the general purpose garbage is selected. The rope is manufactured by sorting the general purpose garbage of fixed quantity and drying the general purpose garbage.    USE - Method for manufacturing solid fuel using combustible waste such as plastic, gunny bag, fiber, and timber.    ADVANTAGE - The waste is recycled to fuel, and the import expenses of the fossil fuel are reduced. The production cost of the fuel is reduced. The damage of the apparatus for manufacturing solid fuel is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart explaining the process for manufacturing solid fuel using combustible waste. (Drawing includes non-English language text)
NOVELTY - A low-temperature flow improver composition comprises a monomer mixture containing (in wt.%) vegetable oil-derived ester monomer (10-95) produced by activating methacrylic acid or acrylic acid and vegetable oil-derived fatty alcohol, and monomer(s) (5-90) chosen from styrene, maleic acid anhydride, and ester monomer.    USE - Low-temperature flow improver composition is used in fuel oil containing biodiesel (claimed).    ADVANTAGE - The low-temperature flow improver effectively improves the cold flow of fuel oil, and prevents crystal growth of saturated fatty acid methyl ester and wax crystals by cooling, and thus filter clogging.    DETAILED DESCRIPTION - A low-temperature flow improver composition comprises a monomer mixture containing (in wt.%) vegetable oil-derived ester monomer (10-95) produced by activating methacrylic acid or acrylic acid and vegetable oil-derived fatty alcohol, and monomer(s) (5-90) chosen from styrene, maleic acid anhydride, and ester monomer of formula: H2C=CR1-COOR2.    R1=H or methyl;and    R2=linear or branched 1-18C alkyl.    An INDEPENDENT CLAIM is included for fuel oil composition comprising biodiesel and the low-temperature flow improver.
NOVELTY - Method for preparing hydroxyalkanoate alkyl ester, involves culturing microorganism in a culture medium containing polyhydroxyalkanoate to obtain polyhydroxyalkanoate, autolysing the polyhydroxyalkanoate to obtain hydroxyalkanoate, adding alcohol to hydroxyalkanoate, and reacting the mixture to obtain hydroxyalkanoate alkyl ester.    USE - The method is useful for preparing hydroxyalkanoate alkyl ester chosen from 87 compounds e.g. (D)-hydroxy carboxylic acids, 3-hydroxypropionic acid, 3-hydroxyhexanoic acid, 3-hydroxy-octanoic acid, 3-hydroxynonanoic acid, 3hydroxydecanoic acid, 3-hydroxyundecanoic acid, 3-hydroxydodecanoic acid, 3hydroxytetradecanoic acid, 3-hydroxyhexadecanoic acid, 4-hydroxyvaleric acid, 2hydroxybutyrate, 3-hydroxypropionate, 3-hydroxyvalerate, 3-hydroxy-tetradecanoic acid, 3-hydroxy-4-methyl-valeric acid, 3(hydroxy)(chlorohexanoic acid), 3-hydroxypimelic acid-propylester, 3-hydroxysebacic acid-benzylester, para-cyanophenoxy-3-hydroxyhexanoic acid, 3-hydroxy-3-phenylvaleric acid, 7-cyano-3-hydroxyheptanoic acid and 3,8(hydroxy)(tetradecanoic acid) (claimed), which is used for producing biodiesel.    ADVANTAGE - The method is suitable for industrial production and environmentally-friendly, and enables mass production of hydroxyalkanoate alkyl ester.
NOVELTY - The invention relates to a bioreactor for obtaining biogas. According to the invention, the bioreactor consists of a spherical enclosure (1) for fermenting a biomass, being covered with a transparent roofing (18), provided with photovoltaic cells, for using the solar energy, said enclosure being carried out of prefabricated concrete segments, being positioned on a base consisting of two joined steel layers, said enclosure consisting of some double walls between which there is an air layer (2) wherein there are positioned supporting columns or posts, the enclosure (1) being provided at the external side, at the ground level, with some circular openings (3) through which the cold air penetrates, with some circular openings (4) at the upper side, through said openings there being discharged the warm air resulting after cooling the biomass, some openings (13) for discharging the residue of the fermented material.
NOVELTY - Cooling system (2) comprises at least one compressor (4), at least one condenser, at least a first heat exchanger, at least one flow restriction, at least one evaporator (22), and a first non-azeotropic mixture of refrigerants, in which the non-azeotropic mixture comprises butane, isobutane, ethylene, and a further refrigerant having a nature boiling point of below -75 degrees C.    USE - The cooling system is useful as air condition systems in industrial applications such as cooling of computer systems (all claimed).    ADVANTAGE - The cooling system: utilizes non-azeotropic refrigerant mixture having environmentally friendly refrigerants, which can be used in container cooling systems for achieving storage temperature in container below -60 degrees C, thus it is a low temperature cooling system; easily exchanges the refrigerant if it is allowed to let at least smaller amount of the refrigerant flow out of the cooling system; can be a single compressor system especially designed for ultra low temperature purposes; and achieves low energy consumption, low noise, and low heat dissipation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the non-azeotropic refrigerant mixture.    DESCRIPTION OF DRAWING(S) - The figure shows a cooling system.    Cooling system (2)    Compressor (4)    Receiver (16)    Capillary tube (20)    Evaporator (22)
NOVELTY - Hydrogen storage structure comprises: many graphene sheets arranged to form a stack (9); and many spacers arranged between adjacent graphene sheets in the stack.    USE - The hydrogen storage structure is useful for storing hydrogen (claimed) for use as a fuel and in alternative fuel vehicles.    ADVANTAGE - The hydrogen storage structure utilizes the graphene sheets which are thermodynamically stable, and have a high crystal quality and macroscopic continuity, pronounced electric field effect, and are doped with lithium, which help in stabilizing the hydrogen molecules, and can store 7.7 wt.% of hydrogen.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a hydrogen storage structure, comprising: a first graphene sheet (2); a second graphene sheet (4) adjacent to the first graphene sheet and arranged to form a stack; and many spacers arranged between the first graphene sheet and the second graphene sheet in the stack; and    (2) storing hydrogen, comprising arranging many graphene sheets to form a stack and spacing adjacent graphene sheets in the stack apart with many spacers, where the spacers are arranged between the adjacent graphene sheets.    DESCRIPTION OF DRAWING(S) - The figure shows an elevation view showing hydrogen storage structure having graphene spheres positioned between graphene sheets.    First graphene sheet (2)    Second graphene sheet (4)    Graphene spheres (6, 8)    Stack (9)
NOVELTY - Method for preparing Dehalococcoides bacterial broth, involves culturing Dehalococcoides bacteria and filamentous bacteria in culture medium under anaerobic condition, performing first fractionation process to separate anaerobic culture solution and supernatant, performing second fractionation process by carrying out membrane filtration of anaerobic culture solution, and obtaining culture solution.    USE - The method is useful for preparing Dehalococcoides bacterial broth used in chlorinated ethylene purifier for chlorinated ethylene clean-up method in soil and/or underground water (all claimed).    ADVANTAGE - The method prepares bacterial broth with high bacterial content.    DETAILED DESCRIPTION - Method for preparing Dehalococcoides bacterial broth, involves (a) culturing Dehalococcoides bacteria and filamentous bacteria in culture medium under anaerobic condition to obtain enrichment culture of consortium, (b) performing first fractionation process by gravitational force or centrifugal force to separate anaerobic culture solution and supernatant, and (c) performing second fractionation process by carrying out membrane filtration of anaerobic culture solution using membrane having hole diameter of 3-100 mu m to obtain permeation liquid, and obtaining culture solution with high occupancy of Dehalococcoides bacteria. INDEPENDENT CLAIMS are included for the following:    (1) chlorinated ethylene purifier comprising the above-mentioned bacterial broth; and    (2) chlorinated ethylene clean-up method in soil and/or underground water, involves accreting the above-mentioned chlorinated ethylene purifier in soil and/or underground water.
NOVELTY - Compost wand is inserted every few inches apart throughout the compost and watered for a few seconds at each location keeping the compost damp but not sloppy wet. Too wet and the compost stinks, too dry and the compost won't decay. On average using the compost wand every two weeks throughout the growing season works well, more often in dry weather and less often in wet weather is necessary to keep the compost consistently damp.    USE - The compost wand is useful for watering and aerating compost for producing well rotted compost in one growing season.    ADVANTAGE - The compost wand avoids the need of turning the compost, and waters and aerates compost in one operation with very little effort. Consistent good test results are achieved in four consecutive growing seasons.
NOVELTY - A sewage-treatment apparatus (G1) has a biological reactor (1) in which activated sludge flows, an oxidation-reduction potential measurement unit (4), an aerator (2), and a controller (3). The reactor processes sewage using activated sludge by bioreaction. The oxidation-reduction potential measurement unit measures the oxidation-reduction potential of liquid in the biological reactor. The dinitrogen-oxide gas production amount of the reactor is estimated based on the measured potential. The controller controls the aerator based on the estimated value.    USE - Apparatus is used for treating sewage.    ADVANTAGE - The sewage-treatment apparatus efficiently reduces greenhouse gas and carbon dioxide emitted during sewage treatment, power consumption, and dinitrogen-oxide emission amount. The aeration gas volume is reduced by controlling the operation of biological reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the sewage-treatment apparatus. (Drawing includes non-English language text)    Biological reactor (1)    Aerator (2)    Controller (3)    Oxidation-reduction potential measurement unit (4)    Sewage-treatment apparatus (G1)
NOVELTY - A tar decomposing catalyst comprises barium titanate as a main component, and iron and strontium as subsidiary components held on barium titanate.    USE - Catalyst is used for decomposing tar contained in gasifying gas formed by thermal decomposition of biomass containing sulfur compound (claimed) e.g. sewage sludge.    ADVANTAGE - The catalyst has excellent carbon precipitation resistance, and catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method to decompose-remove tar contained in gasifying gas formed by thermal decomposition of biomass containing sulfur compound, involves passing gas through the tar decomposing catalyst.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph illustrating result of tar decomposition performance test of the catalyst. (Drawing includes non-English language text)
NOVELTY - Method for manufacturing blast furnace coke, involves drying sludge e.g. sewage sludge, granulating dried sludge, mixing dry granulated sludge with raw coal, and transferring the mixture to a coal oven and dry distilling the mixture.    USE - The method is useful for manufacturing blast furnace coke using sludge including sewage sludge (claimed), sludge from purification tank, activated sludge, and kitchen waste sludge.    ADVANTAGE - The method enables to manufacture blast furnace coke with equivalent or high strength compared to blast furnace coke manufactured using only raw coal.
NOVELTY - The method involves sending retentate stream (6) to a molecular sieve adsorbent bed (10) to remove carbon dioxide and impurities from the retentate stream to produce a natural gas product stream (2). Regeneration gas stream is sent through the adsorbent bed to desorb the carbon dioxide, where the regeneration gas stream is sent with the carbon dioxide to be combined with a permeate stream (28). The permeate stream is sent to an absorbent column to remove carbon dioxide from the permeate stream to produce another natural gas product stream.    USE - Method for treating natural gas stream to remove impurities such as carbon dioxide on a floating platform i.e. ship, in ocean (all claimed).    ADVANTAGE - The method enables minimizing foot print and weight of a combined treatment train while maximizing reliability of the treatment train. The method enables generation of flow mal-distribution inside an amine absorber and a stripping regenerator so as to meet low carbon dioxide concentration in the treated gas. The method permits an optimized hybrid system to avoid membrane permeate venting so as to significantly reduce hydrocarbon loss.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of processing steps of treating natural gas in a hybrid treatment system.    Natural gas product stream (2)    Retentate stream (6)    Molecular sieve adsorbent beds (10, 12)    Blower (24)    Permeate stream (28)    Compressor (30)
NOVELTY - A fluorosilane compound (I) and hydroxyl group-containing compound (II) are reacted in presence of salt of alkali metal and heterocyclic compound having basicity to obtain silyl compound (III).    USE - Manufacture of silyl compound used as intermediate for pharmaceuticals and agrochemical.    ADVANTAGE - The method efficiently and economically provides silyl compound without affecting the environment, by simple method. The fluorosilane compound which is used as silylating agent during manufacture of silyl compound, is recyclable.    DETAILED DESCRIPTION - A fluorosilane compound of formula: R1R2R3SiF (I) and hydroxyl group-containing compound of formula: A-OH (II) are reacted in presence of salt of alkali metal and heterocyclic compound having basicity to obtain silyl compound of formula: A-O-SiR1R2R3 (III).    R1-R3=heteroaryl, aryl (both optionally substituted), 1-20C alkyl, 3-8C cycloalkyl, 2-20C alkenyl or 2-20C alkynyl;and    A=organic group.
NOVELTY - The apparatus has critical band in which the masking sound is provided. The critical band is settled at the resonant frequency of the motor. The resonant frequency and masking frequency which are not corresponding with each other, are generated.    USE - Control apparatus of motor used as motive power source for fuel cell vehicle or hybrid vehicle.    ADVANTAGE - Since the resonant frequency and masking frequency which are not corresponding with each other, are generated, the protrusion of the sound pressure level of electromagnetic noise can be reduced effectively through masking process. Thus the efficiency of the motor can be raised.    DESCRIPTION OF DRAWING(S) - The drawings show a graphical view illustrating the frequency spectrum of in-vehicle noise when masking. (Drawing includes non-English language text)
NOVELTY - Method for preparing granulation improved soil, involves recycling construction sludge discharged from construction site and road work field, pulverizing waste plaster board to obtain waste plaster board powder, mixing the powder with the construction sludge in the ratio of 50% or less with respect to weight of the construction sludge to obtain primary mixture, mixing cement with the primary mixture in the ratio of 20% or less with respect to the weight of the primary mixture to obtain secondary mixture, and drying and solidifying the secondary mixture.    USE - The method is useful for preparing granulation improved soil which is used as road surfacing material, backfill material, slope face curing and weed proof material.    ADVANTAGE - The method suppresses elution of toxic chemical substance, preferably fluorine and hexavalent chromium in soil below to soil environmental standard value, and can be performed with excellent practicability and workability without soil pollution. The granulation improved soil does not generate hydrogen sulfide and hence highly safe, has excellent intensity which is not mud reformed, can be obtained easily, and is environmentally-friendly.
NOVELTY - Recovering, purifying and enriching hydroxy fatty acids from source oil involves methylating the source oil to form a mixture of hydroxy fatty acid methyl esters and non-hydroxy fatty acid methyl esters; separating the hydroxy fatty acid methyl esters from the non-hydroxy fatty acid methyl esters with an organic solvent mixture containing short-chain alcohol and a pentane/hexane; and separately recovering the hydroxy fatty acid methyl esters and the non-hydroxy fatty acid methyl esters.    USE - For recovering, purifying and enriching hydroxy fatty acids selected from ricinoleic acid, densipolic acid, lesquerolic acid, and auricolic acid from a source oil, derived from e.g. castor bean plant materials, legume plant materials, Lesquerella species plant materials, Brassica species plant materials, and Brassicacea species plant materials, useful as a cold-tolerant biodiesel (claimed).    ADVANTAGE - The process recovers hydroxy fatty acid (HFA) from seed or nut materials containing less than 6 wt.% HFA, and purifies and enriches the HFA methyl ester (HFAME) to greater than or equal to 68 wt./wt.%, while concurrently recovers, purifies and enriches the NHFAME to greater than or equal to 90 wt./wt.%. The process is simple; and requires small amount of solvents, and less processing time.
NOVELTY - Method for producing biofuel involves (a) culturing (S1) photosynthetic microorganism in culture solution, where the photosynthetic microorganism is capable of accumulating fat/oil and carbohydrate in cell, (b) converting (S2) carbohydrate into fat/oil, (c) extracting (S3) fat/oil from the cell and (d) modifying (S4) the extracted fat/oil.    USE - The method is useful for producing biofuel e.g. biodiesel, light oil and bio-jet fuel using photosynthetic microorganism e.g. Euglena, diatom, golden algae, Cyanobacteria, Chroococcaceae and Stigonematales. The degreased microorganism cell is useful as feed, fertilizer, and biomass feedstock.    ADVANTAGE - The method produces large amount of biofuel when compared with existing method as conversion process is included and the process is carried out in series with continuous supply of carbon dioxide in the form of combustion exhaust gas emitted from e.g. factories, and thus reduces environmental load.    DESCRIPTION OF DRAWING(S) - The drawing is a flow chart illustrating biofuel production process. (Drawing includes non-English language text)    Culture step (S1)    Fat/oil conversion step (S2)    Extraction step (S3)    Modification step (S4)    Concentration step (S12)    Drying step (S22)    Collection step (S32)
NOVELTY - The system has a motor (64) e.g. electric motor, and a fixture adjusting height of a roller and height of a shaft in reference to a floor portion of a compost receptacle (12) e.g. tray. The fixture comprises an end coupled to a shaft end and a mid-section coupled to a sleeve, where another end of the fixture is mounted onto a support e.g. channel, of the receptacle. A web or liner (28) conveys mushroom compost e.g. pre-spawned phase-II mushroom compost, into a nip between the roller and the floor portion of the receptacle.    USE - Mushroom compost compacting system for composting mushroom compost e.g. pre-spawned phase-II and spawn run phase-III mushroom composts, in a mushroom compost bed. Can also be used for phase-I mushroom compost.    ADVANTAGE - The system performs composition of the mushroom compost without adversely impacting a mushroom crop, where a successful degree of compaction is determined at a mushroom grower's discretion for allowing the system to obtain uniform compaction of the mushroom compost at the top, middle and bottom of a compacted compost bed. The mushroom compost bed using the system can reduce a mushroom grow time cycle by one or two days. The system expedites mushroom bed preparation with the compost and produces a consistent compost compaction to enhance yield in a shorter grow time cycle.    DESCRIPTION OF DRAWING(S) - The drawing shows a top perspective view of a mushroom compost bed including a mushroom composting system.    Mushroom compost bed (10)    Compost receptacle (12)    Roller assemblies (14)    Liner (28)    Motor (64)
NOVELTY - Detoxified and purified Argemone oil, without trans-esterification, for edible use as well as non-edible use such as biodiesel, where the process of detoxification and purification comprises: (a) degumming of Argemone oil by treating with methanolic O-phosphoric acid solution to obtain alkaloid and gum free oil; and (b) detoxifying the degummed oil by treating with aqueous sodium hydroxide (NaOH) solution to obtain alkaloid free detoxified Argemone oil.    USE - The detoxified and purified Argemone oil without trans-esterification is for edible as well as non-edible use such as biodiesel, and where the trans-esterified Argemone oil is for non-edible use such as biodiesel (claimed).    ADVANTAGE - The detoxified and purified Argemone oil is highly improved, economical and can be prepared cost-effectively.
