NOVELTY - Composite fertilizer comprises 10-20 pts. wt. plant ash, 20-30 pts. wt. animal feces, 3-8 pts. wt. potassium sulfate, 10-12 pts. wt. carrot leaf, 8-15 pts. wt. stone powder, 1-2 pts. wt. magnetite powder, 5-12 pts. wt. shale and 8-10 pts. wt. humic acid.    USE - The composite fertilizer is useful for crops.    ADVANTAGE - The composite fertilizer can be simply and economically prepared with improved working efficiency and high nutrient content, and without pollutant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composite fertilizer, comprising mixing animal feces, plant ash, carrot leaf and stone powder in a stirrer, drying the mixed materials and then stirring and adding potassium sulfate, magnetite powder, shale and humic acid, conveying the dried material into a pelletizer and then drying.
NOVELTY - Composite rice seedling substrate comprises 50-60 vol.% domestic sludge, 20-30 vol.% charcoal and 20 vol.% nutritional soil.    USE - Used as a composite rice seedling substrate.    ADVANTAGE - The substrate utilizes wide range of resources, so as to achieve good quality rice seedlings; transforms organic waste which can be re-utilized; maintains ecological balance; facilitates the growth of rice seedling in a greenhouse room under sunlight, where the seedling growth can be observed; and promotes good growth of rice seedlings based on experimental results.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the substrate, comprising dehydrating domestic sludge, drying, and sieving to obtain particles with 1-4 mm particle size, and uniformly mixing by adding nutritional soil and charcoal, fermenting, adjusting the acid content, to obtain the product.
NOVELTY - Manufacturing photosynthetic bacteria fertilizer comprises mixing photosynthetic bacteria, Azotobacter chroococcum, Bacillus megaterium, Bacillus, and actinomycete, mixing bran, soybean meal, hydroxylapatite, and water uniformly, sterilizing, cooling, adding the strain, stirring uniformly to prepare solid culture agent, spreading the solid culture agent on the clean cement soil, covering with algae and rice straw, turning once a day, fermenting to obtain bacterial fertilizer, adding strain into fermented deodorized organic fertilizer, and stirring uniformly.    USE - The method is useful for manufacturing photosynthetic bacteria fertilizer (claimed).    ADVANTAGE - The method has simple processing technique. The fertilizer contains whole nutrients, has high utilization rate, and is environmentally friendly.    DETAILED DESCRIPTION - Manufacturing photosynthetic bacteria fertilizer comprises (i) mixing photosynthetic bacteria, Azotobacter chroococcum, Bacillus megaterium, Bacillus, and actinomycete according to ratio of 1:1, (ii) mixing 50% bran, 10% soybean meal, 10% hydroxylapatite, and 30% water uniformly, sterilizing, cooling, adding the strain, stirring uniformly to prepare solid culture agent, (iii) spreading the solid culture agent on the clean cement soil, covering with algae and rice straw, turning once a day, fermenting for 7 days to obtain bacterial fertilizer, where the amount of bacteria per gram is 1.5x 109 e/a, and (iv) adding 20% strain into 80% fermented deodorized organic fertilizer, and stirring uniformly to obtain the fertilizer.
NOVELTY - Organic-inorganic fertilizer comprises a molasses fermentation broth, 10-25 wt.% of a water-soluble nitrogen, water-soluble phosphate and water-soluble potassium, 15-40 wt.% of an organic material, 5-10 wt.% of a biological bacteria, and 1-3 wt.% of ferrous sulfate. The molasses fermentation broth is present in sufficient amount to make up to 100%, and contains 35-95 wt.% of molasses solution.    USE - The fertilizer is useful for crop plants.    ADVANTAGE - The fertilizer can be economically prepared using waste materials in an industrial manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer, comprising (1) adding the molasses fermentation broth, the organic material and the biological bacteria in a fermentation tank, (2) adding ferrous sulfate to the tank with stirring, (3) fermenting the mixture for 16-28 hours at room temperature, precipitating to remove insoluble matter, discarding colloidal fermentation broth, and reacting at high temperature for inactivation, and (4) adding the water-soluble nitrogen, water-soluble phosphate and water-soluble potassium to molasses fermentation broth with stirring, granulating and drying.
NOVELTY - Microbial rice seedlings matrix comprises deep peat, straw, rice hull, livestock manure fermented material, perlite, vermiculite, bio-organic fertilizer and microbial strains. The total amount of deep peat, straw, perlite and vermiculite, is 65-75 wt.%. The total amount of perlite and vermiculite, is 5 wt.%. The total amount of microbial strains is 1 wt.%. The total amount of bio-organic fertilizer is 4 wt.%. The amount of rice hull and livestock manure fermented material, used accounts to the remaining amount.    USE - The matrix is useful for developing rice root system.    ADVANTAGE - The matrix saves time and labor intensity than traditional rice seedling; does not scatter when applied on roots, and require additional nutrition components; has strong disease resistance; and is suitable for mechanical transplanting, and large-scale plant nursery field.
NOVELTY - Substrate fermentation involves utilizing paper making sludge, mushroom residue and sawdust, where volume ratio of paper making sludge, mushroom residue and sawdust is 1-3:6-8:1. Urea is added to the obtained material, and then mixed. The mixed material is fermented at 55-60 degrees C. The obtained material is fermented at 50-55 degrees C, and then fermented at 40 degrees C, where time duration is 15-20 days. The obtained material is dried in a drying device. The obtained compost is mixed with perlite and peat to obtain the substrate.    USE - Method for fermenting substrate used in nursery (claimed) and for cultivating Eucalyptus.    ADVANTAGE - The method is simple, convenient and enables to produce substrate that is eco-friendly and cost-effective, and has improved resistance and growth speed.
NOVELTY - Method for enriching coalbed methane involves adsorbing methane in coalbed methane using diethyl ether solvent, desorbing solvent-rich liquid, separating methane, collecting methane-rich gas, removing diethyl ether, and obtaining methane product.    USE - Method for enriching coalbed methane (claimed).    ADVANTAGE - The method enables economical enrichment of coalbed methane with methane recovery rate of 85.38%, by simple process.
NOVELTY - Preparation of aspirin comprises adding salicylic acid to acetic anhydride, mixing with catalyst, heating and stirring at 65-85 degrees C for 25-55 minutes, adding ice water, dissolving acetic anhydride for 15 minutes, separating out solid, filtering, washing with cold water, drying to obtain crude aspirin, adding saturated sodium carbonate solution, stirring, filtering, adding to beaker filled with concentrated sulfuric acid, stirring, gradually separating out solid, cooling solid matter in ice water bath, filtering, and drying.    USE - Method for preparing aspirin (claimed).    ADVANTAGE - The catalyst does not cause corrosion to device and potential pollution and can be repeatedly use and the product has high yield.
NOVELTY - Environment-friendly clean production of glycine comprises reacting hydroxy acetonitrile and ammonium hydrogen carbonate, ammonia gas, and water or hydroxy acetonitrile with carbon dioxide, ammonia and water; rapidly heating, hydrolyzing; recovering unreacted carbon dioxide and ammonia gas mixture to obtain glycine water solution, recycling carbon dioxide and ammonia gas mixture; concentrating glycine solution, cooling and crystallizing to obtain glycine crystals, recycling crystallization mother liquor, mixing with mixture obtained in third step and batch concentrating.    USE - Method for producing glycine (claimed).    ADVANTAGE - The method reduces by-product, has high raw material conversion rate and high glycine yield, produces stable glycine, and solves pollution problems.    DETAILED DESCRIPTION - Environment-friendly clean production of glycine comprises reacting hydroxy acetonitrile and ammonium hydrogen carbonate, ammonia gas, and water or hydroxy acetonitrile with carbon dioxide, ammonia, and water at 4-7 MPa and 80-120 degrees C to obtain reaction mix liquid; rapidly heating mix liquid to 120-200 degrees C, hydrolyzing at 4-7 MPa; recovering unreacted carbon dioxide and ammonia gas mixture to obtain glycine water solution, recycling carbon dioxide and ammonia gas mixture; concentrating glycine solution, cooling and crystallizing to obtain glycine crystals, recycling crystallization mother liquor, mixing with mixture obtained in third step and batch concentrating. An INDEPENDENT CLAIM is included for glycine production device comprising static mix reactor, hydrolyzing reaction kettle, gas stripping tower, concentrate kettle, crystal kettle, first level static mix reactor, and second level static mix reactor.
NOVELTY - Preparation of florfenicol succinate comprises dissolving florfenicol in organic solvent, adding succinic anhydride, stirring under catalyst reaction for 4-10 hours, distilling, removing solvent, adding sodium bicarbonate, filtering until no bubbles, adjusting pH of filtrate, stirring to precipitate crystals, filtering, washing with water, drying, dissolving in water-soluble organic reagent, adding activated carbon, heating to 40-45 degrees C for 20-30 minutes, filtering, pouring into distilled water, stirring, standing to precipitate crystals, filtering, washing, and drying to obtain white solid.    USE - Method for preparing florfenicol succinate (claimed).    ADVANTAGE - The simple, cost-saving and environment-friendly method has short reaction time and product yield of 85%.    DETAILED DESCRIPTION - Preparation of florfenicol succinate comprises dissolving florfenicol in organic solvent, adding succinic anhydride, stirring under catalyst reaction for 4-10 hours, distilling under reduced pressure, removing solvent, adding sodium bicarbonate, filtering until no bubbles, adjusting pH of filtrate to 2, stirring to precipitate crystals, filtering, washing with water, drying in oven, dissolving in water-soluble organic reagent, adding activated carbon, heating under stirring to 40-45 degrees C for 20-30 minutes, filtering, pouring filtrate into distilled water, stirring, standing in refrigerator to precipitate crystals, filtering, washing, and drying in oven to obtain white solid.
NOVELTY - Preparation of denagliptin key intermediate (I) comprises mixing acetonitrile and potassium tert-butoxide, heating, adding toluene and acetonitrile to obtain amino compound (V), heating, adding hydrochloric acid, reacting obtain amino compound (IV), adding organic base, high temperature reacting to obtain nitro compound (III), adjusting pH to obtain benzene derivative (II), and reacting.    USE - Method for preparing denagliptin key intermediate (claimed).    DETAILED DESCRIPTION - Preparation of denagliptin key intermediate of formula (I) comprises mixing acetonitrile and potassium tert-butoxide, heating, adding toluene and acetonitrile to obtain amino compound of formula (V), heating, adding hydrochloric acid, reacting obtain amino compound of formula (IV), adding organic base, high temperature reacting to obtain nitro compound of formula (III), adjusting pH to obtain benzene derivative of formula (II), and reacting.    P'=H, t-butoxycarbonyl, benzyl or benzyloxycarbonyl.
NOVELTY - Preparation of 1,2,3-triazole compound involves reacting terminal alkyne compound and organic azide compound as raw materials, in presence of pullulan triazole/cuprous chloride as catalyst and water as solvent. The molar ratio of terminal alkyne compound, organic azide compound, pullulan triazole and cuprous chloride is 100:100:0.1-5:0.001-1. The terminal alkyne compound is 1-(ethynyloxy)-4-nitrobenzene (I), 1-chloro-4-(ethynyloxy)benzene (II), 1-(ethynyloxy)-4-methylbenzene (III), (ethynyloxy)benzene (IV), 1-ethynyl-4-propylbenzene (V) and 1-ethyl-4-(ethynyloxy)benzene (VI).    USE - Preparation of 1,2,3-triazole compound (claimed).    ADVANTAGE - The method environmentally-friendly and stably provides 1,2,3-triazole compound with high yield and reliability, and reduced usage amount of catalyst, by a simple process. The catalyst used in method has excellent reusability.    DETAILED DESCRIPTION - Preparation of 1,2,3-triazole compound involves reacting terminal alkyne compound and organic azide compound as raw materials, in presence of pullulan triazole/cuprous chloride as catalyst and water as solvent, at room temperature to 100 degrees C. The molar ratio of terminal alkyne compound, organic azide compound, pullulan triazole and cuprous chloride is 100:100:0.1-5:0.001-1. The terminal alkyne compound is 1-(ethynyloxy)-4-nitrobenzene of formula (I), 1-chloro-4-(ethynyloxy)benzene of formula (II), 1-(ethynyloxy)-4-methylbenzene of formula (III), (ethynyloxy)benzene of formula (IV), 1-ethynyl-4-propylbenzene of formula (V) and 1-ethyl-4-(ethynyloxy)benzene of formula (VI). The organic azide compound is ethyl-2-azidoacetate, azidobenzene of formula (VII), (azidomethyl)benzene of formula (VIII), 1-azido-3-chlorobenzene of formula (IX), 1-azido-3-nitrobenzene of formula (X) and 1-azido-3-chloropropane of formula (XI).
NOVELTY - Combined treatment of polycyclic aromatic hydrocarbon polluted soil and municipal organic waste comprises mixing 40-50 pts. wt. organic waste, 25-40 pts. wt. polycyclic aromatic hydrocarbon polluted soil, 5-10 pts. wt. waste biomass and 5-30 pts. wt. additive at not less than 10 degrees C, stacking and fermenting. The organic waste comprises kitchen garbage, sludge and/or livestock garbage. The waste biomass comprises straw, rice hull, sawdust, tree bark, bagasse and/or mushroom residue. The additive comprises diatomite, activated carbon, ferric chloride and magnesia.    USE - Method for combined treatment of polycyclic aromatic hydrocarbon polluted soil and municipal organic waste (claimed).    ADVANTAGE - The simple and fast method does not add organic fertilizer or other additives. By adapting combined treatment, the method greatly reduces single-process cost.
NOVELTY - Synthesizing vinpocetine comprises using vincamine as raw material, hydrolyzing, dehydrating, reacting with ethyl ester, carrying out separate extraction, purifying, and crystallizing to obtain vinpocetine.    USE - Method for synthesizing vinpocetine (claimed).    ADVANTAGE - The method is simple and environment-friendly, has high yield and can provide product having high purity.
NOVELTY - A clarithromycin intermediate methyl compound is prepared by subjecting erythromycin to conventional process by hydroxyl etherification protection and silylation protection of 2' and 4''-hydroxyl, dissolving in non-protonic solvent, water-insoluble solvent, and/or bottom water-soluble polar solvent, adding methylation reagent and phase transfer catalyst, continuously stirring, controlling temperature, adding powder of strong base, stirring for 1 hour, layering, separating aqueous phase, adding solvent extraction agent to aqueous phase, combining organic phase, washing, and recovering solvent.    USE - Preparation of clarithromycin intermediate methyl compound (claimed).    ADVANTAGE - Preparation process is safe, low-cost, and environment-friendly and has good product quality and selectivity, high product yield, easy solvent recovery, low toxicity and catalyst dosage, and stable reaction.    DETAILED DESCRIPTION - A clarithromycin intermediate methyl compound is prepared by subjecting erythromycin to conventional process by hydroxyl etherification protection and silylation protection of 2' and 4''-hydroxyl, dissolving in non-protonic solvent, water-insoluble solvent, and/or bottom water-soluble polar solvent, adding methylation reagent and phase transfer catalyst, continuously stirring until uniform, controlling temperature, gradually adding powder of strong base, stirring for 1 hour, stirring water and layering, separating aqueous phase, adding solvent extraction agent to aqueous phase, combining organic phase, washing with water, and recovering solvent.
NOVELTY - Diosgenin is flocculated and extracted by crushing Dioscorea zingiberensis, soaking in sodium dodecyl sulfate solution (SDS), ultrasonically extracting for 2-4 hours, centrifuging, filtering residue, repeating, and combining extracts; adding flocculant A, stirring, standing for 5-20 minutes, filtering, adding 2-6 wt.% flocculant B, standing at 40-50 degrees C for 1-3 hours, centrifuging, and combining residues; and adding sulfuric acid, hydrolyzing at 105-108 degrees C for 4-6 hours, cooling, neutralizing, filtering, washing with water, drying, reflux extracting, cooling, and crystallizing.    USE - Method for flocculating and extracting diosgenin (claimed).    ADVANTAGE - The process is simple, low-cost, clean and environment-friendly.    DETAILED DESCRIPTION - Diosgenin is flocculated and extracted by: (A) crushing Dioscorea zingiberensis, soaking in sodium dodecyl sulfate solution (SDS), ultrasonically extracting for 2-4 hours, centrifuging, filtering residue, repeating, and combining extracts; (B) adding 0.8-1.2 wt.% flocculant A at volume ratio of 100:4-10, stirring, standing for 5-20 minutes, filtering, adding 2-6 wt.% flocculant B, standing at 40-50 degrees C for 1-3 hours, centrifuging, and combining residues; and (C) adding 1.3-1.8 mol/L sulfuric acid at ratio of 1 g:2.5-3 mL, hydrolyzing at 105-108 degrees C for 4-6 hours, cooling, neutralizing, filtering, washing with water, drying, reflux extracting, cooling, and crystallizing. Flocculant A comprises 95-100 wt.% chitosan and 0-5 wt.% xanthan gum. Flocculant B comprises 55-60 wt.% bar-shaped bentonite and 40-45 wt.% bentonite clarifier.
NOVELTY - Preparation of crop organic fertilizer comprises coarse crushing protein-rich animal body into blocks of less than 4 cm, steam heating at 120 degrees C for 5-10 minutes, fine crushing to 80-150 mesh at less than or equal to 70 degrees C by colloid mill at rotating speed of 30-300 revolutions/minute, feeding 20-40 tons into fermentation tank, adding water at weight ratio of 1-4:1, airlift aeration stirring for 20-24 hours, fermenting, adding 0.15-0.3% complex enzyme comprising papain protease and Bacillus subtilis protease at ratio of 1:1, adding 1% yeast, fermenting, centrifuging and filtering.    USE - Method for preparing crop organic fertilizer (claimed).    ADVANTAGE - The fertilizer has protein which is decomposed into small molecule amino acid polypeptide components for convenient plant absorption. It has safe operation, no pollution and harmful residue, and rich nitrogen source and minerals.
NOVELTY - A natural compost composition comprises 250-500 pts. wt. gold needle mushroom residue, 200-350 pts. wt. canal mud, 50-150 pts. wt. peanut, 50-200 pts. wt. chestnut shell, 200-350 pts. wt. bagasse, 50-100 pts. wt. plant ash, 50-120 pts. wt. lime powder and 5-15 pts. wt. viable fungi preparation.    USE - Natural compost composition.    ADVANTAGE - The natural compost composition utilizes waste, thus changing waste into high-value product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composting method using natural compost composition comprising building composting tank which is 2 m long, 1.5 m wide and 0.6 m deep and has plastic film cover, bottom and four sides, weighing raw materials, uniformly mixing plant ash, viable bacteria preparation and gold needle mushroom residue, adding 50-150 pts. wt. water to prepare first mixture, uniformly mixing canal mud, peanut, chestnut shell, bagasse and lime powder to prepare second mixture, stacking second mixture and first mixture, primary fermenting for 24-36 hours and secondary fermenting for 20-30 days.
NOVELTY - A biological organic fertilizer comprises medical stone microbial inoculum and rice bran solid fermentation liquid at weight ratio of 1:1-4. The medical stone microbial inoculum is prepared by taking medical stone which is strain ACCC10388, uniformly stacking and fermenting for 20-26 hours. The rice bran solid fermentation liquid is prepared by taking rice bran which are strain ACCC10634 and strain ACCC10626, and fermenting at water content of 50-60 wt.% and pH of 5.5-8.0 for 5-7 days.    USE - Biological organic fertilizer used for preventing and controlling soil continuous cropping obstacle, and fertilizing shallot, ginger, garlic, cotton, wheat, cucumber, watermelon or melon (claimed).    DETAILED DESCRIPTION - A biological organic fertilizer comprises medical stone microbial inoculum and rice bran solid fermentation liquid at weight ratio of 1:1-4. The medical stone microbial inoculum is prepared by taking medical stone which is strain ACCC10388 and has viable bacteria content of 8x 109-1x 1010 units/mL, uniformly stacking and fermenting for 20-26 hours. The rice bran solid fermentation liquid is prepared by taking rice bran which are strain ACCC10634 having viable bacteria content of 1x 1010-1.5x 1011 units/mL and strain ACCC10626 having viable bacteria content of 1x 109-2x 109 units/mL, and fermenting at water content of 50-60 wt.% and pH of 5.5-8.0 for 5-7 days.
NOVELTY - Tea tree mushroom dreg Agaricus bisporus culture base material comprises main material and auxiliary material. Main material is 150-250 pts. wt. tea tree mushroom dreg. Auxiliary materials are 50-100 pts. wt. grass, 120-180 pts. wt. dairy manure, 5-15 pts. wt. compound fertilizer, 1-2 pts. wt. fermentation agent, 1-3 pts. wt. chlorine imidacloprid urea, 1-2 pts. wt. paclobutrazol, 12-18 pts. wt. gypsum powder and 25-40 pts. wt. lime powder.    USE - Tea tree mushroom dreg Agaricus bisporus culture base material.    ADVANTAGE - The material saves fodder resource, reduces cost and improves total yield.
NOVELTY - Wheat yield insecticidal liquid fertilizer contains 2.1-3.1 wt.% microbial flora, 20-40 wt.% liquid fertilizer, 0.5-1.5 wt.% plant growth regulator, 0.6-1 wt.% pesticide, 1-2 wt.% release agent and balance water.    USE - Wheat yield insecticidal liquid fertilizer.    ADVANTAGE - The fertilizer has 87.9-93.1% drug fatality rate, 11-37% increase rate, 15-38.1% decrease in residual rate, and long-term storage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of wheat yield insecticidal liquid fertilizer comprising mixing microbial flora, fertilizer, plant growth regulator, insecticide, release agent and water, and stirring continuously.
NOVELTY - Fertilizer comprises (in pts.wt.): leguminous plant root (60-120), rapeseed cake (50-120), beet (100-200), sweet potato vine (70-150), plant ash (30-100), shell powder (60-130), fish meal (20-50) and regulator (3-9), which is sodium nitrophenolate and multipaclobutrazol in the mass ratio of 1:1-2:1.    USE - Fertilizer used for crop (claimed).    ADVANTAGE - The fertilizer is cost-effective, is prepared simply, and has improved nutrition value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) selecting leguminous plant root, rapeseed cake, beet, sweet potato vine, plant ash, shell powder, fish meal and regulator;    (B) crushing leguminous plant root, beet and sweet potato vine;    (C) mixing the crushed material with remaining material;    (D) adding water and lime powder to the obtained material;    (E) fermenting the obtained material at 20-35 degrees C for 30-60 days;    (F) drying the fermented material in a drying furnace; and    (G) packaging the dried material to obtain the desired product.
NOVELTY - Mushroom culture material composition comprises (in pts.wt.): sawdust (50-120), white ant nest soil (42-80), edible fungi slag (100-200), pumpkin stem leaf powder (42-85), soybean straw (35-80), reed straw pole (55-100), Abrus herb (20-55), calcium superphosphate (20-48), gypsum powder (35-72) and quicklime (70-120).    USE - Mushroom culture material composition.    ADVANTAGE - The mushroom culture material composition is cost-effective and increases yield and nutrition value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing mushroom culture material composition, which involves:    (A) selecting sawdust, white ant nest soil, edible fungi slag, pumpkin stem leaf powder, soybean straw, reed straw pole, Abrus herb, calcium superphosphate, gypsum powder and quicklime;    (B) mixing sawdust, white ant nest soil, edible fungi slag, pumpkin stem leaf powder, soybean straw, reed straw pole, Abrus herb, calcium superphosphate and gypsum powder;    (C) adding water and quicklime to the obtained material;    (D) fermenting the obtained material at 18-25 degrees C;    (E) packaging the obtained material in bags; and    (F) sealing the obtained bag to obtain the desired product.
NOVELTY - This utility new type relates to one a turner with lifting mechanism, and comprises a bracket main body (1), a bracket main body (1) top part set with a driving room (2), and the bottom set with a track walking mechanism (3) and turning mechanism (4), said lifting mechanism comprises a connecting pole one (7.1), a connecting rod a (7.2) and a connecting rod (7.3), a connecting pole one (7.1) one end and the bracket main body (1) is hinged with the A point, and the other end with the driving room (2) is hinged with the C point, a connecting pole two (7.2) one end and the bracket main body (1) is hinged with the B point, and the other end with the driving room (2) is hinged with the D point, one pole (7.1) is parallel to the connecting pole two (7.2), a connecting pole (7.3) is one end with the connecting pole one (7.1) is a pole body, and the other end is connected with the second pole (7.2) of pole body is hinged with the connecting pole (7.3) is parallel to the AB and CD. This utility new type one a turner with lifting mechanism, use life is long and the work effect is good.
NOVELTY - Oil shale powder forming additive comprises 40-70 wt.% of cement, 10-30 wt.% of sodium silicate and 5-10 wt.% of corn stalk biomass having a granularity size of less than 3 mm.    USE - The oil shale powder forming additive is useful for producing a cold pressing ball (claimed).    ADVANTAGE - The additive can safely and economically produce the cold pressing ball with high porosity and reduced space consumption and without any risk of pollution to the environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing cold pressing ball comprising adding additive to 3-10 wt.% of oil shale powder, where the diameter of cold pressing ball is 30-50 mm, the yield of oil shale powder is more then 90% and the intensity and strength of cold pressing ball is 200-400 N/ball and 600-1000 N respectively; and    (2) preparing additive comprising adding 80 wt.% of oil shale powder in 3-10 wt.% of forming additive, then adding water, uniformly mixing and stirring to obtain mixture, then placing the obtained mixture in roller forming machine for pressing, cooling and then drying, where the diameter of oil shale powder is 30-50 mm, where the diameter of forming additive is 6 mm, preferably 3 mm.
NOVELTY - The fuel oil additive comprises 20-35 pts.wt. of ethyl acrylate, 6-13 pts.wt. of hydrogenated carbonyl, 1-25 pts.wt. of fatty acid ethoxylates, 1-10 pts.wt. of dicyclohexylamine nitrite, 4-12 pts.wt. of dimethyl acetamide, 3-8 pts.wt. of polyisobutylene, 5-25 pts.wt. of ethylene, 10-14 pts.wt. of isopropanol, and 2-6 pts.wt. of ethyl acrylate.    USE - Fuel oil additive.    ADVANTAGE - The fuel oil additive obviously saves fuel, maintains a clean fuel gas system and reduces pollution content of discharge.
NOVELTY - The system comprises a circulation heat pipe, a heating up circulation pipeline set with a hot water circulation pump, and a compressor set with water cooling device of compressor cooling system. The compressor cooling system is designed for heating gas of a heat exchange device.    USE - System for heating biogas purification membrane.    ADVANTAGE - The system comprises a circulation heat pipe and a heating up circulation pipeline set with a hot water circulation pump, and thus reduces energy consumption and gas membrane purification time, and improves energy utilization rate in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for heating biogas purification membrane, which involves dividing heat recovery pipeline into a circulation pipeline and a water circulation loop.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for heating biogas purification membrane. (Drawing includes non-English language text).    Compressor cooling system (1)    Cooling and drying machine (2)    Piezoelectric heating device (3)    Temperature sensor (4)    Water storage tank (6)
NOVELTY - The system comprises a film separating and purifying device (200), source heat pump device (400), a central control device, and a compression control device. The compression device is a compressor.    USE - System for purifying membrane for separating methane biogas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for purifying membrane for separating methane biogas, which involves:    (A) entering gas into compressor for preprocessing;    (B) cooling and drying the gas;    (C) separating the gas by using film purifying device according to different working condition; and    (D) permeating carbon dioxide gas for condensing into liquid carbon dioxide product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for purifying membrane for separating methane biogas. (Drawing includes non-English language text).    Compressing device (100)    Purifying device (200)    Rear compression device (300)    Source heat pump device (400)
NOVELTY - The wood charcoal briquette powder comprises 60-80 vol.% of wood active carbon powder, and 40-20 vol.% of quicklime powder.    USE - Wood charcoal briquette powder.    ADVANTAGE - The wood charcoal briquette powder provides smokeless combustion and reduces environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing wood charcoal briquette powder, which involves:    (A) mixing 40-20 vol.% of quicklime powder and quantitative water uniformity;    (B) cooling the formed mixture for 4-10 hours;    (C) adding 60-80 vol.% of wood active carbon powder in the cooled mixture; and    (D) pressing the formed mixture for rear drying wood active carbon powder to obtain the molded coal.
NOVELTY - Biodiesel production device comprises raw material recycling storage box (1), circulation pump (2), inflow pipe (3), adjustable butterfly valves (4), flowmeters (5), hydrodynamic cavitation reactors (6), upstream pressure gauges (7), hydrodynamic cavitation orifices (8), downstream pressure gauges (9), motors (10), impact chamber (11), return line (12) and non-adjustable butterfly valve (13).    USE - Biodiesel production device.    ADVANTAGE - The device increases yield of biodiesel and shortens production time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biodiesel comprising feeding ethanol and grease in raw material recycling storage tank, adding catalyst, controlling temperature, opening circulation pump, adjusting adjustable butterfly valve, passing through inflow pipe, entering first hydrodynamic cavitation reactor, passing through hydrodynamic cavitation orifices, entering second hydrodynamic cavitation reactor, passing to impact chamber and returning to raw material recycling storage tank.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biodiesel production device.    Raw material recycling storage box (1)    Circulation pump (2)    Inflow pipe (3)    Adjustable butterfly valves (4)    Flowmeters (5)    Hydrodynamic cavitation reactors (6)    Upstream pressure gauges (7)    Hydrodynamic cavitation orifices (8)    Downstream pressure gauges (9)    Motors (10)    Impact chamber (11)    Return line (12)    Non-adjustable butterfly valve (13)
NOVELTY - Bacillus flexus NJNpd41 with the preservation number CGMCC NO.7072, is new.    USE - The Bacillus flexus NJNpd41 is useful for producing agricultural amino acid fertilizer by hydrolysis of rapeseed cake. The agricultural amino acid fertilizer is useful for promoting eggplant growth (all claimed).    ADVANTAGE - The fertilizer reduces the toxin content, and significantly promotes eggplant growth, and increases the quality and yield of the eggplant.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (i) use of Bacillus flexus NJNpd41 for producing functional broth, comprising inoculating Bacillus flexus NJNpd41 into fermentation broth, carrying out submerged fermentation at pH 6-7.5, and at temperature of 30-35 degrees C, stirring speed of 180-200 revolutions per minute for 20-24 hours, to obtain fermentation solution containing 1x 1010 bacterial cells/ml, where the fermentation broth includes 10 g/l glucose, 1 g yeast extract, 1 g/l ammonium sulfate, 0.5 g/l sodium chloride and water (balance), and pH of 7.2-7.5; (2) use of Bacillus flexus NJNpd41 for producing agricultural amino acid fertilizer by hydrolysis of rapeseed cake; (3) producing agricultural amino acid fertilizer by hydrolysis of rapeseed cake, comprising adjusting the rapeseed cake moisture content to 40-50%, adding 1 ton rapeseed cake into 50-60 l functional broth, carrying out solid fermentation, turning 1-2 times a day, recording pile temperature until the temperature returns to room temperature at the end of the fermentation, and at not more than 60 degrees C evaporating 30% water; (4) agricultural amino acid fertilizer, prepared as mentioned above.