NOVELTY - Integrated biogas separator comprises an air inlet pipe (1), sulfur chamber (4) and an air outlet (9). The air inlet pipe is connected with water seal tank (2). The water seal tank is fixed at the bottom of gas-guide tube hole, which is fixed with gas-guide tube (3). The gas guide tube is located higher than the upper water seal tank in liquid level. The water seal tank is located below lower part of sulfur chamber. The desulfurization chamber is located at lower part of gas-water separating chamber. The sulfur-smelting chamber and gas-water separating chamber are separated with grid plate.    USE - Used as an integrated biogas separator.    ADVANTAGE - The device has compact structure and occupies less area.    DETAILED DESCRIPTION - Integrated biogas separator comprises an air inlet pipe (1), sulfur chamber (4) and an air outlet (9). The air inlet pipe is connected with water seal tank (2). The water seal tank is fixed at the bottom of the gas-guide tube hole, which is fixed with gas-guide tube (3). The gas guide tube is located higher than the upper water seal tank in the liquid level. The water seal tank is located below the lower part of sulfur chamber. The desulfurization chamber is located at the lower part of gas-water separating chamber. The sulfur-smelting chamber and gas-water separating chamber are separated with grid plate. A gas-guide tube through the lower port of the desulfurizing chamber and gate board extends into the gas water separating chamber. The gas-guide tube is equipped with a lower port of the horn cover of the bell mouth vertically and downwards. The sulfur-smelting chamber of the side wall of the upper end is opened with an air outlet.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the integrated biogas separator.    Air inlet pipe (1)    Water seal tank (2)    Gas-guide tube (3)    Sulfur chamber (4)    Air outlet (9)
NOVELTY - Utilizing reed and arbuscular mycorrhiza for restoring oil-polluted wetland comprises planting reed in soil of the oil-polluted wetland, where the planting density is 3 roots/kg, and cultivating for 120 days after the reed begins to germinate and grow, inoculating arbuscular mycorrhiza in the soil matrix near the reed roots, where the inoculum amount according to the spore density is 5-8/g, and continuously growing the reed for restoring the oil-polluted wetland under the combined action of arbuscular mycorrhiza.    USE - The method is useful for restoring oil-polluted wetland.    ADVANTAGE - The method has a wide range of sources and requires less quantity of sources, is simple and economical; ensures good restoring effect; does not produce secondary pollutants, and hence is ecofriendly; and is suitable for in-situ restoration of oil-polluted wetlands with large area.
NOVELTY - Composting food waste comprises: pre-processing by removing the inorganic substance from the kitchen waste; adding sawdust and animal waste into kitchen waste; crushing the particle processed in the kitchen waste to the particles with diameter of less than 5 mm and simultaneously controlling the moisture content of these particles to 50-60%; composting by naturally stacking the processed kitchen waste for 3-5 days, and when the temperature of the waste compost rises to more than 75 and is no longer increased, processing, again after 3-5 days when temperature no longer rises, turning.    USE - The processed kitchen waste is useful as organic fertilizer or culture medium.    ADVANTAGE - The method thoroughly degrades the kitchen waste, and converts the waste into utilizable product.    DETAILED DESCRIPTION - Composting food waste comprises: (i) pre-processing by removing the inorganic substance from the kitchen waste; (ii) adding sawdust (20-25 vol.%) and animal waste (8-12 vol.%) into kitchen waste; (iii) crushing the particle processed in the kitchen waste to the particles with diameter of less than 5 mm and simultaneously controlling the moisture content of these particles to 50-60%; (iv) composting by naturally stacking the processed kitchen waste for 3-5 days, and when the temperature of the waste compost rises to more than 75 and is no longer increased, processing, after 3-5 days when temperature no longer rises, turning by circulate operation, during the period maintaining the waste at more than 70 degrees C every time by turning until the temperature does not increase.
NOVELTY - Organic bio-fertilizer comprises humic acid, livestock manure, zeolite powder, rice bran, wheat bran and strain, and auxiliary materials comprising oil cake, calcium superphosphate, ammonium phosphate, potassium sulfate, ammonium carbonate, borax, zinc sulfate and brown sugar.    USE - Used as an organic bio-fertilizer.    ADVANTAGE - The composition: is eco-friendly, is of good quality and improves the crop yield by 10-45%; contains organic matter up to 44.5% and the efficient strain of 3.1 billion/g and hence is above the national standard requirements; and eliminates the chemical pollutants. The method is simple and economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the bio-fertilizer comprising: (i) preparing the manure with a total weight of 30% proportion by adding the strain (0.3%), rice bran (1.3%), wheat bran (1.4%), brown sugar (0.15%) and stirring, covering with a film for 24-48 hours, self-fermenting, heating to 70-85 degrees C, maintaining for 0.5-1 hour, cooling, heating, cooling, repeating the same for 2-3 times until the manure is dry, deodorizing and sterilizing; (ii) crushing zeolite powder (0.15%) and ammonium carbonate (0.05%), adding into humic acid and stirring, where the weight of humic acid and zeolite powder are 40% and 10% of the total weight of the finished product and performing stacking fermentation; (iii) adding the stacked humic acid and zeolite powder mixture to the above processed manure, turning to uniform dryness, further crushing to 80-150 meshes; and (iv) adding the auxiliary materials in proportions of oil cake (10%), calcium superphosphate (6%), ammonium phosphate (0.3%), potassium sulfate (0.21%), ammonium carbonate (0.2%), borax (0.07%), zinc sulfate (0.07%), stirring uniformly, granulating, sieving and packaging.
NOVELTY - Composite organic breeding nutrient block having reed residue and cattle manure comprises (in wt.%/100%) dried paper mill waste reed residue (60-85), dried cattle manure (12-40), urea (0.1-2), potassium dihydrogen phosphate (0.1-3), straw decomposition agent (0.1-0.5) and polyacrylamide adhesive (0.1-0.5).    USE - The method is useful for preparing composite organic breeding nutrient block.    ADVANTAGE - The method performs resource recovery of organic waste comprising the reed residue and the cattle manure in paper making factory to prepare the breeding nutrient blocks instead of peat, which is useful for developing the peat resource in protection manner, and changes the waste into treasure, thus it is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the preparation of the composite organic breeding nutrient block, comprising: (i) obtaining (in kg) dried paper mill waste reed residue (600-850), dried cattle manure (120-400), urea (1-20), potassium dihydrogen phosphate (1-30) and straw decomposition agent (1-5), adding them to a stirrer, uniformly mixing them and pouring the mixture to a fermentation pond, adding 100-200 kg of water to a fermentation pond, controlling the moisture content of the mixture to 55-65%, uniformly stirring, using a grass curtain to cover the mixture to perform fermentation for 40-60 days, stirring the mixture once in every 8-12 days until the raw materials are completely fermented and decomposed, where the mixture is gray black, drying, grinding and screening the mixture after complete fermentation, aerating and drying the mixture; and (ii) taking fermentation product (99.5-99.9%) obtained in the step (i) and polyacrylamide adhesive (0.1-0.5%), adding to a stirrer, completely mixing and uniformly stirring and pressing by a nutrient block briquetting machine to obtain the nutrient blocks.
NOVELTY - A peanut fertilizer is produced by mixing (pts. wt.) animal and plant residues (10), monosodium glutamate leftovers (15), dry livestock and poultry excrement (13), organic fertilizer leaven (1), deodorant (1), 46% urea (10), diammonium phosphate (25) having nitrogen (10) and 10-40% phosphorus, 98% potassium chloride (15), calcium carbonate (5), zinc sulfate (1), ferrous sulfate (1), ammonium molybdate (1), magnesium sulfate (1), and borax (1).    USE - Method of producing a peanut fertilizer.    ADVANTAGE - The method produces product having high efficiency and anti-lodging property; and that can be used for a long time, improves soil physicochemical property, and can resist disease, insects and pests.
NOVELTY - A wheat fertilizer is produced by mixing (pts. wt.) animal residue (5), plant straw (10), castor bean cake (10), lees (10), livestock and poultry excrement (14), organic fertilizer (1), deodorant (1), OA soil activating improved agent (2), urea (18), diammonium phosphate (12), potassium sulfate (16), zinc oxide (1), calcium carbonate (0.5), and magnesium sulfate (0.5).    USE - Method of producing a wheat fertilizer for promoting growth.    ADVANTAGE - The method produces fertilizer that can increase soil permeability, promotes development of developed root system, and improves and cultivates soil; that is environment-friendly; and having improved nutrient absorption fertilizer utilization rate and synergistic effect.
NOVELTY - A special fruit tree fertilizer is produced by mixing (pts. wt.) plant straw (8), bean cake (4), lees (10), dried livestock and poultry excrement (3), dried canal mud (5), organic fertilizer (1), monosodium glutamate (4), 46% urea (27), diammonium phosphate (12) having nitrogen (10%) and phosphorus (40%), 51% potassium sulfate (17), zinc oxide (2), calcium carbonate (1), magnesium sulfate (1), deodorant (1) and amino acid waste liquid (4).    USE - Method of producing a special fruit tree fertilizer for inhibiting pathogenic microorganism propagation, enhancing tree stress resistance, reducing diseases and insect pests, or stimulating growth of tree.    ADVANTAGE - The method produces fertilizer that is more natural and environment-friendly, slowly releases fruit needed nutrient elements, can resist flood and drought, improves taste of fruits, improves fruit vitamin content and soluble solids content, extends storage fresh keeping time, and reduces nitrate content.
NOVELTY - Organic-inorganic compound controlled-release fertilizer comprises (wt.%) marine polysaccharide (0.5-10), urea (8-15), calcium superphosphate (10-14), composite salt (6-15), seaweed meal (30-65), and common household organic fertilizers.    USE - Organic-inorganic compound controlled-release fertilizer.    ADVANTAGE - The fertilizer preserves water, and has synergistic effect and long-term effect for sequence fertilization, thus, reducing farmer labor intensity and improving fertilizing efficacy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of controlled-release fertilizer by homogenizing marine polysaccharide, calcium superphosphate, household organic fertilizers, urea, composite potassium salt and algae powder at normal temperature for 10-20 minutes; adding obtained mixture to a granulator, preparing solution of marine polysaccharide (0.3-0.5 wt.%) and seaweed powder (0.2-0.5 wt.%) in water, and spraying the aqueous solution (0.5-5% of mixed material) to the granulator; adding obtained particles to a dryer and controlling inlet temperature at 110 degrees C and outlet temperature at greater than 65 degrees C to ensure strain survival rate; cooling at normal temperature or with cold air until water content of product is less than 8%; grading through rotating sieve to ensure uniform particle size; uniformly spraying aqueous solution of marine polysaccharide (0.3-0.5 wt.%) and seaweed powder (0.5-0.8 wt.%) on surface of particles to form a film layer so that the product is sustained-release and does not form block, and effective viable bacteria further reaches design standard; and metering and packaging.
NOVELTY - Preparation of fermentation agent involves activating production strain in shaking flask, mixing with the same amount of seed culture medium to form seed solution, and inoculating seed solution to a sterilized fermentation medium and aerobically fermenting; and absorbing and fixing fermentation solution to a carrier. The production strain is Bacillus subtilis (CGMCC 1.1200), B. licheniformis (CGMCC 1.520), Rhodopseudomonas palustris (CGMCC 1.2180), Aspergillus niger (CGMCC 3.350), or Candida tropicalis (CGMCC 2.006).    USE - Method for preparing fermentation agent for sludge composting (claimed).    ADVANTAGE - The fermentation agent has short fermentation period, low cost, high device utilization ratio and good deodorizing effect.    DETAILED DESCRIPTION - Preparation of fermentation agent involves activating production strain in shaking flask, mixing with the same amount of seed culture medium to form seed solution, and inoculating the seed solution (5-10 vol.%) to a sterilized fermentation medium and aerobically fermenting at 300 revolutions/minute (rpm), 37 degrees C and pH 7.8 for 12 hours, with ventilation amount of 5-10 L/minute to form fermentation solution; and absorbing and fixing the fermentation solution to a carrier. The production strain is Bacillus subtilis (CGMCC 1.1200), B. licheniformis (CGMCC 1.520), Rhodopseudomonas palustris (CGMCC 1.2180), Aspergillus niger (CGMCC 3.350), or Candida tropicalis (CGMCC 2.006). The fermentation medium has pH of 7.2-7.4 and comprises soluble starch (20 g) or corn powder (30 g), potassium nitrate (1 g), monopotassium sulfate (0.5 g), magnesium sulfate (0.5 g), sodium chloride (0.5 g), ferrous sulfate (0.01 g), humic acid (5 g) and distilled water (1000 ml).
NOVELTY - Production of functional organic fertilizer involves adding fermenting agent to powdered peat, rapeseed residue and Chrysanthemum residue, and uniformly stirring; piling the mixture and fermenting for 8-15 days; turning over the pile, uniformly mixing, and fermenting for 6-12 days; sieving and crushing the large blocks; and adding biological nematicide and uniformly stirring.    USE - Method for producing functional organic fertilizer used for tobacco (claimed) for inhibiting and controlling root-knot nematode.    ADVANTAGE - The method has high fermentation temperature and high effect on organic material decomposition, and completely kills harmful bacteria. The fertilizer improves tobacco quality. The tobacco has high fragrance in the leaf, tender and fresh fragrance, low irritation, and clean and comfortable remaining taste.
NOVELTY - A microbial fertilizer comprises composite microbial fermentation solution embedding medium at pts. vol. ratio of 1:5-1:4. The fermentation solution is formed by compounding culture of Candida, lactic streptococci, Lactobacillus acidophilus and Bacillus subtilis and single culture solution of slow-growth Rhizobium of bean, fat-producing Azospirillum, Rhodopseudomonas palustris, Bacillus megatherium, colloid Bacillus and Azotobacter chroococum.    USE - Microbial fertilizer.    ADVANTAGE - The fertilizer effectively improves permanent planting amount and has improved effect time of the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer which comprises (A) culturing Candida, lactic streptococci, L. acidophilus and B. subtilis through fermentation until total bacteria number is greater than or equal to 1x 109/mL, mixing with slow-growth Rhizobium of bean, fat-producing Azospirillum, R. palustris, B. megatherium, colloid Bacillus and A. chroococum that are cultured to exponential phase, and obtaining fermentation substance of microorganism, in which mixing ratio is that fermentation substance is 40%, and each single culture bacteria is 10%; (B) dissolving (wt.%): sodium alginate (2-3), starch (0.5-1), and gelatin glue (1-2) in water to obtain mixed solution and preparing embedding medium; and (C) adding the microbial fermentation solution to embedding medium, uniformly mixing, adding to calcium chloride solution (0.2 mol/L) under agitating condition, and obtaining desired fertilizer whose particle size is 2-3 mm.
NOVELTY - A retention period of microorganism fertilizer is prolonged by adding molasses and bran to the fertilizer, where added amount of molasses and bran is 2-5 wt.% of total weight of the fertilizer.    USE - Method for prolonging retention period of microorganism fertilizer (claimed).
NOVELTY - The fan has an electric motor (1) arranged in a cylinder of a motor support cylinder (3) and fixed by a fixed component (2). A bearing (5) is arranged on a step unit (6) of a bearing seat supporting cylinder (8). A baffle plate (11) is arranged between the bearing seat supporting cylinder and a main air cylinder (17). A lower part of a main shaft (12) is penetrated through a fan impeller unit (14) and arranged in the main air cylinder. An upper part of the main shaft is passed through a wind shield. A main shaft bearing assembly is connected with an output shaft of the motor by a coupler (4).    USE - Guide fan for a straw gasification furnace.    ADVANTAGE - The fan has temperature resistance, corrosion resistance, prolonged service life and high cleanliness. The fan avoids adhering of tar and smoke dust.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a guide fan.    Electric motor (1)    Fixed component (2)    Motor support cylinder (3)    Coupler (4)    Bearing (5)    Step unit (6)    Bearing seat supporting cylinder (8)    Baffle plate (11)    Main shaft (12)    Fan impeller unit (14)    Main air cylinder (17)
NOVELTY - The furnace has a hearth (2), and a furnace body (1) connected with a feeding hole (3). A bottom part of the furnace body is provided with an ash outlet (4), an inlet pipe (7) and an infrared heating plate (9). A side part of the furnace body is connected with a filter (5). A bottom side part of the furnace body is provided with a through-water outlet (6). The furnace body and the filter are provided with a vent valve (8).    USE - Biomass energy-saving furnace.    ADVANTAGE - The furnace avoids sealing without oxygen, pressure, tar pollution and ensures green and Eco-friendly functions.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass energy-saving furnace.    Furnace body (1)    Hearth (2)    Feeding hole (3)    Ash outlet (4)    Filter (5)    Through-water outlet (6)    Inlet pipe (7)    Vent valve (8)    Infrared heating plate (9)
NOVELTY - A biomedicine fertilizer is produced by (A) pre-processing bio-residue and obtaining sterile culturing material; (B) inoculating Bacillus thuringiensis in sterile culturing material and performing solid fermentation for 8-11 hours, using initial fermentation temperature of 2-5 degrees C, and fermenting for 35-50 hours; and (C) drying and crushing fermentation material, adding chitosan oligosaccharide powder, and obtaining desired fertilizer product.    USE - Method for producing biomedicine fertilizer (claimed) for killing pest, inhibiting virus, adjusting plant metabolism and accelerating plant growth.    ADVANTAGE - The method has low cost, simple technique, little device investment and environment-friendly production process.