NOVELTY - Method of preparing long chain fatty acid ester, involves reacting short chain alcohol with aqueous solution of oil producing microbial cells and converting short chain alcohol to long chain fatty acid ester.    USE - The method is useful for preparing long chain fatty acid ester used for preparing long chain fatty alcohol, aviation fuel and other chemical product (claimed).    ADVANTAGE - The long chain fatty acid ester can be mass produced simply and cost-effectively without adding additional catalyst and complex recombinant bacterial strain with less energy consumption. The method is environmentally-friendly.
NOVELTY - Biodiesel preparation involves separating food waste solid-liquid with acidification by using an inorganic acid, where the separated solid-liquid material is mixed with inoculate yeast cell uniformly for liquid fermentation. The fermentation liquid is filtered, where the residue is crushed with extracting solvent to obtain mixed oil. The solvent is evaporated from the mixed oil to obtain microbial oil of microorganism grease by methyl esterification reaction to obtain biodiesel oil.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method prepares the biodiesel in a simple manner with high product quality on industrial scale.
NOVELTY - A large one turner, a turner comprises a large bracket main body (1), a bracket main body (1) top part set with a driving room (2), and the bottom set with a track walking mechanism (3) and turning mechanism (4), wherein said bracket main body (1) comprises a main plate with front and back two set of parallel and symmetrical (1.1), two a main board (1.1) through connecting plate.
NOVELTY - The utility model relates to a glycerol water desalination unit for the production of biodiesel, glycerin water desalination technologies are biodiesel production, comprising an outlet including a trough concentrator, connected by pipeline and connected to the slot. In the pipeline and trough concentrator is installed between the condenser and turn plate and frame filter, condenser and line filter installed on the machine frame between the diaphragm pump in the line between the condenser and the concentrated feed pump attached to the condenser. The utility model is simple in structure, using a technique of cooling by freezing, the solubility of the salt in the solution is decreased, so that the crystallization, then filtered through a plate and frame filter, the salt filtered off. When the process is running, and the relative costs are greatly reduced and the heating energy is concentrated at reduced production costs.
NOVELTY - Alcohol-based fuel burning furnace comprises alcohol-based fuel that comprises methanol and dimethyl ether in mass ratio of 70-80:20-30. An alcohol-group combustion furnace is set with a gas guide tube. The gas guide tube is set in top side of a fuel storage tank (1). A valve (4) is connected with an alcohol based fuel tube (14). The alcohol based fuel tube is set with a time delay electromagnetic valve (5). The time delay electromagnetic valve is connected with a three-way tube (9). The three-way tube is set with a liquid guiding tube.    USE - Furnace for burning alcohol-based fuel (claimed).    ADVANTAGE - The furnace enables burning alcohol-based fuel is safe and cost-effective.    DETAILED DESCRIPTION - Alcohol-based fuel burning furnace comprises alcohol-based fuel that comprises methanol and dimethyl ether in mass ratio of 70-80:20-30. An alcohol-group combustion furnace is set with a gas guide tube. The gas guide tube is set in top side of a fuel storage tank (1). A valve (4) is connected with an alcohol based fuel tube (14). The alcohol based fuel tube is set with a time delay electromagnetic valve (5). The time delay electromagnetic valve is connected with a three-way tube (9). The three-way tube is set with a liquid guiding tube. Another valve (7) is connected with the alcohol based fuel tube. An INDEPENDENT CLAIM is included for a method for burning alcohol-based fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an alcohol-based fuel burning furnace.    Fuel storage tank (1)    Valves (4,7)    Time delay electromagnetic valve (5)    Three-way tube (9)    Alcohol based fuel tube (14)
NOVELTY - Smoldering device (1) comprises a box body that is connected to a smoldering smoke pipeline, where a smoldering box body layer is paved with a standard biomass fuel layer (1-2) and catalytic filter layer (1-1). The thickness of biomass fuel layer is more than 30 millimeter. A catalytic filter layer is provided, where the thickness of the catalytic filter layer is 5-6 millimeter. Biomass ash is also provided, which is made of metal oxide i.e. silicon dioxide.    USE - Smoldering device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional schematic view of a smoldering device.    Smoldering device (1)    Catalytic filter layer (1-1)    Standard biomass fuel layer (1-2)
NOVELTY - Microbial fuel cell reactor comprises an anode reaction area (1), a transition area (2), cathode reaction area (3), an aeration room (4) and buffering room (5) that is connected to the cathode reaction area. A reactor is provided, which is set with a top cover. The anode reaction area is set with a mud discharging pipe (6). A sludge discharging pipe of side wall is set up anode return tube B (7-2). A water inlet tube (8) is provided with a baffle plate A (9-1).    USE - Microbial fuel cell reactor for nitrification and de-nitrification (claimed).    ADVANTAGE - The microbial fuel cell reactor enables to perform nitrification and de-nitrification simultaneously in a cost-effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a microbial fuel cell reactor.    Anode reaction area (1)    Transition area (2)    Cathode reaction area (3)    Aeration room (4)    Buffering room (5)    Mud discharging pipe (6)    Anode return tube B (7-2)    Water inlet tube (8)    Baffle plate A (9-1)
NOVELTY - An alkane mixture comprises more than 89 wt.% and 99 wt.% or less propylene, 0.5 wt.% or more and less than 10 wt.% isobutene and 0.5 wt.% or more and less than 10 wt.% butane.    USE - Alkane mixture used as refrigerant for refrigeration apparatus e.g. air conditioner (all claimed).    ADVANTAGE - The alkane mixture has excellent cooling effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) application of alkane mixture as refrigerant; and    (2) refrigeration method, which involves mixing R1270-type propylene, R600a-type isobutane and R600-type butane, and compressing the mixture in a compressor of refrigeration apparatus.
NOVELTY - HCR22 hydrocarbon refrigerant comprises 70-90 wt.% propene and 10-30 wt.% propane.    USE - The refrigerant is used in air conditioner as heat transfer fluid as R22 substitute (claimed).    ADVANTAGE - The refrigerant has low freezing point, and larger evaporation latent heat; ensures quick cooling effect; has less isentropic compression ratio; assures easy operation of the compressor and prolongs the use life of compressor; has small molecular weight, good fluidity, and low pressure; and reduces the loading of the compressor.
NOVELTY - The device has fire grate (1) that is set between furnace (2) and hopper (17) whose lower end is set with ash-scraping trolley (16). Pneumatic charging valve (4) is set at top of inner cylinder (3) provided in furnace whose upper end is set with fuel gas exit (5). A spraying exit (6) of purification system is installed above fuel gas exit. The spraying exit, cyclone sprayer (7), spray system (8), water cyclone (9) and touch foam device (10) are connected together by pipeline. A swage processor (15) is set at lower portion of cyclone sprayer and spray system.    USE - Ceramic firing biomass gas generation device used in ceramic and steel enterprise.    ADVANTAGE - The high gasification rate of raw material is obtained, by the stable combustion process and complete gasification of the raw material. The tar and moisture in gas are eliminated, by purification process of fuel gas, so that the gas quality is ensured. The purification system is enabled to perform the wastewater treatment, so as to avoid the generation of pollution. By utilizing the water seal to the complete extent, the use of valve is reduced and the safety is enhanced. As the device is operated in a simple manner due to the electronic centralization control, the labor intensity of the worker is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the ceramic firing biomass gas generation equipment.    Fire gate (1)    Furnace (2)    Inner cylinder (3)    Pneumatic charging valve (4)    Fuel gas exit (5)    Spraying exit (6)    Cyclone sprayer (7)    Spray system (8)    Water cyclone (9)    Touch foam device (10)    Swage processor (15)    Ash-scraping trolley (16)    Hopper (17)
NOVELTY - A biological diesel oil comprises 40-50 wt.% low-grade diesel oil, 10-20 wt.% methanol, 5-15 wt.% purified water, and 15-30 wt.% animal and plant oil.    USE - A biological diesel oil for motor vehicle.    ADVANTAGE - Biological diesel oil is energy-saving and environment-friendly, reduces engine wear and engine noise, prolongs engine life, improves diesel oil efficiency, and saves resources and cost.
NOVELTY - Biogas is purified by pressurizing raw material biogas to 1-1.5 MPa.    USE - Purification of biogas for gas cutting (claimed).    ADVANTAGE - Purified biogas is non-toxic and has high methane gas concentration, and purification has small methane loss and improves biogas utilization and thermal efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for purification of biogas.(Drawing includes non-English language text).
NOVELTY - Preparation of biodiesel oil involves removing impurities from raw material bio-oil, dehydrating to obtain standard raw material oil, mixing standard raw material oil, dimethyl carbonate and silicate compound of alkali metal, fully stirring, mixing, reacting for 8-30 minutes, centrifuging obtained mixture to separate solid alkali catalyst and mixture of biodiesel oil and methyl carbonate, distilling separated mixture of biodiesel oil and dimethyl carbonate to recover dimethyl carbonate and crude biodiesel oil, and decoloring.    USE - Preparation of biodiesel oil (claimed).    ADVANTAGE - The biodiesel oil is prepared by environmentally-friendly method.    DETAILED DESCRIPTION - Preparation of biodiesel oil involves removing impurities from raw material bio-oil, dehydrating to obtain standard raw material oil, performing transesterification reaction by mixing the standard raw material oil and dimethyl carbonate in reactor, then adding solid alkali catalyst, mixing to form mixed material, controlling reaction temperature of mixed material at 250-300 degrees C under pressure of 2-5 MPa, fully stirring, mixing, reacting for 8-30 minutes, centrifuging obtained mixture to separate solid alkali catalyst and mixture of biodiesel oil and methyl carbonate, distilling separated mixture of biodiesel oil and dimethyl carbonate to recover dimethyl carbonate and crude biodiesel oil, and decoloring the crude biodiesel oil. The solid alkali catalyst is hydroxide or silicate compound of alkali metal. The molar ratio of standard raw material oil and methyl carbonate is 1:3-9. The addition amount of solid alkali catalyst is 0.01-0.2% of standard raw material oil.
NOVELTY - Reduction of tobacco leaf chromium content comprises taking parasitic pear-shaped tobacco spore root and reducing chromium content.    USE - Method for reducing tobacco leaf chromium content (claimed).    ADVANTAGE - The method is easy, simple, inexpensive, practical and environment-friendly.
NOVELTY - Producing honeysuckle based on comprehensive utilization of waste materials, comprises (i) taking decoction liquid waste raw material, performing alcohol precipitation, and extracting honeysuckle crude polysaccharide, and sterilizing the remaining supernatant by adding distilled water to antioxidant skin care lotion, where honeysuckle crude polysaccharide is obtained by e.g. stirring honeysuckle decoction and anhydrous ethanol; and (ii) taking solid residue and substance A, mixing, centrifuging solid residue raw material, dehydrating, and stirring to obtain pure powder of biodiesel catalyst.    USE - The method is useful for producing honeysuckle based on comprehensive utilization of waste materials (claimed).    ADVANTAGE - The method does not discharge solid waste directly, and thus it is environmental friendly; has simple operation, and thus it does not produce waste water.    DETAILED DESCRIPTION - Producing honeysuckle based on comprehensive utilization of waste materials, comprises (i) taking decoction liquid waste raw material, performing alcohol precipitation, and extracting honeysuckle crude polysaccharide, and sterilizing the remaining supernatant by adding distilled water into an antioxidant skin care lotion, where the honeysuckle crude polysaccharide is obtained by taking 100-200 pts. wt. honeysuckle decoction, adding 300-400 pts. wt. anhydrous ethanol, stirring, allowing to stand overnight, centrifuging, performing vacuum drying to obtain the honeysuckle crude polysaccharide, and then taking the centrifugal supernatant, adding 100 pts. wt. distilled water and 100-300 pts. wt. diluent, and filling, sterilizing to obtain the antioxidant skin care lotion; and (ii) taking 100 pts. wt. solid residue and 100-300 pts. wt. substance A, mixing, centrifuging the solid residue as raw material, dehydrating, and stirring to obtain pure powder of biodiesel catalyst.
NOVELTY - Composition comprises 10-35 wt.% of cefuroxime axetil, 50-85 wt.% of coating material, and 0.5-15 wt.% of regulator. The regulator is povidone. The coating material is obtained by hot-melt coating method.    USE - The composition is useful for treating acute pharyngitis or tonsillitis, acute otitis media, maxillary sinus, inflammation, chronic bronchitis, and urinary tract infection.    ADVANTAGE - The composition has good taste, high dissolution rate, high bioavailability and drug content uniformity, reduces patient compliance, can be prepared without use of any solvent, and is simple, short time and less energy consuming manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composition, comprising mixing coating material and regulator, heating the mixture to melt, then adding cefuroxime axetil, uniformly stirring to mix, and spray-freezing the mixture, and curing.
NOVELTY - Adsorbent composition preparation involves drying biogas residue, where biogas residue is added with potassium hydroxide solution. The obtained solution is centrifuged to obtain supernatant liquid. The obtained supernatant liquid is added with hydrochloric acid and hot deionized water. The obtained mixture is dried, crushed and then sieved to obtain desires product.    USE - Method for preparing adsorbent composition used in adsorption of ammonia and nitrogen (claimed).    ADVANTAGE - The method enables to prepare adsorbent composition in a cost-effective manner.
NOVELTY - Catalyst comprising 85.38-91.42 wt.% of zirconium dioxide, 6.75-9.72 wt.% of aluminum oxide, and 2.68-4.16 wt.% of titanium dioxide, is new.    USE - The catalyst is useful for preparing biological diesel oil (claimed).    ADVANTAGE - The catalyst reduces reaction time and production cost of biological diesel oil, and has high conversion rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing the catalyst; and    (2) preparing a biological diesel oil, comprising uniformly mixing grease and low carbon alcohol according to the volume ratio of 1:1-5:1, pre-heating the mixture at 200-250 degrees C, adding mixed material with filling and catalyst into a tube-type reactor, performing low ester exchange reaction at 260-285 degrees C under pressure of 8-12 MPa, heating the material to reaction at 80-120 degrees C under the pressure of 2-3 MPa to obtain flash material, distilling the material with methanol at 65-80 degrees C at normal pressure, standing to separate upper layer product, adding the product into a rectifying tower, and heating at 200-350 degrees C.
NOVELTY - A catalyst comprises a carrier, active components, and additional component. gamma -Alumina carrier is immersed in magnesium source as additional component and roasted to form spinel with magnesium supported on alumina carrier, and nickel as active component is supported on the catalyst surface in the form of nickel oxide.    USE - Catalyst is used for catalytic pyrolysis of coal to tar and hydrocarbon, and for pyrolysis of biomass, food waste, and oil shale (all claimed).    ADVANTAGE - The catalyst is applicable for both in-situ catalytic pyrolysis and secondary catalytic pyrolysis outside the furnace. The catalyst reduces content of heavy tar components, has excellent stability, is economical, and increases yield of benzene, toluene, xylene, phenol, cresol and xylenol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst, which involves roasting gamma -alumina carrier at 400-650 degrees C for 4-5 hours, preparing a solution of soluble magnesium salt, immersing the carrier in the solution at 10-80 degrees C for 1-5 hours to load magnesium on the carrier, drying at 100-110 degrees C, heating the product in a muffle furnace at 400-1000 degrees C for 1-5 hours to form spinel carrier surface, preparing a soluble nickel salt solution, immersing the carrier at 10-80 degrees C for 1-5 hours, drying at 100-110 degrees C, heating in a muffle furnace at 400-1000 degrees C for 1-5 hours, and cooling.
NOVELTY - A white one consumable resource type garbage processing system, which include a one thermal cracking system, one a gas purification system, a one oil liquid collecting device, a one ash discharge system, cracking system of the pneuma tube and gas purification system of air inlet tube, air outlet tube of gas purification system connecting to the combustion room of a thermal cracking, in thermal cracking system is added with white wastes for pyrolysis of catalyste, system connecting with the ash discharging system. This utility new type aims to provide one of a white for a resource from a garbage processing system, there is no waste pneuma, and tail pneuma heating cracking furnace, at the same time, by using a white thermal produce of organic oil liquid mixture, a tail pneuma reach national standard, at the same time, it saves resource, and is environment-friendly and energy-saving.
NOVELTY - Preparing glyphosate isopropylamine salt comprises adding iminodiacetonitrile to sodium hydroxide solution, carrying out hydrolysis process, mixing the hydrolyzed material with phosphorus trichloride and hydrogen chloride, carrying out acidification process, then adding formaldehyde to carry out condensation process, separating the condensed crystals to obtain an intermediate of phosphonomethyl iminodiacetic acid and waste salt solution, and then carrying out an oxidation process of phosphonomethyl iminodiacetic acid with an intermediate of isopropylamine to obtain waste salt solution.    USE - The method is useful for preparing glyphosate isopropylamine salt (claimed).    ADVANTAGE - The method is capable of preparing glyphosate isopropylamine salt in a cost-effective manner.    DETAILED DESCRIPTION - Preparing glyphosate isopropylamine salt comprises adding iminodiacetonitrile to sodium hydroxide solution, carrying out hydrolysis process, mixing the hydrolyzed material with phosphorus trichloride and hydrogen chloride, carrying out acidification process, then adding formaldehyde to carry out condensation process, separating the condensed crystals to obtain an intermediate of phosphonomethyl iminodiacetic acid and waste salt solution, carrying out an oxidation process of phosphonomethyl iminodiacetic acid with an intermediate of isopropylamine to obtain waste salt solution, then adding ammonium bicarbonate to the waste salt solution, separating to obtain sodium bicarbonate crystal, drying the sodium bicarbonate crystal, then carrying out decomposition of the sodium bicarbonate crystal to obtain sodium carbonate solution, and reacting the sodium carbonate solution and lime milk in sodium hydroxide solution to obtain iminodiacetonitrile for alkaline hydrolysis process.
NOVELTY - Organic solid waste high efficient dry-type anaerobic fermentation device comprises a horizontal main tank body equipped with a feeding port, a slag outlet, an air outlet and a liquid outlet. The inner main tank body is divided into multiple fermentation chambers. A stirrer is inserted into the center of the horizontal main tank body. The bottom of the main tank body is equipped with marsh gas discharging device. The discharging device is connected to the slag outlet. The bottom of clapboard is provided with a connecting hole.    USE - Used as organic solid waste high efficient dry-type anaerobic fermentation device.    ADVANTAGE - The fermentation device: is organically loaded, high gas production efficiency and small floor space; saves energy; avoids the presence of marsh gas crust in wet-type anaerobic fermentation process; and avoids secondary pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the organic solid waste high efficient dry-type anaerobic fermentation device.
NOVELTY - Preparing immobilized lipase, comprises performing carbonization of thatched biomass and biological carbon matrix, coating the surface of biological carbon matrix with oleic acid molecule modified nano gel-coated carbon, packaging by completely contacting the biological carbon matrix with lipase coating solution, and performing lipase interfacial activation, and cross-linked fixation, and carrying out freeze-drying to obtain the product.    USE - The method is useful for preparing immobilized lipase (claimed).    ADVANTAGE - The method produces product with high catalytic activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for immobilized lipase prepared as mentioned above.
NOVELTY - This utility new type relates to a one solar energy garbage fermentation device, comprise a fermentation, wherein the fermentation system comprise used for containing a processing waste of fermentation chamber, the fermentation chamber using glass material or solar energy transmitting material preparation, a fermentation cabin set with feeding door and discharge door, the bottom of fermentation cabin, a bottom plate set with a fermenting chamber set with liquid from the fermentation chamber entering into the liquid storage tank of inner through hole, inner fermenting chamber set with pneuma tube, exit of entrance, exit of the fan discharge tube connecting the fan connecting a waste treatment system of pneuma; inner fermenting chamber is further set with regular spray microorganism for a spray device. This utility new type using solar energy to supply heat for garbage fermentation, especially time temperature in winter is low, the waste of needed temperature, use green energy and heating energy consumption; it does not need regular spray through microorganism fermentation cabin inner, at the same time ensure uniform distribute and high efficiency of microorganism, a better a rotten degree of ferment compost garbage, realize a garbage degradation efficient of fast degradation, a is a concentrated processing garbage decrement of 70 to 80%.
NOVELTY - This utility new type claims a one for compost reaction of reaction tank, reaction tank main body comprise, a. inner tank body set one end set with temperature control cylinder, reaction tank main body set with a cloth pneuma cavity, a temperature control cylinder of inner wall set with several stir a tooth, one end said stir tooth of are connected with the gas distribution chamber, wherein said stir tooth is L shape, the upper surface are set with several vent hole. This utility new type has high controllability, according to temperature controllable oxygen supply can be controlled. The risk in the effect of the compost aspect, it can increase efficiency of sludge compost, compost product increase fertilizer effect and reduce the second pollution.
NOVELTY - NOVELTY -A one aerobic composting device comprise: one perforated plate, the one container up to a lower two part, upper part is compost reactor, lower part of top part of the wind room, compost reactor is a a detachable seal cover, and set with an air outlet, gas sampling port and greenhouse gas sampling opening on the upper seal cover, air inlet and an external of compost reactor of ammonia sampling opening connecting device air inlet, gas sampling opening of gas absorption device connecting greenhouse gas collecting set with first measuring point, inner compost reactor set with different height of second and third measuring point measuring point, temperature sensor is carried out by measuring temperature, air room is equipped with vent-pipe, air tube through a rotor flow meter and an electromagnetic valve connecting the air outlet of the air compressor, the bottom of the air room set with leachate discharge tube, temperature sensor and electromagnetic valve electrically connect to a PLC controller in the PLC automatic control system, a PLC control system by a scene touch screen.
NOVELTY - This utility new type is a biological fermentation tower one a high effect of environment-friendly, set with the feeding device on the upper part of the conical column body, the bottom set with the discharging device, the inner cavity of the conical column body set with the fermentation chamber, the fermentation cavity center axis a center set with replenishing pneuma tube, lower end of center the pneuma tube passes through a bottom of the tube wall of the centre tube of pneuma tower body set with several replenishing pneuma hole, set with several transverse set with a air inlet tube, an air inlet tube by the tower body wall of tapered tower body to the tower centre are radially arranged inner the fermentation chamber, a tube wall of air inlet tube set with multiple ventilating hole. This utility new type fermentation total process realizes totally enclosed, no dust, no smell, no sewage leakage, centre of inner tower body the pneuma tube and the pneuma can be a tube of air inlet amount in the fermentation process, realize aerobic fermentation or anaerobic fermentation, increase the efficiency of the fermentation tower body top part of waste pneuma collecting cover can be the waste pneuma collected out of the tower a process so as to reduce a pollution for environment, the fermentation material is a high-quality of bio-organic fertilizer.
NOVELTY - NOVELTY -This utility new type relates to one a biomass organic carbon base fertilizer production device, include placing groove, front processing device, dryer, packing machine and control system, a groove with the front processing device is set with the feeding conveyor, a front processing device comprise stir mixing machine, sieving and crushing machine, a control unit comprise a panel, a programme controller and a metering unit, a control unit a front processing device, dryer, starting and stopping a packaging machine. The production device and production process through screening and stir mix, a granulator, drying to obtain the biomass of organic carbon base fertilizer production device, the fertilizer not only is sanitary and clean, at the same time, for a little pollution to the environment, a high efficiency, automatic degree high, convenient control and saves the cost, this utility new type out of a fertilizer mainly is carbon element, the soil in the decomposed without residue, with improved soil of long-acting.
NOVELTY - NOVELTY -One a biomass gasification device, a feeding port (1) connecting the hearth (2), air blower (8) through air inlet channel (5) connecting a one time air inlet tube (4) and a secondary air inlet tube (7), the upper inner hearth in turn from up to down set one air ring tube (21), a secondary air ring tube (19) and ash discharging fence (10), one air ring tube and one secondary air inlet connecting tube, a secondary air ring tube set with one with one air nozzle (22), a second wind tube set with a secondary air nozzle (20). The utility model is new type the second air and supplied to a water vapour, low water vapour tar form the second air of high temperature carbon layer and water vapour nozzle into a co-acting is cracked, some reaction in water vapour and tar component of a CO, H2, CH4, increasing a value of gas at the same time reduces the tar content of a raw fuel gas, valid to solve low-suction type fixed bed biomass gasification furnace of a a low inner the gasification furnace, a tar content of high.
NOVELTY - NOVELTY -This utility new type relates to a biomass fixed bed one pure oxygen for device, comprising an oxygen supply device, a feeding device, a furnace body and the furnace body bracket, said oxygen supply device include liquid oxygen storing groove and liquid oxygen, liquid oxygen gasifier gas outlet of the furnace body through the air inlet of the gas pipeline and the bottom of the furnace body is connected with the bottom of the furnace body set with one furnace gate, furnace grid fixed in the hollow furnace gate of a rotating shaft, a furnace body through air inlet of furnace grid hollow rotating shaft inside of the connected with the furnace body, furnace gate rotating shaft and the transmission mechanism is connected with a furnace body outer wall is cylindrical, inner wall of the furnace body is cone-shaped, inner wall of upper part smaller than the lower part diameter, the top part of the furnace body set with feeding device, the furnace body of upper part one side set with an air outlet, the bottom of furnace body set with an ash outlet, the utility model is new type structure is simple, the operation is convenient, it can increase conversion efficiency of gasification, the gasification gas heat value a valid increase.
NOVELTY - NOVELTY -This utility new type claims a biomass gasification furnace for one combined type furnace gate device, comprise furnace gate bracket, a bracket and a furnace gate type of a certain number, furnace gate is set on the bottom of the bracket, the embedded type bracket by a certain number the same as thickness of a lower connecting disk, the disk from upper to lower in turn, furnace gate thickness and the disk thickness a. upper and lower connection disc are uniformly distributed around the furnace gate of a certain number, furnace gate through a fastener embedded connecting with each other. Furnace gate. is fan-shaped double-arc surface structure, fan-shaped double-arc surface of furnace grid module set with air opening structure. This utility new type device can effectively prevent the slag and ventilation effect is good.
NOVELTY - NOVELTY -This utility new type relates to a biomass two section one airflow bed gasification device and gasification method, comprise inner furnace shell, furnace shell is set with gasification room and synthetic pneuma cooling room, a gasification room is divided into upper and lower section gasification room, a gasification room top section set with overhead synthetic pneuma exit, the axis b, furnace shell of upper, lower section gasification room set with bottom slag tank, a slag tank bottom slag tank set with slag discharging port, upper section end gasification room set with at least one layer around the side process nozzle room, at least two side process burner are symmetrically set with a burner chamber side process, a lower section gasification room side coaxial set with two opposed process nozzle room, two opposed process a coaxial nozzle on opposed process nozzle room, the side between the process nozzle room and the lower section is set with at least two room a second secondary oxygen spraying gun room, a secondary oxygen blow lance inner room is equipped with a secondary oxygen blow lance. This utility new type a continuous gasification process for pure oxygen gas with the intermittent gasification process compared with production rate is increased by 1 times.
NOVELTY - This utility new type belongs to the clean moulded coal production technology field, especially relates to a biomass carbon powder and one inferior coal mix synthesis clean moulded coal of a device. Include faulty coal, and coal conveyor connecting with inferior coal crusher, the inferior coal crusher connecting with inferior coal screen, inferior coal classifier exit connecting up the mixer;    DETAILED DESCRIPTION - At the same time, connecting with biomass carbon powder feeding device, a water supply device and a device adhesive in a mixer, mixing a mixture exit device connecting with a coal pressing machine, a moulded coal pressing machine exit and the moulded coal drying machine connecting coal dryer exit connecting with a briquette machine, briquette machine output port connecting with a coal packing machine. This utility new type has simple structure, reasonable design, increase the combustion efficiency of coal, reduces the pollution so as to indirectly increase the boiler working efficiency, and the production efficiency is high, the operation is convenient to use.
NOVELTY - This utility new type belonging to the biomass a material production technology field, especially relates to a biomass granule material forming one line. From the raw material to the finished product in turn are set between with a presser, a crusher, a selecting sieve, drying device, and cooling and packaging machine;    DETAILED DESCRIPTION - Further comprise a master control, in turn are arranged adjacent a two part are set with conveyor, each one set with a transfer warehouse before and after the drying device, set with the storage hopper prior to granulating machine, a transfer warehouse are set with hoisting machine before the storage and cooling and packaging. This utility new type biomass a material forming production line technique is simple and reasonable, it is suitable for continuous production, increase production efficiency and increase yield and reduce production cost, reduce the energy consumption, saving resource, convenient use and suitable for popularization.