NOVELTY - Typhonium giganteum extract, obtained by supercritical fluid extraction and its extraction, are claimed. The supercritical parameters are as follows: carbon dioxide is an extraction solvent, the flow rate of carbon dioxide is 10-20 l/hour; the pressure range of an extraction kettle is 30-45 MPa and the temperature is 40-50?0C; the pressure of a separation kettle is 5-15 MPa and the temperature is 40-50 degrees C; 100 ml of 80% ethanol is pumped as a cosolvent every 50 minutes; the total extraction time is 4 hours. A blackish green oily extract is obtained in the separation kettle.    USE - The extract is useful for inhibiting cancer cells, e.g. colon cancer HCT-116, ovarian cancer HO-8910, stomach cancer SGC-7901, liver cancer BEL-7402 and liver cancer SMMC-7721 (all claimed).    ADVANTAGE - The method: has high extraction selectivity, has rapid extraction speed, causes no pollution of the extract, and is simple, convenient and environment friendly.    DETAILED DESCRIPTION - Typhonium giganteum extract, obtained by supercritical fluid extraction and its extraction, are claimed. The supercritical parameters are as follows: carbon dioxide is an extraction solvent, the flow rate of carbon dioxide is 10-20 l/hour; the pressure range of an extraction kettle is 30-45 MPa and the temperature is 40-50?0C; the pressure of a separation kettle is 5-15 MPa and the temperature is 40-50 degrees C; 100 ml of 80% ethanol is pumped as a cosolvent every 50 minutes; the total extraction time is 4 hours. A blackish green oily extract is obtained in the separation kettle. A gas chromatography mass spectrometry (GC-MS) analysis indicates that the extract contains beta -sitosterol and campesterol as main ingredients.
NOVELTY - The furnace has a water tank connected with a hopper through a pipeline (4). An upper circulating pipe (6) and a lower circulating pipe (7) are connected with a secondary body (11). A main furnace cavity is connected to a smoke pipe (15) by the pipeline and a valve. The valve is connected to a combustion cooking range (18) and a burning furnace head (20). An air filter tank is connected to a combustion stove through a connecting pipe (13). A secondary stove body cavity is connected to an exhaust pipe by a connecting pipe. A filter tank (21) is provided with a clapboard.    USE - Straw gas integrative furnace.    ADVANTAGE - The furnace improves combustion and heat efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a straw gas integrative furnace.    Pipeline (4)    Upper circulating pipe (6)    Lower circulating pipe (7)    Secondary body (11)    Connecting pipe (13)    Smoke pipe (15)    Combustion cooking range (18)    Burning furnace head (20)    Filter tank (21)
NOVELTY - Method for preparing pellet using food waste compost, involves washing the compost using water to minimize the salinity of the compost, pulverizing the compost, dehydrating the compost, subjecting the compost to freeze-drying process, removing greasiness from the product, mixing the product with red clay, drying the mixture, and compressing the dried mixture into pellet.    USE - The method is useful for preparing pellet which is useful for preventing damage of crops by animals and insects (claimed).    ADVANTAGE - The method prepares pellet easily by utilizing food waste, and the pellet does not cause soil acidification.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pellet, which is obtained by the above-mentioned method.
NOVELTY - Nutrient biological fertilizer comprises (in parts weight): plant activin, biological liquid extract of monocotyledon and dicotyledon plant enzymes (18-20), biological liquid extract of plant flavone (18-20), biological liquid extract of seaweed mineral substance (18-20), biological liquid extract of plant nucleic acid (18-20), biological liquid extract of plant basic polysaccharide (18-20), acetic acid bacteria (1-3), Saccharomyces (1-3), lactic acid bacteria (1-3), sugar (6-8) and sugar water (6-8).    USE - The nutrient biological fertilizer is useful for plants producing fruits.    ADVANTAGE - The biological fertilizer activates soil, removes hardened soil, and reduces use of agrochemical and chemical fertilizer to improve quality of fruits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned fertilizer, which involves (a) preparing the above-mentioned liquid raw materials, mixing the materials in a mixer for 30 minutes, and transferring the mixture to fermentation tank, (b) dividing the mixture into two parts, filling the mixture in two containers, adding and mixing (in parts) acetic acid bacteria (1-3) to one container to obtain aerobic bacteria biological liquid, and adding Saccharomyces and lactic acid bacteria to the other container to obtain anaerobe biological liquid, (c) filling the aerobic bacteria biological liquid to the fermentation tank filled with mixed biological liquid, completely mixing the mixture, fermenting the mixture anaerobically at 45 degrees C or more, opening the tank, radiating the product, and biologically fermenting the product for 6-12 hours to obtain fermented product, (d) adding the anaerobic biological liquid prepared in the second (b) to the fermented product, completely mixing the mixture, anaerobically fermenting the product at 25-39 degrees C for 7-11 days, and packaging the product.
NOVELTY - Production of lightweight organic matrix involves crushing Eucalyptus bark and adding water until water content reaches 60%; adding nitrogen source, chicken manure and urea to regulate carbon/nitrogen ratio to 45:1; adding effective microorganisms (EM) microbial inoculum and enzymes with pile body volume ratio of 0.2%; repeatedly pile turning for fermentation; air-drying until water content is less than 12%; and crushing, bagging according to particle size, and storing.    USE - Method for producing lightweight organic matrix used for seedling and flower planting (claimed).
NOVELTY - A liquid fertilizer contains (pts. wt.) organic fertilizer (5-8), yeast (3-5), and waste vegetable leaves (90-95). The organic fertilizer comprises (wt.%) modified zeolite (5-8), brown sugar (0.5-1), rice bran (8-10), phosphate ore powder (8-10), lignite fine powder (45-55), and chicken or duck manure (balance).    USE - Liquid fertilizer.    ADVANTAGE - The liquid fertilizer kills pathogenic bacteria in the soil; improves softness, ventilation, water-holding capacity, fertilizer-holding capacity, drought resistance, dryness resistance, ground temperature and fertility of the soil; prevents continuous crop disease; controls pest disease; stably increases yield; and improves quality and mouthfeel of agricultural product.    DETAILED DESCRIPTION - A liquid fertilizer contains (pts. wt.) organic fertilizer (5-8), yeast (3-5), and waste vegetable leaves (90-95). The organic fertilizer comprises (wt.%) modified zeolite (5-8, preferably 6-7), brown sugar (0.5-1, preferably 0.8-1), rice bran (8-10, preferably 9-10), phosphate ore powder (8-10), lignite fine powder (45-55, preferably 50-52), and chicken or duck manure (balance). The organic fertilizer is prepared by grinding zeolite into 180-220 mesh powder and fermenting at 280-320 degrees C for 5-6 hours to obtain modified zeolite powder; and uniformly mixing modified zeolite powder with other materials, stacking, and maintaining temperature at 60-70 degrees C in first and second days, at 30-40 degrees C in third and fourth days, and at normal temperature in fifth and sixth days. An INDEPENDENT CLAIM is included for preparation of liquid fertilizer by mixing yeast, waste vegetable leaves and organic fertilizer, storing in fermentation tank in the field, sealing opening of tank with plastic thin film, fermenting for 13-17 days, and withdrawing fertilizer when material in the tank is converted into liquid.
NOVELTY - A biological organic fertilizer comprises (wt.%) modified zeolite (5-8), brown sugar (0.5-1), rice bran (8-10), phosphorite powder (8-10), brown coal fine powder (45-55), and chicken manure or duck manure (balance).    USE - Biological organic fertilizer used in vegetables.    ADVANTAGE - The fertilizer utilizes raw material having wide resource and which are safe, and can achieve high yield of agriculture produce. The vegetables applied with the fertilizer can be harvested 7 days earlier in comparison with the vegetables which are planted with the same method and are not applied with the fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising:    (A) milling zeolite into powder with granularity of 180-220 meshes, and fermenting at 280-320 degrees C for 5-6 hours to obtain modified zeolite;    (B) mixing the modified zeolite powder with the other materials;    (C) piling and maintaining temperature at 60-70 degrees C in the first and second days;    (D) maintaining temperature at 30-40 degrees C in the third and fourth days;    (E) maintaining constant temperature in the fifth and sixth days to obtain the fertilizer; and    (F) packaging the fermented fertilizer.
NOVELTY - An organic selenium-enriched biological fertilizer comprises (wt.%) animal manure (10-40), straw powder or rotten soil (20-50), selenium ore powder (20-40) containing 50 ppm of selenium of 80 meshes, microorganism soil repairing agent (0.02-0.07), and zymophyte (0.01-0.03).    USE - Organic selenium-enriched biological fertilizer used in plants.    ADVANTAGE - The fertilizer utilizes microorganism to completely rot the raw material containing various nutritive components at high temperature and to convert the inorganic selenium into organic selenium which is absorbed by the plant and animal, thus producing selenium-enriched organic product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, comprising uniformly and completely stirring the raw materials, stacking and fermenting, and turning once every other day when the temperature is 40 degrees C, turning when the temperature is 65 degrees C and the hypha appears, stacking and fermenting for three days, grinding, sieving, packaging and storing.
NOVELTY - An amino acid plant nutrient solution is produced by extracting mycelium from the waste solution of fermented monosodium glutamate, evaporating, concentrating, crystallizing, filtering to obtain ammonium sulfate and concentrated liquor, treating concentrated liquor with calcium oxide and liquid ammonia, fixing sulfate radical, and regulating pH.    USE - Method of producing an amino acid plant nutrient solution.    ADVANTAGE - The method converts wastewater into amino acid plant nutrient solution thus reducing pollution.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of a method of producing an amino acid plant nutrient solution. Drawing includes non-English language text.
NOVELTY - A microbial organic fertilizer is produced by drying abamectin waste residue to control moisture content at less than or equal to 30%, and crushing; fermenting Bacillus subtilis, Bacillus megaterium and Bacillus mucilaginosus; adding powdered rice hulls to adsorb fermented bacteria liquid; mixing the three adsorbed single fungicides at a mass ratio of 0.1-8:0.1-4:0.1-4; crushing; adding composite microorganism bactericide (2-15 wt.%) to the powder waste residue; and mixing.    USE - Method of producing microbial organic fertilizer.    ADVANTAGE - The method is simple, can be applied to large scale production, and utilizes waste thus reducing pollution.
NOVELTY - Microbial organic fertilizer is obtained by fermenting, pelleting and drying traditional Chinese medicinal dreg sludge (60), animal excrement (25), crop straw powder (10), acid free lignin (1), acidity regulator (1), pelleting adhesive (2), and microorganism leaven (1). The acidity regulator is calcium oxide, coal ash or calcium magnesium phosphate fertilizer.    USE - The microbial organic fertilizer is useful for equilibrating absorption of nitrogen, phosphorus potassium, improving soil and crop quality, and stress resistance of crop, and promoting maturation and yield of the crop.    ADVANTAGE - The fertilizer causes no pollution, and is environmentally-friendly and has high-efficient, abrasion resistant, broad spectrum activity, improved long residual activity, uniform particles, and glossiness.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the microbial organic fertilizer, which involves (a) (i) passing the condensate of traditional Chinese medicinal dreg sludge to a drier, and (ii) drying and treating the sludge using hot air (90-130 degrees C) until the water content of the sludge is 35-45%, where the air quantity is 5000-8000 m3/hour, (b) (i) adding animal excrement, crop straw powder and acidity regulator to the dried traditional Chinese medicine dreg sludge to obtain mixture, (ii) adjusting pH of the mixture to be 6.0-7.5, (iii) then adding the microorganism leaven to the mixture, and (iv) continuously fermenting the mixture for 7-8 days in fermentation pool under oxic conditions, and (c) (i) finishing the fermentation process, (ii) adding the pelleting adhesive to fermented mixture, (iii) pelleting and drying until the water content is reduced to 18-20%, where drying temperature is 70 degrees C, and air quantity is 6000 m3/hour, and (iv) packaging the dried pellets after weighing the dried pellets.
NOVELTY - An organic fertilizer liquor comprises livestock manure, microorganism fungicide and water having a weight ratio of 100:0.4-0.6:400-600.    USE - An organic fertilizer liquor.    ADVANTAGE - The liquor solves problem of live stock manure pollution to the environment, can be stored and transported conveniently, and allows easy fertilizer application.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the organic fertilizer liquor comprising adding microorganism fungicide and water into livestock manure, sealing the mixture, regulating the temperature at 30-40 degrees C, fermenting for 7-10 days, heating fermented product at 55-65 degrees C for 7-10 days, subjecting to ultrasonic treatment, centrifuging, subjecting supernatant to sand leaching treatment to obtain concentrated solution having macromolecular organic matters, and filling into the bottle.
NOVELTY - A compound organic fertilizer is manufactured by mixing fresh human excrement and bean cake at a ratio of 3-5:1.5-2.5, naturally retting at 20-40 degrees C for 30-60 days, insulating for 5-45 days under strong sunlight, crushing, mixing plant ash and black alum at a weight ratio of 9-11:1-2:1-2, and stirring the mixed materials for 3-5 minutes to obtain the compound organic fertilizer.    USE - A compound organic fertilizer for foliage potted plant when planting, changing soil and topdressing (claimed).    ADVANTAGE - The raw materials are easy to obtain and the cost is low; moreover. The manufacturing method and the operation are convenient and the manufacturing cost is low.    DETAILED DESCRIPTION - A compound organic fertilizer is manufactured by collecting fresh human excrement and eliminating the impurities; and crushing peanut cake, sesame cake, or bean cake and screening in 1-2 mm. The fresh human excrement is mixed with the bean cake at a ratio of 3-5:1.5-2.5 for 3-5 times. All the materials are stacked and covered by plastic film. Natural retting is carried out at 20-40 degrees C for 30-60 days. The materials are arranged on the hard floor with the thickness of 4-6 cm, and insulated for 5-45 days under strong sunlight. Stirring is conducted each 3-5 days. The materials are prevented from stir and water. The materials are arranged in a grinder and 0.5-2 mm screen. The plant ash is mixed with black alum at a weight ratio of 9-11:1-2:1-2. The mixed materials are stirred for 3-5 minutes to obtain the compound organic fertilizer.
NOVELTY - A tea tree fertilizer comprises (pts. wt.) chicken manure (60-79), hot pepper extraction (11-29), zeolite powder (2-5), rotten agent (0.05-1), and furfural slag (50-65).    USE - A fertilizer for tea tree (claimed).    ADVANTAGE - The fertilizer has simple technology and convenient manufacture, and can improve soil environment and potential of hydrogen and increase nitrogen content of fertilizer, which is helpful for crop growth.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer comprising mixing chicken manure and hot pepper extract with a blender and processing water detection, requiring the water in 57-62% to prepare a primary mixture; mixing rotten agent and plant powder at a ratio of 1:9 and at 0-35 degrees C, and storing for 3-12 hours to prepare secondary mixture; and mixing the mixtures.
NOVELTY - Non-woven fabric container nursery biotype matrix comprises matrix host material comprising (pts.wt.) peat (20-30), straw fermenting materials (20-30), earthworm excrement (5-10), pearlite (15-25), vermiculite (5-10), and special solid biological microbial inoculum (8-12); and fertilizer comprising calcium superphosphate and controlled-release fertilizer. The biotype matrix comprises 0.3-0.8% calcium superphosphate and 0.8-1.5% controlled-release fertilizer based on weight of matrix host material.    USE - Non-woven fabric container nursery biotype matrix.    ADVANTAGE - The biotype matrix can be assorted with greenhouses, plastic tents and electronic automatic spraying apparatus. It relieves roots by air, prolongs afforesting duration and improves soil. It is advanced by good root cultivation, wide application scope, has very strong application and promotion value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of non-woven fabric container nursery biotype matrix by air-drying peat, straw fermenting material, and earthworm excrement; controlling water contents of peat and straw fermenting material at less than 15% and that of earthworm excrement at less than 25%; sieving them to grain diameter of less than 10 mm; adding all other raw materials; and mixing uniformly.
NOVELTY - An organic fertilizer comprises (units no given): earthworm manure (35-40), pulverized maize straw (25-30), wood dust (28-30) and vermiculite (8-10).    USE - Organic fertilizer for reducing disease incidence of cucumber knot nematode (claimed).    ADVANTAGE - The fertilizer can be directly acted as the base fertilizer of the cucumber. It can relieve the harm of cucumber knot nematode. The disease incidence can be reduced by 79.4%. The yield of cucumber can be improved by 34.4%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer which comprises providing earthworm manure, pulverized maize straw, wood dust and vermiculite, where length of pulverized maize straw is 3-4 cm; fully and uniformly mixing maize straw, wood dust and vermiculite, wetting by water until water content of the stacked fertilizer is 50-60%; stacking pulverized maize straw, wood dust and vermiculite in plastic shed or outside, and adding fermentation bacterial agent to ferment; and uniformly mixing totally fermented maize straw, wood dust and vermiculite mixture with earthworm manure, pulverizing, drying and packaging to obtain the product.
NOVELTY - An energy-saving environment-friendly liquid organic fertilizer comprises (pts. mass): solid leavening (8-12), soil (1-3) and liquid leavening (30-50).    USE - Energy-saving environment-friendly liquid organic fertilizer.    ADVANTAGE - The fertilizer has easy to obtain raw material resource and simple preparation. It does not need to evaporate or dry, has low energy consumption, convenient and uniform fertilization, labor conversation, time conversation, low production cost and good fertility effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer which comprises putting all solid leavening to bottom layer in the enclosed space; adding soil and uniformly stirring; pouring liquid leavening, submerging solid leavening and soil and enclosing space; opening enclosed space each 5-8 days, stirring liquid leavening, solid leavening and soil uniformly and enclosing space again; and obtaining desired fertilizer after 25-35 days starting from stocking.
NOVELTY - A higher fatty acid ester ether compound comprises higher fatty acid and ester ether compound as raw materials.    USE - Higher fatty acid ester ether compound for biological diesel oil and additives.    DETAILED DESCRIPTION - A higher fatty acid ester ether compound comprises higher fatty acid and ester ether compound as raw materials. The higher fatty acid ester ether compound is of formula R1COO(CH2CH2O)xCyH(2y+1) (I) or R1COO(C(CH3)H2CH2O)xCyH(2y+1) (II).    R1=saturated fatty acid including positive-CH3(CH2)12-, positive-CH3(CH2)14-, positive-CH3(CH2)16-, positive-CH3(CH2)18-, positive-CH3(CH2)20-, positive-CH3(CH2)22-, positive-CH3(CH2)24-, positive-CH3(CH2)26, or unsaturated fatty acid including CH3(CH2)5CH=CH(CH2)7-, cis-CH3(CH2)7-CH=CH(CH2)7-, trans-CH3(CH2)5CH=CH(CH2)9-; trans-CH3(CH2)4CH=CHCH2CH=CH-; (CH2)7-; CH3CH2CH=CHCH2CH=CHCH2CH=CH-(CH2)7-, trans, trans, trans-CH3(CH2)4-CH=CHCH2CH=CHCH2CH=CH(CH2)4-, trans, trans, trans, trans-CH3(CH2)4(CH=CHCH2)3, or -CH=CHCH2CH=CH(CH2)3-; and    a, x, y=1-10, preferably 1-6.