NOVELTY - The utility model provides a coal mine ventilation air methane extraction device, which includes: air shaft diffusion tower, absorbing cover, the desorption device and a conveying channel, lower port cover of said absorbing cover is set on said air shaft diffusion upper part of tower and the air shaft diffusion tower of said side wall seal, wherein a cover body surface provided with a through hole by a steel frame, and a steel frame in filled with a sieve, the desorption device is at least one one end sealing of a hollow tube, a hollow tube joint set on the outer surface of said absorbing cover and with it, said hollow tube and surface of said absorbing cover set with through hole, said inlet is connected with a using device of a conveying channel is further set with a water ring type vacuum pump. The methane extraction device can effectively purify coal mine ventilation air by extracting methane, which can subsequently be used to provide a gas source.
NOVELTY - This utility new type claims a biomass fluidized bed one multi-return pneuma for boiler, include first furnace body, a second furnace body, hopper, air blower, first furnace body is divided into upper and lower two part, upper part is a combustion chamber, lower part is gasification room, a gasification room of one side set with vent hole, a vent through air channel and the air blower connecting gasification room is further set with furnace gate, second inner furnace body is further set with water tank, a gasification room one side is further set with a, a packing auger is connected with the gasification room through connecting;    DETAILED DESCRIPTION - Further set with valve, a gasification room top set with room connected with the combustion gas exit of the auger, a combustion room one side set with an ignition port, and the other side set with an air outlet, lower part of the furnace body set with one second a reflection room, upper part set with the pneuma room and the pneuma room, an air inlet room and the pneuma room through fire tube reflection room with a certain number of connected, second body air inlet room and air outlet through a first connecting body. This utility new type device has simple structure, convenient use, a high utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of Multi-return bed biomass gasification boiler. (Drawing includes non-english language text)
NOVELTY - Method for recycling fermentation bed material involves converting bed material containing organic compound and microbial fertilizer.    USE - The method is useful for recycling fermentation bed material for obtaining microbial fertilizer (claimed).
NOVELTY - Preparation of cushion material comprises uniformly mixing straw, sawdust, and wheat bran; adding ferrous sulfate, salt, copper sulfate, manganese sulfate to prepare 1-5% solution; spraying solution on straw, sawdust and bran, uniformly stirring; mixing sodium selenite, drying for 2 hours; adding Bacillus subtilis and Alkalibacillus; adding fine sand and uniformly mixing.    USE - Method for preparing cushion material used for livestock and poultry breeding (claimed).    ADVANTAGE - The method prolongs cushion material change period and reduces breeding animal disease, thus reducing amount of antibiotic used which greatly saves cost.
NOVELTY - Invention relates to an additive for the increase of the cetane number of Diesel fuel based on alkylnitrate, characterised by the fact, that the additive represents an alkylnitrite-containing product of nitration of the fraction IBP-195 degrees C, separated from the bottom residue of production of butyl alcohols and which contains isopentanol from 0 to 5.0 wt %, isoheptanols from 5.0 to 10.0 wt %, dimethylcyclohexanols from 5.0 to 10.0 wt %, isooctanols from 10.0 to 40.0 wt %, polybutoxybutanes from 0 to 15.0 wt %, dibutoxybutanes - the remaining part. The invention also relates to a method of obtaining the additive for the increase of the cetane number of Diesel fuel by nitration of the fraction IBP-195 degrees C, separated from the bottom residue of production of butyl alcohols, by a mixture of sulphuric acid in the range of temperatures of 0-8 degrees C for 1.0-1.5 hours.    USE - Chemistry.    ADVANTAGE - Application of the said fraction makes it possible to extend resources of the raw material for the production of the cetane-increasing additive, excludes the necessity of the said fraction separation, reduces expenditures for the additive obtaining, the application of the additive makes it possible to increase the cetane number of Diesel fuel.3 cl, 1 tbl, 2 ex
NOVELTY - Separation of ethylene involves contacting a mixed gas containing ethane and ethylene with a composition containing an adsorbent, obtaining gas having ethylene concentration higher than the ethylene concentration of the mixed gas, and adsorbing ethane using the adsorbent. The adsorbent is a metal complex (I).    USE - Separation of ethylene used as starting material for manufacture of synthetic chemistry industrial materials e.g. vinyl chloride, acetaldehyde, styrene, and polyethylene.    ADVANTAGE - The method enables the efficient separation of ethylene from the mixed gas, by simple process.    DETAILED DESCRIPTION - Separation of ethylene involves contacting a mixed gas containing ethane and ethylene with a composition containing an adsorbent, obtaining gas having ethylene concentration higher than the ethylene concentration of the mixed gas, and adsorbing ethane using the adsorbent. The adsorbent is a metal complex of formula: (M(L)2) (I).    L=organic ligand of formula (ii);    M=metal chosen from beryllium, magnesium, calcium, strontium, barium, titanium, zirconium, vanadium, chromium, molybdenum, tungsten, manganese, iron, ruthenium, cobalt, rhodium, nickel, palladium, platinum, copper, zinc, cadmium, aluminum, or indium;and    R1-R3=H, optionally substituted 1-4C alkyl, 2-4C alkenyl, 1-4C alkoxy, halo, hydroxy, cyano, nitro, amino, 1-4C monoalkyl amino, or 2-8C dialkylamino.
NOVELTY - A dry-type methane fermentation apparatus is operated by setting a day of the week other than that to the holiday which does not perform operation of the dry-type methane fermentation apparatus for 1 or continuous day of the week and stream day which operates the dry-type methane fermentation apparatus, setting the day before yesterday on the day preceding the holiday to 2nd stream day, setting stream day other than that to 1st stream day, and supplying organic waste of 1st injected quantity into the fermenter of dry-type methane fermentation apparatus at 1st stream day.    USE - An operation process of dry-type methane fermentation apparatus (claimed).    ADVANTAGE - Amount of biogas generations in dry-type methane fermentation apparatus is equalized, and a stable biogas more than constant rate can be supplied.    DETAILED DESCRIPTION - A dry-type methane fermentation apparatus is operated by setting a day of the week other than that to the holiday which does not perform operation of the dry-type methane fermentation apparatus for 1 or continuous day of the week and stream day which operates the dry-type methane fermentation apparatus, setting the day before yesterday on the day preceding the holiday to 2nd stream day, setting stream day other than that to 1st stream day, supplying organic waste of 1st injected quantity into the fermenter of dry-type methane fermentation apparatus at 1st stream day, and supplying organic waste of 2nd injected quantities to 2nd stream day than 1st injected quantity into the fermenter of dry-type methane fermentation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the dry-type methane fermentation apparatus. (Drawing includes non-English language text).    Crushing apparatus (11)    Supply apparatus (12)    Mixing apparatus (13)    Input apparatus (14)    Dry-type methane fermentation tank (15)    Sludge drawing-out apparatus (16)
NOVELTY - This utility new type claims a one for biogas purifying of first-stage desorption, include steam exit, a safety valve interface, a water outlet, a saddle tube, tube end set with two end enclosure, safety valve interface, a steam exit tube located at the top of the water outlet is located at the bottom of cylinder body, one side of tube top part set with water inlet, and the other tube is connected to one head of the middle lower part set with the water inlet, the inner tube set with baffle plate, the tube. The horizontal tank is vertical tank reduces a height, saves energy consumption, at the same time, which greatly reduces the cost of device and saves the aritificial and a installation cost, through baffle plate device of tube, inner tube, the space of extension of fluid, the fluid the baffle plate of collision and baffle, so as to increase desorption effect, set with filler and foam.
NOVELTY - This utility new type claims high efficiency membrane bio-reactor biogas slurry processing device, include membrane bio-reactor, a first hole in the membrane bio-reactor of, several parallel set with a pipeline interface of which is set at the water inlet of membrane bio-reactor upper part, the film biological reactor is set at the bottom of the water outlet and discharging port, the structure occupies small space, sewage treatment efficiency is high, the purification ability is good, the structure is compact.
NOVELTY - A garbage composting system comprises stockyard, garbage transfer device, conveyor belt, magnetic suction device, bag breaking machine, wind sorter, hydraulic packing machine, drum screening machine and compositing machine comprising biogas inlet and biogas tank.    USE - Garbage composting system for preparing biofertilizer for agricultural production.    ADVANTAGE - The simple and safe method has low processing cost.
NOVELTY - Microbial fuel cell comprises a cathode and an anode, where volume ratio of sludge (1) and the cathode liquid is 1:9. The anode is inserted into sludge layer to form the anode area and the cathode is inserted into acidic mine waste water layer containing sulfate-reducing bacteria (2) to form cathode area. Electric loop is formed between anode and cathode with a lead and an external resistance to obtain the desired product. Microbial fuel battery comprises a carbon film (3), a spherical stainless steel wire (4) and a sealing plug (5).    USE - Microbial fuel cell used for treating acid mine drainage (claimed).    ADVANTAGE - The microbial fuel cell reduces concentration of sulfate ion and heavy metal ions in acidic mine waste water, and has residual sludge and anaerobic membranous structure that is cost-effective.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of microbial fuel cell.    Sludge (1)    Acidic mine waste water layer containing sulfate-reducing bacteria (2)    Carbon film (3)    Spherical stainless steel wire (4)    Sealing plug (5)
NOVELTY - System for drying fermentation residues, preferably from biogas plants, comprises (a) a hot water cycle, (b) a heat exchanger (WT) with at least one pipe system (RG1), (c) a low temperature evaporator (NV) with a first hot water device, a high temperature evaporator (HV) with a second hot water device, and (c) at least one device for producing a vacuum in the entire system.    USE - The system is useful for drying fermentation residues, preferably from biogas plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for drying fermentation residues comprising pumping the fermentation residues through a first pipe system of a heat exchanger and heating, supplying the fermentation residues from the heat exchanger to a low temperature evaporator, and further heating, supplying the fermentation residues from the low temperature evaporator to a high temperature evaporator and further heating, and hermetically discharging the dried fermentation residues from the high temperature evaporator.    DESCRIPTION OF DRAWING(S) - The figure shows system for fermentation residues drying.    Hot water circulation (32)    High temperature evaporator (HV)    Low temperature evaporator (NV)    Pipe system (RG1)    Heat exchanger (WT)
NOVELTY - Mixed organic composition comprises 0.0001-0.001 parts weight microorganism, 0.001-0.1 parts weight chitosan, 30-50 parts weight clay, 30-50 parts weight mature soil, 5-15 parts weight sawdust compost, 5-15 parts weight fiber composition and 2-5 parts weight cow dung.    USE - The mixed organic composition or method is useful for afforestation of steep slope (claimed).    ADVANTAGE - The mixed organic composition is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for afforestation of steep slope, which involves greening the inclined plane using the mixed organic composition.
NOVELTY - Nickel-metal-alumina hybrid xerogel catalyst (I), is claimed.    USE - The catalyst is useful in methane synthesis by methanation reaction of carbon dioxide and hydrogen (claimed).    ADVANTAGE - The catalyst has conversion rate of 50-70% (claimed); exhibits excellent reproducibility and heat resistance; and is porous.    DETAILED DESCRIPTION - Nickel-metal-alumina hybrid xerogel catalyst of formula (nickel-X-alumina) (I), is claimed.    X = Fe, Co, Ni, Zr, Y, Zn, Ce, La, Sm, Mg or Ca.    . INDEPENDENT CLAIMS are also included for:    (1) preparing catalyst, comprising (a) forming aluminum precursor sol by mixing and hydrating aluminum precursor in alcohol solvent diluted with water and acid, (b) forming nickel-metal-alumina sol by mixing prepared aluminum precursor sol, nickel precursor and metal (X) precursor, (c) forming nickel-metal-alumina gel by mixing prepared nickel-metal- alumina sol, 50-70 pts. wt. alcohol and 200-420 pts. wt. water, and (d) aging, drying and calcining the prepared nickel-metal-alumina gel; and    (2) preparing methane, comprising (i) pretreating the prepared nickel-metal-alumina xerogel catalyst with hydrogen and nitrogen gas introduced into continuous flow reactor for methanation reaction, and (ii) synthesizing methane by methanation reaction by passing carbon dioxide, hydrogen and nitrogen gas into pretreated nickel-metal-alumina xerogel catalyst.
NOVELTY - An Aspergillus niger with preservation number CGMCC No. 8438 is new.    USE - An Aspergillus niger with preservation number CGMCC No. 8438 for sulfonylurea herbicide used for remediation of polluted soil, microbial inoculum, and biodegradable fertilizer (all claimed).    ADVANTAGE - A. Niger is environment-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparation of microbial inoculum which involves inoculating A. niger in potato dextrose (PD) liquid culture medium at 25-30 degrees C, shaking at speed of 125-150 rpm, culturing for 3-4 days, adjusting spore concentration to 1x 106/ml to obtain 2nd level liquid culture, adding bran, straw, corn powder, and rice hull in 1 L flask in which ratio of bran, straw, corn powder, and rice hull is 12:6:2:1.5, adding water until humidity is 100%, sterilizing, adding 10 ml 2nd level liquid culture in flask, and fermenting at 25-30 degrees C for 3-4 days; and (2) biodegradable fertilizer comprising A. Niger spore solution, inorganic fertilizer, and organic fertilizer in which weight ratio of A. niger spore solution, inorganic fertilizer, and organic fertilizer is 1:6:13, inorganic fertilizer is nitrogenous fertilizer which is urea or ammonium sulfate, phosphate fertilizer which is ammonium phosphate or calcium phosphate, potash fertilizer which is potassium sulfate or potassium chloride, and organic fertilizer is compost or biogas fertilizer.
NOVELTY - An anti-overcharging electrolyte preparation method, involves mixing lithium salt, organic solvent, anti-overcharge additives, film forming agent and functional additives, where lithium salt is 0.6-1.3 M/l lithium hexafluorophosphate and0.1-0.5 M/l high temperature stable lithium salt, the amount of anti-overcharge additives are 2-5 wt.%, the amount of film forming agent is 2-5 wt.%, and the amount of functional additives are 0.4-0.8 wt.%.    USE - Method for preparing anti-overcharging electrolyte for lithium ion battery.    ADVANTAGE - The method enables preparing anti-overcharging electrolyte for lithium ion battery with improved safety performance of lithium ion battery and operation at high temperature, in environmentally-friendly manner.
NOVELTY - This utility new type relates to one used for a praziquantel production process of improved system, comprise reaction tank, a feeding tube, the electrodialysis cell, electrodialysis device, a discharging tube, wherein the electro-dialysis device comprise inverter power supply, an anode, a cathode and a cationic, anionic, the cation and said anion membrane of a multi-group for, and uniformity are arranged at intervals, wherein said electrodialysis cell is divided into several area, exit of said feeding tube with multi -, correspond to interval of said area. This utility new type using electrodialysis device, the a praziquantel process produce a production alkali liquid process electrodialysis, a discharging tube through a 99% of sodium hydroxide solution, a sodium hydroxide solution of a circulation for praziquantel of industrial production, reduces the pollution for environment of.
NOVELTY - A domestic waste and straw integrated recycling system comprises a solid waste crushing sorting device, a straw crusher, a steam ejection type organic waste treatment device, a waste organic slurry drying device, a fertilizer preparing device, a straw organic slurry storage tank, and a methane production device. The crushing and sorting device and the straw crusher via a transfer belt are connected to the steam ejection type organic waste treatment device.    USE - Domestic waste and straw integrated recycling system.    ADVANTAGE - The recycling system has reduced energy consumption and low cost, and is capable of quickly composting domestic waste and straw into fertilizer while producing natural gas and carbon dioxide.    DETAILED DESCRIPTION - A domestic waste and straw integrated recycling system comprises a solid waste crushing sorting device, a straw crusher, a steam ejection type organic waste treatment device, a waste organic slurry drying device, a fertilizer preparing device, a straw organic slurry storage tank, and a methane production device. The crushing and sorting device and the straw crusher via a transfer belt are connected to the steam ejection type organic waste treatment device. The steam ejection type organic waste treatment device is connected with the waste organic slurry drying device and the straw organic slurry storage tank. The garbage organic slurry drying device via a transfer belt is connected with the fertilizer device. The straw organic slurry storage tank is connected with the methane production device. The outlet of methane production device is connected with the garbage organic slurry drying device.
NOVELTY - A fuel from sewage sludge and biomass producing method involves mixing partially dehydrated sludges containing dry solids with plant biomass, and mechanically squeezing the strands or granular form to obtain mixture. Plant biomass waste is utilized, and added to sludge to obtain a mixture. The mixture is allowed for autothermal thermophilic bacteria participation, and vegetable waste is again added with resulting mixture followed by finely dividing 5-10 wt.% cellulose fibers with a length to 1 cm and mixing the material by extrusion and storing to obtain finished product.    USE - Method for producing fuel from sewage sludge and biomass.    DETAILED DESCRIPTION - A fuel from sewage sludge and biomass producing method involves mixing partially dehydrated sludges containing 15-30 wt.% dry solids with plant biomass, and mechanically squeezing the strands or granular form to obtain mixture. Plant biomass waste with humidity of 25% containing shredded cellulose fibers with a length of 1 cm and a diagonal measurement of 0.1-1.0 mm is utilized, and added to the 10-35% sludge to obtain a mixture having a moisture content of 45-65%, pH of 5.5-6.5 and an organic matter content of 40-80% with C: N ratio of 25-35. The mixture is allowed for autothermal thermophilic bacteria participation over a period of 1-7 nights, and vegetable waste is again added with resulting mixture with water content of 40-50 wt.% and moisture content of 25%, followed by finely dividing 5-10 wt.% cellulose fibers with a length to 1 cm transverse dimension of 0.1-1.0 mm, and mixing the material by extrusion and storing to obtain finished product.
NOVELTY - Hydraulic screw stirred type device comprises: an anaerobic digester (10) including inner and outer cylinders for processing organic waste; a screw stirrer (20) installed in the inner cylinder for stirring sludge; an upper horizontal stirrer (30) connected at the top of the screw stirrer for removing bubbles and scum; a lower horizontal stirrer (40) connected at the bottom of the screw stirrer for horizontally stirring the precipitated sludge; a circulating pump (50) connected to the lower horizontal stirrer to circulate the precipitated sludge to the upper part of the anaerobic digester.    USE - The device is useful for anaerobic digestion of the organic waste (claimed).    ADVANTAGE - The device easily removes bubbles and scum, improves anaerobic digestion and increases production of the biogas.    DETAILED DESCRIPTION - Hydraulic screw stirred type device comprises: an anaerobic digester (10) consisting of dual cylinder type of an inner cylinder and an outer cylinder for processing organic waste; a screw stirrer (20) installed in the inner cylinder for stirring sludge; an upper horizontal stirrer (30) connected at the top of the screw stirrer for removing bubbles and scum; a lower horizontal stirrer (40) connected at the bottom of the screw stirrer for horizontally stirring the precipitated sludge; a circulating pump (50) connected to the lower horizontal stirrer to circulate the precipitated sludge to the upper part of the anaerobic digester; a heating tubes wrapped around the inner cylinder for adjusting and maintaining the temperature of the anaerobic digestion; and a hydraulic motor for operating the screw stirrer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the anaerobic digestion device.    Anaerobic digester (20) Screw stirrer (10)    Upper horizontal stirrer (30)    Lower horizontal stirrer (40)    Circulating pump (50)
NOVELTY - Coumarin synthesis involves reacting 2-hydroxy aryl aldehyde or 2-hydroxy aryl ketone (II) with active methylene (III) in presence of a mesoporous solid heterogeneous catalyst having organic inorganic hybrid characteristics under Knoevenagel condensation.    USE - Method for synthesizing coumarin of general formula (I) (claimed). R1 and R2=CO2R5, COR6, CN, NO2, SO2Ph; R5=alkyl, allyl, aryl or benzyl group; R6=alkyl or aryl group; R3=H, CH3, phenyl, OH or OR5 group; and R4=H, F, Cl, Br, alkyl, naphthyl, OH, OMe, NO2 or CN group.    ADVANTAGE - The method synthesizes coumarin in a simple, cost-effective and eco-friendly manner with high yield by using non-toxic solid catalyst containing secondary amine groups.    DETAILED DESCRIPTION - Coumarin synthesis involves reacting 2-hydroxy aryl aldehyde or 2-hydroxy aryl ketone of general formula (II) with active methylene of general formula (III) in presence of a mesoporous solid heterogeneous catalyst having organic inorganic hybrid characteristics under Knoevenagel condensation.
NOVELTY - Bacillus species CBW4 strain having a preservation number of KACC91722P, is new.    USE - The Bacillus species CBW4 strain is useful as a microorganism purifying agent in a mud purification process (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) sprinkling the microorganism purifying agent in the mud purification process; and (2) preparing the microorganism purifying agent comprising inoculating the Bacillus species CBW 4 strain in a culture fluid and then cultivating at 25-30 degrees C.
NOVELTY - Reducing agent comprises a culturing liquid including Pichia farinosa NAAS-2 strain having a preservation number of KACC 93160P and Bacillus amyloliquefaciens NAAS-1 strain having a preservation number of KACC 91751P.    USE - The agent is useful for reducing bad odor in livestock waste or food waste (all claimed).    ADVANTAGE - The agent easily reduces the bad odor in the wastes.
NOVELTY - A hydrogen generating apparatus is operated by performing step (S1) of adding hydrogen to raw material so that molar ratio of hydrogen with respect to oxygen in raw material may become greater than or equal to 2, performing step (S2) of supplying raw material to hydrodesulfurization device provided with catalyst which oxidatively degrades raw material and removes sulfur compound in raw material, and performing step (S3) of generating hydrogen-containing gas in modifier using raw material.    USE - Operating method of hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Oxidative degradation of hydrodesulfurization catalyst is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of fuel cell system which involves generating fuel cell electric power using hydrogen-containing gas supplied from hydrogen generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the operating method of hydrogen generating apparatus. (Drawing includes non-English language text).    Hydrogen addition step (S1)    Sulfur compound removal step (S2)    Hydrogen-containing gas generation step (S3)
NOVELTY - A water-retaining composite biofertilizer comprises 8-10 wt.% bioorganic fertilizer, 10-20 wt.% weathered coal, 5-15 wt.% carbonized grass, 3-5 wt.% Azotobacter, 3-5 wt.% phosphobacteria, 3-5 wt.% potassium bacteria, 1-3 wt.% ammonium lauryl ether sulfate, 2-4 wt.% composite bacteria, 3-5 wt.% humic acid, 1-3 wt.% zeolite powder, 1-3 wt.% bentonite, 3-5 wt.% chitin, 1-3 wt.% polypeptide, 5-15 wt.% algae fertilizer, 10-20 wt.% potassium dihydrogen phosphate, and 5-7 wt.% water-retaining agent.    USE - Water-retaining composite biofertilizer.    ADVANTAGE - The biofertilizer decomposes organic pollutants, improves nutrition absorption capacity of crops, reduces fertilizer waste and chemical fertilizer damage to soil, achieves nutritional balance needed by crop growth, and has water retention function.
NOVELTY - Revegetation of areas involves applying different materials for creating layers that are attached to surface along with placement of mesh retention and fiber mats.    USE - Method of revegetation of areas for erosion control (particularly in rainy season) used in construction of civil engineering in any conformation or orography (surface slope).    ADVANTAGE - The method enables to secure low maintenance of vegetation with reduction of environmental impact.
NOVELTY - A saline soil modifier comprises Pinacea material and black tea bacteria.    USE - A saline soil modifier for repairing saline desert and farmland.    ADVANTAGE - Saline soil modifier reduces soil salinity, improves soil physical and chemical structures, and increases soil fertility. Process is simple, low cost, and fast.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of saline soil modifier which involves using Pinacea material and black tea bacteria in which Pinacea material contains fermented Pinacea powder and water mixture, Pinacea powder and solid manure powder, or Pinacea powder, manure powder, and fermented liquid mixture, and formulating black tea bacteria culture liquid by mixing high starch plant waste powder, Pinacea powder, and manure powder, high starch plant waste powder and manure, or Pinacea powder and high starch plant waste powder with water, and fermenting.
NOVELTY - Preparation of bio-char by using agriculture and forestry waste involves washing, drying and crushin, agricultural and forestry wastes to give a dry powdery raw biomass material; adding raw anaerobic biomass material and protective gas into sealed processor; processing by two-stage heating, where first stage is the rapid heating at 220-260 degrees C, and second stage is slowly heating at 350-750 degrees C, continuously cracking oxygen for 1-3 hours; and then cooling to room temperature, grinding obtained material, sieving, activating by using activators, washing and drying to obtain biochar.    USE - For preparation of biochar (claimed) used in preparation of bio-tar, gas and other fuels in energy and chemical fields.    ADVANTAGE - The preparation process is simple, utilizes agricultural and forestry wastes as raw materials, is low cost; prepares biochar having a porous characteristics, surface area, high surface energy, bio-functional groups include carboxyl carbon surface, a phenolic hydroxyl group, a carbonyl group, acid anhydride, lactone, and other groups, and a great cation exchange capacity (CEC), good adsorption characteristics, eliminates potential environmental risks; and reduces greenhouse gas emissions.
NOVELTY - The furnace has a blasting device (5) installed on a furnace body (7). A generating device (1) is connected with a power storage device (2) that is connected with an ignition device (3). An exhaust device (9) is connected with an oil filtering device (8) and equipped with an exhaust valve (10). The furnace body is connected with the oil filtering device (8). The blasting device, a control circuit and the power storage device are connected with the oil filtering device through a grade filter. The power storage device is connected with an illuminating lamp (12) and a power supply socket (13).    USE - Self-generating biomass gasification furnace.    ADVANTAGE - The furnace avoids need of external power supply, increases ignition speed of the ignition device, improves biomass gasification acceleration speed of the blasting device, eliminates smoke of the oil filtering device and solves the problem of tar blocking pipeline, and is simple in structure and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a self-generating biomass gasification furnace.    Generating device (1)    Power storage device (2)    Ignition device (3)    Blasting device (5)    Furnace body (7)    Oil filtering device (8)    Exhaust device (9)    Exhaust valve (10)    Illuminating lamp (12)    Power supply socket (13)
NOVELTY - The furnace has an inner furnace body formed with a furnace cavity. A lower part of a furnace cavity is formed with ash discharging space. The furnace body is provided with flat head teeth and sharp teeth. A butt joint part is fixed with the flat head teeth. An opening end is provided with a cooling water leading-in tube. An internal furnace body is fixed with a cooling water circulation channel. Two ends of a furnace bar i.e. hollow tube body, are connected with a support bearing, where the furnace bar is connected with a transmission chain.    USE - Rotating type removal biomass gasification furnace.    ADVANTAGE - The furnace ensures high production efficiency and reduces energy waste by pneumatic biomass effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a rotating type removal biomass gasification furnace.
NOVELTY - The furnace has an upper furnace body fixed with a furnace cavity. A furnace chamber and a lower furnace body are connected together. Flat head teeth and sharp teeth are arranged at furnace intervals. A furnace ash is crushed into the lower furnace body. A furnace gate is fixed with a base that is moved into the lower furnace body. A furnace strip is arranged with the flat head teeth. An open end of the furnace strip is inserted into the cooling water. An internal furnace is fixed with a cooling water circulation channel. The furnace strip is fixed with a support bearing part.    USE - Biomass gasification furnace.    ADVANTAGE - The furnace smoothly discharges the slag, increases pneuma production efficiency, reduces wastage of energy, and has high significant rate for preparing innovative ferment, thus reducing sugar level from biomass pneuma.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a biomass gasification furnace.
NOVELTY - The furnace has an upper furnace body whose inner part is formed with a furnace cavity. A lower furnace body is filled with biomass granules and connected with a furnace gate. The furnace gate is located at an end opening of a lower furnace cavity. Flat head teeth and sharp teeth are arranged on the furnace body at regular intervals. A furnace strip is arranged on the flat head teeth and the sharp teeth along an axial direction. Ends of the furnace strip is formed with an opening and connected with a support bearing. Cooling water is entered into the furnace body.    USE - Furnace bar integrated slag removing biomass gasification furnace for use during fermentable sugar preparing process.    ADVANTAGE - The furnace can smoothly discharge slag in an effective manner so as to improve pneuma production efficiency and reduce waste of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a furnace bar integrated slag removing biomass gasification furnace.
NOVELTY - A methanol fuel comprises 90-99 wt.% methanol and 1-10 wt.% stability modifier.    USE - A methanol fuel with machine protection function for car (claimed).    ADVANTAGE - Fuel has good anti-knock property and stability, excellent cleanness, and anti-corrosive property, and does not produce carbon.
NOVELTY - A methanol gasoline contains 73-75 mass% methanol, 0.004-0.006 mass% sodium hydroxide, 0.3-0.5 mass% corrosion inhibitor, 0.2-0.4 mass% antioxidant, 0.5-0.7 mass% lubricant, 3-4 mass% methyl tert.-butylether, 3-5 mass% petroleum ether, 0.4-0.6 mass% cyclohexylamine, 7-9 mass% naphtha, 4-6 mass% low-temperature point ignition additive, and 2-2.5 mass% stabilizer.    USE - A methanol gasoline for vehicles.    ADVANTAGE - Methanol gasoline has stable property, clean combustion discharge, low production cost, low ignition oil consumption, and good lubrication property, corrosion resistance, and antioxidant property and saves fuel cost.
NOVELTY - An alcohol-based civil liquid fuel contains 80-85 wt.% methanol, 6-8 wt.% coking light oil, 1.5-2 wt.% water, 1.5-2 wt.% 9-10 carbon-containing aromatic hydrocarbon, and 1-2 wt.% incense material.    USE - Alcohol-based civil liquid fuel (claimed).    ADVANTAGE - The fuel has reduced peculiar smell, improved solution uniformity and transparency, rich raw material, high economical efficiency and calorific value, maximum combustion extent, no residue, pollution, smoke, and special device, and simple process, and is energy-saving and convenient to use.