NOVELTY - The method involves mixing animal waste with organic municipal waste to obtain mixtured waste. The mixtured waste is subjected to a pre-composting process in a bioreactor until completion of a hygienization process.    USE - Method for manufacturing an organic fertilizer from organic waste such as animal waste and organic municipal waste.
NOVELTY - A microbial organic fertilizer is produced by taking oil shale as raw material comprising oil shale powder and organic material, where water content is 40-65%; putting total materials to stirrer and stirring, adding water and uniformly stirring; adding 1-5% fermenting agent, uniformly stirring, transporting to fermenting tower, ventilating and fermenting; ventilating once every hour, each time for 5 minutes when air temperature is lower than 15 degrees C, and accessing hot wind; and after fermenting, adding functional bacterium solution (3-15% of total material).    USE - Method for production of microbial organic fertilizer (claimed) used for rice crops, vegetables and fruit trees including wheat, corn, cucumber, cabbage and apple.    ADVANTAGE - The method can increase wheat yield to 16.8-19.3%, corn yield to 17.1-21.6%, cucumber yield to 15.1-18.4%, cabbage yield to 14.6-17.8% and apple yield to 15.3-17.8%. It also can improve crops quality and increase apple soluble solid matter to 7.6-8.3%.
NOVELTY - A fertilizer is produced by crushing wheat straw to 100 meshes and mixing ammonium bicarbonate at wt ratio of 10:1, adding water, when external temperature is 20 to 30 degrees C, fermenting for 1 month in sealing, and crushing other raw materials into 100 meshes; drying fermented wheat straw in drying chamber, and obtaining fermented powder; mixing fermented powder, crushed phosphatic fertilizer and urea at ratio of 22:2:1, mixing, and obtaining semi-finished product; and adding 2-3% control release preparation in semi-finished product, and pelleting by fertilizer pelleting machine.    USE - Method for producing fertilizer (claimed).    ADVANTAGE - The method fully uses large amount of straw resource such as wheat straw, thus efficiently utilizing resource materials. The fertilizer has the ability of the ordinary fertilizer and can compensate necessary elements for plant, such as iron, copper, zinc, manganese, molybdenum and boron.
NOVELTY - Method (M1) for producing feed additive using food waste, involves separating food waste from primary effluent of wastewater treatment, reducing salt content of obtained product, removing foreign substances from the obtained product, breaking the food waste to small particles, heat treating the obtained particles, again removing the foreign substances from obtained product, separating dehydrating liquid from the obtained food waste, dehydrating the food waste, and compressing the dehydrated food waste to obtain the product.    USE - The method is useful for producing feed additive and liquid fertilizer using food waste.    ADVANTAGE - The method is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - Method (M1) for producing feed additive using food waste, involves separating food waste from primary effluent of wastewater treatment, filtering the obtained product, reducing salt content of the obtained product by filtering the obtained food waste in lower portion of storage tank, removing foreign substances from the obtained product, passing the obtained food waste through net having 15-25 mm mesh for breaking the food waste to small particles, heat treating the obtained particles at 90-100 degrees C for 5-30 minutes, passing the heat treated food waste through net having 6-10 mm mesh, again removing the foreign substances from the obtained product, separating dehydrating liquid from the obtained food waste, dehydrating the food waste, and compressing the dehydrated food waste to obtain the product. An INDEPENDENT CLAIM is included for method (M2) for producing liquid fertilizer, which involves fermenting the dehydrating liquid obtained in method (M1) using microorganism in liquid fertilizer tank.
NOVELTY - Producing organic liquid bacterial fertilizer with kitchen waste liquid, comprises providing a strain, cultivating and activating the strain, preparing bacterial liquid formulation and propagating the strain.    USE - The method is useful for producing organic liquid bacterial fertilizer with kitchen waste liquid.    ADVANTAGE - The method: does not produce waste gas, waste liquid and waste residue, thus there is less environmental hazard; reuses the organic matter in waste water to save waste water processing cost; and is environmental friendly.
NOVELTY - A brown azotobacter microbial bacterial fertilizer is prepared by (A) preparing bacterial suspension, (B) fermenting and composting, and (C) preparing bacterial fertilizer. The step (A) includes preparing brown azotobacter into 60-80 hundred million/ml of bacteria suspension. The step (B) includes fermenting (pts. wt.): farmyard manure (60-70), straw powder (20-30), adsorbent (4-6), calcium superphosphate (2-3) or monopotassium phosphate (1.5-2.5), and water (1-2). The step (C) includes fermenting compost (90-95), sugar (0.5-1.5), sterilizing water (5-7), and bacterial suspension (0.3-1-2).    USE - Method for preparation of brown azotobacter microbial bacterial fertilizer (claimed).    ADVANTAGE - The prepared fertilizer has high efficiency, and can effectively increase product of crops. It is convenient and is suitable for forage grasses. The annual yield of ryegrass can be 5000-5500 kg/667m2. The amount of beneficial bacteria is 151 hundred million/g, where amount of brown azotobacter can be 7x 108 piece/g.    DETAILED DESCRIPTION - Brown azotobacter microbial bacterial fertilizer is prepared by (A) preparing bacterial suspension, (B) fermenting and composting, and (C) preparing bacterial fertilizer. The step (A) includes preparing brown azotobacter into 60-80 hundred million/ml of bacteria suspension. The step (B) includes taking (pts. wt.): taking solid farmyard manure (60-70), adding straw powder (20-30), adsorbent (4-6), calcium superphosphate (2-3) or monopotassium phosphate (1.5-2.5), water (1-2), uniformly mixing, and fermenting for 3-4 days at 60-70 degrees C to obtain compost. The step (C) includes taking (pts. wt.): compost (90-95), sugar (0.5-1.5), sterilizing water (5-7), bacterial suspension (0.3-1-2), uniformly mixing, fermenting for 5-6 days at 25-30 degrees C, and drying to obtain product.
NOVELTY - A fertilizer is produced by extracting neutral oil from plant oil residue, adding plant ash and ammonium bicarbonate, thoroughly stirring averagely to ferment in piles or in fermentation pool, and post-processing to obtain product. The post-processing includes pelleting, drying and sterile processing.    USE - Method for producing fertilizer (claimed).    ADVANTAGE - The method turns oil residue of plant oil factory to valuable material, thus transferring pollution to beneficial material, and meets environmental friendly theme of saving energy and resource. It has simple process and low production cost. The composite feed obtained using the method meets agricultural department industrial standard NY525-2002.
NOVELTY - A composite biofertilizer comprises (%) organic matter (30-40), plant straw (15-25), mixed fermented biological strain liquor (14-15), and inorganic nutrient (30-31). The mixed fermented biological strain comprises mixed fermentation product comprising (%) Rhodopseudomonas palustris (2-4), saccharomycetes (1-2), nitrogen-fixing bacteria (3-5), phosphorus-decomposing Bacillus megaterium (3) and silicate bacteria (3) in exponential phase.    USE - Composite biofertilizer used for crops.    ADVANTAGE - The biofertilizer can improve physical and chemical property of soil and yield and quality of agricultural product. It is suitable as base fertilizer or additional fertilizer. The yield of agricultural product is increased by 8-10%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the composite biofertilizer, comprising crushing 15-25 wt.% aired plant straw, and then adding organic matter, saccharomycetes fermentation liquor and Rhodopseudomonas palustris fermentation liquor, fermenting for 3-4 days at 30-40 degrees C, and then adding phosphorus-decomposing bacteria, nitrogen-fixing bacteria and silicate bacteria, continuously fermenting for 1-2 days at 25-30 degrees C, and finally adding inorganic nutrient to obtain the composite biofertilizer.
NOVELTY - A plant oil ester ether biodiesel comprises plant oil, ester ether (I) and n-procetane (II).    USE - Plant oil ester ether biodiesel as fuel of normal diesel oil, and additive of discharging performance (claimed).    ADVANTAGE - The biodiesel has better discharging performance and combustion performance than traditional plant oil methyl ester, ethyl ester biodiesel, and can replace fuel independently.    DETAILED DESCRIPTION - A plant oil ester ether biodiesel comprises plant oil, ester ether of formula R1COO(CH2CH2O)xCyH2y+1 (I) and n-procetane of formula R1COO(C(CzH2z+1)HCH2O)xCyH2y+1 (II).    R1=hydrocarbon in plant oil fatty acid with unsaturated double-bonds;    x, y=1-6;and    z=1-2.    Provided that when x is 1, y is greater than 2.
NOVELTY - A composition for stabilizing reduction of weight contains (in parts weight) paraffin-based material (100), hydroxide-based material (5-50), carbonate-based material, silica-based material (20-200), and dry Artemisia princeps Pampanini (1-10) or acetic acid (1-10).    USE - Composition for stabilizing reduction of weight used for fuel recycling promotion composition for manufacturing solid sludge (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel recycling promoting composition, which includes the composition (100) for stabilizing reduction of weight and primarily promoting material (50-200); and    (2) manufacture of solid sludge.
NOVELTY - The system has a precipitating bath (10) that precipitates excrements and wastewater. An aeration bath (20) biologically decomposes the wastewater from the precipitating bath using microorganism. A de-coloring and de-odoring bath (30) decolorizes and deodorizes the wastewater from the aeration bath. A processed water storing bath (40) stores processed water from the de-coloring and the de-odoring bath. The processed water is circulated to a toilet.    USE - Self purifying and sterilizing system for bathroom.    ADVANTAGE - The wasted water from the bathroom can be purified using the precipitating bath, aeration bath, de-coloring and de-odoring bath and processed water storing bath. The replacement of the filter medium can be facilitated. The biodegradation of the aerobic microorganism can be accelerated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the self purifying and sterilizing system.    Precipitating bath (10)    Aeration bath (20)    De-coloring and de-odoring bath (30)    Processed water storing bath (40)    Counter (61)
NOVELTY - The system has driven shaft (4) and driving shaft (3) that are installed at fixed bearing connected with scraper support plate (2). A chain (6) is installed in chain sprocket (5) of driven shaft and driving shaft. Multiple scrapers (7) with supporting plate (71) and conveying plate (72) is fixed to chain with pin.    USE - Agitation system for compost manufacture system.    ADVANTAGE - The productivity is improved while manufacturing cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the agitation system.    Scraper support plate (2)    Driving shaft (3)    Driven shaft (4)    Chain sprocket (5)    Chain (6)    Scraper (7)    Supporting plate (71)    Conveying plate (72)
NOVELTY - A straw rotten agent comprises (billion/g) Bacillus subtilis (0.2-1.5), Bacillus licheniformis (0.2-1.5), Sporotrichum thermophile (0.02-0.15), Trichoderma koningii (0.02-0.15), and Phanerochaete chrysosporium (0.02-0.15).    USE - A straw rotten agent.    ADVANTAGE - The agent is short, can be used conveniently, and has short rotten time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of rotten straw comprising crushing straw (15 kg); layering the crushed materials at a thickness of 3 cm; mixing B. subtilis, B. licheniformis, S. thermophile, T. koningii, and P. chrysosporium; spreading the mixture on the layered materials; setting aside for 10 days; and plowing.
NOVELTY - The system has pre-heating unit (200) that pre-heats livestock excreta introduced into a livestock excreta introducing unit, at temperature between 52-55 degrees C. A high temperature fermenting unit (300) circulates and ferments the livestock excreta. A gas storing unit (500) collects and stores methane and carbon dioxide gas. An electricity generating unit (600) combusts methane and generates electricity.    USE - Eco-friendly system for generating biogas.    ADVANTAGE - Since the high temperature fermenting unit ferments livestock excreta and electricity generating unit combusts methane and generates electricity, wastage of resources can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the eco-friendly system for generating biogas.    Pre-heating unit (200)    High temperature fermenting unit (300)    Desulphurization unit (400)    Gas storing unit (500)    Electricity generating unit (600)
NOVELTY - The system has autonomous distributed control parts (4a, 4b) connected with a fuel cell (5a). A power distribution system is utilized for accommodating electric power. The electric power produced by the fuel cell is supplied to the power distribution system. A hydrogen-producing part (6a) produces hydrogen. A hydrogen accommodation system provides hydrogen accommodation system information. The hydrogen-producing part provides hydrogen producing part information.    USE - Fuel cell control system for a personal computer and a mobile telephone.    ADVANTAGE - The electric power produced by the fuel cell is supplied to the power distribution system, so that reliability of the system can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell control system.'(Drawing includes non-English language text)'    Autonomous distributed control parts (4a, 4b)    Fuel cell (5a)    Hydrogen-producing part (6a)
NOVELTY - The apparatus has a waste inlet provided at the upper side of transferring pipe (10), and outlet is provided at one end of the transferring pipe. The wastes are transferred in longitudinal direction to the transferring pipe. The screws (22,23) are arranged is parallel to the longitudinal direction in the transferring pipe. A specific screw is arranged at the lower side of screws. Several through holes are formed in a perforated plate (30), and the compressed wastes are discharged through the through holes. The perforated palate is arranged at the outlet.    USE - Solid fuel molding apparatus.    ADVANTAGE - The stirring efficiency and the productivity of the apparatus are improved by changing the arrangement and the number of screws. The improved working dependability and excellent space conjugation capability can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the solid fuel molding apparatus.    Transfer pipe (10)    Screws (22,23)    Perforated plate (30)    Cutter (40)    Driving unit (50)
NOVELTY - The method involves mixing circulating waste water with effluent which is nitrogen and residual oxygen gas rich in dissolved oxygen using multiple ejector type mixers (20,50) under pump dispensed pressure of 0.5-4 kg/cm2. The circulating waste water having dissolved oxygen concentration is supplied to an upper layer of bioreactor (10). The effluent is supplied to a blower and discharged to microorganism lower end of bioreactor during suction mixing and discharge process of effluent.    USE - Method for treating organic waste water from livestock excretions, food factory, or farming and fishing villages.    ADVANTAGE - The effluent can be purified effectively by naturally supplying oxygen to the organic waste water. High concentration organic waste water treatment can be achieved by maximizing the supply of oxygen in the effluent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for disposing organic waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the treatment process of organic waste water.    Apparatus (1)    Bioreactor (10)    Ejector type mixers (20,50)    Pressurized circulating pump (30)    Discharge tube (32)    Pressure cyclone (40)
NOVELTY - Bio-sludge organic fertilizer with double-layer structure comprises inner layer and an outer layer, where the fertilizer is present in granular form. The inner layer comprises 6-15wt.% of Ganoderma lucidum fungus and 1-5wt.% of Bacillus. The outer layer comprises 6-15wt.% of giant Bacillus.    USE - Bio-sludge organic fertilizer with double-layer structure.    ADVANTAGE - The bio-sludge organic fertilizer with double-layer structure can convert sludge into organic fertilizer with improving nutritional activity of soil, where the fertilizer can reduce side effect of the chemical fertilizer and improve plants growth with economic and environmental benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing bio-sludge organic fertilizer with double-layer structure, which involves:    (A) fermenting sludge and measuring water content of fermented sludge, where water content is regulated to 8-18%;    (B) adding Ganoderma lucidum fungus and giant Bacillus agents in the fermented sludge with regulated water content; and    (C) processing particles by a granular machine to obtain dual-layer structure, where the inner layer comprises 6-15wt.% of Ganoderma lucidum fungus and 1-5wt.% of giant Bacillus, and the outer layer comprises 6-15wt.% of giant Bacillus.
NOVELTY - Compost comprises organic matter (35-45wt.%), total carbon content (18-35wt.%), total nitrogen content (1-2.5wt.%), carbon-nitrogen content (12-20), phosphorus pentoxide (7500-12000mg/kg), potassium oxide (7000-12500mg/kg), calcium oxide (17000-25000mg/kg) and magnesium oxide (3000-5900mg/kg), where pH of compost is 7.0 plus minus 0.6.    USE - Compost used for manufacturing fertilizer or substrate for plant growth (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing compost, which involves using mixture of components including residual ash that is obtained from combustion of biomass and performing aerobic digestion.