NOVELTY - A M20 methanol gasoline power performance improving agent contains 18-31% 1,1,-dimethyl pentane, 15-29.5% 4-trifluoromethoxy benzyl alcohol, 15-24.5% bis(diethylamine) phenylphosphine, 13-24% 3-amino-N-methyl-benzylamine, 10-20.5% tert.-butoxy-bis(dimethylamino) methane, and 9-19.5% 2-o-acetyl-benzofuran.    USE - Methanol gasoline power performance improving agent (claimed).    ADVANTAGE - The agent has no toxicity, secondary pollution manganese, and iron, simple and convenient preparation, and proper amount of materials, increases combustion efficiency, and enhances power effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of M20 methanol gasoline power performance improving agent which involves uniformly stirring 1,1-dimethyl pentane, 2-o-acetyl-benzofuran, and bis(diethylamine) phenylphosphine at normal temperature, adding 4-trifluoromethoxy benzyl alcohol and 3-amino-N-methyl-benzylamine, and uniformly mixing.    DESCRIPTION OF DRAWING(S) - The drawing shows a contrast graph of different oil based on torque and fuel consumption rate. (Drawing includes non-English language text).
NOVELTY - A composite methanol gasoline additive is prepared by using 10-55 mass% methyl tert.-butyl ether, 0.05-10 mass% benzotriazole, 15-60 mass% isopropanol, 0.03-25 mass% toluidine, 0.02-12 mass% octadecylamine, and 0.1-15 mass% 2,6-di-tert.-butyl para-cresol.    USE - Preparation of composite methanol gasoline additive (claimed).    ADVANTAGE - The preparation has simple operation and wide source of raw material, and additive has low water content, no combustion ash produced, solves problem on swelling and corrosion of engine rubber and metal part, prevents colloidal oxidation or deposition, improves mix of complete combustion and power, and does not influence normal working operation of spark plug.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process of applying composite additive to methanol gasoline which involves adding composite additive to methanol gasoline in which amount of additive is 0.2-4.5 mass% of methanol in methanol gasoline, and amount of methanol in methanol gasoline is 1-18 vol.%, uniformly mixing, adding basic gasoline, uniformly mixing, and standing for 6 hours.
NOVELTY - A vertical industrial kiln furnace type coal contains 80-85% anthracite coal, 8-10% adhesive, 1-2% sulfur-fixing agent, and 4-8% anthracite biomass in which anthracite coal has greater than or equal to 6100 kcal/ton heat value, coal has less than or equal to 6% ash content and less than or equal to 0.4% sulfur content, and adhesive is composed of 18-22 mass% plant cellulose, 18-22 mass% cement, 35-47 mass% starch, 7.5-12 mass% humic acid, and 7.5-12 mass% high molecular polymer.    USE - Vertical industrial kiln furnace type coal (claimed).    ADVANTAGE - The coal has high strength, big value, and uniform particle size distribution, satisfies heat value requirement in vertical industrial kiln furnace, increases product sintering quality and kiln inner temperature uniformity, is non-toxic and tasteless, and meets environment standard requirements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of vertical industrial kiln furnace type coal which involves crushing anthracite coal to greater than or equal to 80 mesh particle size, drying until water content is less than or equal to 3%, mixing 78-83 mass% lime, and 17-22 mass% periclase, crushing to 80-150 mesh particle size powder to obtain 100 mass sulfur-fixing agent, crushing biomass to 50-150 mesh particle size, mixing plant cellulose, cement, starch, humic acid, and high molecular polymer to obtain 100% adhesive slurry, mixing obtained raw materials, and press-kneading 50-65 tons.
NOVELTY - A straw powder mechanism composite charcoal comprises cylindrical charcoal main body (1) composed of charcoal and bamboo wooden meal, straw powder, or sawdust mixed with shell formed by pressing, and spiral rib (3) or annular groove set at outer surface of main body.    USE - Straw powder mechanism composite charcoal (claimed).    ADVANTAGE - The charcoal can process large amount of straw, recovers biomass and energy, reduces environment pollution, fully combusts, has high density and heat value, and is combustion-resistant.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural schematic diagram of straw powder mechanism composite charcoal.    Cylindrical charcoal main body (1)    Spiral rib (3)
NOVELTY - A mechanism composite charcoal comprises hollow structured main body (1) composed of straw powder and sawdust, wood shavings or scrap mixture formed by pressing, charcoal carbide layer (2) set with main body, and circular or rectangular structured center hole (3) in middle of main body connected with multiple combustion-supporting hole (4).    USE - Mechanism composite charcoal (claimed).    ADVANTAGE - The charcoal can process large amount of straw, recovers biomass and energy, reduces environment pollution, fully combusts, has high density and heat value, and is combustion-resistant.    DESCRIPTION OF DRAWING(S) - The drawing shows a structural schematic diagram of mechanism composite charcoal.    Charcoal main body (1)    Charcoal carbide layer (2)    Center hole (3)    Combustion-supporting hole (4)
NOVELTY - The methane gas generating device comprises: a cylindrical fermentation tank; a rotating shaft arranged in a bottom portion of the fermentation tank, and provided with a rotary wheel; a set of radial stirring poles connected with the rotary wheel; a rotating handle formed in an end of the rotating shaft; and an electrical machine coaxially connected with another end of the rotating shaft. The rotating shaft is connected a cylindrical surface wall of the fermentation tank through a bearing. The stirring poles are welded on a cylindrical surface of the rotary wheel.    USE - Methane gas generating device.    ADVANTAGE - The device can effectively generate the methane gas with increased fermentation efficiency and improved yield, and is simple in structure.    DETAILED DESCRIPTION - The methane gas generating device comprises: a cylindrical fermentation tank; a rotating shaft arranged in a bottom portion of the fermentation tank, and provided with a rotary wheel; a set of radial stirring poles connected with the rotary wheel; a rotating handle formed in an end of the rotating shaft; and an electrical machine coaxially connected with another end of the rotating shaft. The rotating shaft is connected a cylindrical surface wall of the fermentation tank through a bearing. The stirring poles are welded on a cylindrical surface of the rotary wheel, where each of the stirring poles has a length of 30-50 cm.
NOVELTY - The anaerobic tank has a cylindrical tank housing whose bottom portion is provided with a material inlet and an outlet pipeline. A pedestrian ladder is provided in the side portion of the tank housing. An observation hole (6) is formed in upper side portion of a gas cabinet (5) arranged in top portion of the tank housing. A seal glass observation hole (8) is provided in side portion of tank housing. An insulating layer is provided in the tank housing.    USE - Automatic alarm glass anaerobic tank for biogas such as methane.    ADVANTAGE - The leakage of biogas is reduced, and the construction cost of the tank is reduced. The space occupied by the tank is reduced, and the production of biogas is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic alarm glass anaerobic tank.    Port switch valve (1)    Gas cabinet (5)    Observation hole of gas cabinet (6)    Annular corridor (7)    Seal glass observation hole (8)
NOVELTY - An automatic alarm carbon steel mixed-membrane anaerobic tank comprises cylindrical tank body (15) made of carbon steel in which bottom of tank body is provided with biogas slurry outer loop discharge port (14) and inlet and outlet material pipes, inlet and outlet material pipes are merged together, inside of tank body contains 3-way pipe used by turning opening valve, ladder (11) is set on side of tank body, automatic alarm (4) is set on upper part of tank body, and top of ladder is set with transparent glass observation hole (10) which can be opened and close.    USE - An automatic alarm carbon steel mixed-membrane anaerobic tank (claimed).    ADVANTAGE - Automatic alarm carbon steel mixed-membrane anaerobic tank improves biogas yield, fully uses material liquid, and has reduced construction cost.    DETAILED DESCRIPTION - An automatic alarm carbon steel mixed-membrane anaerobic tank comprises cylindrical tank body (15) made of carbon steel in which bottom of tank body is provided with biogas slurry outer loop discharge port (14) and inlet and outlet material pipes, inlet and outlet material pipes are merged together, inside of tank body contains 3-way pipe used by turning opening valve, ladder (11) is set on side of tank body, automatic alarm (4) is set on upper part of tank body, top of ladder is set with transparent glass observation hole (10) which can be opened and close, top of tank body is set with storage cabinet (7) and annular walkway, and tank top is in contact with storage cabinet and provided with ventilation hole round cover for supporting gas membrane from collapsing in absence of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of automatic alarm carbon steel mixed-membrane anaerobic tank.    Automatic alarm (4)    Storage cabinet (7)    Anaerobic tank observation hole (10)    Ladder (11)    Outer loop discharge port (14)    Tank body (15)
NOVELTY - The anaerobic tank has a cylindrical tank housing whose bottom portion is provided with an inlet material pipeline and an outlet material pipeline. The tank housing is provided with rubber arranged with a nylon network line. A pedestrian ladder is provided in side portion of tank housing. An observation hole (6) is formed in upper side portion of a gas cabinet (5) arranged in top portion of the tank housing.    USE - Automatic alarm rubber steel concrete anaerobic tank for biogas such as methane.    ADVANTAGE - The leakage of biogas is reduced, and the construction cost of the device is reduced. The production of biogas is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic alarm rubber steel concrete anaerobic tank.    Port switch valve (1)    Gas cabinet (5)    Observation hole of gas cabinet (6)    Annular corridor (7)    Biogas slurry external circulation hole (9)
NOVELTY - The anaerobic tank includes: a slurry outlet and a discharge pipe arranged in a bottom portion of the tank, where the discharge pipe includes a set of opening valves, where the tank is cylindrical in shape; a ladder arranged in a side of the tank, and including an enamel structure, an automatic alarm unit and a biogas outlet, where the ladder is made of transparent glass and includes an observation hole; a ring structure arranged in a top portion of the tank; and a gas container in contact with the top portion of the tank, and including a cover plate with circular holes for supporting a film.    USE - The anaerobic tank is useful producing biogas.    ADVANTAGE - The anaerobic tank effectively produces the biogas.
NOVELTY - An automatic alarm enameled steel mixed-membrane anaerobic tank comprises cylindrical tank body made of enameled steel-concrete in which bottom of tank body is provided with biogas slurry outer loop discharge port and inlet and outlet material pipes (14) merged together, inside of tank body contains 3-way pipe used by turning opening valve, ladder (10) is set on side of tank body, automatic alarm (3) and biogas slurry outer loop inlet port are set on upper part of tank body, and top of ladder is set with transparent glass observation hole (8) which can be opened and closed.    USE - An automatic alarm enameled steel mixed-membrane anaerobic tank (claimed).    ADVANTAGE - An automatic alarm enameled steel mixed-membrane anaerobic tank (claimed).    DETAILED DESCRIPTION - An automatic alarm enameled steel mixed-membrane anaerobic tank comprises cylindrical tank body made of enameled steel-concrete in which bottom of tank body is provided with biogas slurry outer loop discharge port and inlet and outlet material pipes (14) merged together, inside of tank body contains 3-way pipe used by turning opening valve, ladder (10) is set on side of tank body, automatic alarm (3) and biogas slurry outer loop inlet port are set on upper part of tank body, top of ladder is set with transparent glass observation hole (8) which can be opened and closed, top of tank body is set with storage cabinet (5) and annular walkway, and tank top is in contact with storage cabinet and provided with ventilation hole round cover for supporting gas membrane from collapsing in absence of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of automatic alarm enameled steel mixed-membrane anaerobic tank.    Automatic alarm (3)    Storage cabinet (5)    Observation hole (8)    Ladder (10)    Inlet and outlet material pipe (14)
NOVELTY - The device has a dry fermentation tank (1) whose one end is provided with a cone-shaped door hole (2) and other end is provided with an emptying valve. Several marsh gas collecting tubes (7) are connected with the marsh gas storage cabinet. A liquid inlet is provided on an upper portion of a leachate storage tank (19), and a liquid outlet is provided on a lower portion leachate storage tank. The dry fermentation biogas is produced with predetermined percentage of methane and hydrogen sulfide by the dry fermentation tank.    USE - Device for processing domestic garbage and crop straw biologic dry fermentation.    ADVANTAGE - The purity of the dry fermentation biogas is improved. The discharge of dry fermentation biogas is prevented, thus the secondary pollution to environment is prevented. The processing time for domestic garbage and crop straw biologic dry fermentation is reduced. The slag fertilizer efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the biological anaerobic dry fermentation tank.    Dry fermentation tank (1)    Cone-shaped door hole (2)    Door hinge shaft (5)    Marsh gas collecting tube (7)    Leachate storage tank (19)
NOVELTY - Microbial formulation comprises acid, Saccharomyces cerevisiae, Bacillus subtilis, Bacillus coagulans and Lactobacillus fermentium.    USE - Microbial formulation for deodorizing garbage.    ADVANTAGE - The microbial formulation is non-toxic, eco-friendly and stable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing microbial formulation, which involves:    (A) inoculating Saccharomyces cerevisiae, Bacillus subtilis, Bacillus coagulans and Lactobacillus fermentium;    (B) culturing the strain at 35-36 degrees C for 48 hours;    (C) adding (in wt.%): malt extracting powder (0.3), beef extract (0.3), peptone (0.5), yeast extract (0.3), monopotassium phosphate (0.05), dipotassium phosphate (0.2), hydrated magnesium sulfate (0.025), agar (1.8) and balanced amount of water;    (D) sterilizing the mixture at 121 degrees C for 20 minutes;    (E) transferring the culture medium in a triangular flask;    (F) stirring the mixture at 30-35 degrees C for 36-48 hours; and    (G) cooling the mixture to obtain desired product.
NOVELTY - Kitchen garbage fermentation involves crushing dry yeast, where crushed yeast is added with kitchen waste (2-5%). The mixture is stirred and then fermented at 20-30 degrees C for 72-96 hours. The fermented mixture is added with calcium carbonate, where the pH of the fermented mixture is 5.5-6.5. The fermented mixture is inoculated with acetic acid bacteria. The inoculated mixture is purified by reflux distillation to obtain desired product, where dry yeast is of Angel (RTM: not defined).    USE - Method for fermenting kitchen garbage for producing acetic acid.    ADVANTAGE - The method enables to ferment kitchen garbage in a cost-effective manner.
NOVELTY - Multifunctional biodegradable mulching film comprises dustproof paper layer A (1), degradation and nutrition layer (2), fiber network layer (3), nutrition layer (4), and dust-proof paper layer B (5).    USE - The multifunctional biodegradable mulching film is useful for exhibiting insecticidal, antibacterial and herbicidal effects.    ADVANTAGE - The multifunctional biodegradable mulching film has controlled degradation time and low production cost, leaves no residue after degradation, improves soil properties, and is convenient to use and suitable for industrial large-scale production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited multifunctional mulching film, which involves crushing the straw and sawdust into granule of diameter 10-100 mm, crushing mushroom into granules of diameter not greater than 3 mm, mixing straw powder, garbage powder, sawdust powder and mushroom powder, drying until the moisture content is less than or equal to 15%, subjecting to aerobic fermentation at 60-90 degrees C for not less than 48 hours to obtain fermentation product, adding preservative, biological glue, trace element fertilizer and pesticide to the fermentation product and forming a degradation and nutrition layer, and mixing the fermentation product with biological glue, trace element fertilizer and pesticide and forming a nutrition layer, placing fiber network layer in between degradation and nutrition layer, and the nutrition layer, pressing, placing a dust-proof layer above and below the pressed material, sterilizing, drying at 70-100 degrees C till the moisture content is 8-12%, and processing to obtain the finished product.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of multifunctional biodegradable mulching film.    Dustproof paper layer A (1)    Degradation and nutrition layer (2)    Fiber network layer (3)    Nutrition layer (4)    Dust-proof paper layer B (5)
NOVELTY - Method for reducing cadmium content in rice shoots involves (a) preparing 0.01 g/l nano zinc oxide medium by adding 10 mg nano zinc oxide in 1 l medium, where nano zinc oxide is used instead of original zinc sulfate heptahydrate in Kafer medium, (b) inoculating pear-shaped spores in Kafer liquid culture medium, collecting mycelia, preparing pear-shaped spores mycelium liquid, pouring in roots of rice seedlings, irrigating, and colonizing roots of rice, and (c) transplanting to field after colonization, performing regular water and fertilizer management measures, and harvesting rice.    USE - The method is useful for reducing cadmium content in rice (claimed).    ADVANTAGE - The method is simple, easy, cost-effective, environmentally-friendly and suitable for heavy metal polluted soil and non-polluted soil.
NOVELTY - This utility new type claims a marsh gas heating one pigsty, lower part set with pigsty fermenting bed, between the lower set with marsh gas tank fermenting bed and fermenting bed piggery through bushing connected to the bottom of the fermenting bed set with a sewage outlet, a drain outlet through fermentation bed feed port on a drain pipeline with the marsh gas tank, the air outlet of marsh gas tank and the storage tank connecting pneuma, an air storage tank connected with the boiler, a piggery in side wall set with heating pipeline, a heating pipeline connected with the boiler, the marsh gas tank fermenting bed and set with return pipeline, a return pipeline set with pump. This utility new type is a cleaning pig house of the labour amount is reduced, the pig manure and so on is valid by defecation, and a fermenting bed set with a reduced odor of piggery inner, at the same time, produce a organic matter fermenting bed for a pig is good for the growth of pig, marsh gas pool of ferment product by fermenting bed produce marsh gas by the marsh gas collecting tank, used for boiler combustion through the heating pipeline to the piggery.
NOVELTY - Colloidal cell structure dreg with biomass energy is hydrothermally treated by obtaining aqueous solution, mechanically dehydrating biomass solid fuel having moisture content of 35-50% and wastewater, regulating moisture content of biomass solid fuel in which ratio water:carbon is 0.9-1.2:1, feeding into combustion device having excess air coefficient of 1.1-1.4, temperature of 750-1000 degrees C within adiabatic combustion, and discharged nitrogen oxide (NOx) content in flue gas of 150-400 ppm, and heating to obtain steam.    USE - Hydrothermal treatment of colloidal cell structure dreg with biomass energy for fermentation of biopharmaceuticals and potentially toxic and hazardous substances.    ADVANTAGE - Process has less equipment, low operation cost, and low waste emission, and product has high energy efficiency and good dehydration effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for hydrothermal treatment of colloidal cell structure dreg with biomass energy. (Drawing includes non-English language text).
NOVELTY - Oxyacetylene flame is produced by filling natural gas into container under 1.5-2 MPa pressure, spraying oxygen into oxygen steel cylinder, mixing, injecting hydrogen into hydrogen steel cylinder, mixing, and igniting gas in which addition amount of hydrogen is greater than or equal to 20% volume of natural gas.    USE - Production of oxyacetylene flame for shipbuilding, sulfur-free welding and cutting, vehicle, and electronics.    ADVANTAGE - Oxyacetylene flame is low cost and reduces welding cost and danger in transportation and storage.
NOVELTY - The furnace has a burner (2) connecting with a gas generator that is provided with a grate (1.3). Upper end of the burner is provided with a burner bracket (5) that is provided with an air inlet hole of the burner. A side wall is provided with an air inlet hole. A cooker bracket (3) of a top part is provided with an opening. The cooker bracket is provided with a hole. An external wall is provided with a heat preservation layer. A water tank (6) of an outer wall is welded with an outer wall of the burner.    USE - Lower biomass combustion furnace for a burning device.    ADVANTAGE - The furnace saves energy.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a lower biomass combustion furnace.    Grate (1.3)    Burner (2)    Cooker bracket (3)    Burner bracket (5)    Water tank (6)
NOVELTY - This new type utility claims one aiming at resource utilization device of a DMF rectifying. With pre-heating disk tube of storage tank discharging port through the feeding port of the asphalt pump and the vacuum drier connect the gas exit of vacuum drier is connected to the condenser of the first port, a residue exit retort furnace of vacuum drying machine is connected to a discharging port of the condenser through the first material pump is connected with the feed port of product storage tank, the air outlet of the condenser is connected to the first fuel entrance of dry distillation furnace, the discharging port of the product storage tank conditioning kettle is connected to the rectifying kettle of the feeding port, the feeding port residue exit vacuum drying machine is connected to the air outlet of the rectifying kettle through the second condenser is divided into three way in turn through valve is connected to the water storage tank, a middle fraction tank and inlet of pure DMF solvent storage tank, rectifying kettle of the dry distillation furnace with dry mix gas exit and bio-char exit. The device a high purity DMF solvent and obtain bio-char and no other two secondary pollution, realize resource utilization of DMF rectifying.
NOVELTY - Concentration of oxygen-containing coal bed methane gas comprises subjecting low-concentration methane gas to three-stage process comprising low-pressure methane enrichment; pressurized adsorption deoxidation with different adsorbent through 2-12 adsorption towers; and methane concentration to greater than 90%. The coal bed methane gas has oxygen content of 0.5% or less.    USE - Method for concentration of oxygen-containing coal bed methane gas (claimed).    ADVANTAGE - The method solves the concentration defect problems.
NOVELTY - A carbon dioxide collecting method within hydrophobic microchannel, involves passing absorbent and gas mixture into microchannel at the same time, and absorbing carbon dioxide using the microchannel. Hydraulic radius of the microchannel is 100-1500 mu icrons, where the absorbent comprises 5-50 mass% organic amine, 0-50 mass% sulfolane, 0-0.5 mass% surfactant, 0-0.5 mass% water-soluble defoaming agent and remaining water, the gas mixture comprises 1-30 mol.%, carbon dioxide and 70-99 mol.% nitrogen, and 50-99 mol.% methane and 1-50 mol.% carbon dioxide.    USE - Method for collecting carbon dioxide from hydrophobic microchannel.    ADVANTAGE - The method enables collecting carbon dioxide with high absorption rate, increasing carbon dioxide absorption as absorbent has low surface tension, consuming less energy, and reducing process pressure drop.    DETAILED DESCRIPTION - A carbon dioxide collecting method within hydrophobic microchannel, involves passing absorbent and gas mixture into microchannel at the same time, and absorbing carbon dioxide using the microchannel. Hydraulic radius of the microchannel is 100-1500 mu icrons. Contact angle with the absorbent is not less than 90 degrees , where the absorbent comprises 5-50 mass% organic amine, 0-50 mass% sulfolane, 0-0.5 mass% surfactant, 0-0.5 mass% water-soluble defoaming agent and remaining water, the gas mixture comprises 1-30 mol.%, carbon dioxide and 70-99 mol.% nitrogen, and 50-99 mol.% methane and 1-50 mol.% carbon dioxide, the volumetric flow rate of the gas mixture in the microchannel is 50-500 Nml/minute, the molar ratio of organic amine and carbon dioxide is 2.2-5, and microchannel has operation pressure of 0.1-8 MPa and operation temperature of 20-65 degrees C.
NOVELTY - A co-polymerizable modified graphite carbon nitride hollow spheres photocatalyst, is claimed. The photocatalyst has graphite-type phase, and is a polymer semiconductor.    USE - The photocatalyst is useful in the photocatalytic decomposition of water to produce hydrogen (claimed).    ADVANTAGE - The photocatalyst has uniform particle size, suitable energy band gaps, surface area than the traditional bulk graphite nitride, and high catalytic efficiency; enhances the utilization rate of sunlight; and exhibits high efficiency during the hydrogen production performance. The method is simple, and economical; and meets the actual production requirements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the photocatalyst, comprising taking cyanamide and small organic molecule monomer as a precursor, and mesoporous silica spheres as a hard template to obtain the product.
NOVELTY - This utility new type relates to a compost one air distribution device, comprise ventilation pipeline and the air groove, the number of said air distributing groove is a one or multiple said a ventilation pipeline set with a air groove and match with a vent hole, a wind groove and vent hole and the phase match of connected, the top end of said air groove is opened a opening structure, said inner groove set with air permeable or air groove of said upper top surface set with a plurality of air outlet, a plurality of said air uniform distribute on the top of said upper air groove. This utility new type through the air distribution groove and the ventilation pipeline set with integrated structure, which simplifies the utility new type in process of installation, the use thereof has quick installation, good uniformity, distributing compost efficiency is high and the energy consumption is low and so on.
NOVELTY - An air inlet, discharge hole of gas-solid separator outlet connected gas-solid separator of this utility new type claims a biomass double-level one reactor system, by main reactor, a gas-solid separator and with a feeding port and the secondary reactor, the main reactor of connected sub-reactor of a feeding port, a sand falling tube of the secondary reactor connected sand inlet of main reactor and secondary reactor is provided with one air inlet and a secondary air inlet, through reasonable distribution, the biomass carbon combustion is more sufficient, the quartz sand slag quartz sand circulation promoting smooth flow in the system.
NOVELTY - This utility new type belonging to the biomass comprehensive utilization field, provide the one synthesized in a gas adjust material retention time in the plant base of stirrer. Flow guide plate include, stir shaft, fixing nut, a supporting rod, a locking nut. Wherein the guide plate with the stir shaft rotate included angle alpha of the axis a regulating process, when alpha is a time, stir shaft rotate, the guide plate can promote material flow forward action of the inner reactor, the material near the residence time is reduced when the flow guide plate is parallel to the stir shaft time, a guide plate for material does not produce along the axial pushing action, time when alpha is negative value, stir shaft rotate, a guide plate material to block the inner forward flow of reactor.
NOVELTY - This utility new type provide a one biomass thermal cracking oil device, the device include negative pressure feeding system, reaction system, a cooling system of biomass raw material from entrance of the negative pressure feeding system is sucked, the exit of negative pressure feeding a discharged combustion reaction a reaction process, product of rear reaction through combustion reaction system into a cooling a cooling process. This utility new type provide a biomass thermal cracking oil device, the stable property can be long-term operation so as to increase the efficiency of the biomass thermal cracking oil.
NOVELTY - This utility new type claims a one ecological oil preparation system, include the cracking for biomass fuel gas and produce a carbon reactor, biomass pneuma condensing for condenser of obtain ecological oil, continuously burning biomass carbon heater to heating circulation medium of, further include tubular heat exchange device, a heat pipe heat exchange device by at least two erect level connected in parallel and at least one of a horizontally in two adjacent a connecting a heat exchanger set with a bulk tank and is composed of a dust removing tank through opening connecting heat exchanger, a first-stage heat exchanger connecting air pre-heater. Because the connecting tubular heat exchanging the waste heat smoke pneuma exit of heater, the heat of smoke pneuma can be circulation used, reduces the consumption of energy.
NOVELTY - This utility new type claims a polyethylene alcohol microorganism fixed one a production device, belonging to the field of microbial preparation production technology field. It comprise the tank body, a feeding port, a bracket, a granulating device, leakage, device, pressure table, an inflating tube, seal cover, a charging tube valve and making the valve, the tank body is a bracket, the feeding port is located on one side part of the top of said seal cover of the upper feeding port; the pressure table connecting on the top part of the tank body, the air tube connecting a the tank body, the air tube valve set with the inflation tube a, the granulating device connecting the lower part of the tank body, making the valve set with a connecting device connected with the grain between the tank body; the leakage in the particle set with a device. This utility new type can be continuous production to achieve a high production efficiency, at the same time, solves the problem that the pure gravity dropping granulating speed is slow and difficult to control of the problem, fix a microorganism in a large scale application in sewage treatment engineering.
NOVELTY - This utility new type claims a one pneuma cover water pressure type soft marsh gas tank, and the fermentation include the soft hood, pneuma cover opening by arc-shaped angle iron connecting to a circle, the fermentation chamber upper port, then pneuma cover fixed valve, inner soft seal cover connect feeding soft tube, a feeding hard tube inclined angle of 45 degrees is inserted in the feeding soft tube and a soft cover, fermenting at the bottom of slag liquid from the discharge tube to discharge slag liquid storage pool in, precipitating out of liquid water, inner liquid through water circulation tube, a return to tank, liquid water circulation. This utility new type the following beneficial effects: the soft hood light weight, large strength, good air tightness, convenient to carry, fast installation, low cost, pool liquid water circulation water-saving and environment-friendly, current is of advanced and has high use of popularization value.
NOVELTY - A food waste treatment and utilization of livestock and poultry manure comprises adding different variety of animals manure into simple container, mixing, adding auxiliary material and fermentation bacteria pollutant, material, mixing, sealing, transporting to fermentation field, and fermenting.    USE - Method for treating food waste and utilizing livestock and poultry manure (claimed) used as organic fertilizer.    ADVANTAGE - The method solves the problem of pollutant transport and secondary pollution fermentation.
NOVELTY - Fertilizer is prepared using 40-60 pts. wt. municipal sewage residue, 10-40 pts. wt. residue from riverbed, 10-30 pts. wt. pine bark chip, 3-10 pts. wt. hay powder, 3-10 pts. wt. mushroom residue and 0-10 pts. wt. fly ash, where the above-mentioned raw materials are fermented by inoculating microbial inoculum.    USE - As fertilizer containing municipal sewage residue (claimed).    ADVANTAGE - The fertilizer is cost-effective and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the fertilizer, which involves (a) weighing and mixing above-mentioned raw materials to obtain mixture having moisture content of 55-65%; (b) inoculating the microbial inoculum into mixture obtained in step (a) and mixing uniformly; and (c) fermenting the obtained mixture to obtain product having moisture content of 18-30%, where the fermentation product comprises 2000 million/g microbial content.
NOVELTY - Biological organic fertilizer and its preparation method are claimed. The method involves mixing municipal sludge, chicken manure and waste straw, performing fermentation, drying the fermented mixture, mixing the dried mixture with fly ash, and crushing the mixture to obtain product. The weight ratio of the municipal sludge, chicken manure and waste straw is 6:(2-3):(2-3). The dried mixture and fly ash are mixed in a weight ratio of 8:(1-2). The waste straw includes waste corn straw and waste wheat straw, or their mixtures.    USE - As biological organic fertilizer.    ADVANTAGE - The biological organic fertilizer can be prepared cost-effectively, provides effect for a long period of time, and is easily absorbed by human body.
NOVELTY - Fast heating device has (a) storage container for placing materials and allowing the placed materials to react, where the feed inlet is placed at top or side of the storage container; (b) at least one electric hot plate located at bottom of the storage container for heating process; and (c) at least one insulating cloth, where the insulating cloth is coated outside the heating plate and side of the storage container or covering the heating plate from bottom to top of the storage container.    USE - The fast heating device is useful for converting organic waste into fertilizer (claimed).