NOVELTY - Apparatus for processing livestock excretion, comprises mixer, hopper, cylinder, cylinder fixing block, pressure screw, baffle plate, extrusion die, extrusion die cartridge for fixing extrusion dies to be replaceable to each other, and cutter for cutting the extruded livestock excretion processed products.    USE - The apparatus is useful for processing livestock excretion to produce livestock excretion processed product, preferably fertilizer.    ADVANTAGE - The apparatus reduces environmental contaminations caused by livestock excretion, and can be installed and managed easily.    DETAILED DESCRIPTION - Apparatus for processing livestock excretion (1), comprises mixer (20) for mixing additives with livestock excretion, hopper (30) for supplying livestock excretion mixture, cylinder (40) for pressurizing livestock excretion mixture, cylinder fixing block (50), in which the cylinder is fitted and fixed on the upper side of a supporting board (10), pressure screw (60), which is installed in an inner pressurization space of the cylinder, and pressurizes and transfers the livestock excretion mixture to a discharge side end portion, baffle plate (70) installed at the discharge side end portion of the cylinder, an extrusion die (80) for extruding the livestock excretion mixture passing through a rectifying plate to livestock excretion processed products, extrusion die cartridge (90) for fixing extrusion dies to be replaceable to each other, and cutter (100) for cutting the extruded livestock excretion processed products.    DESCRIPTION OF DRAWING(S) - The figure shows plane view of apparatus for processing livestock excretion.    Livestock excretion (1)    Supporting board (10)    Mixer (20)    Hopper (30)    Cylinder (40)    Cylinder fixing block (50)    Pressure screw (60)    Baffle plate (70)    Extrusion die (80)    Extrusion die cartridge (90)    Cutter (100)
NOVELTY - The device has a draught fan (13) connected with an upper part of an air-cooling pipe (9). An outlet of a second-stage cooling gas conveying pipe (10) is connected with an upper part of a pipe for connecting a tar filter (11) and a tar reflowing tank (18). An upper part of the tar filter is connected with the draught fan. An outlet of the draught fan is located in a tar-sinking tank (14). An upper part of the tar-sinking tank is connected with a burning device by a gas-conveying pipe (15). A lower part of the tar-sinking tank is connected with the tar reflowing tank.    USE - Tar processing, recycling and burning device for a domestic straw gasification furnace.    ADVANTAGE - The device is provided with a clean production system, which is utilized for improving rural environment and saving a resource. The device is environmental-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a tar processing, recycling and burning device.    Air cooling pipe (9)    Second-stage cooling gas conveying pipe (10)    Tar filter (11)    Draught fan (13)    Tar sinking tank (14)    Gas conveying pipe (15)    Tar reflowing tank (18)
NOVELTY - Biofuel composition comprises glycerin, water and at least one alcohol.    USE - The biofuel composition is useful: in biofuel (claimed); as a direct fuel, a fuel additive, a fuel supplement or as fuel for generation of power or electricity; in internal combustion engines including diesel engines; in furnaces, boilers, power generating equipment, e.g. gas or combustion turbines; and in different types of oil burners (for domestic and other heating purposes) including sleeve burners, natural-draft pot burners, force-draft pot burners, rotary wall flame burners, and air-atomizing and pressure-atomizing gun burners.    ADVANTAGE - The biofuel composition: is renewable; and can be prepared at lower cost, without the need for complicated chemical processes or equipment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) making the biofuel composition, comprising mixing the glycerin, water and the alcohol; and    (2) a biofuel, comprising the biofuel composition, and a liquid biofuel or liquid fuel.
NOVELTY - Treating biological waste for preparation of fertilizers, comprises: mixing the biological waste with a dilute sulfuric acid in a predetermined ratio; filtering the mixture of the biological waste and the dilute sulfuric acid to obtain an organic slurry and an acidic liquid; and thermally cracking the organic slurry at an elevated temperature to obtain at least one of an ammonia gas, at least one flue gas, and char and ash, where the ammonia gas, the acidic liquid and the char and ash are used for preparation of the fertilizers.    USE - The method is useful for treating biological waste to prepare fertilizers (claimed), such as soil conditioner.    ADVANTAGE - The method provides fertilizers in less duration without producing foul odors and without using specialized machines and equipments, hence cost-effective. The method extracts a large percentage of nutrients from the biological wastes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for treating biological waste for preparation of fertilizers, comprising a mixing chamber for mixing the biological waste with a dilute sulfuric acid in a predetermined ratio, where the predetermined ratio is six parts of the dilute sulfuric acid and one part of the biological waste; a filtering unit for filtering the mixture of the biological waste and the dilute sulfuric acid to obtain an organic slurry and an acidic liquid, and a thermal cracking unit for heating the organic slurry at an elevated temperature to obtain an ammonia gas, and at least one of flue gas, char and ash.
NOVELTY - Process for catalytic isomerization of fatty acid esters to form branched fatty acid esters, comprises: (a) contacting a feedstock having at least one fatty acid ester with a catalyst comprising a crystalline porous silicoaluminophosphate catalyst having silicon, aluminum, and phosphorus atoms in lattice framework positions; and (b) isolating from other reaction products the branched fatty acid esters.    USE - The process is useful for catalytic isomerization of fatty acid esters to form branched fatty acid esters, which are useful in various applications, such as biofuels, biolubricants and deicing agents.    ADVANTAGE - The products produced by the method: have higher chemical stability against oxidation, reduced pour points, cloud points and cold filter plug points; and lessen or eliminate the need for fuel additives such as pour point depressants and viscosity modifiers. The catalyst used in the process is reusable or capable of regeneration through methods that include combustion of the carbonaceous deposits in air.    DETAILED DESCRIPTION - Process for catalytic isomerization of fatty acid esters to form branched fatty acid esters, comprises: (a) contacting a feedstock having at least one fatty acid ester with a catalyst comprising a crystalline porous silicoaluminophosphate catalyst having silicon, aluminum, and phosphorus atoms in lattice framework positions; and (b) isolating from other reaction products the branched fatty acid esters, where the fatty acid ester has a structure of formula (R-COOR1).    R, R1 = methyl, ethyl, propyl or butyl.    An INDEPENDENT CLAIM is included for a mixture comprising at least one branched fatty acid ester having a structure of formula (R-COOR1), which is prepared by the above method, where the branched fatty acid ester has at least one more alkyl side chain than the fatty acid ester in the feedstock.
NOVELTY - Method of biological denitrification using an anaerobic ammonia oxidation reaction, involves allowing a support having a biofilm deposited on the surface of the support, under aerobic conditions, and adding to-be-processed water containing dissolved nitrogen into a reaction tank.    USE - The method is useful for biological denitrification of to-be-processed water, preferably industrial effluent, sludge water, city sewage and household wastewater.    ADVANTAGE - The method avoids need of abundant organic substance e.g. methanol, and is simple, cost-effective and performed at normal temperature.    DETAILED DESCRIPTION - Method of biological denitrification using an anaerobic ammonia oxidation reaction, involves allowing a support having a biofilm deposited on the surface of the support, under aerobic conditions, and adding to-be-processed water containing dissolved nitrogen into a reaction tank, where the biofilm comprises two dominant species chosen from nitrite-producing nitrifying bacteria and anaerobic ammonia-oxidizing bacteria, or three dominant species, chosen from nitrite-producing nitrifying bacteria, aerobic bacteria capable of decomposing dissolved nitrogen other than ammonia nitrogen into ammonia, and anaerobic ammonia-oxidizing bacteria. The nitrite-producing nitrifying bacteria perform nitrite-producing nitrification reaction. The anaerobic ammonia-oxidizing bacteria perform anaerobic ammonia oxidation reaction. The proportion of the support to-be-introduced is regulated such that the nitrite-producing nitrification reaction caused by the nitrite-producing nitrifying bacteria yields nitrite in an amount sufficient to inhibit the nitrate-producing nitrification reaction, while maintaining the to-be-processed water alkaline in the reaction tank. The reaction tank is partitioned into several divisions without blocking circulation of the to-be-processed water.
NOVELTY - Treating a lignocellulosic material, comprises: degrading lignin of the lignocellulosic material with at least one fungus; and hydrolyzing cellulose of the lignocellulosic material with at least one microorganism.    USE - The method is useful for treating lignocellulosic material for producing ethanol (claimed).    ADVANTAGE - The method provides ethanol in an economical and environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing ethanol, comprising: providing a lignocellulosic material; degrading lignin of the lignocellulosic material with the fungus; hydrolyzing cellulose of the lignocellulosic material with the microorganism; further hydrolyzing the cellulose with one or more cellulase enzymes into one or more fermentable sugars; and fermenting the one or more sugars.
NOVELTY - Producing mixture of fuel components, comprises providing a feed of biological origin, subjecting the feed of biological origin and a hydrogen gas feed to a hydroprocessing in the presence of a catalyst system comprising nickel-tungstate (NiW) catalyst to form a mixture of fuel components.    USE - The process is useful for producing a mixture of fuel components, which is useful as a fuel or as an additive in a fuel composition, where the fuel is a diesel fuel, a gasoline fuel, a jet fuel or a naphtha grade fuel (all claimed).    ADVANTAGE - The process: does not require any pretreatment procedure to remove sulfur from the feed of biological origin prior to its further processing, thus provides a simple one-step, efficient and economical process for the treatment of the hydrocarbon feeds of biological origin to provide a product that is usable for fuel applications; and utilizes non-toxic catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for producing a mixture of fuel components from a feed of biological origin, comprising: a first feed inlet (2) for feeding the feed of biological origin; at least one first hydrogen feed inlet (4); and at least one hydroprocessing reactor (8) comprising a catalyst bed (12) of NiW catalyst for producing a mixture of the fuel components in a single step.    DESCRIPTION OF DRAWING(S) - The figure shows an apparatus for carrying out a single-step process for producing fuel components from the feed of biological origin.    First feed inlet (2)    First hydrogen feed inlet (4)    First hydrogen recycle outlet (6)    Hydroprocessing reactor (8)    Catalyst bed (12)
NOVELTY - Method (M1) for processing target object involves adding the target object to microbial bed comprising microorganisms chosen from Bacillus, Ureibacillus and Brevibacillus and mixing the target object with microbial bed, where the microorganisms are capable of decomposing organic substance present in the target object.    USE - The methods (M1) and (M2) are useful for decomposing sewage sludge and reducing water content of biomass which is culture of microalgae respectively (claimed). The biomass is useful for producing biofuel. The method is also useful for decomposing other waste materials, preferably discharge from industries, food factories and general household activities and recycling various components e.g. phosphorus.    ADVANTAGE - The method enables simple and effective decomposition of target object up to 100% and also reduces water content of the target object significantly hence reduces the amount of fossil fuel required for evaporation of water from the target object. The amount of residue left out after decomposition which requires incineration is also reduced hence carbon dioxide emission during incineration is reduced which reduces global warming and thus reduces environmental load compared to existing incineration processing methods.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for decreasing water content of target object, which involves adding and mixing the target object to the microbial bed and subjecting to fermentation, where heat generated during the fermentation decreases the water content of the target object.
NOVELTY - Process (I) of producing fuel from vegetable oil by using a dolomite catalyst, comprises: (a) preparing a raw material containing vegetable oil for cracking; and (b) performing pyrolysis for cracking by contacting the raw material with a dolomite catalyst, which is prepared by calcining natural ore dolomite at greater than or equal to 900 degrees C, to form a liquid material, and cracking the liquid material in a reactor by mixing the liquid material at 250-600 degrees C.    USE - The process is useful for producing fuel from vegetable oil containing raw material and/or natural fat in a pure state or in a mixture with residual hydrocarbon oil, where the vegetable oil (pure or wasted) is palm oil, soybean oil, grape seed oil, olive oil, sunflower oil, corn oil, sesame oil, and rice bran oil (all claimed), and the fuel includes gasoline and diesel oil.    ADVANTAGE - The process provides high quality oil for fuel comprising mainly light and heavy naphtha and gas oil, with reasonable cost and with high efficiency, by using a very low cost catalyst.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for process (II) of producing fuel from vegetable oil containing raw material and/or natural fat that may be used in a pure state or in a mixture with residual hydrocarbon oil by using a dolomite catalyst, comprising (a1) preparing a raw material by mixing vegetable oil and/or natural fat, (b1) performing pyrolysis of plastic waste material to produce a residual hydrocarbon oil as a raw material for cracking, and (c1) mixing the raw materials from steps (a1) and (b1) for cracking with the dolomite catalyst.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic flow chart of the process of producing fuel from vegetable oil.
NOVELTY - The process involves sending an untreated natural gas stream (1) to an ocean vessel through a membrane unit (3) containing a membrane for selective separation of acid gases from natural gas. A partially purified natural gas stream (7) having an acid gas content lower than the untreated natural gas stream is formed. The partially purified natural gas stream and the untreated natural gas stream are passed to an amine column (8). An acid gas content of a natural gas product effluent is less than that of the partially purified natural gas stream.    USE - Process for removal of acid gases such as carbon dioxide and hydrogen sulfide, from an untreated natural gas stream on a floating liquefied natural gas vessel.    ADVANTAGE - The process enables avoiding problem of maldistribution of liquid within vessels and impact the effectiveness of the amine column in removing acid gases by integrating a membrane system and an amine system by changing the membrane operation conditions or process configurations and changing the feed acid gas concentration to the amine absorber, thus mitigating the effect of maldistribution and delivering the treated gas meeting the feed specifications for liquefied natural gas liquefaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a membrane/amine column system for treating a natural gas stream in which a bypass stream adjusts the amount of natural gas being treated by a membrane part of the system.    Untreated natural gas stream (1)    Membrane unit (3)    Partially purified natural gas stream (7)    Amine column (8)    Lean solvent (11)
NOVELTY - Production (M1) of glycerol related products involves: introducing a biomass and alkylation reagent to a oxygen free environment; hydrolyzing at least one lipid glyceride in the biomass at greater than or equal to 200 degrees C; methylating at least one fatty acid in the biomass with methyl groups from the alkylation reagent, where the hydrolyzing and methylating occur contemporaneously; and separating resulting biodiesel and methylated glycerol-related products from a residue of the biomass by condensation.    USE - For production of glycerol related products (claimed); for production of fatty acid alkyl esters e.g. biodiesel from a biomass; for the synthesis of polish, as a cryoprotective agent for prevention of ice formation during cooling of vascular tissues and organs, for the synthesis of optical immersion oil, or as a fuel additive.    ADVANTAGE - The transesterification takes place in an oxygen free environment or under ambient pressure conditions. This reduces the cost of the process and increases the simplicity of the process. The method does not require to removes the catalyst residue.
NOVELTY - The system has a kiln (104) provided with an inner core and an outer shell (103). Two airlocks (102, 114) are affixed to a proximal end and a distal end of the core by a part of two rotating seals, respectively. Two fans (108, 111) are connected to tubulation (1011) emanating from the proximal and distal ends of the core, respectively. A helical steel rail (105) is affixed along an inner surface of the core. The tubulation is connected between one of the fans and a condenser separator (109). A circular baffle (18, 19) and baffle stem support mounts to elevate the system above a ground level.    USE - System for pyrolyzing carbonaceuous material such as coal and biomass.    ADVANTAGE - The system is provided with a master control unit so as to regulate and monitor speed of the fans, the temperature of the kiln core, the rotation speed of the inner core and monitor the temperature of thermo-couples mounted in the space between the core and the outer shell of the kiln, thus regulating the temperature of the heater coils in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a motor and gear structure to implement rotation of the inner core carrying the material to be processed by way of heat from the heating coils mounted on the inner surface of the kiln shell in a system.    Circular baffle (18, 19)    Airlocks (102, 114)    Outer shell (103)    Kiln (104)    Helical steel rail (105)    Fans (108, 111)    Condenser separator (109)    Tubulation (1011)
NOVELTY - The boiler has multiple heating pipes inserted in three water tanks. A primary gasification chamber and a secondary gasification chamber are connected with each other. An upper part of the first water tank is provided with an outlet passage. A water inlet is fixed on the second water tank. A water outlet is arranged at an upper end of the third water tank. The primary gasification chamber and the secondary gasification chamber are respectively provided with oxygen supply holes. A lower part of a hearth is connected with the primary gasification chamber.    USE - Biomass gasification boiler.    ADVANTAGE - The boiler can burn the fuel uniformly. The boiler improves heat absorption of water in the furnace body.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass gasification boiler.
NOVELTY - Producing synthesis gas from biomass, comprises preconditioning the biomass either by synthesis gas fermentation or by hot coking for further process. The plants of the biomass comprises aquatic plants, whose starch content is maximized by the defined addition of element boron or chemical compounds containing boron during the growth of the aquatic plants, to the culture medium.    USE - The activated carbon is useful for purifying water, waste water or mine water (claimed).    ADVANTAGE - The method produces the synthesis gas with better gas yields and better gas quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of an arrangement for pumping up the water from a disused mine shaft using a pump. Drawing includes non-English language text.
NOVELTY - 4,4'-Dibenzyl-biphenyl compounds are new.    USE - (I) is useful as chemical markers for liquid hydrocarbons and other fuels and oils.    DETAILED DESCRIPTION - 4,4'-Dibenzyl-biphenyl compounds of formula (I) are new.    G = 1-12C alkyl or 1-12C alkoxy, preferably 2 or 3 methyl or ethyl.    An INDEPENDENT CLAIM is included for marking a petroleum hydrocarbon, biodiesel fuel or ethanol fuel comprising adding to the petroleum hydrocarbon, biodiesel fuel or ethanol fuel at least one compound comprising (I).
NOVELTY - Marking a petroleum hydrocarbon, biodiesel fuel or ethanol fuel, comprises adding to the petroleum hydrocarbon, biodiesel fuel or ethanol fuel at least one compound.    USE - The methods are useful for marking a petroleum hydrocarbon, biodiesel fuel or ethanol fuel; and for identifying the petroleum hydrocarbon, biodiesel fuel or ethanol fuel (all claimed).    ADVANTAGE - The method effectively and efficiently marks a petroleum hydrocarbon, biodiesel fuel or ethanol fuel.    DETAILED DESCRIPTION - Marking a petroleum hydrocarbon, biodiesel fuel or ethanol fuel, comprises adding to the petroleum hydrocarbon, biodiesel fuel or ethanol fuel at least one compound having formula (I).    R1 and R2=independently represent at least one substituent selected from hydrogen, 1-12C alkyl, 1-12C alkoxy and nitro; and    R3 and R4=independently represent hydrogen, methyl or ethyl.    An INDEPENDENT CLAIM is a method for identifying the petroleum hydrocarbon, biodiesel fuel or ethanol fuel marked with at least one compound having formula (I); where each compound of formula (I) is present at a level of 0.05-20 ppm; the method comprising separating each compound of formula (I) using a chromatographic method and identifying each compound of formula (I) by mass spectral analysis.
NOVELTY - A cell culture comprises a population of bacterial cells of the genus Streptomyces; and a non-sterile or pasteurized cultivation medium containing organic waste(s) and/or residue(s) as carbon and/or nutrient source.    USE - For producing lipid useful as a starting material for biofuel, as lubricant or as a starting material for lubricant; and for the production of biodiesel or renewable diesel (all claimed).    ADVANTAGE - The cell culture effectively produces lipids on a medium comprising organic waste(s) and/or residue(s).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1) producing (P1) lipids for biofuel or lubricant involving cultivating bacterial cells of the genus Streptomyces in a medium comprising organic waste(s) and/or residue(s) as carbon and/or nutrient source(s), recovering lipids from the cells of bacteria or from the cultivation medium, using the recovered lipids or fraction as biofuel and/or lubricant, or as a starting material for biofuel and/or lubricant production; 2) a host (H1) selected from Streptomyces roseosporus, Streptomyces griseus, Streptomyces albus, Streptomyces peucetius, Streptomyces aureofaciens, Streptomyces lividans, Streptomyces hygroscopicus, Streptomyces avermitilis, Streptomyces lydicus genetically modified to express an endogenous or exogenous gene encoding diacylglycerol acyltransferase (EC 2.3.1.20) and/or 3-ketoacyl-acyl carrier protein synthase III (FabH) (EC: 2.3.1.41), or a nucleotide sequence causing the same or an equivalent function as gene products ID 101096381 or ID 101101330; and 3) biofuel or lubricant comprising the lipids or lipid composition produced by the process (P1) or a fraction of lipids or lipid composition, and suitable additives for biofuel use.