NOVELTY - Preparing water soluble organic fertilizer comprises processing molasses fermentation by-product of yellow humic acid liquid, adjusting the pH value using ammonium hydrogen carbonate, crushing urea, phosphamidon, amino acid powder, potassium nitrate, magnesium sulfate, ferrous sulfate, copper sulfate and zinc sulfate, adding processed product into a reaction tank, heating the mixture, and then adding urea, stirring the mixture, stirring the mixture at a constant-temperature for 70-90 minutes, and spray drying the mixture and then adding functional bacteria, cooling at 35 degrees C and packaging.    USE - The method is useful for preparing water soluble organic fertilizer for tobacco plant (claimed).    ADVANTAGE - The method is capable of simply preparing the water soluble organic fertilizer with improved soil fertility and high safety thus improving quality and yield of the tobacco plant.    DETAILED DESCRIPTION - Preparing water soluble organic fertilizer comprises processing molasses fermentation of by-product of yellow humic acid liquid with concentration of 50%, adjusting the pH value to 5.5-6.5 using ammonium hydrogen carbonate, crushing urea, phosphamidon, amino acid powder, potassium nitrate, magnesium sulfate, ferrous sulfate, copper sulfate and zinc sulfate, adding processed product into a reaction tank, heating the mixture at 68-90 degrees C and then adding urea, stirring the mixture for 15-25 minutes, then adding phosphamidon, amino acid powder, potassium nitrate, magnesium sulfate, ferrous sulfate, copper sulfate, zinc sulfate and borax, stirring the mixture at a constant-temperature for 70-90 minutes, and spray drying the mixture and then adding functional bacteria, cooling the mixture at 35 degrees C, and packaging the obtained product.
NOVELTY - Culture medium comprises 45-65 pts. wt. mushroom slag, 25-35 pts. wt. livestock manure, 0.5-1.5 pts. wt. ammonium bicarbonate, 1-2 pts. wt. urea, 1 pts. wt. potassium hydroxide, 1-1.5 pts. wt. lime, 1-2 pts. wt. gypsum, 2 pts. wt. calcium superphosphate, 1-1.5 pts. wt. kelp residue, 1.5-2.5 pts. wt. corn cob, and 0.5-1 pts. wt. protein mud.    USE - The culture medium is useful for culturing mushroom (claimed).    ADVANTAGE - The culture medium is capable of culturing the mushroom with high yield in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the culture medium, comprising (a) crushing mushroom slag and corn cob and drying, (b) pre-wetting the livestock manure for 3-4 days, after mixing the manure with mushrooms, adding the mixed slag in a reactor, when the temperature of the reactor begins to drop by 72-76 degrees C, turning the reactor, adding urea, potassium and ammonium bicarbonate to the reactor during first turning, adding protein mud and kelp residue to the reactor during the second turning, adding gypsum, lime and calcium superphosphate to the reactor during the third turning, and adjusting the pH to 7.5-8, where moisture content is maintained at 64-70% during the entire turning process.
NOVELTY - Oyster mushroom culture base material comprises 30-70 pts. wt. oyster mushroom bacteria slag, 30-40 pts. wt. livestock manure, 0.5-1 pts. wt. wheat bran, 0.5-1 pts. wt. urea, 1 pts. wt. ammonium phosphate, 1-1.5 pts. wt. lime, 0.5-1 pts. wt. calcium carbonate, 2 pts. wt. calcium superphosphate, 0.5-1 pts. wt. potassium sulfate and 1-1.5 pts. wt. castor cake.    USE - Oyster mushroom culture base material.    ADVANTAGE - The culture base material increases mushroom yield to 30-35%, is inexpensive and eco-friendly, and has high biological conversion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the culture base material comprising crushing oyster mushroom bacteria slag and castor cake, drying the crushed material, then pre-wetting livestock manure for 2-3 days, uniformly mixing the dried material and pre-wetted livestock manure, then stacking at 70-75 degrees C, primarily adding urea and ammonium phosphate, and secondarily adding calcium superphosphate and calcium carbonate, then adding potassium sulfate, lime and wheat bran, and then regulating the pH value to 7.8-8, until the moisture content is 63-65%.
NOVELTY - Preparing a floor coat material comprises: crushing rosin and then drying; cleaning a pot; mixing a dissolving agent with a rosin oil, and preheating the mixture; removing moisture form the heated mixture; feeding the crushed rosin into the pot and then stirring, and heating the pot to dissolve the rosin; further heating the pot to completely dissolve the rosin, and standing the mixture; discharging the dissolved rosin from the pot into a resin pot; and distilling the dissolved rosin, and softening the distilled rosin to obtain a rosin product.    USE - The method is useful for preparing a floor coat material (claimed).    ADVANTAGE - The method is capable of preparing the floor coat material with excellent color, reduced energy consumption and sulfur dioxide emission, and improves rosin recovery rate of 98%.    DETAILED DESCRIPTION - Preparing a floor coat material comprises: crushing rosin with a diameter of 150-200 mm and then naturally drying; cleaning a pot; mixing a dissolving agent with a rosin oil, and preheating the mixture at 80 degrees C; removing moisture form the heated mixture; feeding the crushed rosin into the pot and then stirring, and heating the pot to dissolve the rosin; further heating the pot to completely dissolve the rosin, and standing the mixture for 8 hours; discharging the dissolved rosin from the pot into a resin pot; distilling the dissolved rosin at 170 degrees C using a distillation kettle, softening the distilled rosin at 76 degrees C to obtain a rosin product; performing an oil water separation process by connecting an upper part of the distilling pan with a cooler and connecting an outlet of the cooler with an inlet of an oil water separator, guiding the rosin oil into a rosin oil tank, guiding the separated water into a water purification tank; separating a residue form the rosin oil using a centrifugal separation machine; and evaporating the residue stored in a slag pot.
NOVELTY - A microwave apparatus for pyrolysis of biomass smoke pumping port, with straight lower portion, upper curve and flange comprises: box-shaped lower portion of straight waveguide suppressing section (2), waveguide section (2) communicating bottom of microwave heating chamber (1), where top side of opening of mounting flange (3), and opening communicating the other side of the upper top corners, the upper curve is a small ramp tee large Through member (4), the bottom of the ramp tee member (4) mounting flange (5), then the top of the external flue pipe.    USE - For pyrolysis of biomass smoke pumping port (claimed).    ADVANTAGE - The apparatus uses microwave transmission characteristic reverse to inhibit waveguide section, large-caliber, large smoke channel feeding and discharging port of the special structure design. The apparatus uses industrial microwave energy for pyrolyzing biomass of continuity production practice in not only the microwave safety, and a shield heating furnace inner cavity microwave, but also solves the problem that the tar blocking valid small hole and elongated, attachment cannot be a cleaning, it does not need to stop in time, is convenient for the deposition of tar collecting and using, production efficiency is greatly increase.    DESCRIPTION OF DRAWING(S) - The figure shows schematic diagram of microwave apparatus.    Microwave heating chamber (1)    Waveguide suppressing section (2)    Opening mounting flange (3)    Ramp tee member (4)    Bottom mounting flange (5)
NOVELTY - Nano biodiesel comprises 75-85 kg of diesel oil, 8-10 kg of water, 4-5.5 kg of oleic acid, 1-1.2 kg of 25-30% aqueous ammonia and 3-4 kg of 95-99% of methanol.    USE - The nano biodiesel is useful in an internal combustion engine and an external combustion furnace.    ADVANTAGE - The nano biodiesel can be economically prepared in an environmentally friendly manner, and improves combustion in the engine, and avoids carbon deposition and coking effect in the external combustion furnace.
NOVELTY - Coal-based synthetic gas is subjected to desulfurization, and converted and separated into fresh gas (A) and (B). Fresh gas (A) is burned by supplying heat, and methanation reaction is carried out in methanation reactor (a). The fresh gas (B) enters into reactor (b), and methanation reaction is performed. A portion of gas from the reactor (a) is circulated into compressor, and other portion of gas is directly entered into reactor (c), methanation reaction is performed, condensed and separated, and methanation reaction is performed, to obtain methane substitute natural gas.    USE - Methanation process (claimed).    DETAILED DESCRIPTION - Coal-based synthetic gas is subjected to desulfurization, and converted and separated into fresh gas (A) and (B). The fresh gas (A) is burned in a chemical reactor, by supplying heat from an electric heater, and methanation reaction is carried out in a methanation reactor (a). The fresh gas (B) enters into methanation reactor (b), and methanation reaction is performed. A portion of gas from the methanation reactor (a) is circulated into a compressor, and other portion of gas is directly entered into methanation reactor (c), methanation reaction is carried out, condensed and separated, then passed into methanation reactor (d), and methanation reaction is performed, to obtain more than 95% methane substitute natural gas.
NOVELTY - Preparation of biological diesel oil involves sequentially carrying out preprocessing of oil, preparation of catalyst, preparation of aromatic mixture and preparation of diesel oil.    USE - Preparation of biological diesel oil (claimed).    ADVANTAGE - The biological diesel oil is economically prepared.
NOVELTY - Preparation of bazedoxifene acetate (I) comprises subjecting 1-(4-Pg1-methoxyphenyl)propanol (II) and N-(4-(2-azepan-1-yl-ethoxybenzyl))-N-(4-(Pg2 methoxyphenyl))hydrazine (III) to condensation cyclization reaction to obtain 1-(4-(2-azepan-1-yl-ethoxybenzyl))-2-(4-Pg1-oxyphenyl)-3-methyl-5-(Pg2-yloxy)-1H-indole intermediate (IV), deprotection reaction and salt formation with acetic acid to obtain (I).    USE - Preparation of bazedoxifene acetate (I) (claimed).    ADVANTAGE - The method is simple, economical, environment-friendly and suitable for industrial production and has high yield.    DETAILED DESCRIPTION - Preparation of bazedoxifene acetate of formula (I) comprises subjecting 1-(4-Pg1-methoxyphenyl)propanol (II) and N-(4-(2-azepan-1-yl-ethoxybenzyl))-N-(4-(Pg2 methoxyphenyl))hydrazine (III) to condensation cyclization reaction to obtain 1-(4-(2-azepan-1-yl-ethoxybenzyl))-2-(4-Pg1-oxyphenyl)-3-methyl-5-(Pg2-yloxy)-1H-indole intermediate (IV), deprotection reaction and salt formation with acetic acid to obtain (I).
NOVELTY - Organic matter-decomposing inoculant is prepared by using 8-12 pts. wt. strain A and 0.5-2 pts. wt. strain B. The strain A comprises 40-55 pts. wt. Bacillus subtilis, 25-35 pts. wt. Lactobacillus, 7-13 pts. wt. Flavobacterium oryzae, 1-5 pts. wt. Rhizopus, and 3-8 pts. wt. Aspergillus niger and the strain B comprises 0.5-1.5 pts. wt. red yeast, and 1-1.5 pts. wt. Pichia pastoris.    USE - As organic matter-decomposing inoculant.    ADVANTAGE - The organic matter-decomposing inoculant is cost-effective, and convenient to use, not only promotes decomposition of non-degradable substance e.g. pectin, cellulose, lignin, but also satisfies nitrogen, phosphorus and potassium content in fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic matter-decomposing inoculant which involves preparing the above-mentioned strain A, and inoculating into solid fermentation culture medium with inoculum size of 0.8-1.2% and water content of 35-50%, performing fermentation at 45-65 degrees C for 7 days, and detecting the total bacteria number reaches 15 hundred million/g, where the solid fermentation culture medium comprises 40 wt.% rice bran, 10 wt.% soybean meal, 40 wt.% bran, and 10 wt.% corn starch, preparing the above-mentioned strain B, and inoculating into liquid culture medium, performing fermentation at 25-35 degrees C for 13 days, and detecting the total bacteria number reaches 20 hundred million/g, where the liquid culture medium comprises 3 pts. wt. water, 10 pts. wt. soybean and 0.2 pts. wt. cooking liquor of soybean, preparing the organic matter decomposing inoculant by adding 500 pts. wt. rice bran, 500 pts. wt. brown sugar, 15-20 pts. wt. fungus water, and 300-500 pts. wt. lactylate glutathione, uniformly stirring the mixture, and adding the strain A and B, uniformly stirring the mixture for at 45 degrees C for 48 hours, and spreading and drying the obtained product.
NOVELTY - This utility new type provide the one a solar energy and biomass energy combined generating a system, include biomass pyrolysis system 1, collect solar energy and transforming system 2, steam generating system 3. The illumination and electricity generation system 4, wherein the biomass pyrolysis include a hopper 11, a burner 12, biomass pyrolysis furnace 13, a condenser 14, a purification device 15, a gas storage tank 16, a hopper 11 in turn with the biomass pyrolysis furnace 13, a condenser 14, a purification device 15, storage tank 16, a burner 12, a burner 12 and the biomass pyrolysis furnace 13, the condenser (14) in turn and collect solar energy and transforming system 2, steam generating system 3. The illumination and electricity generation system 4, the storage tank 16 with the steam generating system 3, the power generation system 4 and the condenser 14. This utility new type can realize a two energy complementary advantages, increase stability of a power generation system, at the same time, would not cause discharge of harmful substance.
NOVELTY - Biomass granulation mold comprises a mold main body and a feeding hole. The feeding hole is integrally connected to a first, second and third conical holes and a straight hole from the inlet to the outlet with a height of respectively 3.8-4.2 mm, 15.8-16.2 mm, 15.8-16.2 mm and 19.8-20.2 mm. The circular three-dimensional hole diameter of the first conical hole, second conical hole, and third conical hole and straight hole are respectively 10.8-11.5 mm, 8.8-9.2 mm, 6.8-7.2 mm and 5.8-6.2 mm.    USE - Used as biomass granulation mold.    ADVANTAGE - The method increases the yield of the product; reduces the production cost; increases single-time yield; reduces the feeding resistance; reduces the driving force energy consumption; enhances the wear resistance of the mold and prolongs the use life of the mold; carries out three-step feeding, thus gradually increasing the particle density by 0.2%; is fast; and increases the raw material calorific value by 200-300 KCal.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass granulation mold.
NOVELTY - A poultry and livestock manure is reduced and utilized by treating wastewater with circulating water treatment pond and treating solid waste with bio-bed in which wastewater is treated by constructing circulating water treatment pond, installing assorted equipment, introducing biological species, and optimizing equipment use to obtain bioproduct, and solid waste is treated by constructing bio-bed, laying nutrient medium, maintaining bio-bed, introducing biological species, introducing biological species, and optimizing storing and transport of living body to obtain bio-product.    USE - Reduction and utilization of poultry and livestock manure for producing fresh bait material, aquatic product, and vegetables (all claimed).    ADVANTAGE - Reduction and utilization of poultry and livestock manure reduces air pollution, completely digests poultry and livestock manure, and removes heavy metal pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of circulating water treatment pond and bio-bed.    Livestock farm (1)    Circulating water primary treatment pond (4)    Floating microbial culture tank (5)    Water earthworm rinsing and storing tank (7)    Circulating water secondary treatment pond (9)
NOVELTY - A SAPO-35 molecule sieve comprises silicon-aluminum-phosphorus oxide complex (I).    USE - SAPO-35 molecule sieve is used as adsorbent for separation of methane/carbon dioxide and nitrogen/carbon dioxide (claimed) and catalyst in acid-catalyzed reaction e.g. methanol to olefin reaction.    DETAILED DESCRIPTION - A SAPO-35 molecule sieve comprises silicon-aluminum-phosphorus oxide complex of formula: mR1.nCh+.(SixAlyPz)O2 (I).    R1=alcohol amine;    m=0-0.03;    Ch+=choline cation;    n=0.05-0.25;    x=0.01-0.30;    y=0.35-0.55;    z=0.25-0.49;and    x+y+z=1.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of SAPO-35 molecule sieve, which involves adding aluminum source, silicon source, phosphorus source, choline cation-containing compound and deionized water into a high-pressure reactor, sealing the reactor, increasing the temperature of the reactor at 150-220 degrees C crystallizing for 5-120 hours, separating the resultant solid product, washing using deionized water to neutral and drying. The molar ratio of silicon source and aluminum source is 0.01-1.5. The molar ratio of phosphorus source and aluminum source is 0.5-3. The molar ratio of deionized water and aluminum source is 3-20. The molar ratio of choline cation-containing compound and aluminum source is 0.01-3; and    (2) usage method of SAPO-35 molecule sieve as adsorbent for separation of methane/carbon dioxide and nitrogen/carbon dioxide, which involves calcining SAPO-35 molecule sieve at 400-700 degrees C under air.
NOVELTY - Hydrogen is produced from separation of urine via microbial electrolysis by microbial electrolysis cell screening and enriching microorganism, separating ammonia from urine by anaerobic oxidation, simultaneously generating and transmitting electronic microorganism to solid electrode in which microorganisms adhere to anode surface where urine is anaerobically oxidized to ammonia, electron transfer to cathode is driven by applied voltage, and anode produces protons to form hydrogen gas.    USE - Production of hydrogen from separation of urine by microbial electrolysis (claimed).    ADVANTAGE - Process allows long term use of inoculate, produces clean energy while removing ammonia, and has low energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogen production system.    Anode chamber (1)    Cathode chamber (2)    Graphite anode plate (3)    Graphite cathode plate (4)    Ammeter (7)
NOVELTY - Granular sludge processing involves percolating leaf in distilled water, and then adding soil for microbial growth. The obtained material is stirred to obtain turbid liquid. The obtained turbid liquid is placed in batch reactor, and then glucose is added to the reactor, where pH is controlled 7-8 by adding dilute hydrochloric acid solution. The obtained material is stirred at 15-25 degrees C. The obtained material is cultured for 18-22 days. The process is observed through the reactor for appearance of fine appearance of soil granules.    USE - Method for processing granular sludge (claimed).    ADVANTAGE - The method enables to process granular sludge ensures improved sedimentation effect.    DETAILED DESCRIPTION - Granular sludge processing involves percolating leaf in distilled water, and then adding soil for microbial growth. The obtained material is stirred to obtain turbid liquid. The obtained turbid liquid is placed in batch reactor, and then glucose is added to the reactor, where pH is controlled 7-8 by adding dilute hydrochloric acid solution. The obtained material is stirred at 15-25 degrees C. The obtained material is cultured for 18-22 days. The process is observed through the reactor for appearance of fine appearance of soil granules. Microorganism is added to the obtained material, and then covered it. Granule-shaped sludge domestication is performed, when reflection of light is not produced by illumination, and removal rate of water chemical oxygen demand is 75%.
NOVELTY - Water processing device device comprises assistant device buried in ground, water distribution system (17) and water collecting device (18). Assistant device is made of upper and lower layers of wire mesh (6), which is filled with calcium carbonate particles. Calcium compound particles are prepared by mixing a calcium carbonate powder and melt adhesive at room temperature in a hollow spherical column. The water processing device has heating device and sewage pump. The hollow spherical column is sealed after methanol is added to it. Mass ratio of calcium carbonate and methanol in hollow spherical column is 15:8.    USE - Subsurface infiltration filter device used for filtration of ground surface water for cultivation of plat (claimed).    ADVANTAGE - The subsurface infiltration filter device enables to filter surface ground water in simple manner, ensures reduced contamination effect of Acorus calamus, cattail, reed, canna, fleur-de-lis and Thalia dealbata.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a subsurface infiltration filter device.    Water inlet (1)    Wire mesh (6)    Gravel (9)    Water distribution system (17)    Water collecting device (18)
NOVELTY - Town sewage treatment system comprises a series of multi-grid bed of biological treatment zone, which is provided with an inner tank. The inner tank is filled with microbial load (30-60).    USE - Town sewage treatment system.    ADVANTAGE - Town sewage treatment system is simple and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for treating town sewage, which involves:    (A) removing suspended solids from sewage;    (B) passing the obtained sewage through multi-grid bed of biological treatment zone;    (C) passing the obtained material through grid containing microbial lode; and    (D) sterilizing the obtained material, and then recycling the sterilized material.
NOVELTY - The device has micro-organism electrolytic cell casing (2) whose inner portion is set with refraction baffle (3). The left side wall of casing is fixed with sewage water inlet tube (1) equipped with sewage flow control valve. The top end of casing is set with gas collecting tube (6). Light biological reactor (11) is set with illumination intensity detector and nitrogen-phosphorus concentration detector. The signal output end of controller is connected to illumination intensity detector. The nitrogen-phosphorus concentration detector is connected with signal input end of controller.    USE - Micro-organism electrolytic cell combined duckweed organic waste water treatment device.    ADVANTAGE - The microorganism electrolytic cell is included in the duckweed organic waste water treatment device, so that the waste water treatment effect is improved. The biological fuel and biomass can be obtained easily. The sewage treatment cost can be reduced. The energy-saving effect of the device is improved. The gas emission amount is reduced. The waste water treatment process can be performed irrespective of the weather conditions. The processing device can be operated even in rainy days. The waste water treatment efficiency is improved. The water treatment process can be controlled automatically under different climate conditions.    DETAILED DESCRIPTION - The anode electrode (4) and cathode electrode (5) are connected with direct current stabilized voltage power supply portion (8) through titanium lead. An INDEPENDENT CLAIM is included for the duckweed organic waste water treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the waste water treatment device.    Sewage water inlet tube (1)    Micro-organism electrolytic cell casing (2)    Baffle (3)    Anode electrode (4)    Cathode electrode (5)    Gas collecting tube (6)    Power supply portion (8)    Reactor (11)
NOVELTY - Sludge fermentation involves dewatering the sludge material to give the sludge moisture content. The obtained sludge moisture content is added with organic matter, conditioning agent and water content. The obtained sludge mixture is dried that comprises vertical fermenting tower (1), dehumidifying heat pump machine set (3) and feeding port (101), where vertical fermenting tower is set with a reverse turning bed structure (103). The reverse turning bed structure is connected with a fermenting chamber (104). The obtained sludge material is inoculated with a fungus.    USE - Method for fermenting sludge used for dehumidification (claimed).    ADVANTAGE - The method enables to ferment sludge in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sludge drying system, which comprises ventilation hole, fermenting chamber, reverse turning bed structure, where dry hot air enters into the fermenting chamber through ventilation hole.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sludge drying device.    Vertical fermenting tower (1)    Dehumidifying heat pump machine set (3)    Feeding port (101)    Reverse turning bed structure (103)    Fermenting chamber (104)
NOVELTY - This utility new type refers to a spiral discharging one domestic garbage gasification furnace is one a domestic garbage of a special facility. This utility new type using a new design idea, by furnace body, a furnace body shell, water set shell, a foot ring flange, lower foot ring flange, a water level gauge, a steam tube, a safety valve, an upper end enclosure, the water tube interface, a drain tube, a bracket, a fire grate, a spiral slag extractor, a slag outlet, a shaft joint, a speed reducer, a feed chute, a piston pusher, a connecting rod, a hydraulic machine, a distributing plate, a distributor bearing bracket assembly, a distributor, a distributor transmission gear, a speed reducer transmission gear A, a speed reducer transmission gear B, a speed reducer, a gas exit, vent-pipe, air blower, a cavity, wherein the furnace body is bucket by the metal shell is a framework body inner space, the upper part furnace body shell by a cover, and the lower part by spiral extractor, one forming a sealing of the furnace body inner space. The condition of lower full seal, for a domestic garbage gasification, valid cutting dioxin substance produce a condition to reach the harmless treatment of domestic garbage. The furnace has simple and convenient use, automatic degree high, continuous operation of the characteristics.
NOVELTY - This utility new type claims a biomass solid fuel of one mixing device, wherein it comprise a system, a multi-used for loading biomass raw material of a water storage tank, a feeding mechanism and main transmission belt, output end of and water storage tank is equipped with a valve, a system connecting a feeding mechanism, main transfer belt and valve, a feeding mechanism set with the input end of a, a multi-hopper along the transfer direction of main transfer with a part in turn, output end of main transfer belt set with a cylinder, the output end of the corresponding cylinder. This utility new type has simple structure, a convenient operation, a high efficiency.
NOVELTY - Chitin-rich organic fertilizer preparation involves drying insect or crustacean shell, and then crushing them into powder of 20-40 mesh size. Organic waste (225-375 parts) and biologic humic acid (70-80 parts) are mixed with the prepared powder (1 part) in water (60-80%). The obtained mixture is heated at 30-70 degrees C, and then kept the obtained material for fermentation for 15-30 days. Breeding earthworm is added to the fermented base material, where moisture content and temperature are maintained to 50-60% and 16-25 degrees C respectively during the process.    USE - Method for preparing chitin-rich organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare chitin-rich organic fertilizer in simple and cost-effective manner with improved yield, ensures improved soil structure and quality of agricultural products in eco-friendly manner.    DETAILED DESCRIPTION - Chitin-rich organic fertilizer preparation involves drying insect or crustacean shell, and then crushing them into powder of 20-40 mesh size. Organic waste (225-375 parts) and biologic humic acid (70-80 parts) are mixed with the prepared powder (1 part) in water (60-80%). The obtained mixture is heated at 30-70 degrees C, and then kept the obtained material for fermentation for 15-30 days. Breeding earthworm is added to the fermented base material, where moisture content and temperature are maintained to 50-60% and 16-25 degrees C respectively during the process. The prepared earthworm manure mixture is collected and dried, and then filtered to separate un-complete fermented product. The obtained material is filtered to separate earthworm excrement and earthworm eggs to obtain the chitin-rich organic fertilizer.
NOVELTY - Processing bio-organic fertilizer involves using pig manure. Inoculate is added into pig manure and then fermentation is performed. Microelements are added according to need and fermentation is performed continuously to obtain fermentation product. The obtained fermentation product is dried, crushed and sieved to obtain the bio-organic fertilizer.    USE - Method for processing bio-organic fertilizer (claimed).
NOVELTY - Fermenting bio-organic fertilizer involves drying a cattle manure for carrying out dehydration to obtain a block shaped dry manure. The block shaped dry manure is mixed with chicken manure in ratio of 1:2 with stirring uniformly, and then coenzyme and metal protease are mixed uniformly to obtain a product. The product is polished with oxygen-increasing material and then carrying out piling process. The product is cooled and performing repiling. Fermentation process is carried out at the interval of 2-3 days and decomposed in presence of oxygen, where moisture is reduced to 15-25%.    USE - Method for fermenting bio-organic fertilizer (claimed).    ADVANTAGE - The method enables to ferment bio-organic fertilizer in a reliable manner, and bio-organic fertilizer is easy to use.
NOVELTY - Microbial bio-organic fertilizer composition comprises mixture of chelating strain and fermented culture medium in weight ratio of 1:9 respectively. Fermented culture medium comprise (in pts.wt.): carbon mud (60), active carbon (10), mashed vegetable (10) and wheat bran (5). Chelating strain comprise (in pts.wt.): Aspergillus niger (0.5), white rot fungi (0.5), bacteria (1), Candida tropicalis (1.5), lactic acid bacteria (1.5), iron-sulfur (0.5), Streptomyces (0.5), cellulase (1.5), amylase (1.5) and non-ionic surface active agent (1).    USE - Microbial bio-organic fertilizer composition used for removing heavy metal in organic solid waste (claimed).    ADVANTAGE - The microbial bio-organic fertilizer composition is eco-friendly.
NOVELTY - Composting municipal and mushroom waste involves crushing waste bacteria package, chicken manure, municipal waste and water, where moisture content of mixture is maintained. Compost fermentation bacteria is activated and then cultured in liquid medium for 3-5 days to obtain composting agents. The obtained composting agent and waste mixture are mixed and then obtained mixture is fermented for 8-12 days to obtain organic fertilizer.    USE - Method for composting municipal and mushroom waste (claimed) used for preparing nitrogen, phosphorus and potassium fertilizer.    ADVANTAGE - The method enables to compost municipal and mushroom waste in simple, cost-effective and eco-friendly manner.
NOVELTY - Fly ash and rice composite material preparation involves keeping rice in stirrer and rotating at 10 revolutions per minute for 20-30 minutes to obtain fly ash and rice composite material. Fly ash is deep grey powder and water content of rice straw is 50-70% and volume ratio of fly ash and rice straw is 1-5:1.    USE - Method for preparing fly ash and rice composite material used for preparing sludge compost (claimed).    ADVANTAGE - The method enables preparation of fly ash and rice composite material in a simple, cost-effective and eco-friendly manner.
NOVELTY - Shell sheet is arc-shaped and uniformly distributed in seven small magnetic container. Expanding agent and fertilizer are present inside the shell sheet, where adhesive plastic plate is coated is coated on shell sheet both sides. The adhesive plastic plate has thickness (5mm), length (60mm), width (20mm) and height (14.3mm). The magnetic container has small holes of (1mm), where its length is (7mm), width (4mm) and thickness is (3mm). Inner part of the magnetic container is equipped with magnesium (0.05g).    USE - Shell sheet.    ADVANTAGE - The shell sheet is eco-friendly, and increases release speed fertilizer, oxygen and expansion agent and easy to operate.    DETAILED DESCRIPTION - Shell sheet is arc-shaped and uniformly distributed in seven small magnetic container. Expanding agent and fertilizer are present inside the shell sheet, where adhesive plastic plate is coated is coated on shell sheet both sides. The adhesive plastic plate has thickness (5mm), length (60mm), width (20mm) and height (14.3mm). The magnetic container has small holes of (1mm), where its length is (7mm), width (4mm) and thickness is (3mm). Inner part of the magnetic container is equipped with magnesium (0.05g). The magnetic container is covered by three-layer gauze and expanding agent is fixed on the expanding agent.
NOVELTY - Preparing organic fertilizer involves crushing straw materials to obtain 90-100 mesh sieve size grain and then soaking in ammonium hydroxide (5%) for 30 days to obtain straw ammonia mixture. Straw ammonia mixture (5 kg) and water (5kg) are mixed to obtain mixture. Nutrition liquid (0.1l) and microbial inoculums are added into mixture and water content is regulated to 65%. The mixture is decomposed for 20 days to obtain the product.    USE - Method for preparing organic fertilizer (claimed).