NOVELTY - Producing energy, comprises: providing or producing a propylene-glycol-water mixture having a propylene-glycol content of 30-94 vol.%; producing a secondary energy carrier, preferably hydrogen and/or carbon monoxide from the propylene-glycol-water mixture by reformation; and converting the secondary energy carrier, preferably hydrogen and/or carbon monoxide into energy, preferably electrical and/or thermal energy, by a converter by oxidizing the hydrogen and/or carbon monoxide in a galvanic cell, preferably fuel cell.    USE - The propylene glycol-water mixture having a propylene glycol content of 30-94 vol.% is useful for the generation of energy, preferably electrical energy and/or thermal energy, by oxidation/galvanic reaction of the secondary energy carrier, preferably hydrogen and/or carbon monoxide, produced from the propylene glycol-water mixture (claimed).    ADVANTAGE - The method produces energy in an improved and in an inexpensive manner by using the propylene glycol-water mixture with above specified propylene glycol content that can be easily handleable.
NOVELTY - An anaerobic bioreactor contains a methane fermentation unit which generates biogas containing methane gas from organic waste, a separation unit connected to the methane fermentation unit which separates emitted biogas into methane gas and carbon dioxide and produces solid carbon dioxide, and a conversion unit which converts methane gas into electrical energy. The anaerobic bioreactor carries out anaerobic fermentation of organic waste using an anaerobic methane fermentation microbe and produces methane gas.    USE - An anaerobic bioreactor for organic wastes (claimed).    ADVANTAGE - Methane is efficiently converted into an energy source, solid carbon dioxide is recovered, and operating and installation costs are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the anaerobic bioreactor. (Drawing includes non-English language text).
NOVELTY - Method for producing methane using carbon dioxide and hydrogen, involves reacting carbon dioxide and hydrogen, where the molar ratio of hydrogen and carbon dioxide in the reaction process is 4.1-4.5.    USE - The method is useful for producing methane.    ADVANTAGE - The method is simple and environmentally-friendly, as it uses highly purified hydrogen as raw material.
NOVELTY - Austenitic stainless steel is processed (S1). The processed austenitic stainless steel is heated (S2) under fluorine-gas atmosphere, carburized (S3) at 400-680 degrees C and washed (S4), to obtain separator.    USE - Manufacture of separator used for polymer electrolyte fuel cell (claimed) used as power supply for motor vehicle and household appliances.    ADVANTAGE - The method economically and efficiently provides separator. The polymer electrolyte fuel cell using the separator has excellent mechanical strength, electroconductivity, contact resistance and corrosion resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows flowchart of manufacture of separator. (Drawing includes non-English language text)    Processing of austenitic stainless steel (S1)    Heating (S2)    Carburizing (S3)    Washing (S4)
NOVELTY - The system (100) has a reactive gas supply part (20) supplying reactive gas to a fuel cell (10). A control part (60) controls supply amount of the reactive gas by the reactive gas supply part, and is connected to the fuel cell for gas piping reactive gas. A downstream pressure measuring part (24d) measures downstream of a shut-off valve (22) based on a pressure value, which is controlled by the control part. The system closes the shut-off valve at target flow volume reaching time.    USE - Fuel system for supplying a fuel cell and generating reactive gas in a vehicle.    ADVANTAGE - The system closes the shut-off valve at target flow volume reaching time, so that the pressure value of the reactive gas can control supply amount of the reactive gas in a fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling supply amount of reactive gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit block diagram of a fuel system.'(Drawing includes non-English language text)'    Fuel cell (10)    Reactive gas supply part (20)    Shut-off valve (22)    Downstream pressure measuring part (24d)    Control part (60)    Fuel system (100)
NOVELTY - Catalyst comprises a physical mixture of particles of a catalytic material and char.    USE - The catalyst is useful for removing tars from syngas stream (claimed). It can also be used in various processes, including reforming tars present in syngas generated during biomass gasification.    ADVANTAGE - The catalyst is produced through a mechanical mixing of the catalytic material and char particles, which results in significant time and energy savings over methods of catalyst preparation that involve impregnation and calcining of a support material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a method of removing tars from a syngas stream comprising providing a catalyst comprising a physical mixture of particles of a catalytic material and particles of char; and contacting a syngas-containing stream having tars present with the catalyst under conditions for converting at least a portion of the tars into syngas components;    (2) a system for removing tars from a syngas stream comprising a reactor vessel comprising a quantity of a catalyst, the catalyst comprising a physical mixture of particles of a catalytic material and particles of char; and a source of syngas operably connected with the reactor vessel, the syngas having tars; and    (3) a method of producing a catalyst comprising mechanically mixing particles of a catalytic material with particles of char.
NOVELTY - Method for recycling organic waste liquid using Spirodela, involves acquiring culture solution from the organic waste liquid for culturing Spirodela, subjecting the Spirodela to initial culturing process by adding the culture solution to Spirodela growth system, subjecting the Spirodela to secondary culturing process, where the amount of culture solution added is reduced compared to first culturing process, and collecting the cultured Spirodela.    USE - The method is useful for recycling organic waste liquid e.g. palm extraction waste liquid, using Spirodela, Wolffia or Lemna minor, preferably Spirodela. The refined residue chosen from hyaluronic acid, lactic acid, ethanol, squalene, cadaverine and shikimic acid, obtained in the method is useful in processes of obtaining fertilizer or soil modifier (all claimed). The organic waste liquid includes human and livestock excrement liquids and the refined residue also includes alcohol, hydrocarbons, vitamins, amino acids, and organic acids e.g. itaconic acid, ornithine, ubiquinone, vitamin B, astaxanthin, arachidonic acid, butanol, and propanol. The method is also useful in manufacture of chemical substances and for cleaning contaminant.
NOVELTY - A plasma processing apparatus (100) comprises chamber (102) for processing substrate; plasma generator for generating plasma within the chamber; window in a sidewall of the chamber, for transmitting light from the plasma within the chamber; and photocatalytic layer on an inner surface of the window such that the photocatalytic layer is activated as a result of exposure to light from the plasma to decompose residual product on inner surface of the window.    USE - A plasma processing apparatus.    ADVANTAGE - The apparatus is capable of precisely monitoring plasma process, and increasing sensitivity of optical signal from window.    DESCRIPTION OF DRAWING(S) - The drawing is a cross-sectional view of a plasma processing apparatus.    Substrate (10)    Plasma processing apparatus (100)    Chamber (102)    Lower electrode (120)    Power supply (150)
NOVELTY - Aviation bio-kerosene production involves producing biodiesel from raw materials including vegetable oil rich in triglycerides containing 6-14C atoms. The vegetable oil is selected from a group consisting of coconut oil, palm oil, palm kernel or their mixtures. The obtained biodiesel is fed into a vacuum fractionation unit, where fraction of bio-kerosene aviation is removed from top of distillation column.    USE - Method for producing aviation bio-kerosene used in aviation kerosene composition (claimed).    ADVANTAGE - The method produces the aviation bio-kerosene having freezing point below -10 degrees C in a simple and cost-effective manner.
NOVELTY - Biomass cracking comprises (i) introducing the biomass into an open rectangular container; (ii) lighting the fire at the middle and the lower parts for 1-2 hours, covering the surface of the biomass to block the oxygen using the carbon powder in 30% of water content, performing thermal cracking for 6-8 hours; and (iii) performing temperature decreasing separating, cyclone separating, temperature decreasing, air baffling, catalyzing, cleaning, dehydrating and multi-layer filtering to the rough fuel gas to decompose the combustible gas, tar, acetic acid liquid and indefinite-form carbon.    USE - The method is useful for biomass cracking.    ADVANTAGE - The method does not discharge polluted gas and polluted water, thus it is environmental-friendly; and has high vaporization rate, precise extraction component, and consumes less energy.    DETAILED DESCRIPTION - Biomass cracking comprises (i) introducing the biomass into an open rectangular container; (ii) lighting the fire at the middle and the lower parts for 1-2 hours, covering the surface of the biomass to block the oxygen using the carbon powder in 30% of water content, performing thermal cracking for 6-8 hours; and (iii) performing temperature decreasing separating, cyclone separating, temperature decreasing, air baffling, catalyzing, cleaning, dehydrating and multi-layer filtering to the rough fuel gas to decompose the combustible gas, tar, acetic acid liquid and indefinite-form carbon. The plane of the container is slant, and the short wall of the container is provided with a flue along the bottom, and the other three walls are provided with an air channel along the bottom. The flue is connected with multiple ventilation paths in the bottom of the container. The bottom surface of the container is provided with multiple wind suction paths connected to the ventilating paths. The container wall and the container bottom are provided with ventilating holes.
NOVELTY - The fuel cell (1) has a modifier (5) which produces reformed fuel that is supplied to a fuel cell stack (3) by performing steam reforming of fuel introduced from the outside. The air exhausted from exhausted fuel (EF) are discharged from the fuel cell stack and are burned. A combustor (9) supplies the generated heat to the modifier. The modifier and the combustor are formed integrally.    USE - Fuel cell for transforming chemical energy into electrical energy.    ADVANTAGE - Exhibits excellent electric power generation efficiency, efficiently and cleanly transforms chemical energy into electrical energy directly by effectively using heat energy which radient heat from fuel cell stack and hot waste gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fuel cell. (Drawing includes non-English Language text).    Fuel cell (1)    Fuel cell stack (3)    Modifier (5)    Combustor (9)    Exhausted fuel (EF)
NOVELTY - Scattered type rural household waste processing system comprises a waste sorting machine and an anaerobic aerobic bioreactor. The waste sorting machine is connected with the parallel anaerobic aerobic bioreactor through a discharging pipe. The anaerobic aerobic bioreactor is connected with an anaerobic leachate collecting pool and an aerobic leachate collecting pool through a pipeline. The anaerobic leachate collecting pool and the aerobic leachate collecting pool are connected with a peristaltic pump, where each anaerobic aerobic bioreactor is connected with an air compressor.    USE - Used as scattered type rural household waste processing system.    ADVANTAGE - The system: solves the problem of village integrated waste processing system; improves the efficiency of treating household waste; does not need expert management and hence is convenient to promote and use in rural areas.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the scattered type rural household waste processing system.
NOVELTY - Method for producing electricity by fermentation of livestock excretion, involves adding livestock excrement (30-50%) from storage tank to fermentation tank, mixing the livestock excretion with composition in mixing furnace, transferring the obtained mixture to fermentation room for performing fermentation to obtain compost and methane gas, collecting the obtained methane gas from the fermentation room, and producing electricity from the obtained methane gas.    USE - The method is useful for producing electricity and compost by fermentation of livestock excretion.    ADVANTAGE - The method produces compost with high quality without leaving fluid residues, shortens fermentation period, and produces large amount of methane gas in short-term process and thus produces large amount of electricity.    DETAILED DESCRIPTION - Method for producing electricity by fermentation of livestock excretion, involves adding livestock excrement (30-50%) from storage tank to fermentation tank, mixing the livestock excretion with composition in mixing furnace, transferring the obtained mixture to fermentation room for performing fermentation to obtain compost and methane gas, collecting the obtained methane gas from the fermentation room, and producing electricity from the obtained methane gas, where the composition comprises pulverized plant portion having 50-500 meshes, and soil collected from earth at 50 cm depth containing beneficial microorganism and naturally dried.
NOVELTY - The method involves manufacturing slurry including metal powder and solvent, where the metal powder is selected from a group consisting of nickel, aluminum, chromium, copper, iron, cobalt, silver and titanium. An electrode substrate (110) is prepared, where the electrode substrate is made of graphite paper. An electrode activity layer is formed on the electrode substrate. The slurry is coated on the electrode substrate. A porous metal film is arranged on a surface of the electrode substrate after preparing the electrode substrate.    USE - Method for manufacturing an electrolyte-filled electrode in a molten carbonate fuel cell (MCFC).    ADVANTAGE - The method enables reducing the manufacturing cost of the electrolyte-filled electrode, and simplifying the manufacturing process of the electrolyte-filled electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating an electrolyte-filled electrode manufacturing method.    Electrolyte-filled electrode (100)    Electrode substrate (110)
NOVELTY - The method involves generating high concentration bad smell during process of a food waste, and generating high concentration bad smell during process of a livestock excretion. Bad smell of a bad smell unit is collected by utilizing a diffuser that is installed at a bottom surface of a compost fermentation unit. A bio-filter role of a compost fermentation phase of the compost fermentation unit is performed. A screw burr is arranged by the compost fermentation unit.    USE - Method for removing odor of an organic compound such as food waste and livestock excretions.    ADVANTAGE - The method enables removing the bad smell of the organic compound by utilizing the compost fermentation phase and a succeeding bath. The method enables removing odor of the organic compound in an inexpensive manner. The method enables improving removing process of the bad smell.
NOVELTY - Non-oxygen pyrolysis purification comprises putting formed straw rod or other straw material into distillation kettle, then using pyrolysis furnace to seal and heat the straw rod or other straw materials in kettle, and pyrolyzing to generate straw gas with high temperature.    USE - Method for non-oxygen pyrolysis purification (claimed).    ADVANTAGE - The method generates straw gas having good quality, has high resource utilization rate, low production cost and production efficiency is high and the safety is strong.    DETAILED DESCRIPTION - Non-oxygen pyrolysis purification comprises:    (A) putting formed straw rod or other straw material into distillation kettle, then using pyrolysis furnace to seal and heat the straw rod or other straw materials in kettle, and pyrolyzing to generate straw gas with high temperature;    (B) entering the straw gas into a tar separator, spraying wood liquid to dilute atomizing, and entering into a cooling separator to obtain straw gas;    (C) cooling the straw gas into a first gas-liquid separator with friction sheet for water, tar, vinegar liquid for removing operation, then entering into neutralizing separator, spraying alkali liquid, neutralizing after entering into a second gas-liquid separator in second friction sheet with water, tar, and vinegar liquid for removing to obtain the liquid straw gas;    (D) removing the liquid straw gas by separating tower of air inlet tower enter into left cavity in tower friction stopper, then lapboard entering into lower part of the tower right cavity in tower filter core, and discharge port tower to obtain the catalysts; and    (E) filtering air by entering into roots blower group, and then through gas filters to obtain filtered straw gas.
NOVELTY - An organic planting soil has moisture content of 15-30 wt.%, carbon nitrogen ratio of 15-25, and removal rate of germs, ovum and grass seed of more than 99%.    USE - An organic planting soil.    ADVANTAGE - The soil has high removal rate of bacteria, grass or ovum, is environment-friendly, and utilizes waste thus reducing pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic cultivation soil comprising:    (A) air drying garden soil under the shade to control water content to 30 wt.%, crushing to obtain particles having diameter of not less than 1 mm, and screening;    (B) air-drying waste biological organic matter having carbon nitrogen ratio of 35-50 to control water content to 40-60 wt.%;    (C) piling, composting at 50 plus minus 2 degrees C while turning daily, screening, mixing compost product and processed garden soil at a volume ratio of 1:0.02, and controlling water content to 40-60 wt.%;    (D) re-stacking, and composting at 50 plus minus 2 degrees C until volume ratio of compost product and processed garden soil is at a volume ratio of 1:0.1-0.7;    (E) re-stacking, and composting at 50-70 degrees C for 48-70 hours; and    (F) cooling at 30 plus minus 2 degrees C, adding agricultural microorganism (1x 106 to 1x 108), mixing, cooling to room temperature, crushing to obtain particle having a diameter of less than 2 mm, and aging for 30-45 days in a shady place to obtain organic cultivation soil having moisture content of 15-30 wt.% and carbon nitrogen ratio of 15-25.
NOVELTY - A fungi culture medium comprises non-medicinal portion of Chinese medicinal material. A component of crushed non-medicinal portion of Chinese medicinal material is 10-50 wt.%. A total carbon/nitrogen ratio of the culture medium is (10-80)/1, and a pH value of the medium is 5-8.    USE - Fungi culture medium for cultivating A. polytricha (claimed).    ADVANTAGE - The medium solves the problem of recycling of a large amount of wasted non-medicinal portions of the Chinese medicinal materials, is in accordance with low carbon economic development, and improves yield and quality of A. polytricha without changing conventional cultivating and operating method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bag type cultivation of Auricularia polytricha, in which the crushed non-medicinal portion of the Chinese medicinal material in the fungi culture medium is soaked in water, and then mixed with other conventional culture medium nutrient components, sterilized and inoculated. The A. polytricha is cultivated in the culture medium at a temperature adaptive to its growth habit.
NOVELTY - Increasing production of carbinol comprises adding carbinol purge gas combined with carbinol into transformation absorption device to extract hydrogen, extracting carbinol purge gas to form gas including carbide and gas including hydrogen, entering gas including carbide enter into carbinol synthetic system directly, and regarding gas including hydrogen as fuel gas for heating coke oven.    USE - Method for increasing production of carbinol by purge gas (claimed).    ADVANTAGE - The method utilizes purge gas effectively, avoids dispersing or combusting of purge gas to pollute environment, can increase enterprise benefit, controls carbon and hydrogen ratio effectively, increases carbinol output, prolongs flame and improves coke quality.
NOVELTY - Producing methane involves cutting the biomass straw into soft strips, transferring the stripped straw to pre-treating pool, adding liquid returned from anaerobic reactor into the pre-treating pool, stirring the mixture, adding the straw material liquid into the pre-treating pool to compost the mixture for 5-7 days, and transferring the straw material liquid into anaerobic reactor provided with a shell breaking device to ferment and produce methane.    USE - The method is useful for producing methane.    DETAILED DESCRIPTION - Method of producing methane by biomass straw anaerobic fermentation, involves (a) cutting the biomass straw into soft strips using cutting and kneading machine, where the strips have length of 1.5-2.5 cm, (b) transferring the stripped straw to pre-treating pool using conveyer, adding liquid returned from anaerobic reactor into the pre-treating pool, stirring the mixture completely, where the concentration of the total solid of stirred straw material liquid is 20%, and adding the straw material liquid into the pre-treating pool to compost the mixture for 5-7 days, and (c) transferring the straw material liquid into anaerobic reactor provided with a shell breaking device to ferment and produce methane, where the fermenting temperature is 30-40 degrees C, and fermenting time is 20-25 days.
NOVELTY - Method for producing alcohol fuel by fermenting crop straw, involves obtaining corn straw, Sorghum stalk, wheat straw or their mixtures as raw material, pulverizing the crop straws, subjecting the straw to acid hydrolysis using dilute sulfuric acid, subjecting the product for performing enzymolysis using cellulase, inoculating the product with yeast, fermenting the mixture, distilling fermented product, and sieving the product using a molecular sieve.    USE - The method is useful for producing alcohol fuel.    ADVANTAGE - The method relieves tension of national petroleum resources and develops new energy resource substitute product using crop straws.    DETAILED DESCRIPTION - Method for producing alcohol fuel by fermenting crop straw, involves obtaining corn straw, Sorghum stalk, wheat straw or their mixtures as raw material, firstly pulverizing the crop straws into 1-1.5 cm, adding 1% dilute sulfuric acid (3-4 times) to the raw material for acid hydrolysis at 125 degrees C for 50 minutes, adding equal volume of water to dilute the product, regulating pH of the hydrolyzate using sodium hydroxide to 4.8-5, reducing the temperature of the product to 50 degrees C, adding cellulase (400 unit) to the product for performing enzymolysis for 16 hours, adding cellulase (200 unit) to continue enzymolysis for 8 hours, reducing the temperature of the product to 30 degrees C after enzymolysis, adding alcohol (0.2-0.3 %mass) to the product, inoculating the product with yeast, fermenting the mixture at 28-30 degrees C for 64-72 hours, distilling fermented product, and sieving the product using a molecular sieve.
NOVELTY - Bioprocessing shrimp waste involves performing solid state fermentation by using Lactobacillus spp. isolated from cheese curd and sucrose, glucose, fructose or xylose as a carbon source.    USE - Method for bioprocessing waste of shrimp, crab and lobster for obtaining chitin, protein pigment i.e. astaxanthin and calcium carbonate (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for obtaining chitosan by deacetylation of chitin, which involves fermenting chitin by using sodium hydroxide at 60 degrees C for an hour.
NOVELTY - A Pseudomonas sp. DS1001 deposited as CGMCC No. 4366, having the following characteristics: round and yellow and white, the surface is smooth, the edge is orderly, the surface is wet, the thallus is in short rhabditiform and is Gram-negative, has flagellum, the 165 rDNA has a nucleotide sequence comprising fully defined 1497 bp (SEQ ID NO. 1) given in the specification, can grow using high-molecular compounds such as polylactic acid (PLA), poly-beta hydroxybutyrate (PHB) or polycaprolactone (PLC) as a carbon source, and can degrade compounds with high efficiency, is new.    USE - The bacterial strain and its fermented enzyme liquid can be used for the treatment and biological cycle utilization of plastic waste with components such as PLA, PHB or PLC (claimed).
NOVELTY - Method for producing fuel ethanol, involves selecting species, filling the selected fully ripened persimmon in a box, ripening the persimmon using ripener, pulping softened and non-astringent persimmon, adding 10% of pulverized persimmon to a yeast multiplication tank to obtain activated yeast and 90% of pulverized persimmon to a primary tank of fermentation tanks, culturing activated yeast, passing the qualified cultured yeast mash to the primary tank, fermenting the mixture, distilling the fermented mixture, and adsorbing and dewatering the fermented product.    USE - The method is useful for producing fuel ethanol.    ADVANTAGE - The method is cost-effective as it utilizes inexpensive raw material and does not require saccharification process, and improves yield of ethanol per unit area compared to yield of ethanol obtained from maize and cassava. The persimmon tree prevents increase of crop's price as it does not compete for land with crops e.g. sugarcane crop.    DETAILED DESCRIPTION - Method for producing fuel ethanol using persimmon, involves (a) selecting species having high sugar content, (b) filling the selected fully ripened persimmon in a box, (c) adding ripener to ripe the persimmon, (d) pulping softened and non-astringent persimmon by pulping machine, (e) adjusting pH of the pulverized persimmon to be 3.8-4 using sulfuric acid, (f) adding pulverized persimmon (10%) to a yeast multiplication tank to obtain activated yeast and 90% of pulverized persimmon to a primary tank of fermentation tanks, (g) culturing activated yeast, (h) continuously passing the qualified cultured yeast mash to the primary tank, (i) fermenting the mixture in fermenting tanks which are connected in series, (j) maintaining the temperature of fermentation process at 28-33 degrees C for 40 hours, (k) distilling the fermented mixture, (l) adsorbing and dewatering the fermented product using molecular sieve, and (m) processing methane fermentation for waste undecanted wine.
NOVELTY - Method for preprocessing biomass, involves adding alkali solution to powdered biomass and stirring mixture uniformly until the added alkali solution infiltrates and submerges biomass filing interface, placing the biomass-alkali solution mixture at room temperature to 50 degrees C for 12-100 hours, adding excessive organic acid to the mixture until the solution reaches micro acidity, placing the mixture at room temperature to 50 degrees C for 12-100 hours, filtering, drying naturally or drying, and adding cellulose to hydrolyze the product.    USE - The method is useful for preprocessing biomass chosen from straw, grass and wood (claimed).    ADVANTAGE - The method is simple, convenient to perform and inexpensive, does not require high voltage and high temperature, produces secondary biomass for paper manufacturing black liquid and inhabiting Saccharomyces for alcohol fermentation, performs secondary delignification of the acid at the same time when performing residual alkali neutralization, and reduces combination of xylogen and cellulose by adding organic acid.
NOVELTY - A plant residue oil mixed low carbon fossil fuel contains 10-50 mass% of residue oil byproduced in manufacture process of edible plant fats and oils, and fossil fuel.    USE - A plant residue oil mixed low carbon fossil fuel.    ADVANTAGE - The low carbon fossil fuel has excellent combustion efficiency, and suppresses consumption of heavy oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of purification process of edible plant fats and oils. (Drawing includes non-English language text).
NOVELTY - The method involves subjecting the liquid to anaerobic fermentation in a biogas reactor (9) resulting in a digestate (17,23) and subjecting the digestate to ultrafiltration unit (31) and reverse osmosis unit (45). The digestate from the biogas reactor is centrifuged in a centrifugation process unit (25) resulting in a centrifugate liquid fraction (29) and a centrifugate concentrate fraction (27), before subjecting ultrafiltration, and in which the centrifugate concentrate fraction is returned to the biogas reactor.    USE - Method for treatment of organic waste material such as sewage sludge, animal waste, food-processing industry waste, household waste, agricultural waste.    ADVANTAGE - The centrifugation process can reduce the volume of liquid to be treated by the ultrafiltration unit without any loss of organic material. The suspension material can be separate from the liquid to protect the ultrafilter membrane at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for plant for treatment of organic waste material in liquid form.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating the process of treatment of organic waste material in liquid form.    Biogas reactor (9)    Digestate (17,23)    Centrifugation process unit (25)    Centrifugate concentrate fraction (27)    Centrifugate liquid fraction (29)    Ultrafiltration unit (31)    Reverse osmosis unit (45)
NOVELTY - The method involves heating liquid fuel solvent containing anthracene, at 200-300 centigrade so as to obtain the biomass raw material. The obtained product is divided into biomass fuel products with different boiling ranges. The biomass raw material is selected from a group of biomass waste bagasse, vinasse slag, cassava dregs, straw, wheat straw, bean sticks, stalk, straw, corn core, leaves and wooden meal.    USE - Method for preparing biomass fuel by biomass pyrolysis.    ADVANTAGE - The biomass pyrolysis process is performed efficiently so as to obtain the biomass fuel with different boiling ranges.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the process for preparing biomass fuel by biomass pyrolysis. (Drawing includes non-English language text)
NOVELTY - Incendiary matter and incendiary agent, which are prepared by mixing corn stalks with leaves, which are minced in petroleum wax (paraffin) in a ratio of 1:1, and heating the mixed amount and pressing together after cropping into small pieces, are claimed.    USE - The incendiary matter and incendiary agent are useful for generating heat and energy.    ADVANTAGE - The incendiary matter and incendiary agent are prepared in a simple manner by using inexpensive raw materials, which are easy to transport.
NOVELTY - Fuel briquette (4) from renewable raw materials (5, 6), obtained by subjecting a raw material mixture (1) comprising non-woody or non-lignified fine material and woody or lignified structural material, preferably a raw material mixture from a forest residual wood resulting during thinning and stem wood harvesting in forestry operations, bark and wood resulting from short rotation plantations and plants and/or plant parts resulting during the landscape conservation to at least one single-stage rotting process, is claimed.    USE - Used as a fuel briquette from renewable raw materials.    ADVANTAGE - The fuel briquette: exhibits high calorific value, high stability, improved mechanical stability during loading and packing, improved dimensional stability: and can be produced at low energy and production costs.    DETAILED DESCRIPTION - Fuel briquette (4) from renewable raw materials (5, 6), obtained by subjecting a raw material mixture (1) comprising non-woody or non-lignified fine material and woody or lignified structural material, preferably a raw material mixture from a forest residual wood resulting during thinning and stem wood harvesting in forestry operations, bark and wood resulting from short rotation plantations and plants and/or plant parts resulting during the landscape conservation to at least one single-stage rotting process, is claimed. The rotting process is carried out so that the fine material of the raw material mixture is biologically converted at least up to a rotting degree-II and a maximum up to a rotting grade-III, and the obtained partially rotten raw material mixture (7) is used for the production of the fuel briquettes.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow of the method of obtaining the fuel briquette from renewable raw materials.    Raw material mixture (1)    Fuel briquette (4)    Renewable raw materials (5, 6)    Partially rotten raw material mixture (7)    Coarse fraction (10)
NOVELTY - Methane fermenting method, involves adjusting carbon concentration in sugar liquid to 0.3 mol/l containing monomer and/or multimer of glucose units, and fermenting the sugar liquid.    USE - Methane fermenting method is useful for producing methane used as energy source.    ADVANTAGE - The method is cost-effective as it uses cellulase waste as raw material and consumes less energy.
NOVELTY - A fuel-formation apparatus of organic sludge (1) comprises high temperature dust collector which removes dust of waste gas (G1-G5) of combustion furnace, heat-medium oil (M), heat exchanger (7) which heat-exchanges between waste gas of high temperature dust collector and heat-medium oil, and indirect heating type sludge fuel formation apparatus (11) which dries or carbonizes organic sludge and manufactures fuel.    USE - A fuel-formation apparatus of organic sludge.    ADVANTAGE - The apparatus manufactures fuel from organic sludge efficiently and inexpensively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel-formation method of organic sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of fuel-formation apparatus of organic sludge. (Drawing includes non-English language text).    Fuel-formation apparatus of organic sludge (1)    Heat exchanger (7)    Indirect heating type sludge fuel formation apparatus (11)    Waste gas (G1-G5)    Heat-medium oil (M)
NOVELTY - A fuel-formation apparatus (1) contain a heat exchanger (8) for performing heat-exchanging between the superheated steam and heat-medium oil (M), which is generated using waste gas (G1-G4) of combustion furnace. An organic sludge is dried or carbonized using resultant heated heat-medium oil to manufacture fuel (F).    USE - Apparatus is used for forming fuel (claimed).    ADVANTAGE - The fuel-formation apparatus has excellent voltage resistance. The apparatus efficiently and economically provides harmless fuel having excellent quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel-formation method.    DESCRIPTION OF DRAWING(S) - The drawing shows the flow chart of fuel-formation apparatus.    Fuel-formation apparatus (1)    Cement kiln (2)    Heat exchanger (8)    Fuel (F)    Waste gas (G1-G4)    Heat-medium oil (M)
NOVELTY - The device has a connecting pipeline connecting an upper level processing unit and a lower level processing unit. The connecting pipeline is connected with a water inlet pipe. An end of the connecting pipeline is connected with a water sample collecting end part. A through-hole is formed on a pipe wall of the water inlet pipe, where area of the through-hole is not less than cross-sectional area of the water inlet pipe.    USE - Artificial wetland water sample collecting device for sewage treatment purpose.    ADVANTAGE - The device collects water sample for sewage treatment by utilizing an artificial wetland monitoring process in a convenient manner. The device eliminates the need of a special embedded device and reduces construction cost. The device is simple to manufacture, inexpensive, easy to construct and convenient to use, and has wide application range.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an artificial wetland system, comprising a packed bed.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an artificial wetland water sample collecting device.
NOVELTY - The device has gasification furnace (2) that is connected by lower absorbing type gasification section (3) and up-draft gasification section (6). Up-draft gasification section is installed at lower end of fire grate (8) type gasification section and upper end of primary gasification inlet and ash (11). The device structure is comprised of gas outlet (5) which is installed between absorbing type gasification from lower section of primary gasification agent entrance and up-draft gasification section of the primary gasification agent entrance (9).    USE - Biomass high-efficiency gasification device.    ADVANTAGE - The device provides low tar content and gas component control ability can be achieved. Strong load adaptability can be obtained, so that stable operation can be provided. The efficiency of the gasification device can be increased.    DETAILED DESCRIPTION - An independent claim is included for method for preparing biomass gasification.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biomass high-efficiency gasification device. (Drawing includes non-English language text)    Gasification furnace (2)    Absorbing type gasification section (3)    Gas outlet (5)    Up-draft gasification section (6)    Fire grate (8)    Up-draft gasification section of primary gasification agent entrance (9)    Ash (11)
NOVELTY - The furnace has a grate (2) arranged inside a furnace body (1). The furnace body is provided with a gas outlet (3) and a feed port (8) above the grate. An ash outlet (5) and an ignition port (6) are arranged below the grate. A sidewall of the furnace body is provided with a fuel gas channel above the grate. Ends of the fuel gas channel are interconnected with interiors of a fuel gas outlet and the furnace body. The fuel gas channel is provided with a catalyst (16) i.e. methanation catalyst. A dust outlet is provided with a liquid seal (7).    USE - Biomass gasification furnace.    ADVANTAGE - The furnace has feeding effect, high gas quality, high energy utilization rate and high gas heat value, eliminates gas in tar content, and reduces production time.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification furnace.    Furnace body (1)    Grate (2)    Gas outlet (3)    Ash outlet (5)    Ignition port (6)    Liquid seal (7)    Feed port (8)    Catalyst (16)
NOVELTY - The craft has gasification furnace (5,6) in which herbaceous or woody biomass powder raw material is deposited at feeding port of the lower portion of the furnace. The gasification reaction gas solid mixture of biomass gas contains un-reacted carbon-containing solid substance and tar at bottom of gasification medium maintained air temperature up to 70 to 80? o. The gas-solid mixture is discharged from top of gasification furnace by fuel nozzle (7). The gas enters into the furnace for purifying and cooling the device, after cooling biomass synthesis gas.    USE - Craft for preparing synthesis gas for agriculture application.    ADVANTAGE - The heating efficiency of the system is improved. The production capacity of the device can be increased with high yield due to simplified process. The carbon conversion can be performed effectively and purifies the gas with high heat value.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the craft for preparing synthesis gas.    Spiral feeder (2)    Bunker (3,4)    Gasification furnace (5,6)    Gas-solid fuel nozzle (7)    Ash chamber (8)
NOVELTY - The system has a gas pipe (37) whose upper part is connected with a filter barrel connected through a gas conveying pipe and a sulfur removal tank (3). The sulfur removal tank is located in a caustic soda solution tank (6). A conveying pipe (8) is entered into a sulfur removal tank liquid distributor (44), a liquid discharging pipe and the removal tank. A clearing liver fire tank (9) is provided with the gas pipe and a vacuum pump (2). The vacuum pump or an outlet pipe of a roots blower (73) is separated from a gas-water tank connected with a drying tank.    USE - System for converting domestic rubbish and solid waste into combustible gas.    ADVANTAGE - The system reduces pollution to an environment and avoids wastage of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a system for converting domestic rubbish and solid waste into combustible gas.    Vacuum pump (2)    Sulfur removal tank (3)    Caustic soda solution tank (6)    Conveying pipe (8)    Clearing liver fire tank (9)    Gas pipe (37)    Sulfur removal tank liquid distributor (44)    Roots blower (73)
NOVELTY - The method involves conveying biomass material to microwave carbonization device (2). Heat decomposition gas is lead to combust with oxidant (13). Gasification agent is conveyed to reduction area to reduce with carbon-containing fuel to generate synthetic gas (23). Synthetic gas produced in high temperature gasification furnace (11) is conveyed to purification device (16). Purified synthetic gas is lead to pass through sensible heat recovery device (18) to absorb sensible heat of synthetic gas. Synthetic gas temperature is controlled in outlet of recovery device.    USE - Biomass gasification method.    ADVANTAGE - Coke content in synthetic gas is reduced by heat decomposition and gasification. The produced synthetic gas is free of coke and achieves high heat value by adopting advanced microwave heating technology in the carbonization stage. Gasification efficiency and carbon conversion rate are improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the biomass gasification device.    Microwave carbonization device (2)    High temperature gasification furnace (11)    Oxidant (13)    Purification device (16)    Sensible heat recovery device (18)    Synthetic gas (23)
NOVELTY - The method involves attaching cold face insulation to the interior surface of the shell, and positioning hot face insulation over a secondary side of the cold face insulation. The hot face insulation is secured to the cold face insulation by inserting an auger into the hot face insulation and partially into the cold face insulation, without securing the hot face insulation to the outer shell, and without preparing a securement portion for the anchor.    USE - Method for securing hot face insulation to cold face insulation in enclosed heating area e.g. kiln, furnace, incinerator, process heater and fuel cell (all claimed).    ADVANTAGE - Since the hot face insulation is secured to the cold face insulation by inserting an auger into the hot face insulation and partially into the cold face insulation without securing the hot face insulation to the outer shell, and without preparing a securement portion for the anchor, damage occurring to high temperature insulation can be prevented, and timely and cost-effective maintenance can be provided for the interior of the furnace, due to which lower cost and thermally efficient lining with broken or staggered seams to combat the flow of heat can be provided.    DESCRIPTION OF DRAWING(S) - The drawing shows a front perspective view of the ceramic bolt.    Ceramic lag bolt (10a)    Drive head (12)    Shank (14)
NOVELTY - The apparatus has a processing tank (6) performing drying, powdering and high British thermal unit gasification of organic-refuse biomass. A gas turbine (7) burns and drives high calorie gas generated for generation of electric power, where the high calorie gas is generated by the processing tank. An electric power generator (12) is connected with the gas turbine. A high temperature gas selection program selects high temperature air or superheated steam supplied to the processing tank.    USE - Apparatus for generating electricity from organic-refuse biomass.    ADVANTAGE - The gas turbine can burn the organic-refuse biomass without consuming the fossil fuel, and generates electricity from the high calorie gas generated by performing high British thermal unit gasification, so that generation of by-product during gasification can be minimized, thus increasing power generation efficiency of the apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an apparatus for generating electricity from organic-refuse biomass.    Air supply apparatus (1)    Water supplying apparatus (2)    T-shaped coupling (3)    Processing tank (6)    Gas turbine (7)    Electric power generator (12)
NOVELTY - The method involves decomposing to-be-processed oil by indirect heating under reduced pressure. Condensation for condensing distillation gas is generated by thermal decomposition. An oil-water separation for separating the condensate is generated at the condensation. Residues generated by the thermal decomposition are recovered as a carbonized material (23). A stirring contact of the thermal decomposition with the carbonized material is carried out to heat the to-be-processed oil. Pressure reduction operation of the thermal decomposition is performed in noncondensable gas.    USE - Method for purifying waste oil i.e. biodiesel fuel.    ADVANTAGE - The stirring contact of the thermal decomposition with the carbonized material is carried out to heat the to-be-processed oil so as to obtain fuel oil in an easy manner, thus reducing energy cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for purifying waste oil.'(Drawing includes non-English language text)'    Purifier main body (A)    Material supply unit (B)    Carbonized material collection unit (C)    Horizontal type agitator (13)    Carbonized material (23)
NOVELTY - Method for producing biogas, involves performing anaerobic fermentation of at least one micro algae chosen from Euglena, Chlorella, Scenedesmus, and Chlorococcum.    USE - The method is useful for producing of biogas, preferably methane which is used as fuel for factory, protected horticulture and city gas pipeline.    ADVANTAGE - The method is cost-effective and environmentally-friendly, can be performed within short period of time, and consumes less energy.