NOVELTY - Slow release composite fertilizer comprises (in pts.wt.): biofertilizer (60-70), medicinal fertilizer (20-30), calcium phosphate (2-5), magnesium sulfate (2-5), zinc sulfate (0.5-1), borax (0.5-1) and sodium nitrophenolate (0.1-0.5). Medicinal fertilizer comprises (in pts.wt.): molasses alcohol waste (30-50), animal feces (30-50), bagasse (20-30), straw (20-30) and fermenting agent (0.2-5). Medicine comprises (in pts.wt.): cypress tea (20-30) and chlorantraniliprole (0.5-2), and is prepared crushing, mixing, granulating and sieving raw materials and then coating granule using coating material.    USE - Slow release composite fertilizer used for providing nutrition to crops, promoting growth of crop, improving soil quality and killing crop insects.    ADVANTAGE - The slow release composite fertilizer increases utilization rate of fertilizer and reduces pesticide use in eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing slow release composite fertilizer, which involves:    (A) mixing alcohol waste liquid, animal feces, bagasse or straw in fermentation tank;    (B) drying obtained mixture at 40-70 degrees C;    (C) fermenting mixture in aerobic condition for 7-15 days at 70 degrees C to obtain the bio-fertilizer;    (D) mixing cypress tea and chlorantraniliprole;    (E) pelleting and then coating granules to obtain medicinal fertilizer;    (F) biological fertilizer, calcium phosphate, magnesium sulfate, zinc sulfate, manganous sulfate, borax or sodium nitrophenolate;    (G) pelleting obtained mixture in machine;    (H) adding fertilizer with granules; and    (I) drying obtained granules at 70 degrees C to obtain product.
NOVELTY - Organic fertilizer comprises (in pts.wt.): bio-fertilizer (60-70), tea (20-30), calcium superphosphate (2-5), magnesium sulfate (2-5), zinc sulfate (0.5-1), borax (0.5-1) and sodium nitrophenolate (0.1-0.5). Bio-fertilizer (in pts.wt.): molasses alcohol (30-50), animal feces (30-50), bagasse (20-30), straw (20-30) and microbial fermenting agent (0.2-5).    USE - Organic fertilizer used for promoting growth of crop, improving soil quality and killing insect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) weighing molasses alcohol, animal feces, bagasse and straw according to weight proportion and adding microbial fermenting agent;    (B) mixing and then fermenting at 40-70 degrees C for 7-15 days to obtain fertilizer;    (C) adding tea, calcium superphosphate, magnesium sulfate, zinc sulfate, borax and sodium nitrophenolate into bio-fertilizer to obtain mixture;    (D) crushing mixture through 60 mesh sieve size and then mixing; and    (E) drying at 70 degrees C to obtain the product.
NOVELTY - Preparing fertilizer involves utilizing (in wt.%): lees (30-40), mushroom slag (20-30), carbonized rice hull (20-30) and Rehmannia rhizome (1-10). Carbonized rice hull (0.02%) is mixed with salicylic acid solution to obtain a mixture. The mixture is added in dried lees, mushroom slag and Rehmannia rhizome, and then fermentation process is carried out to obtain fertilizer with particle diameter of (4mm).    USE - Method for preparing fertilizer for tobacco seedling (claimed).    ADVANTAGE - The method enables to prepare fertilizer in a simple and eco-friendly manner.
NOVELTY - Conditioning agent comprises (in pts.wt.): fermented biogas slurry (15-25), dipotassium hydrogen phosphate (0.1-3) and potassium carbonate (1-5).    USE - Conditioning agent for acidic soil (claimed) and used for regulating normal crop growth by adjusting pH value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing conditioning agent, which involves:    (A) putting fermented biogas slurry into cylinder, clean glass beaker or plastic container (1-2 liters); and    (B) mixing dipotassium hydrogen phosphate and potassium carbonate, and the stirring to dissolve to obtain the desired product.
NOVELTY - Extraction of high purity sodium glycolate from diclofenac sodium production wastewater comprises decolorizing wastewater, adding extractant to remove organic impurities, concentrating, crystallizing, mixing with solvent and heating under reflux.    USE - Method for extracting high purity sodium glycolate from diclofenac sodium production wastewater (claimed).    ADVANTAGE - The method is simple and environment-friendly and has high yield.
NOVELTY - Acetic acid and dimethyl sulfoxide are recovered by taking dithianone production mother liquor, adding acid at mass ratio of 8-16:1, stirring, filtering, adding solvent and/or cosolvent at volume ratio of 1:0.5-2, filtering, performing normal pressure azeotropic distillation at 70-85 degrees C, vacuum distilling to obtain acetic acid, vacuum distilling to recover dimethyl sulfoxide, and discharging residual liquid.    USE - Method for recovering acetic acid and dimethyl sulfoxide (claimed).    ADVANTAGE - The environment-friendly recovery method has no waste liquid discharge and residue, and reduced production cost.
NOVELTY - (1S,3aR,6aS)octahydrocyclopenta(c)pyrrole-1-carboxylic acid ester or its salt is prepared by oxidizing octahydrocyclopenta(c)pyrrole hydrochloric acid salt using oxidant to obtain octahydrocyclopenta(c)pyrrole derivative, performing cyanation reaction using cyanating reagent to obtain cyano-containing octahydrocyclopenta(c)pyrrole derivative, hydrolyzing using acid-alkyl alcohol solution to obtain carbonyl-containing octahydrocyclopenta(c)pyrrole derivative, and splitting.    USE - Preparation of (1S,3aR,6aS)octahydrocyclopenta(c)pyrrole-1-carboxylic acid ester or its salt for Telaprevir (RTM: (3S)-3-(((1S,3aR,6aS)-2-((2S)-2-((2S)-2-cyclohexyl-2-(pyrazin-2-ylformamido)acetamido)-3,3-dimethylbutanoyl)-octahydrocyclopenta(c)pyrrol-1-yl)formamido)-N-cyclopropyl-2-oxohexanamide) intermediate.    ADVANTAGE - Preparation method is low in cost, simple, and environment-friendly, has high yield and low device requirement, and uses cheap raw materials, and prepared product is optically pure.    DETAILED DESCRIPTION - (1S,3aR,6aS)octahydrocyclopenta(c)pyrrole-1-carboxylic acid ester of formula (I) or its salt is prepared by oxidizing octahydrocyclopenta(c)pyrrole hydrochloric acid salt of formula (V) using oxidant to obtain octahydrocyclopenta(c)pyrrole derivative of formula (IV), performing cyanation reaction using cyanating reagent to obtain cyano-containing octahydrocyclopenta(c)pyrrole derivative of formula (III), hydrolyzing using acid-alkyl alcohol solution to obtain carbonyl-containing octahydrocyclopenta(c)pyrrole derivative of formula (II), and splitting.    R=1-4C alkyl.
NOVELTY - (2R,3R)-dihydroquercetin is synthesized by using caffeoyl chloride and phloroglucinol as raw materials, performing Friedel-Crafts acylation, oxidizing double bond peroxide into epoxy bond, reacting with phenolic hydroxyl compound into ether under acidic open-loop conditions, separating, purifying, and crystallizing to obtain high content and high purity product.    USE - Synthesis of (2R,3R)-dihydroquercetin (claimed).    ADVANTAGE - Synthesis process is simple and environment-friendly and has simple device.
NOVELTY - Rivaroxaban (I) preparation involves hydrolyzing oxomorpholin compound with an acid at 20-100 degrees C to break amide bond to form compound. The formed compound is treated with 2-formyl chloride for performing acylation with lower base catalyst to form the desired compound rivaroxaban.    USE - Method for preparing rivaroxaban (claimed).    ADVANTAGE - The method prepares rivaroxaban in a simple manner by using mild reaction condition with high reaction yield, avoids use of toxic and harmful reagents, and reduces environment pollution.    DETAILED DESCRIPTION - Rivaroxaban (I) preparation involves hydrolyzing oxomorpholin compound of formula (II) with an acid at 20-100 degrees C to break amide bond to form compound of formula (III). The formed compound is treated with 2-formyl chloride for performing acylation with lower base catalyst to form the desired compound rivaroxaban.    R1=1-6C aliphatic hydrocarbon or aromatic hydrocarbon.
NOVELTY - Butylscopolamine bromide synthesis involves dissolving scopolamine in tetrahydrofuran. The mixture is added with bromobutane and then heated. The heated mixture is cooled on ice bath. The upper layer is removed to obtain crude product. The crude product is washed with methanol twice to obtain desired product.    USE - Method for synthesizing butylscopolamine bromide (claimed).    ADVANTAGE - The method enables to synthesize butylscopolamine bromide in an eco-friendly and cost-effective manner.
NOVELTY - (3R,7aS)-3-Phenyl-6-(phenylsulfanyl)-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one (I) preparation involves reacting diphenyl thioether with (3R,7aS)-3-phenyl-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one (II) in presence of a solvent and alkali to obtain the desired product.    USE - Method for preparing (3R,7aS)-3-phenyl-6-(phenylsulfanyl)-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one used as medicine intermediate (claimed).    ADVANTAGE - The method enables preparing (3R,7aS)-3-phenyl-6-(phenylsulfanyl)-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one with high yield at industrial level in a simple, eco-friendly and cost-effective manner.    DETAILED DESCRIPTION - (3R,7aS)-3-Phenyl-6-(phenylsulfanyl)-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one of formula (I) preparation involves reacting diphenyl thioether with (3R,7aS)-3-phenyl-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one of formula (II) in presence of a solvent and alkali to obtain the desired product. The alkali is represented by compound of formula Y'HMDS (III).    HMDS=silicon base group; and    Y'=alkali metal ion.    An INDEPENDENT CLAIM is included for a method for preparing (3R,7aS)-3-phenyl-1H,3H,5H,7aH-pyrrolo(1,2-c)(1,3)oxazol-5-one, which involves:    (A) reacting diphenyl thioether with (3R,7aS)-3-phenyl-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one of formula (II) in presence of a solvent and alkali to obtain (3R,7aS)-3-phenyl-6-(phenylsulfanyl)-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one of formula (I); and    (B) performing eliminate oxidation reaction with (3R,7aS)-3-phenyl-6-(phenylsulfanyl)-hexahydropyrrolo(1,2-c)(1,3)oxazol-5-one of formula (I) to obtain (3R,7aS)-3-phenyl-1H,3H,5H,7aH-pyrrolo(1,2-c)(1,3)oxazol-5-one.
NOVELTY - Synthesizing abiraterone acetate (I) involves mixing dicyclohexyl(2',4',6'-triisopropylbiphenyl-2-yl)phosphine and pyridin-3-ylboronic acid in protection of inert gas, room temperature condition, and palladium catalyst to form mixture (M1); reacting 17-iodo-androstane-5,16-diene-3beta-acetate with polyoxyethanyl-(alpha)-tocopheryl sebacate (PTS) water solution as catalyst in an inert gas, room temperature and alkali condition to form mixture (M2); heating mixture (M1) and (M2) at room temperature to 40 degrees C to form crude (I); and then extracting and water re-crystallizing to form pure (I).    USE - For synthesis of abiraterone acetate (claimed) which is used for treating advanced prostate cancer.    ADVANTAGE - The present method is simple; saves cost and time; reduces the energy consumption; increases the purity of the product; and reduces the toxic and side effect.    DETAILED DESCRIPTION - Synthesis method of abiraterone acetate of formula (I) involves: mixing dicyclohexyl(2',4',6'-triisopropylbiphenyl-2-yl)phosphine of formula (II) and pyridin-3-ylboronic acid of formula (III) in the protection of inert gas, room temperature condition, and palladium catalyst to obtain mixture (M1); reacting 17-iodo-androstane-5,16-diene-3beta-acetate of formula (IV) with polyoxyethanyl-(alpha)-tocopheryl sebacate (PTS) water solution as catalyst in an inert gas, room temperature and alkali condition to obtain mixture (M2); heating the mixture (M1) and (M2) at room temperature to 40 degrees C to obtain crude abiraterone acetate product; using saturated salt water extracting, using an organic solvent (N1) extraction water phase, combining organic phase, concentrating under reduced pressure with organic solvent (N2) and then water re-crystallizing to obtain pure abiraterone product.
NOVELTY - Method for preparing pelletized fertilizer involves mixing biodegradable material and water-soluble polymer material to form first mixture, mixing polyol, water and nutrient salt to form second mixture, mixing the first mixture and second mixture to form conglomerating gathered third mixture, and stirring the conglomerating gathered third mixture to form small lumps of the third mixture, and spraying probiotic endospores, heating and extruding the fertilizer blocks, and cutting the fertilizer strip to form several pelletized fertilizers.    USE - The method is useful for preparing pelletized fertilizer (claimed).    ADVANTAGE - The method enables to prepare pelletized fertilizer which is convenient for preservation and usage.    DETAILED DESCRIPTION - Method for preparing pelletized fertilizer involves mixing biodegradable material and water-soluble polymer material to form first mixture, mixing polyol, water and nutrient salt to form second mixture, mixing the first mixture and the second mixture to form conglomerating gathered third mixture, and stirring the conglomerating gathered third mixture to form small lumps of the third mixture, spraying probiotic endospores on the small lumps of the third mixture to form several fertilizer blocks, heating the fertilizer blocks, extruding the fertilizer blocks to form a fertilizer strip, and cutting the fertilizer strip to form several pelletized fertilizers. An INDEPENDENT CLAIM is included for pelletized fertilizer which comprises biodegradable material including starch, water-soluble polymer material chosen from polyvinyl alcohol, carboxymethyl cellulose, xanthan gum, shellac, guar gum, natto gum, pectin and poly lactic-co-glycolic acid, polyol, nutrient salt, and probiotic endospores, where the biodegradable material, the water-soluble polymer material, the polyol, the nutrient salt and the probiotic endospores are mixed to one another.
NOVELTY - Fractionating lignocellulosic biomass, comprises (a) extracting the biomass with an extracting liquid comprising at least 20 wt.% of a first organic solvent, at a temperature below 100 degrees C, and (b) treating the extracted biomass with a treatment liquid comprising a second organic solvent comprising lower alcohols, ethers or ketones, optionally water and optionally an acid, at a temperature of 120-280 degrees C.    USE - The process is useful for fractionating lignocellulosic biomass which is herbaceous biomass (preferred), softwood and/or hardwood and useful for producing glucose (all claimed).    ADVANTAGE - The process: increases cellulose purity in a cellulose-enriched product (pulp); improves cellulose hydrolysis; provides a lignin-enriched product containing a higher content of native lignin; provides reduction of the required enzyme load and associated costs; and suppresses the compositional variations by removal of (large parts of) the extractives by organic solvent (and optionally aqueous) extraction.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a composition obtainable by the processes, comprising based on total dry weight: at least 65 wt.% cellulose; at most 12 wt.% lignin; at most 6 wt.% ash; and at most 8 wt.% hemicellulose; and    (2) producing glucose, comprising contacting the composition with at least one hydrolytic enzyme, preferably a cellulase.
NOVELTY - Method for optimizing microbiological purification of biogas resulting from anaerobic fermentation of organic waste, involves increasing amount of liquid retained on a filling constituting filter bed in biofilter, biotrickling filter or bioscrubber, where process is conducted on biological filter bed formed from filtering filling composed of cylindrically shaped polyethylene elements with porous or corrugated walls, with porosity not less than 60%, loading density not greater than 289 kg/m3, with sprinkling intensity QL not exceeding 0.5x 104 m3/s.    USE - The method is useful for optimizing microbiological purification of biogas resulting from anaerobic fermentation of organic waste (claimed).
NOVELTY - Process (P1) for converting biomass fiber source into ethanol and a high value product, involves (a) producing a liquid hydrolysate comprising hemicellulose hydrolysate and a biomass residue from the biomass fiber source, (b) separating liquid hydrolysate from the biomass residue, (c) fermenting monosaccharides in the separated liquid hydrolysate using at least one microbial species immobilized in an immobilization medium, and (d) creating a high value product from the biomass residue.    USE - The process (P1) is useful for converting biomass fiber source into ethanol and a high value product, preferably high energy density product chosen from sulfuric acid, acetic acid, phenolic compounds, polyphenolic compounds, nutraceutical products, cosmeceutical products, pharmaceutical products, furans, furfural, and 5-hydroxymethylfurfural. The process (P2) is useful for converting sugarcane bagasse into ethanol and a high energy density biofuel (all claimed).    ADVANTAGE - The process retains microbe biomass as it is immobilized, and facilitates breakdown of the hemicellulose and solubilize the pentoses and hexoses at the same time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process (P2) for converting sugarcane bagasse into ethanol and a high energy density biofuel, which involves (a) producing a liquid hydrolysate comprising hemicellulose hydrolysate and a biomass residue from sugarcane bagasse, (b) separating liquid hydrolysate from the biomass residue, (c) fermenting monosaccharides in the separated liquid hydrolysate using immobilized microbes, and (d) reducing the moisture content of the biomass residue to produce a high energy density biofuel.
NOVELTY - A porous primary electrode layer is formed (S200). A primary electrolyte layer is formed (S210) on the primary electrode layer. The upper edge of the primary electrolyte layer is removed, and the surface of the primary electrolyte layer is planarized (S220). A secondary electrolyte layer having a dense structure is formed (S230) on the planarized surface of the primary electrolyte layer. A secondary electrode layer is formed (S240) on the secondary electrolyte layer. Thus, manufacture of fuel cell is enabled.    USE - Manufacture of fuel cell e.g. solid oxide fuel cell.    ADVANTAGE - The method enables manufacture of fuel cell having reduced short-circuit and leakage of electrolyte, with reduced formation of pinholes in the electrolyte layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram explaining manufacture of fuel cell. (Drawing includes non-English language text)    Formation of electrode layers (S200,S240)    Formation of electrolyte layers (S210,S230)    Planarization of surface of electrolyte layer (S220)
NOVELTY - Performing afforestation on side surfaces of roads comprises cleaning a ground surface of a road, installing a protective sheet on the ground surface, and applying 87-92 wt.% of soil binding agent, 3-8 wt.% of neutralizing agent, 0.1-2 wt.% of solidifying agent, 70-80 wt.% of red clay, 2-6 wt.% of liquid adhesive, 2.5-10 wt.% of a vegetation promoting composition and a curing agent on the surface of the road.    USE - The method is useful for performing afforestation on side surfaces of roads (claimed).    ADVANTAGE - The method is capable of performing the afforestation on the side surfaces of the road without soil run-off and soil erosion in an economical and environmentally friendly manner.
NOVELTY - System comprises: a gas turbine system (14); and an electrolysis unit (10) designed to produce a hydrogen gas for reducing a minimum emissions compliance load of the gas turbine system.    USE - The system is useful for extending minimum turn down load of combined cycle power plant.    ADVANTAGE - The system: has ability to extend the minimum emissions compliance load for combined cycle power plant; decreases emissions during periods of limited loading; and allows operation of combined cycle power plant at lower loads, thus it avoids frequent starts and shutdowns.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for method for extending minimum turn down load of combined cycle power plant, comprising creating hydrogen gas in an electrolysis unit, capturing the hydrogen gas in a storage container, monitoring at least one parameter of gas turbine system, and guiding the hydrogen gas into the gas turbine system to lower a minimum emissions compliance load in response to at least one parameter.    DESCRIPTION OF DRAWING(S) - The figure shows a block diagram of a combined cycle power plant (8) with an electrolysis unit (Drawing includes non-English language text).    Combined cycle power plant (8)    Electrolysis unit (10)    Gas turbine system (14)    Steam turbine system (16)    Heat recovery steam generator (18)
NOVELTY - Gas detector comprises air supply, filtering system (4), main reactor (14) and monitoring system. The air supply system comprises air pump (1), air-through pipe (2), secondary pressure pump (6), return pressure pump (12), throttle valve (7), air inlet valve (3), valve (10) and return valve (11). The filter system removes hydrogen sulfide, hydrogen and dust. The main reactor contains a composite titanium dioxide photocatalyst (13) in its reaction tank. The monitoring system includes an initial methane detector (5) and a rear methane detector (9).    USE - Gas detector for coal mines.    ADVANTAGE - Gas entering the reactor by way of low exhaust pump is decomposed into carbon dioxide and water vapor, thus lowering the catalytic action of composite photocatalyst and reducing the gas concentration.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the gas detector.    Air pump (1)    Air-through pipe (2)    Air inlet valve (3)    Filtering system (4)    Methane detector (5)    Secondary pressure pump (6)    Throttle valve (7)    Rear methane detector (9)    Valve (10)    Return valve (11)    Return pressure pump (12)    Composite titanium dioxide photocatalyst (13)    Main reactor (14)
NOVELTY - This utility new type claims a pneuma chromatography one anlysis system, not only for a of micro CO in high pure gas, CH4 and CO2 process a, further comprising time percentage content is CH4 and trace CO2 on the other process gas in trace CO2 a process for detecting, through for percentage content CH4 a, the small part of CH4 and CO2 a reverse blowing two times anlysis, so as to micro-CO2 percentage content CH4 is separated, solves the problem that the spectrogram percentage content is CH4 the micro peak CO2 peak cover not for micro-CO2 a process of, and expands the application field of the whole pneuma way is not limited to only a trace of a are, even if the background concentration is large, also can be a component of a small amount of expansion so as to application to other pneuma way.
NOVELTY - The device has a container (1) which is connected with a group of high voltage electrode (3), a high voltage negative electrode (4), a low-voltage negative electrode (7), and a low voltage positive electrode (8). A low voltage positive electrode has a high-voltage electrode disposed in the container. The container is divided into oxidation area and reduction area, in which cathode electric field is close to oxidation zone, and the reducing area is close to the positive electric field of the insulation material of the container, and the inner container storages of electrolytic liquid (2).    USE - Electric field induction type electrolysis hydrogen device.    ADVANTAGE - Ensures low-voltage electrode of valid exchange, improves electrolytic speed, and electric exchange electrode electric current of low voltage electrode, and increases electrolysis of the efficiency by improving the moving speed of ion electric pulse.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of electric field induction type electrolysis hydrogen device.    Container (1)    Electrolytic liquid (2)    High voltage electrode (3)    High voltage negative electrode (4)    Low-voltage negative electrode (7)    Low voltage positive electrode (8)
NOVELTY - Electrolysis of sodium chloride aqueous solution involves degrading organic substance contained in sodium chloride aqueous solution using a sulfur type oxidizing agent, and then using the sodium chloride aqueous solution as a raw material of an ion exchange membrane based brine electrolysis.    USE - Electrolysis of sodium chloride aqueous solution containing organic substances including alcohol, aldehydes, ketones, organic acids, carbohydrate, ammonia, ammonium salt, amines, amino acids and organic halogenated compound.    ADVANTAGE - The method enables to effectively, efficiently and easily obtain intensively purified salt water by completely degrading organic substances using an inexpensive sulfur type oxidizing agent, and reduces load on environment.
NOVELTY - Carbon reduction method comprises injecting pure water in electrolytic groove (1), connecting first gas tube to engine intake manifold (21) and second air tube to fuel tube (31), connecting engine intake manifold and fuel tank, supplying electric current to electrolytic groove, injecting pure water, electrolyzing with hydrogen gas and oxygen, and supplying engine with fuel to make hydrogen and oxygen mix to preset ratio of engine.    USE - Carbon reduction method for improving efficiency of engine auxiliary device.    ADVANTAGE - The method realizes energy conservation and emission reduction of carbon.    DETAILED DESCRIPTION - Carbon reduction method comprises injecting pure water in electrolytic groove (1), connecting electrolytic groove with first gas tube and second gas tube, connecting first gas tube to engine intake manifold (21) and second air tube to fuel tube (31), connecting engine intake manifold and fuel tank, supplying electric current to electrolytic groove, injecting pure water, electrolyzing with hydrogen gas and oxygen, conveying oxygen through first gas tube to air inlet pipe entering into the engine (2), and introducing hydrogen gas to fuel pipeline through second gas tube and mixing with fuel, so as to supply the engine with fuel to make the hydrogen and oxygen mix to preset ratio of the engine.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic perspective view of the engine auxiliary device.    Electrolytic groove (1)    Engine (2)    Engine intake manifold (21)    Fuel tube (31)    Nozzle (32)
NOVELTY - Gas separation method involves contacting an adsorbent or membrane containing DDR-type zeolite crystals with an input gas stream containing components (a, b) for forming a primary gas stream enriched in component (a), and collecting a secondary gas stream enriched in component (b). The zeolite crystals are obtained from a mixture having ratio of alkali metal and silica of 0.01 or more. The adsorbent or membrane comprises crystals with 0.05 wt.% or less alkali metal impurities. The alkali metal is sodium, DDR-type zeolite crystals preferably Sigma-1, ZSM-58 and/or SSZ-28.    USE - Gas separation method is used in refinery.    ADVANTAGE - The method enables stable separation of gas for long period of time.    DETAILED DESCRIPTION - Gas separation method involves contacting an adsorbent or membrane containing DDR-type zeolite crystals with an input gas stream containing components (a, b) for forming a primary gas stream, and collecting a secondary gas stream. The primary and secondary gas streams are enriched in components (a) and (b), respectively, with respect to the input gas stream. The DDR-type zeolite crystals are obtained from a synthesis mixture. The mixture has ratio of an alkali metal and silica of 0.01 or more. The adsorbent or membrane comprises crystals with 0.05 wt.% or less alkali metal impurities. The alkali metal of the mixture is preferably sodium, DDR-type zeolite crystals preferably Sigma-1, ZSM-58 and/or SSZ-28.
NOVELTY - Recovering the dry gas refining involves condensing refinery dry pneuma to 40 to 80 degrees C form first pneuma phase and first liquid phase, for first liquid phase process; (B) a first gas phase using liquid nitrogen condensed to 162-180 degrees C form second phase and a second liquid phase and second liquid phase process for rectifying and purifying obtain methane, ethylene, a second gas phase process for rectifying (6) and purifying obtain hydrogen-nitrogen mixture.    USE - For recovering dry gas refining (claimed), for producing hydrogen, light hydrocarbon and light olefins.    ADVANTAGE - The method avoids the dry pneuma of refinery for waste and the environment pollution.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of refinery dry pneuma recovery device structure.    First Separation condenser (1)    Second separation condenser (4)    Rectifying tower (6)
NOVELTY - The underoil apparatus comprises a circular tube way (23) divided from a suction line (21) connected to a return port (14) of a transformer (10) through a return duct way (22). An inlet (12) collects the space gas of a head-space (15) of the transformer through the suction line. A gas chamber (30) stores another circular tube way (24) divided from the return duct way. A control unit (90), in which the oxygen content and carburet hydrogen density are measured. A sensor unit (50) inhales the space gas from the inlet of the transformer. A fluid path controlling element (60) controls a fluid path.    USE - Apparatus for measuring dissolved gas, such as methane, ethane, propane, ethylene and acetylene lamp concentration in an oil filled transformer.    ADVANTAGE - The underoil apparatus comprises a circular tube way divided from a suction line connected to a return port of a transformer through a return duct way, and thus accurately detects the concentration of hydrogen, and also accurately diagnoses the abnormality of the transformer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for measuring dissolved gas in an oil filled transformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an underoil device. (Drawing includes non-English language text).    Transformer (10)    Inlet (12)    Return port (14)    Head-space (15)    Suction line (21)    Return duct way (22)    Circular tube ways (23,24)    Gas chamber (30)    Sensor unit (50)    Fluid path controlling element (60)    Control unit (90)
NOVELTY - Obtaining hydrogen by electrolysis involves feeding energy from source of power to an anode and activated cathode in electrolyzer, and directing electrolyzed hydrogen in accumulator of hydrogen and producing with heat removal, which separates in the process of electrolysis of the heat exchanger, where energy for electrolysis is supplied from renewed sources of energy in the pulse mode of supply of current, and heat removal is by the circulations of heat-transfer agent in hollow heat exchanger-utilizer anode.    USE - The method or device is useful for obtaining hydrogen by electrolysis (claimed).    DETAILED DESCRIPTION - Obtaining hydrogen by electrolysis involves feeding energy from source of power to an anode and activated cathode in electrolyzer, and directing electrolyzed hydrogen in accumulator of hydrogen and producing with heat removal, which separates in the process of electrolysis of the heat exchanger, where energy for electrolysis is supplied from renewed sources of energy in the pulse mode of supply of current, and heat removal is by the circulations of heat-transfer agent in hollow heat exchanger-utilizer anode, where cathode activation is carried out by pulse U-shaped electric current directly in electrolyte of the electrolyzer, as which is used to sea water with content of salt from 3.5 to 40. An INDEPENDENT CLAIM is included for a device for obtaining hydrogen, comprising a supply of electric, electrolyzer and storage of hydrogen, where the cathode of electrolyzer is made from activated alumina, and anode of electrolyzer is made in form of hollow tube for the circulation of heat-transfer agent, where anode and cathode are arranged in the electrolyzer, filled with electrolyte, as which is used the sea water with content of salt from 3.5 to 40 g/L, connected to source of electric with a pulse mode of supply of electric current.
NOVELTY - This utility new type relates to one by using a coal bed gas production of liquefied natural gas device. The character is: include a nitrogen expansion refrigerating system, the nitrogen expansion refrigeration system comprise a expander (9) and a compressor (5), and wherein the expander (9) of exit through pipeline in turn and the second level heat exchanger (2), a first-stage heat exchanger (1) and the compressor (5) of entrance connected the first-stage heat exchanger (1) is a set with a gas inlet and gas exit, and the second level heat exchanger (2) is a set with liquefied natural gas inlet and a liquefied natural gas exit, wherein coal bed gas exit through throttle valve (3) and the gas-liquid separating tank (4) is connected, the pneuma liquid separating tank (4) of liquid exit and liquefied natural gas inlet connected. This utility new type through nitrogen-expansion refrigeration principle for a bed rear purification of a cooling process, the coal bed gas production transportation is liquefied natural gas (LNG), so gas and of use.
NOVELTY - Extraction of azadirachtin comprises cutting neem seeds through blade cutting machine, adding into greater than 95 wt.% ethanol solution, and ultrasonically treating at ultrasonic power of 200-500 W and frequency of 1500-1500 Hz for 15-30 minutes; and filtering to obtain filtrate and residue, vacuum-drying filtrate at 40 degrees C, and removing ethanol.    USE - Method for extraction of azadirachtin (claimed).    ADVANTAGE - The method is simple, easy to control and environment-friendly, obtains high purity azadirachtin, and has high yield.
NOVELTY - The tank has outer tank portion whose bottom portion is provided with inlet and outlet material pipeline. A three-way connecting tube is installed in a switch valve (2). The tank bottom portion of is provided with biogas slurry external circulation exit portion and tank upper portion is provided with inner booster outer circulation entrance portion. The side of tank portion is provided with pedestrian ladder. The top end of tank portion is designed with storage cabinet and pedestrian channel. The cabinet joint is provided with circular cover plate.    USE - Heating brick-concrete anaerobic tank.    ADVANTAGE - The biogas utilization rate of biogas is increased effectively. The gas leakage of liquid producing biogas is reduced. The construction cost of brick-concrete anaerobic tank is reduced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heating brick-concrete anaerobic tank.    Port switch valve (1)    Switch valve (2)    Biogas hole (6)    Cabinet observation hole (8)    Flow port (16)
NOVELTY - The anaerobic tank comprises a cylinder shaped glass fiber reinforced steel concrete structured tank body whose bottom part is provided with inlet and outlet material pipelines, which are provided with a three-way opening valve. One side of the tank body is provided with a pedestrian ladder, and an upper part of the tank body is provided with a booster. The ladder is provided with a glass transparent observation hole, which is opened and closed. A top end of the tank body is provided with a gas storage cabinet and an annular moving part.    USE - The anaerobic tank is useful for processing slurry (claimed) to produce biogas.    DETAILED DESCRIPTION - The anaerobic tank comprises a cylinder shaped carbon steel building structured tank body whose bottom part is provided with inlet and outlet material pipelines, which are provided with a three-way opening valve. One side of the tank body is provided with a pedestrian ladder, and an upper part of the tank body is provided with a booster. The ladder is provided with a glass transparent observation hole, which is opened and closed. A top end of the tank body is provided with a gas storage cabinet and an annular moving part. The gas cabinet is provided with a circular cover plate having a ventilating circular hole. An upper part and a lower part of the tank body are provided with a radiator for heating biogas slurry. The radiator is connected with a heat source.
NOVELTY - Inner heating rubber line anaerobic tank, comprises: cylindrical tank body, material inlet and outlet pipeline, three-way opening valve, outer circulation liquid exit, pedestrian ladder, inner booster, outer circulation entrance, pneuma storage cabinet and radiator.    USE - As inner heating rubber line anaerobic tank (claimed) for producing biogas liquid.    ADVANTAGE - The inner heating rubber line anaerobic tank reduces gas leakage, reduces the construction cost, and increases the biogas liquid producing efficiency.    DETAILED DESCRIPTION - Inner heating rubber line anaerobic tank, comprises: cylindrical tank body, material inlet and outlet pipeline, where the bottom is provided with inlet and outlet material pipeline, three-way opening valve, outer circulation liquid exit, where the bottom is designed with outer circulation liquid exit, where the tank body is designed with rubber line structure building, where the inner rubber is arranged with a nylon network wire, and the side is provided with pedestrian ladder. Upper part is designed with inner booster, outer circulation entrance, ladder designed with transparent glass observation hole, open and close; the top end is designed storage cabinet, and is designed with an annular sidewalk, the water storage tank is contact with top cabinet, and is provided with shield for support gas film caused by free time collapse; and in the tank body, middle is provided with radiator for heating the biogas slurry.
NOVELTY - The tank has tank bottom portion that is provided with inlet and outlet material pipeline. A side of tank portion is provided with a pedestrian ladder. The upper portion of is provided with an alarm. The ladder is designed transparent glass observation hole. The tank top portion is provided with storage cabinet and is provided with annular moving portion. A circular cover plate supports gas film. The middle portion of tank portion is provided with a radiator next to biogas heating.    USE - Heating carbon steel concrete anaerobic tank.    ADVANTAGE - The biogas utilization rate of biogas is increased effectively. The gas leakage of liquid producing biogas is reduced. The construction cost of brick-concrete anaerobic tank is reduced reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heating brick-concrete anaerobic tank.    Switch valve (1)    Cabinet observation hole (8)    Feeding material tube (16)    Steel structure column (17)    Glass steel tank portion (19)    Ladder (20)
NOVELTY - Internal-heating type ceramic mixture film anaerobic tank comprises a cylindrical tank body and a material inlet and outlet pipeline provided at the bottom of the tank body. The material inlet and outlet pipeline are integrated. A three-way tube provided with a rotatable opening valve. The tank body structure is made of enamel and one side of the structure is provided with a pedestrian ladder. The upper part of the tank body is provided with an automatic alarm. The pedestrian ladder is designed with a transparent glass observation hole, which can be opened and closed.    USE - Used as internal-heating type ceramic mixture film anaerobic tank.    ADVANTAGE - The anaerobic tank improves influence of natural environment on the biogas slurry and this improve biogas liquid and biogas production.    DETAILED DESCRIPTION - Internal-heating type ceramic mixture film anaerobic tank comprises a cylindrical tank body and a material inlet and outlet pipeline provided at the bottom of the tank body. The material inlet and outlet pipeline are integrated. A three-way tube provided with a rotatable opening valve. The tank body structure is made of enamel and one side of the structure is provided with a pedestrian ladder. The upper part of the tank body is provided with an automatic alarm. The pedestrian ladder is designed with a transparent glass observation hole, which can be opened and closed. The top end of the tank body is designed with a gas storage cabinet and is provided with an annular sideway channel. The top part of the gas storage cabinet provided with circular cover plate with circular ventilation hole. The circular cover plate prevents collapse of gas storage membrane in absence of gas. The lower, middle and upper part of tank body is provided with a radiator for heating biogas slurry.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the internal-heating type ceramic mixture film anaerobic tank.
NOVELTY - A warming inner enamel steel concrete anaerobic tank contains tank body which is cylinder with enamel steel-concrete structure in which bottom is provided with combined inlet and outlet material pipelines, vitro 3-way valve is used for rotation, side is provided with pedestrian ladder (11) with design glass transparent observation hole which can be opened or closed, upper part is designed with automatic alarm, top end is designed gas storage cabinet (7) with annular sidewalk, water storage tank top and gas cabinet are in contact, and middle of tank body is provided with radiator for heating.    USE - A warming inner enamel steel concrete anaerobic tank (claimed).    ADVANTAGE - Product increases production efficiency of biogas and yield, and construction cost is reduced.    DETAILED DESCRIPTION - A warming inner enamel steel concrete anaerobic tank contains tank body which is cylinder with enamel steel-concrete structure in which bottom is provided with combined inlet and outlet material pipelines, vitro 3-way valve is used for rotation, side is provided with pedestrian ladder (11) with design glass transparent observation hole which can be opened or closed, upper part is designed with automatic alarm, top end is designed gas storage cabinet (7) with annular sidewalk, water storage tank top and gas cabinet are in contact, circular cover plate is designed with ventilating circular hole to support gas film caused due to absence of gas collapse, and middle of tank body is provided with radiator to heat biogas slurry.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of warming inner enamel steel concrete anaerobic tank.    Gas storage cabinet (7)    Ladder (11)    Methane area (12)    Booster (13)    Glass wall (15)
NOVELTY - Biological enzyme complex comprise 16 wt.% protease, 28 wt.% amylase, 37 wt.% cellulase and 19 wt.% lipase.    USE - The biological enzyme complex is useful for processing sewage obtained from pharmaceutical companies (claimed).    ADVANTAGE - The biological enzyme complex degrade antibiotics and organic matter in sewage into carbon dioxide and other stable materials, and eliminates odor, and reduces content of sludge. The method satisfies national effluent standards, and reduces pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing sewage obtained from pharmaceutical companies, involves adopting preparation of bacterial cultures and stable operation of enzymes, where method involves using device (pre-processing stage, biological enzyme complex integrated biological treatment stage, sludge treatment and effluent discharge phase emission stages).
NOVELTY - Organic fertilizer comprises 10-30 pts. mass livestock and poultry manure, 70-90 pts. mass organic material and 0.05-0.3% biological isolates.    USE - The organic fertilizer is useful for cultivating vegetables, fruit trees, tea, tobacco, and potato, and flower and gardens (claimed).    ADVANTAGE - The organic fertilizer is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the above-mentioned organic fertilizer, which involves (a) mixing the above-mentioned livestock and poultry manure with the organic material, (b) adding the above-mentioned biological isolates to the obtained mixture, stirring the mixture in stirrer for 10-15 minutes to obtain compost, and fermenting the compost at 58-62 degrees C for 48 hours, (c) turning the compost once for every 3-4 days (2-33 times), and fermenting for 9-12 days and air drying the compost or drying in sun (sampling), and (d) crushing the obtained product using crusher, sieving the crushed product using sieving machine, metering the product, and packing the product; and    (2) use of the above-mentioned organic fertilizer for cultivating vegetables, fruit trees, tea, tobacco, and potato, and flower and gardens.
NOVELTY - An orange special long-acting composite fertilizer comprises 40-50 wt.% nitrogen, 15-20 wt.% phosphorus pentoxide, 10-15 wt.% potassium hydroxide, 0.03-0.05 wt.% zinc, 0.003-0.005 wt.% molybdenum, 5-8 wt.% ammonium sulfate, and 20-40 wt.% water hyacinth fermentation product.    USE - Orange special long-acting composite fertilizer.    ADVANTAGE - The fertilizer is rich in up to more than 20% humic acid organic matter and better than a single compound fertilizer, can improve soil's aggregate structure, cation exchange capacity and water retention capacity, stimulates the activity of enzymes and beneficial soil microorganisms to improve soil fertility structure, and improves activity of nutrients.
NOVELTY - Organic fertilizer is prepared using 40-50 pts. wt. water hyacinth fermentation product, 10-15 pts. wt. potassium chloride, 10-30 pts. wt. humic acid, 10-20 pts. wt. calcium carbonate, 40-50 pts. wt. boric sludge and 10-15 pts. wt. fermentation agent.    USE - As organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer increases crop yield rate, reduces fruit drop, enables early maturity within 5-7 days, improves appearance, taste, color and quality of product and extends product shelf life.
NOVELTY - Preparation of garbage fuel oil involves sorting garbage into pyrolysis unit (p1), performing pyrolysis at 180-320 degrees C, obtaining pyrolysis product containing gaseous component (G1) and acid component, discharging product, supplying pyrolysis products into pyrolysis unit (p2), performing pyrolysis at 350-550 degrees C, obtaining carbon residue and gaseous component (G2), supplying gaseous component into reactor (r2), reacting with powdered elemental iron at 570 degrees C or more, obtaining gaseous component (G3), condensing, and forming fuel oil and gas.    USE - Preparation of garbage fuel oil (claimed).    ADVANTAGE - The method economically and environmentally-friendly enables preparation of garbage fuel oil with high resource utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for preparing garbage fuel oil, pyrolysis unit (p1), reactor having powdered elemental iron, cracker, condensing unit, liquid storage container, combustion chamber, pyrolysis unit (p2), condensing unit and heater.
NOVELTY - A mixed renewable material and biomass material production device comprises feeding system, reaction furnace, oil and gas separator (18), detritus tank (19), 2 feeding ports, fixed deslagging cylinder (17), rotary cracking tube (10), fixed feeding cylinder (7), electric driving motor, slag removal tank, center tube, central sampling tube and fixed support frame.    USE - Mixed renewable material and biomass material production device.    ADVANTAGE - The production device has automated feeding and discharge, simple operation and small labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of mixed renewable material and biomass material production device.    Fixed feeding cylinder (7)    Rotary cracking tube (10)    Fixed deslagging cylinder (17)    Oil and gas separator (18)    Detritus tank (19)
NOVELTY - Methanol gasoline (III national standard gasoline) comprises 13 pts. methanol, 62 pts. No. 90 gasoline, 1.3 pts. methyl tert-butyl ether and 1.8 pts. acetone additive. The methanol gasoline is obtained by mixing the above-mentioned raw materials, and stirring.    USE - Used as a methanol gasoline.    ADVANTAGE - The preparation process is simple, economical and environmentally friendly. The methanol gasoline has 70-85% lower exhaust gas emission rate than national standard gasoline, reduces environmental pollution, can mix the methanol-based fuels with petroleum fuels, can be directly used in engine without changes, and starts the engine at -40 degrees C.
NOVELTY - Production of synthetic natural gas comprises reacting hydrogen in the synthesis gas with carbon monoxide and methane, carrying out synthesis gas desulfurization and decarbonization through three reactors containing a multi-stage methanation reaction, and condensing water to obtain more than 95% methane gas.    USE - Method for producing synthetic natural gas (claimed).    ADVANTAGE - The method can obtain high levels of methane gas, is simple, and has low energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for producing synthetic natural gas (Drawing includes non-English language text).
NOVELTY - Cow dung matrix for silver radix bupleuri seedling is prepared by mixing 100 pts. wt. rotten cattle manure, 20-30 pts. wt. soil, 5-10 pts. wt. vermiculite, 3-5 pts. wt. perlite, 3-5 pts. wt. river sand, 2-5 pts. wt. macroelements, 0.2-0.4 pts. wt. trace element, and water (suitable quantity).    USE - The cow dung matrix is useful for breeding silver radix bupleuri seedling (all claimed).    ADVANTAGE - The cow dung matrix enables to improve sprouting rate and survival rate of silver radix bupleuri seedling cost-effectively within short period of time.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the cow dung matrix for silver radix bupleuri seedling which involves composting manure, soil, vermiculite, perlite, and river sand mix using thin film cover and performing heat preservation for 24 hours, adding macroelements, and trace elements to the heat preserved raw materials, and adding water (suitable quantity), soaking the mixture, and regulating pH using sodium acetate or ammonium chloride solution to 5.5-6.8, and preparing the obtained matrix into disc for silver radix bupleuri seedling; and    (2) breeding method of silver radix bupleuri seedling using cow dung matrix involves preparing the matrix and sterilizing using UV-rays to kill virus at 9-10 degrees C and air humidity of 15-20%, selecting excellent silver radix bupleuri seedling and sowing on the matrix, performing germination at controlled temperature, air humidity, matrix pH value, ventilation and illumination for 8-10 days to prevent the condition caused by sudden dead sprout, and transplanting the obtained product after 20-30 days.
NOVELTY - A pesticide residue-degrading special liquid fertilizer comprises 16-24 wt.% microbial flora, 32-35 wt.% fertilizer, 1.5-2.5 wt.% pesticide, 3.1-3.9 wt.% release agent, and balance water.    USE - Pesticide residue-degrading special liquid fertilizer used for increasing yield in apple production (claimed).    ADVANTAGE - The fertilizer has long time effect, small dosage, and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of special liquid fertilizer comprising preparing apple special pesticide, mixing with potassium phosphate and release agent to form organic release agent, weighing raw materials, adding microbial flora and organic release agent to reactor, mixing, reacting at 25 degrees C for 30 minutes, adding fertilizer and pesticide, mixing, and filling in bottles.
NOVELTY - Liquid fertilizer is prepared using 1-2 wt.% microbial flora, 20-40 wt.% fertilizer, 0.5-1.5 wt.% plant growth regulator, 0.8-1.2 wt.% pesticide, 1-2 wt.% release agent and remainder water.    USE - The liquid fertilizer is useful for tea plantation (claimed).    ADVANTAGE - The liquid fertilizer is convenient to store and transport.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the liquid fertilizer, which involves (a) mixing above-mentioned raw materials and stirring uniformly to obtain product; and/or (b) mixing above-mentioned raw materials except release agent in a mixer to obtain mixture and adding release agent to the mixture and stirring uniformly to obtain product.
(CN203639158-U)   NOVELTY - This utility new type is a different level N2O of system, comprise containing impurity and N2O m/s air, a compressor of compression pneuma flow, removing cooling drying device of wet steam or water, removing heavy impurity, moisture or water and organic matter of adsorption device, storage from the adsorption device flow of pneuma buffering tank, buffering tank from the air flow at least part of liquid to gas and liquid mixture of liquefied device, the gas exhaust axis mixture absorbing device and the liquid mixture is sent to device of a distillation device, distilling the liquid mixture removing light impurity and organic matter, the N2O and vapour of non-condensable gas of the gas compressor and produce purification liquid exhaust axis N2O of distillation device, and used for storage and a purification liquid N2O of tank, and optionally of the air removing heavy impurity of wet polyester pneuma absorbing device, wherein the distillation device comprises at least one a flash tank, at least one with return-flow of a distillation column or the combination of wet polyester pneuma absorption device comprises alkali scrubbing device, acid scrubbing device, water polyester pneuma. or the combination.
NOVELTY - Hyperbranched macromolecular guanidine salt antibacterial agent (A), are new, where (I) comprises amide or ester hyper branched intermediate compounds (III) and macromolecular guanidine salts, which comprises macromolecular single guanidine salt and macromolecular biguanide salt.    USE - (A) are useful in health care, food processing, household chemicals, daily life, agriculture, aquatic product and animal husbandry (claimed).    ADVANTAGE - (A): have long-term antibacterial agent effect and stability; can easily soluble in water; have wide temperature and pH value range (claimed); and have simple preparation, no side effects, non-corrosive, and no environmental pollution.    DETAILED DESCRIPTION - Hyperbranched macromolecular guanidine salt antibacterial agent (A) of formulae (I) and (II) are new, where (I) comprises amide or ester hyperbranched intermediate compounds of formula (III) and macromolecular guanidine salts, which comprises macromolecular single guanidine salt and macromolecular biguanide salt.    X = N or O;    L1 = 2-12C methylene or oxymethylene;    A1 = (III); and    n = 2-12.    An INDEPENDENT CLAIM is also included for preparation of (A).
NOVELTY - A mixed disinfectant comprises 20-35 wt.% hydrogen peroxide, 3-9 wt.% peracetic acid, 5-12 wt.% acetic acid, 0.1-2 wt.% sulfuric acid, 0.05-2 wt.% stabilizer, 0.05-2 wt. surfactant and balance water.    USE - Mixed disinfectant used for killing bacteria, fungi, yeasts, spores and other microorganisms.    ADVANTAGE - The disinfectant has good stability, fast acting, nontoxic and environment-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for    (1) application of mixed disinfectant comprising mixing with water at 1:10-1:1000 volume dilution ratio, carrying out immersion sterilization, spraying, and disinfecting; and    (2) preparation of mixed disinfectant comprising mixing hydrogen peroxide, peracetic acid, acetic acid and sulfuric acid, stirring, adding remaining raw materials, stirring for 12-36 hours, and filtering into 0.2 mm aperture filter membrane.
NOVELTY - Composite micro-ecological preparation comprises Bacillus subtilis, Saccharomyces cerevisiae, and Lactobacillus in a pts. wt. of 1:1:1, where the B.subtilis has viable count of 1x 1010 colony-forming unit (cfu)/g, the S.cerevisiae has viable count of 1x 1010 cfu/g, and the Lactobacillus has viable count of 1x 1010 cfu/g.    USE - The composite micro-ecological preparation is useful for preparing livestock feed, and useful as manure (all claimed).    ADVANTAGE - The composite micro-ecological preparation reduces nitrogen pollution conservation and phosphorus content, and improves decomposition of nitrogen and phosphorus.
NOVELTY - Medicinal composition comprises dasatinib, 3-15 wt.% hydrophilic gel material and auxiliary material, where the hydrophilic gel material is chosen from hydroxypropyl methylcellulose, methylcellulose, carbopol and alginate.    USE - As medicinal composition.    ADVANTAGE - The medicinal composition improves microenvironment, has improved stability and controlled dissolution rate, and is prepared by simple, inexpensive and pollution-free process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited medicinal composition, which involves weighing the raw materials, sieving the raw materials using 60 mesh nylon sieve, sieving the other materials using 40 mesh sieve, uniformly mixing the materials, subjecting to dry granulation or wet granulation, and directly tableting the granules.
NOVELTY - A polyimide having structure of formulae (I) and (II) is new.    USE - New polyimide is used as gas separation membrane material for separation of gas such as oxygen/nitrogen, carbon dioxide/methane and nitrogen/hydrogen in air during gas purification process (all claimed).    ADVANTAGE - The gas separation membrane containing polyimide has high gas-permeability and selectivity.    DETAILED DESCRIPTION - A polyimide having structure of formulae (I) and (II) is new.    R2=DAF structure of formula (III);    m/(m+n)=0-1;    m,n=0-400;and    m+n=100-800.    An INDEPENDENT CLAIM is included for preparation of polyimide.
NOVELTY - A refined neomycin post cast carbon device comprises turn salt shaker (1) with stirring rod (2) connected to motor (3) in which turn salt shaker is connected to lower pass tube (4), cast carbon outlet (5), and hopper (12) connected to top end of pipeline (6).    USE - Refined neomycin post cast carbon device (claimed).    ADVANTAGE - Device is convenient, improves health of workers, reduces risks, and improves production efficiency. Safe handling and emission of activated carbon dust is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of refined neomycin post cast carbon device.    Turn salt shaker (1)    Stirring rod (2)    Motor (3)    Lower pass tube (4)    Cast carbon outlet (5)    Pipeline (6)    Hopper (12)
NOVELTY - A dewatering sludge settling conditioning agent contains flocculant-producing bacteria e.g. strains C3 and A9 and filamentous bacteria E1 and E10 sewage-pollutant-degrading bacteria e.g. strains S10, S16, B6, B20, and 8 strains in which conditioning agent is prepared by mixing any 2 species of bacteria, inoculating in culture medium, and placing in air bath oscillator to 28 degrees C at 160 rpm for 48 hours.    USE - A dewatering sludge settling conditioning agent for wastewater treatment.    ADVANTAGE - Sludge treatment cost is reduced, sludge settling dehydration property is improved, and process is non-toxic and environment-friendly.
NOVELTY - Sewage sludge treatment method involves adding flocculant to waste so as to avoid formation of floating sludge, which then settles down at bottom during the sludge treatment method. The flocculated sludge is then passed through a frame filter machine to obtain dehydrated sludge cake. The dehydrated sludge cake is then fermented under anaerobic condition to methane gas. The generated methane gas is collected and then utilized in a combustion reaction.    USE - Sewage sludge treatment method.
NOVELTY - Fermentation system comprises septic tank (1) and sewage collecting pipeline (2), where septic tank is set with a pig manure storehouse (3). The pig manure storehouse is connected with a wall body (5) and a marsh gas tank (7). The fermenting tank is divided with partition wall (8) and set with a feeding platform (6) and an excrement opening (9). The marsh gas tank is connected with a pipeline (10).    USE - Fermentation system used for treating pig manure.    ADVANTAGE - The fermentation system enhances the efficiency of organic fertilizer in an eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermentation system.    Septic tank (1)    Sewage collecting pipeline (2)    Pig manure storehouse (3)    Wall body (5)    Feeding platform (6)    Marsh gas tank (7)    Partition wall (8)    Excrement opening (9)    Pipeline (10)
NOVELTY - A low nitrous oxide discharge combustion device comprises chamber (1), hopper (2), piston (3), rotary drying furnace (4), and spiral feeder (5). The combustion device further comprises chiller, fan, pyrolysis gas pipeline, first flue gas circulation tube, second flue gas circulation tube, circulation tube, dense-phase area, dilute phase area, fluidized bed boiler, sludge feeding port, sludge drying pyrolysis gas nozzle, cyclone separator, super-heater, reheater, coal saver, air pre-heater, dust catcher, draft fan, and tail flue.    USE - Low nitrous oxide discharge combustion device used for burning sludge (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the process combustion device comprising feeding sludge into rotary drying furnace, circulating hot flue gas at 600 degrees C, drying sludge, dehydrating, and carrying out partial pyrolysis; drying into coal particles having fuel property; introducing produced pyrolysis gas to pipeline, cooling, injecting into boiler furnace, and carrying out pyrolysis; introducing flue gas for drying sludge in second tube, discharging, and suppressing nitrous oxide generation; heating flue gas; introducing to drying oven; and repeating process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of low nitrous oxide discharge combustion device.    Chamber (1)    Hopper (2)    Piston (3)    Rotary drying furnace (4)    Spiral feeder (5)
NOVELTY - Production of fertilizer from human waste comprises extracting methane from septic tank using extraction machine, pumping out solid and liquid manure as raw slurry, filtering slurry using filter device to remove debris and obtain preliminary manure slurry, mixing preliminary manure slurry with clay powder and fine sand, blending by stirring to obtain manure semi-slag, extracting methane using gas-water separation device, drying combustion gas, heating to evaporate combustion gas, obtaining dry manure residue, evaporating gas and returning residue into septic tank.    USE - Method for producing fertilizer from human waste (claimed).    ADVANTAGE - The method saves resources and reduces pollution. It has good economic and social benefits.
NOVELTY - Preparation of Rhodotorula glutinis biofertilizer comprises carrying out solid-liquid separation of fermented red yeast strain, drying solid bacteria sludge at 40-80 degrees C, and crushing.    USE - Method for preparing Rhodotorula glutinis biofertilizer (claimed) used for cultivating soybean or kidney bean.    ADVANTAGE - The method is simple. The biofertilizer reduces dosage of chemical fertilizer and environment pollution.
NOVELTY - Manufacture of seaweed biological fertilizer comprises selecting cracking kettle algae slag and algae bacteria strain to prepare functional bacteria strain and fermenting functional bacteria strain liquid until culture liquid is 108-1010 cfu/ml; fermenting cracking kettle algae slag and cultured functional bacteria strain to obtain fermentation product; and filtering, granulating, drying, cooling, sieving, and packing.    USE - Method for manufacturing seaweed biological fertilizer (claimed).    ADVANTAGE - The fertilizer meets biological organic fertilizer national standard NY/884-2012 of organic matter content, moisture content, pH value, and ascarid eggs and fecal coliform death rate, has less investment, low energy consumption, and fast effect, and reduces pollution.
NOVELTY - Preparation of earthworm organic liquid fertilizer comprises pulping living earthworm using electric stirrer to obtain earthworm slurry; adding effective microorganism (EM) bacteria and fermenting; filtering and separating solid slag and earthworm liquid, where solid slag is solid earthworm fertilizer; mixing earthworm liquid with yellow humic acid, amino acid, sugar, fermenting base, urea, and bran material, stirring, and fermenting; and filtering.    USE - Method for preparing earthworm organic liquid fertilizer (claimed).    ADVANTAGE - The fertilizer improves soil retain ability of nutrient and water, reduces dosage of fertilizer, avoids nutrient loss, improves fertilizer use efficiency, and improves yield and quality of plant.
NOVELTY - Preparation of high-concentration fertilizer comprises neutralizing slurry with diluted phosphoric acid through concentrating system to obtain concentrated ammonium phosphate slurry, feeding into granulator, mixing with concentrated sulfuric acid and exhaust gas washing liquid, and adding ammonia gas to carry out secondary neutralization to obtain 18-20% moisture-containing monoammonium phosphate, diammonium phosphate and ammonium sulfate mixed slurry; and feeding into nozzle spray, spraying into bed of granulating machine to carry out granulation, drying, cooling, and sieving.    USE - Method for preparation of high-concentration fertilizer (claimed).    ADVANTAGE - The method is energy saving, can effectively improve the material properties of fertilizer, and has low incidence of side effects and low cost.    DETAILED DESCRIPTION - Preparation of high-concentration fertilizer comprises neutralizing slurry with 20-22 wt.% diluted phosphoric acid through concentrating system to obtain concentrated ammonium phosphate slurry, feeding into granulator, mixing with concentrated sulfuric acid and exhaust gas washing liquid, adding ammonia gas to carry out secondary neutralization to obtain 18-20% moisture-containing monoammonium phosphate, diammonium phosphate and ammonium sulfate mixed slurry, and recovering exhaust gas washing liquid and diluted phosphoric acid; and feeding mixed slurry into nozzle spray, spraying into bed of granulating machine to carry out granulation, drying, cooling, and sieving.
NOVELTY - Biological organic liquid fertilizer comprises 500-2000 pts. wt. vitamin C production liquid waste, 5-20 pts. wt. trace elements, 10-100 pts. wt. starch, and 5-15 pts. wt. bio-fungus liquid.    USE - Biological organic liquid fertilizer.    ADVANTAGE - The fertilizer has a shelf life of 3-5 years, is stable, efficient and environment-friendly, reduces cost and dosage by 5-10 times, and does not cause soil pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic liquid fertilizer comprising mixing 1000 pts. wt. vitamin C production liquid waste and 12 pts. wt. trace elements solution, stirring; pasteurizing at 80-90 degrees C, adding 50 pts. wt. starch, mixing; cooling to 25-35 degrees C, adding 6 pts. wt. bio-fungus liquid, stirring; fermenting for 3-8 days, and packing.
NOVELTY - A soilless organic composite matrix comprises 55-65 wt.% rice straw, 25-35 wt.% cow manure, 5-10 wt.% rice husks, 2-3 wt.% urea, 1.5-2.0 wt.% rice straw decomposition agent, 15 wt.% peat, 1-3 wt.% fertilizer, 0.015-0.006 wt.% seedling strengthening agent, and 0.002 wt.% root promoter agent.    USE - Soilless organic composite matrix used for rice seedlings (claimed).    ADVANTAGE - The method is low-cost and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of soilless organic composite matrix comprising cutting rice straw into 0.2-2 m long, drying cow manure, crushing into powder, mixing, adding rice husks, mixing, adding urea and rice straw decomposition agent, mixing, adjusting moisture content to 65%, stacking, covering with sacks or thin film insulator, fermenting at greater than or equal to 60 for 7-10 days, turning once, naturally drying, crushing to particle size of 1-4 mm, adding peat, urea, fertilizer, seedling strengthening agent and root promoter agent, mixing, and spraying 1.84 g/mL concentrated sulfuric acid to adjust pH.