NOVELTY - A composition suitable for bioalcohol production comprises a feedstock comprising holocellulose; and an aqueous acid solution containing formic acid (at least 90%) based on total acid weight.    USE - As a composition for bioalcohol production and for treating a feedstock selected from wood or forestry residue, municipal paper waste, algae, agricultural residue, or dedicated energy crop (claimed).    ADVANTAGE - The composition is environmentally friendly, and provides cost-efficient production of fuels. The use of formic acid concentration in the method often has high efficiency and good performance in dissolving feedstocks comprising holocellulose such as switchgrass sawdust.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for treating a feedstock comprising holocellulose involving: a) mixing the feedstock with an aqueous acid solution of an initial pH of 1-3 at 25 degrees C, where the acid comprises 1-30 wt.% based on the total weight of the aqueous acid solution; and b) hydrolyzing the mixture under conditions sufficient to produce a product comprising monosaccharides and water-soluble oligosaccharides, where the sum of monosaccharides and water-soluble oligosaccharides is at least 50 wt.% of the total holocellulose in the lignocellulosic feedstock.
NOVELTY - The device (13) has feedstock supply pipe that supplies biomass feedstock from above in vertical direction. The pulverizing rollers (16) are connected to pulverizing table (14) with taper shaped opening for pulverizing biomass feedstock. Blower is provided for creating upward current, and separator is provided for classifying pulverized biomass powder. A vertical rim (14a) is provided with slits (32) that are extended towards lower portion of pulverizing rollers to form prescribed gap with upper surface of vertical rim.    USE - Pulverizing device of biomass and coal mixed combustion system (claimed) used in electric power generation application.    ADVANTAGE - The biomass feedstock can be pulverized efficiently and stably by providing slits that are extended towards lower portion of pulverizing rollers to form prescribed gap with upper surface of vertical rim.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass and coal mixed combustion system has boiler furnace to which bio-mass powder pulverized by biomass pulverization device, and coal-dust particles pulverized by coal pulverization device are supplied.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the pulverizing device.    Pulverizing device (13)    Pulverizing table (14)    Vertical rim (14a)    Pulverizing roller (16)    Silt (32)
NOVELTY - The method involves separating gas mixture (1) from solventless gas flow (9) and a solvent e.g. methanol, enriched liquid flow (11) by cooling and partial condensing. The solventless gas flow is separated by cryogenic distillation and/or cryogenic washing to form carbon monoxide enriched flow (17) and hydrogen enriched flow (19). The solventless gas flow is not allowed to contain carbon dioxide, where pressure of the solvent enriched liquid flow ranges between 20 and 70 bar Abs.    USE - Method for separating a gas mixture containing hydrogen, carbon monoxide, solvent e.g. methanol (claimed), rectisol, selexol and methane.    ADVANTAGE - The method enables separation of the gas mixture without requiring regeneration, at reduced installation cost while reducing volume of the installation unit and solvent loss.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an installation unit for separating a gas mixture containing hydrogen, carbon monoxide, acid gas and methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an installation unit for separating a gas mixture containing hydrogen, carbon monoxide, acid gas and methane.    Gas mixture (1)    Solventless gas flow (9)    Enriched liquid flow (11)    Carbon monoxide enriched flow (17)    Hydrogen enriched flow (19)
NOVELTY - The method involves coating a catalyst ink (20), which is distributed with catalyst-carrying carbon and an electrolyte in a lower monoalcohol on a base material (18), and forming a catalyst ink layer on the base material. Polyhydric alcohol (24) is coated on a surface of the catalyst ink layer. The catalyst ink layer is dried. An ink tank (12) is connected with a die head (16) through an ink supply piping (14).    USE - Method for manufacturing an electrode for a fuel cell.    ADVANTAGE - The catalyst ink layer is dried, where surface of the catalyst ink layer is coated with polyhydric alcohol, and the ink tank is connected with the die head through the ink supply piping, so that the catalyst ink can be dried easily, thus suppressing crack in the coating film, and hence improving shortage of the ink in the time of printing and intermittent coating property.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for manufacturing an electrode for a fuel cell.'(Drawing includes non-English language text)'    Ink tank (12)    Ink supply piping (14)    Die head (16)    Base material (18)    Catalyst ink (20)    Polyhydric alcohol (24)
NOVELTY - The device (10) has an interstice (20) formed between the electrode assemblies (16,18), through which hydrogen containing medium is passed. A voltage source (26) produces high voltage for a time duration of less than 1 mu s between electrode assemblies so as to produce electric field in interstice, for separating hydrogen from molecules of hydrogen containing medium. The electrode assembly has pair of round/ball shaped electrodes (22,24).    USE - Device for recovering hydrogen from hydrogen containing medium e.g. water, natural gas and hydrocarbon used in fuel cell of vehicle.    ADVANTAGE - The separation of hydrogen from hydrogen containing medium can be performed reliably, with smaller electric field strength. The energy loss due to intermediate storage of hydrogen can be suppressed. Also the breakdown of electrodes can be prevented due to short voltage pulses.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for recovering hydrogen from hydrogen containing medium.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of device for recovering hydrogen from hydrogen containing medium.(Drawing includes non-English language text)    Hydrogen recovering device (10)    Electrode assemblies (16,18)    Interstice (20)    Electrodes (22,24)    Voltage source (26)
NOVELTY - The device has an electronic display analysis controller connected with a garbage guiding separator, a garbage biomass gasification device, an integral type electrostatic field separation device and a solid product recovery device. The controller monitors the separator, gasification device, separation device and recovery device feeding and discharging operations. The separation device is utilized for separating a product through a feeding channel. A separating device part is provided with a plasma intermittent nozzle.    USE - Kitchen rubbish biomass separating device.    ADVANTAGE - The device ensures safety during kitchen garbage biomass separation process, resource and harmless treatment on the kitchen waste, avoids the damage of swill from the source and solves resource shortage problem.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a kitchen rubbish biomass separating device.'(Drawing includes non-English language text)'
NOVELTY - The furnace has a cylindrical gasification furnace (3) whose oxidation zone of a cylinder wall or lower part reducing area of the cylinder wall is uniformly distributed with multiple air nozzles (4). A peripheral wall of a cylinder of the nozzles is hermetically sleeved with a gasification fan (1) and connected with gasification furnace annular bellows (2). An ash base (8) or a lower part of the gasification furnace on an upper part of a dry pyrolysis area on a cylinder wall part is provided with a gas outlet. The gas outlet is connected with a fuel gas draught fan (7) through a pipeline.    USE - Fixed bed biomass gasification furnace for use in an air craft (claimed).    ADVANTAGE - The furnace realizes balance uniform distribution, solves the burning phenomenon, improves the oxidation temperature, and reduces the tar content, so as to improve the gas quality and gasification efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fixed bed biomass gasification furnace.    Gasification fan (1)    Gasification furnace annular bellows (2)    Cylindrical gasification furnace (3)    Air nozzles (4)    Fuel gas draught fan (7)    Ash base (8)
NOVELTY - The furnace has a furnace body (5) located in a cavity formed in a furnace liner (8), where a lower end of the furnace liner is provided with a grate. A material box (10) is connected with a feeding pipe (13) and arranged at an inner end of the furnace liner. The feeding pipe is equipped with a material pushing auger, where a transmission of the material pushing packing auger is connected with a feeding motor. A wall part of the furnace liner is provided with multiple ventilation holes (4). The grate is installed with an electric heating ignition pipe (3).    USE - Automatic straw grain feeding and gasification furnace.    ADVANTAGE - The furnace adopts a control motor stalling process to ensure that straw particle material is automatically added, and automatically controls charging time, charging time interval and unit time in charging number, thus ensuring high degree of automation.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an automatic straw grain feeding and gasification furnace in partial section.    Electric heating ignition pipe (3)    Ventilation holes (4)    Furnace body (5)    Furnace liner (8)    Material box (10)    Feeding pipe (13)
NOVELTY - The analyzer has gas valves (6) connected with a hydrogen sampling pipe (11), an oxygen sampling pipe (12), a nitrogen sampling pipe (13), a carbon monoxide sampling pipe (14), a carbon sampling pipe (15), a methane sampling pipe (16), an ethane sampling pipe (17), an ethylene sampling pipe (18) and an acetylene sampling pipe (19). A lower part of a gas distribution plate (1) is connected with an air inlet pipe (7) and an air inlet valve (8). A gas analyzer unit (10) is provided with an LCD screen (9), a measuring indication lamp (21) and a gas measuring switch (20).    USE - Analyzer for a gas switching device in a coal mine.    ADVANTAGE - The analyzer has accurate sampling, rapid analysis, safety, stability, advanced design and rational structure. The analyzer adopts micro computer program control, which supports to measure various gases.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an analyzer.    Gas distribution plate (1)    Gas valves (6)    Air inlet pipe (7)    Air inlet valve (8)    LCD screen (9)    Gas analyzer unit (10)    Hydrogen sampling pipe (11)    Oxygen sampling pipe (12)    Nitrogen sampling pipe (13)    Carbon monoxide sampling pipe (14)    Carbon sampling pipe (15)    Methane sampling pipe (16)    Ethane sampling pipe (17)    Ethylene sampling pipe (18)    Acetylene sampling pipe (19)    Gas measuring switch (20)    Measuring indication lamp (21)
NOVELTY - The cover has a cover body (1) for covering a furnace reaction chamber, and a feeding device (2) provided on the cover body. The feeding device comprises a feed port (3) and a housing (4) that is hollow inside and connected to the furnace reaction chamber through the cover body. An U-shaped hopper (5) is provided for conveying a biomass material from a feed port to the furnace reaction chamber by circumlocutory overturning, and equipped in a housing. A lower part of the cover body is provided with a filtering path (6).    USE - Multifunctional furnace cover for a biomass gasification furnace.    ADVANTAGE - The cover effectively carries out filtration and continuous feeding under a sealing condition of the furnace reaction chamber. The cover has a simple and ingenious structure. The cover can effectively filter the tar, such that the tar can flow into the furnace reaction chamber through gaps or pores provided on the filtering path under high temperature for combustion such that cleanliness of the filtering path is improved and smoothness is guaranteed.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a multifunctional furnace cover.    Cover body (1)    Feeding device (2)    Feed port (3)    Housing (4)    U-shaped hopper (5)    Filtering path (6)
NOVELTY - The method involves charging pyrolyzation gas generated by a pyrolyzation furnace (1) to an upper side of a gasification furnace (3), or charging the gas to a cyclone separator (4) with coal gas from the gasification furnace. A solid granule captured by the cyclone separator is conveyed to a dense phase area of the pyrolyzation furnace by a returning unit (5). A gasification temperature of the gasification furnace is 900-1200 degrees Celsius. Pyrolyzation temperature of fuel in the pyrolyzation furnace is 50-200 degrees Celsius.    USE - Pyrolytic gasification combining method for use in a pyrolyzation and gasification of a coal, biomass and other carbon materials.    ADVANTAGE - The method enables obtaining the generated coal gas with high heat value, and obtaining low tar content. The method enables combining the pyrolytic gasification in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a pyrolytic gasification combining device, comprising a pyrolyzation furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a pyrolytic gasification combining device.    Pyrolyzation furnace (1)    Gasification furnace (3)    Cyclone separator (4)    Returning unit (5)    Air-powered control valve (21)
NOVELTY - Lipase produced from Pichia NRRL Y-7723 strain at low temperature, is new.    USE - The lipase which is used as biodiesel catalyst, chiral compound catalyst, esterification reaction catalyst, ester linkage hydrolysis reaction catalyst and enzyme detergent (all claimed).    ADVANTAGE - The lipase enzyme reduces the production cost of biodiesel, chiral compound, ester linkage hydrolysis reaction and esterification reaction, and provides enzyme detergent having excellent cleanability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a vector, which comprises a amino acid sequence of SEQ ID NO: 1.
NOVELTY - The unit has a baffle that is fixed on the bottom plate separately, and an earthworm penetrating network. The earthworm penetrating network is located between the baffles, and the earthworm penetrating network penetrates both the ends of the network to be connected with the baffles. The baffles and earthworm penetrating network cultivates the space for earthworm. The reaction tank has a water collecting slot (2) in which the side wall is located on the drainage hole (5), a heat preservation layer (4) and a heating device (1).    USE - Multiple layer intermittent type earthworm bio-reactor for processing organic waste resource of mechanical device.    ADVANTAGE - The process of earthworm and earthworm manure Separation can be simplified. The strength of working labor can be reduced. The cleaning earthworm manure when dissembling the earthworm bio-reactor can be processed conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of multiple layer intermittent type earthworm bio-reactor.    Heating device (1)    Water collecting slot (2)    Upper nozzle (3)    Heat preservation layer (4)    Drainage hole (5)
NOVELTY - The furnace has air inlet and outlet pipes (9,10) positioned vertically on sides of a straw gasification chamber (3). The air outlet pipe is passed through a separating plate (7) and connected with a movable gas stove (6). A fire grate (12) is positioned between gasification chamber and ash storage chamber (4). The lower pipe ports (13,14) of air inlet and outlet pipes are passed through the fire grate and made to enter into ash storage chamber. An air vent (16) is formed in air inlet pipe corresponding to center of gasification chamber. An ash outlet (17) is formed on ash storage chamber.    USE - Heating type straw gasification furnace.    ADVANTAGE - Since the lower pipe ports of air inlet and outlet pipes pass through fire grate and into the ash storage chamber, the tar formed in chamber can be cracked when gas passes through air inlet and outlet pipes, and the environment can be protected. Since the shell is formed in jacketed structure, the generation of waste water can be avoided, and the pollution can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heating type straw gasification furnace.    Straw gasification chamber (3)    Ash storage chamber (4)    Movable gas stove (6)    Separating plate (7)    Air inlet pipe (9)    Air outlet pipe (10)    Lower pipe ports (13,14)    Air vent (16)    Ash outlet (17)
NOVELTY - An immobilization method of carbon dioxide gas involves contacting carbon dioxide gas containing gases such as air to biological tissue of human such as head hair, and immobilizing carbon dioxide gas between hair stem cells of head hair by hair treatment agent. The hair treatment agent has carbon dioxide gas adsorption agent comprising intercalation compound which consists of layer compound previously prepared for head hair, and interlayer substance.    USE - An immobilization method of carbon dioxide gas.    ADVANTAGE - The method immobilizes carbon dioxide gas safely and inexpensively.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a hair collecting system;    (2) a collecting system;    (3) a hair pulverization method;    (4) a plant type carbon fiber;    (5) a rooftop greening base material;    (6) a greening nurturing substrate material;    (7) an organic fertilizer;    (8) a manufacturing method of concrete; and    (9) a dispersion method of heavy metal in ashes.
NOVELTY - The apparatus has a fuel utilized by oxygen and hydrogen. A controller section controls electricity that is generated by a fuel cell portion. An air inlet port supplies oxygen from air to a power divider. The fuel cell portion is replaced with the electric circuit. A hydrogen sensor part and an inlet part is provided with a hangar, where an inlet inhales hydrogen. A generator substrate is mounted on an upper part of the emergency power plant.    USE - Emergency electric power generation apparatus for a nuclear power plant.    ADVANTAGE - The power plant is set up in multiple stories building to avoid flooding of the tsunami, so that safety of the atomic electrical power plant is maintained. The generator substrate is maintained with multiple stories building.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an emergency electric power generation method for nuclear power plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an emergency electric power generation apparatus.