NOVELTY - A biological organic fertilizer is prepared by mixing biogas residue and leavening agents, controlling moisture content and carbon-to-nitrogen ratio, inoculating composite microbial agent into fermentation feedstock mixture, piling, ventilating, fermenting, adjusting pH value, turning, composting, adding urea, diammonium phosphate and potassium chloride, mixing, adding azotobacter, mycorrhizal fungi, silicate bacteria, photosynthetic bacteria, acetic acid bacteria, bifidobacteria and yeast, and mixing.    USE - Method for preparing biological organic fertilizer (claimed).    ADVANTAGE - The method has short fermentation time.    DETAILED DESCRIPTION - A biological organic fertilizer is prepared by mixing biogas residue and leavening agents at mass ratio of 3-5:1, controlling moisture content to 50-60% and carbon-to-nitrogen ratio to 25-40, inoculating composite microbial agent into fermentation feedstock mixture, piling at height of 0.8-1.5 m, ventilating at wind speed of 8-15 L/minute, fermenting at 50-60 degrees C for 8 days, adjusting pH value to 5.5-7.5, turning once every 2-3 days, composting for 15-20 days to obtain organic fertilizer, adding urea, diammonium phosphate and potassium chloride, mixing, adding azotobacter, mycorrhizal fungi, silicate bacteria, photosynthetic bacteria, acetic acid bacteria, bifidobacteria and yeast, and mixing.
NOVELTY - A soilless plant cultivation substrate is prepared by mixing agricultural and forestry wastes, water, 3-6 kg fermentation catalyst, 9-30 kg fermentation microbial agent, and 1-2.5 mL vinegar and/or wood vinegar, and fermenting.    USE - Method for preparing soilless plant cultivation substrate (claimed).    ADVANTAGE - The substrate is stable.
NOVELTY - A glycosyl-modified polyphenol compound (I) or (II), is new.    USE - The glycosyl-modified polyphenol compound is useful for preparing medicament for providing antioxidant (claimed) and anti-apoptotic effect.    ADVANTAGE - The water-soluble glycosyl-modified polyphenol compound has high removing rate of free radical and apoptotic function, and is prepared without using catalyst by simple and environmentally-friendly process.    DETAILED DESCRIPTION - A glycosyl-modified polyphenol compound of formula (I) or (II), is new.    X=-H or -OH;    Y'=group chosen from group of formulae (i)-(vii);and    Z=-OH, -OMe, -OEt, -F, -Cl, -Me -Et or -NHCOMe.    An INDEPENDENT CLAIM is included for preparation of glycosyl-modified polyphenol compound.
NOVELTY - Preparation of allylamine involves reacting olefin and amine derivative in molar ratio of 1:0.2-1:2 in organic solvent, phosphine ligand, palladium salt and metal catalyst at 25-140 degrees C for 2-60 hours, distilling-off solvent, and performing column chromatography separation to obtain allylamine, or reacting olefin, aldehyde and amine in molar ratio of 1:0.75:0.5-1:3:2 in organic solvent and metal palladium salt and phosphine ligand catalyst system at 25-140 degrees C for 2-60 hours, distilling-off solvent and performing column chromatography separation to obtain allylamine.    USE - Preparation of allylamine e.g. cinnarizine, naftifine and terbinafine.    ADVANTAGE - The allylamine is economically and efficiently prepared by simple and environmentally-friendly method under mild reaction condition with high yield.
NOVELTY - A urea is produced by conveying coke furnace coal into gas cabinet, pressurizing into desulfurization section, primary desulfurizing, compressing into dry desulfurization section, secondary desulfurizing, entering into oxygen enriched conversion device to obtain gas A, conveying converter gas into gas cabinet, purifying, separating carbon monoxide, adding gas A, converting, adding zinc oxide, decarburizing, methanating, and purifying.    USE - Method for producing urea (claimed).    ADVANTAGE - The method has low operation cost, saves energy, and reduces energy consumption and environment pollution.
NOVELTY - A vildagliptin intermediate (2S)-N-chloroacetyl-2-cyano-pyrrolidine is prepared by suspending L-proline in solvent, adding acid binding agent and acetyl chloride, reacting under oil bath, cooling, adding ethyl acetate, separating, washing, drying, concentrating to obtain intermediate I, suspending in solvent, adding condensing agent, reacting, stirring, adding ammonia solution, stirring, filtering, drying to obtain intermediate II, suspending in solvent, adding dehydrating agent, stirring, adding saturated sodium carbonate solution, adjusting pH, extracting, and drying organic phase.    USE - Method for preparing vildagliptin intermediate (2S)-N-chloroacetyl-2-cyano-pyrrolidine (claimed).    ADVANTAGE - The method has mild reaction condition, environment-friendly, low-cost and suitable for large scale industrial production.    DETAILED DESCRIPTION - A vildagliptin intermediate (2S)-N-chloroacetyl-2-cyano-pyrrolidine is prepared by suspending L-proline in solvent, adding acid binding agent, slowly adding acetyl chloride at low room temperature, reacting under oil bath at 0-150 degrees C for 1-72 hours, cooling, adding ethyl acetate, separating organic phase, washing with saturated brine, drying with anhydrous sodium sulfate, concentrating to obtain intermediate I, suspending intermediate I in solvent, dropwise adding condensing agent, reacting at 30-50 degrees C, stirring for 0.5-2 hours, adding ammonia solution, stirring for 4-6 hours, filtering, drying with ethyl acetate to obtain intermediate II, suspending intermediate II in solvent under ice bath, adding dehydrating agent, stirring for 2-5 hours, adding saturated sodium carbonate solution, adjusting pH to 9-10, extracting with dichloromethane, and drying organic phase with anhydrous sodium sulfate.
NOVELTY - Substrate material fructose or fructosyl biomass is added to an open kettle containing catalyst, heated in presence of ionic liquid and dehydrated to obtain hydroxymethylfuran. The resultant reaction mixture is added to mixed solvent of water and a hydrogenation catalyst, mixed, added to a sealed reaction vessel filled with hydrogen, and heated at 250 degrees C or less to obtain 2,5-bis(hydroxymethyl)tetrahydrofuran or 2,5-bis(hydroxymethyl)furan.    USE - Preparation of furan diol (claimed).    ADVANTAGE - The method efficiently and economically provides high yield of furan diol by simple method.
NOVELTY - Preparation of olanzapine crystal comprises reacting thiophene derivative (II) with solvent and N-methylpiperazine and heating at greater than or equal to 111 degrees C.    USE - Method for preparing olanzapine crystal (claimed).    ADVANTAGE - The method is economical and environment-friendly and has high yield. The product has high purity.    DETAILED DESCRIPTION - Preparation of olanzapine crystal comprises reacting thiophene derivative of formula (II) with solvent and N-methylpiperazine and heating at greater than or equal to 111 degrees C.
NOVELTY - A diosgenin is extracted without waste discharge by screening yellow ginger, washing, and crushing; fermenting at 43-48 degrees C for 35.5-36.5 hours, adding sulfuric acid, hydrolyzing for 40-50 minutes, filtering, adjusting pH value to 6-7 using 5% potassium hydroxide solution, and drying; adding 120# gasoline, performing Soxhlet extraction for 4-6 hours, crystallizing, membrane filtering, and drying; and producing steam, mixing sulfuric acid hydrolysis liquid, potassium hydroxide cleaning liquid and saponin gasification ash, and preparing agricultural potassium sulfate compound fertilizer.    USE - Method for extracting diosgenin without waste discharge for preparing potassium sulfate compound fertilizer (claimed).    ADVANTAGE - The method reduces contaminants, reduces pollutant sources, and recycles resources.    DETAILED DESCRIPTION - A diosgenin is extracted without waste discharge by:    (A) screening yellow ginger, washing with water, returning muddy water to paddy field, and recycling supernatant for cleaning;    (B) crushing, introducing steam, and fermenting at 43-48 degrees C for 35.5-36.5 hours;    (C) adding 4.5 wt.% sulfuric acid, introducing steam to pressure of 1.95-2.05 atm, and hydrolyzing for 40-50 minutes;    (D) filtering using plate-and-frame filter press, conveying liquid to potassium sulfate compound fertilizer production, adjusting pH value to 6-7 using 5% potassium hydroxide solution, and drying;    (E) adding 120    (F) gasoline, performing Soxhlet extraction for 4-6 hours, crystallizing, membrane filtering, and drying; and    (G) conveying into gasification furnace, producing steam, mixing sulfuric acid hydrolysis liquid, potassium hydroxide cleaning liquid and saponin gasification ash, and preparing agricultural potassium sulfate compound fertilizer.
NOVELTY - Usage of lees is performed by drying lees, crushing to obtain lees powder, mixing lees powder:catalyst with weight ratio of 20-35:1, performing pyrolysis at 450-530 degrees C for 90-150 minutes under anaerobic conditions to obtain steam cracker and pyrolysis residue, and condensing steam cracker to obtain liquid substance and uncondensed gas in which liquid substance is bio-oil, uncondensed gas is pyrolysis gas, active component of catalyst is nickel, additive of catalyst is cobalt, molybdenum, and/or tungsten, and carrier is gamma -aluminum oxide and mesoporous molecular sieve MCM-41.    USE - Usage of lees (claimed).    ADVANTAGE - Usage process is simple and environment-friendly.    DETAILED DESCRIPTION - Usage of lees is performed by drying lees, crushing to obtain lees powder, mixing lees powder:catalyst with weight ratio of 20-35:1, performing pyrolysis at 450-530 degrees C for 90-150 minutes under anaerobic conditions to obtain steam cracker and pyrolysis residue, condensing steam cracker to obtain liquid substance and uncondensed gas in which liquid substance is bio-oil, uncondensed gas is pyrolysis gas, active component of catalyst is nickel, additive of catalyst is cobalt, molybdenum, and/or tungsten, and carrier is gamma -aluminum oxide and mesoporous molecular sieve MCM-41, and adding bio-oil and dehydrating agent and dehydrating to obtain biofuel or adding bio-oil and solvent and extracting to obtain chemical raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram of pyrolysis of lees. (Drawing includes non-English language text).
NOVELTY - A Bacillus T-5 strain (CCTCC No. M2013588) capable of degrading triethylamine is new.    USE - New Bacillus T-5 strain useful for degrading triethylamine, particularly degrading triethylamine in industrial wastewater chosen from biopharmaceutical wastewater and pesticide wastewater, and bioaugmentation treatment of industrial wastewater containing triethylamine (all claimed).    ADVANTAGE - The Bacillus T-5 strain has 100% triethylamine removal rate and 30-40% chemical oxygen demand (COD) removal rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) use of the strain for degrading triethylamine in industrial wastewater; and    (2) use of the strain for bioaugmentation treatment of industrial wastewater containing triethylamine.
NOVELTY - Aerobic denitrification bacteria which is Pseudomonas sp. strain A00019 with preservation number CGMCC No. 8804 is new.    USE - Aerobic denitrification bacteria which is Pseudomonas sp. strain A00019 with preservation number CGMCC No. 8804 for sewage biological denitrification (claimed).    ADVANTAGE - Aerobic denitrification bacteria has good ammoniacal nitrogen, total nitrogen, and chemical oxygen demand (COD) removing effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage biological denitrification which involves using plug-flow activated sludge reactor or sequencing batch reactor (SBR).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of phylogenetic tree of strain A00019 based on 16S rRNA gene sequence.
NOVELTY - Quinclorac-degrading bacterial strain MC-06, preferably Escherichia coli (CGMCC NO: 8487), is new.    USE - The bacterial strain MC-06 is useful in agent for degrading quinclorac in polluted water and soil (all claimed).    ADVANTAGE - The strain has good colonization ability, does not produce secondary pollution, and causes no negative effects in ecological environment.
NOVELTY - A fiber-based carrier immobilized laccase comprises fibers as carrier, active molecules distributed in the surface of fibers, a coated fibers, mesoporous silicon oxide layer of active molecules, and laccase embedded in mesoporous silicon oxide of silicon oxide layer. The mesoporous silicon oxide layer is formed by depositing organosilane molecules having catalytic activity on surface of fiber.    USE - Fiber-based carrier immobilized laccase is used for food, textile, paper and pulp and sewage treatment applications (all claimed).    ADVANTAGE - The fiber-based carrier immobilized laccase has excellent immobilization efficiency, enzyme activity, reusability and operability, and is manufactured with high recovery rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of immobilized laccase.
NOVELTY - Processing of wood cellulose involves removing the sand and big granule from rough lignocelluloses. Ash is removed from wood cellulose. Wood cellulose raw material is preprocessed. The pre-processed wood cellulose is enzyme hydrolyzed, and then saccharification and fermentation is performed.    USE - Method for processing wood cellulose (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preprocessing wood cellulose, which comprises helical stirring kettle reactor, where ribbon type preprocessing reactor is equipped with a stirring device machinery, machinery stirring device comprises stirring paddle, screw paddle and a bottom scraping blade and spiral ribbon blade is fixed on stirring shaft, where stirring shaft comprises frame body and bottom scraping blade fixed on stirring shaft.
NOVELTY - Preparing biodiesel, involves extracting oil remains containing microorganisms and cytolytic enzymes, (b) mixing water with the obtained product, adding magnesium sulfate, ferric chloride and sodium dihydrogen phosphate with the obtained mixture, and sterilizing to obtain heterotrophic microbial fermentation medium, (c) inoculating oil producing heterotrophic microorganisms in heterotrophic microbial fermentation medium, fermenting at 30-40 degrees C for 48-120 hours, and enzymolyzing the obtained product.    USE - The method is useful for preparing biodiesel (claimed).    ADVANTAGE - The method is cost-effective, and environmentally-friendly.    DETAILED DESCRIPTION - Method for preparing biodiesel, involves (a) extracting oil remains containing microorganisms and cytolytic enzymes in a weight ratio of 10-100:1, magnetically stirring the obtained extract in reactor at 30-50 degrees C, and pH of 5-7, and 50-300 revolutions per minute, for 3 hours, and reacting at 105 degrees C for 10-30 minutes, (b) mixing water with the obtained product in a mass ratio of 5-3:1, adding 25-100 mg/l magnesium sulfate, 5-50 mg/l ferric chloride and 0-75 mg/l sodium dihydrogen phosphate with the obtained mixture, and sterilizing at 115-121 degrees C for 15-30 minutes to obtain heterotrophic microbial fermentation medium, (c) inoculating oil producing heterotrophic microorganisms in heterotrophic microbial fermentation medium, fermenting at 30-40 degrees C (first stage pH of 5-6, second stage pH of 6-7, and third stage pH of 7-8, and aeration of 0.1-1 vvm) for 48-120 hours, and enzymolyzing the obtained product.
NOVELTY - Processing lignocellulose involves removing dust and sand from lignocellulose, and then cleaned product is ground in a pulping machine for reducing particle size of lignocellulose. The obtained product is mixed with water, where solid content is 5-30%, and then obtained mixture is processed for enzyme hydrolysis and fermentation process to obtain product.    USE - Method for processing lignocellulose (claimed).    ADVANTAGE - The method enables to process lignocellulose in simple, cost-effective and eco-friendly manner.
NOVELTY - Method for preprocessing lignocellulose involves mixing carboxyl-functionalized ionic liquid, solvent, lignocellulose biomass raw material in reactor, heat-stirring for 10-48 hours, performing solid-liquid separation, washing with water, drying, removing solvent, adding water to lignin-rich sample, separating, drying, distilling water, mixing lignin-rich sample and distilled water, adding cellulase, xylanase, adjusting pH to 4-5.5 using sulfuric acid, performing enzymolysis process at 35-55 degrees C using enzymolysis liquid, and carrying out solid-liquid separation.    USE - Method for preprocessing lignocellulose (claimed).    ADVANTAGE - The method enables efficient and economical preprocessing of lignocellulose, by simple method.    DETAILED DESCRIPTION - Method for preprocessing lignocellulose involves mixing carboxyl-functionalized ionic liquid, solvent, lignocellulose biomass raw material in reactor, heat-stirring for 10-48 hours, performing solid-liquid separation, collecting the solid sample, washing solid sample with water, drying at 80-200 degrees C, removing liquid phase of solvent, adding water to the lignin-rich sample, separating, drying, distilling water, mixing lignin-rich sample and distilled water, adding cellulase, 0.01-0.1 g/g xylanase, adjusting pH to 4-5.5 using sulfuric acid, performing enzymolysis process at 35-55 degrees C using enzymolysis liquid, and carrying out solid-liquid separation. The mass ratio of carboxyl-functionalized ionic liquid and solvent is 1:20-4:1. The mass ratio of lignocellulose biomass raw material with ionic liquid is 1:20-1:2. The enzymolysis liquid contains glucose as main component. The solid residue is lignin.
NOVELTY - One using a high temperature water vapour gasifying biomass preparing hydrogen of device, belonging to the biomass gasification technology field. It is high temperature gasification reactor, multi-fluid heat exchanger H2 separator device, a fuel gas burner, burner and so on. Gasification need of high temperature water vapour from the pure O2 and H2 of combustion, the reactor heating jacket in the gas combustion maintaining temperature of inner reactor. Temperature of hydrogen-oxygen burner spraying of high temperature water vapour is higher than 1600 degrees C, temperature of high temperature gasification reactor in is 1300 to 1500 degrees C. Exhaust gas and waste heat of synthesis pneuma through multi-fluid heat exchanger for heating H2 and O2, a separator device through the gasified synthesis pneuma separation is H2 and gas two part. The gasification device comprises a hydrogen producing rate is high, not need catalyste, directly a pure H2 and so on.
NOVELTY - This utility new type microbial treatment waste water manufacture combustible device, include waste water treatment device, heating device, marsh gas device and a marsh gas collecting device, the waste water treatment device set with a stirrer, a water inlet of the biogas production device is set with a filter screen, the marsh gas collecting device is installed on the biogas production device upper part, connecting tube of soft air inside the marsh gas collecting device of. This utility new type processing waste water by microorganism for producing combustible of principle of valid collected biogas generated through the device.
NOVELTY - This utility new type new type sewage processing production energy system device, comprise water tank, reaction tank, the vent tube and dryer, of water groove through a connecting pipeline of said reaction tank, the reaction tank is set with a feeding port, the dryer through a vent tube of said connecting of reaction tank, the vent tube in one section is ventilate in the dryer of of is one microorganism-bound a raw fuel of a new device.
NOVELTY - This utility new type provide one collected in a liquid nitrogen, struvite crystallization reaction device of phosphorus, include mix reaction area, a precipitation zone, a buffer zone, struvite crystal sludge area, settling and separating area, an overflow gathering, mix reaction area set with water inlet, NaOH solution is added, MgCl2 liquid adding opening and a stirrer, crystallizing zone is distributed with bird excrement stone crystal collecting network, struvite crystal collecting network fixed on the inner cylinder and the outer cylinder, the bottom end to prevent struvite sludge with water flow entering into separating area, struvite sludge area is cone-shaped, is located at the bottom of device, and set with a mud and a struvite sludge permeating liquid external interface of high concentration struvite; depositing and separating area located on the inner cylinder and the outer cylinder, wherein the inner cylinder and the outer cylinder through fixing frame fixing the overflow gathering groove of lower end with a drain pipe. This utility new type struvite crystallization reaction device valid solves the problem that the existing technology in concentrated biogas liquid phosphorus, the removal rate of ammonia nitrogen and low defect of nitrogen phosphorus element and recovery rate.
NOVELTY - This utility new type relates to one a livestock and poultry corpse treatment and biological deodorization of fermentation device, comprise host, control unit, at least one cutting unit, adding water unit, heating unit, a drainage unit, an air unit and one exhaust and deodorization unit, each unit receives control of control unit and action to finish cutting, stir and drying step and so on. This utility new type of beneficial effects as follows: cutting, stir fermentation and odour discharging and so on are a step in the inner containing space of main machine, and by a unit intelligent control, realize the intelligent integrated control, top cover of the host is angular, produce in the production process of water in steam condensed water dropping groove rear forming water would drop along the inclined surface slide to two side of inner the top cover set with valid ensures the drying degree of product.
NOVELTY - This utility new type claims a self-discharging one cylindrical aerobic compost reactor, compost comprise cylinder, further comprise horizontal rotate device and vertical to rotating device, of a horizontal rotate device comprise a bracket, a first motor, a driving gear and one end driven gear, a first bracket of a through one of the rotating shaft and is set with an opening of the compost cylinder one end rotate connect, the electric machine and the driving gear are set with the upper of said first bracket and electrical machine of the electrical machine shaft is connected with a driving gear of connecting, a circumferential direction with the driving gear correspond to the fertilizer barrel of a set with the said of meshed with the driving gear of the driven gear, the vertical to rotating device comprise second bracket and steering wheel. This utility new type a the chamber of compost material inner turn stack, the material does not need to take out the compost chamber, there is no heat loss, no smell, and the material mix uniform, turning effect is obvious.
NOVELTY - This utility new type claims a one time a cultivation sewage and solid waste of type compost system, used for cultivation waste treatment field, include composting workshop, several of the composting groove is set in the composting workshop and the cultivation sewage is led to inner of sewage tube inner each compost groove, groove bottom of the composting groove are set with port through the stack of wall between fertilizer vehicle set with exhaust tube of the waste pneuma. The same processing cultivation sewage and solid waste of type compost system time in working, the cultivation sewage and solid waste to compost is inner groove, match stack port of bottom fertilizer groove groove, at the same time, a combining process for the, at the same time, the produce of waste pneuma through exhaust tube, this utility new type variable single of sewage treatment is cultivation waste all resource utilization, a cultivation sewage zero discharge, structure is simple, the floor space is small, a greatly reduce the cultivation sewage treatment pressure.
NOVELTY - This utility new type relates to one a waste treatment system, in particular to a one cultivation waste and crop straw earthworm reactor the treatment device, belonging to the processing technology field of rural waste, include comprise in turn. of fermentation bucket, earthworm cultivation tank and fertilizer hopper, a fermenting bucket inner set with a stir paddle, upper part of the fermenting bucket is also set with a air blower, the fermentation bucket of the bottom set with an opening, the opening is located at the feeding port of earthworm cultivation tank, the bottom of said earthworm cultivation box set with a synchronous wheel by drive of track, a synchronous wheel by the top of electric machine drive, earthworm cultivation box is equipped with a water tube and warm lamp. This utility new type a valid the cultivation waste and crop straw through biodegradation and conversion of earthworm into a directly use of organic agricultural fertilizer, and the automatic degree high, it is convenient to use and suitable for popularization and use in countryside.
NOVELTY - This utility new type relates to a one special compound fertilizer for flue-cured tobacco preparation device, include mix tank, a sprayer main body, a nozzle, a fermentation tower, mix tank one side set with sprayer main body, main body upper end set with nozzle, lower mix tank end connecting fermenting tower. The device increase the working efficiency and use life and reduce the manufacturing cost.
NOVELTY - This utility new type claims a one natural gas produced in a production from dimethyl oxalate blocked pipeline of device, comprise dimethyl oxalate conveying pump, a vaporizer, a pre-heater, a hydrogenation reactor, a cooler and gas-liquid separator, oxalate conveying pump at the inlet of methanol groove is connected with the pipeline of one, the dimethyl oxalate conveying pump through pipeline and carburetor connecting, the carburetor through pipeline with the pre-connecting, the pre-heater through pipeline with the hydrogenation reactor connecting, hydrogenation reactor through pipeline connecting with the cooler, the cooler through pipeline with the gas-liquid separator connecting the inlet pipeline of dimethyl oxalate conveying pump is further set with a storage tank is connected with the pipeline of a, using this utility new type of technology scheme to avoid frequent dismantling device, which ensures a continuity.
NOVELTY - This utility new type claims a one a mobile agricultural and forestry waste material, include used for loading of material and is set on the furnace body of the combustion chamber under a furnace body, a combustion room is set on the trolley move up, said upper furnace body is equipped with the material inlet and outlet, a material inlet and outlet is set with a furnace door, a combustion room is provided with a at least one a fuel inlet. The utility model is new in type, a carbonization furnace is pushed to the agriculture and forestry waste accumulation, a mobile local carbonization processing, there is no need to the material to the processing point, so it greatly reduces the transportation cost, time-saving and labor-saving, carbonizing efficiency high.
NOVELTY - This new type utility claims one a biomass gasification furnace, comprising a furnace body, a furnace body of in inner lower part set with grate, a furnace grate of the furnace body is divided into a lower two part a, the upper part of the reaction room, the lower part inner collecting room pneuma and biomass raw material is reaction room, a pneuma collecting room lower end is hopper, further comprising air outlet tube, a gas outlet tube of collecting pneuma end collecting pneuma room top and gas collecting end downwards through the grate, the air outlet end of said air outlet tube of the furnace body upper end wall and end b passes through the furnace body upper end side wall. This utility new type one a biomass gasification furnace with a mounting and convenient of use.
NOVELTY - Biomass gasification furnace, comprise with insulating layer of furnace shell, the upper part of furnace shell is set with a feeding port and is equipped with water sealing cover, set with bin inner the furnace shell, a port connected with the feeding port of the connected storage bin, the lower part of the inner side in turn set with tapered stop storage area and gasification area, a gasification area include pneuma of one cylinder, forming air into the gasification chamber is set between the cylinder and the storage hopper, air inlet cavity through the outer side of the furnace shell is connected with the periphery of the upper part of the gasification barrel is arranged with air inlet hole, a gas discharging hole periphery are arranged on the lower part of the gasification barrel, set with support grate pneuma one side set with leading to the furnace shell at the bottom of the gasification cylinder of ignition door, a gas cover, shell and gas storage hopper lower part outer side cover form the fuel gas chamber, upper part side surface of shell set with fuel gas outlet, gas outlet pipeline and extends to the outer side of furnace shell, at the same time, in turn connecting combustion pneuma treatment device and the fan of the air inlet. Structure is simple, the manufacturing cost is low, the gas of a good quality, high.
NOVELTY - This utility new type claims a one biomass gasification furnace cloth device, comprising a charging barrel, rotate sleeve, fixing pole, a lifting rod and a pull rope, a feeding cylinder is installed on the fixed port a biomass gasification furnace, a feeding cylinder by the upper and lower straight cylinder, feeding cylinder of straight lower end set with outer side rotate sleeve, a rotate sleeve upper end edge set with rotate table-board, said rotate table set with a rotate mechanism, a fixing pole upper end through hinge set with the end surface rotate lower table-board, a fixed lower pole end through hinge set with the hopper upper end, a pull rope set a lifting rod a lifting ring set with the feeding cylinder and the straight coaxial of feeding cylinder, a pulling rope upper end through end lower torsion-proof device and the lifting rod connecting the pull rope lower end with the lower end connecting distributing, rotate lower sleeve port centre set with pull rope set ring, a pull rope passes through the middle straight and rotate sleeve of feeding cylinder of inner.
NOVELTY - A biomass gas oxygen removing one complete device, wherein it comprise: the biomass pneuma to supercharging pressure of compressor 1-10 (1), a heater (2), the heater (2) for the compressor (1) for biomass pneuma of heating to 150-400 degrees C, the heater (2) of the air inlet of the air outlet connected with the compressor, by regenerator (301), adsorbent bed (302) and catalyst bed (303) is composed of catalyzing and deoxidizing device (3), a heat regenerator (301), a catalyst bed (303) exit heat for heat from the heater for entering into the biomass of a further pneuma of heating, to a catalytic bed of self-balance operation, heat exchanger (4), used for the heat exchanger for catalytic deoxidizing device (3) of biomass pneuma process cooling, at the same time, a heat, and the rear heat exchange of biomass pneuma is sent to subsequent purification device in. This utility new type has simple structure, purification efficiency is good, the installation is convenient.
NOVELTY - This utility new type provide a one garbage landfill marsh pneuma purification of a device, referring to environment protection and a renewable sources utilization field, concretely, it is one device for include a large industry, municipal domestic garbage generated biogas purification pneuma, prepare clean vehicle fuel resource utilization of, include the marsh gas collecting pipe, a desulfurizing tank, a drying tube, a dust remover, a marsh gas compressor, first pressure swing adsorption tank, the second adsorption tank, normal pressure CO2/CH4 film separating module, a gathering pneuma buffering tank, a gas filling interface, component and device through pipeline in turn in series. The device marsh gas purification rate high, a valid removal of carbon dioxide in marsh gas, marsh gas concentration of rear purification a is more than 99.6%, and it has good economic benefit and social benefit of and environmental benefit.
NOVELTY - This utility new type claims a intestinal one marsh gas generator a crushing feeding device, marsh gas generating a category feeding device field, comprise a feeding cavity, a crushing beater, niff pipe, the feeding cavity is following, the inside one crushing beater, a crushing beating machine through several support pole fixed on the upper inner wall of the feeding cavity, a crushing beater of the hopper and the feeding cavity cover seal connecting, the crushing machine is provided with a discharging port, a funnel-shaped lower part is a feeding cavity, a discharging port of the feeding cavity and the niff bent pipe. This utility new type is capable of large volume or the rear group of organic garbage crushing to process fast sealing process to prevent stacking the produce odour and growth to prevent the blockage, and the fermentation more complete.
NOVELTY - This new type utility claims laboratory with device for preparing hydrogen, include reaction room, an air storage tank and hydrogen, wherein said reaction room neck part set with a water inlet and an air outlet, the bottom of said reaction room set with a box body, a reaction room of one side set with electrode mounting base, said upper electrode mounting base set with electrode, electrode is set on said reaction room, a box body connecting said electrode, said air outlet connecting tank, a storage tank connect oxygen absorbing device, absorbing device connecting said drying device, a drying device connecting the outlet hydrogen, said hydrogen inlet and the drying device set with a valve, a control valve and the drying device set with hydrogen purity test table. This utility new type has the advantages of: safety coeffcient high, preparation technology is simple, high purity, low energy consumption, the air flow quantity is large, the whole structure is simple and practical range is wide.
NOVELTY - The system has a gas sample pool (10) connected with two air inlet ends (1, 2). An air outlet of the gas sample pool is connected with a suction pump (12) that is connected with a FTIR spectrum instrument (11). An inner part of the gas sample pool is provided with a seal box (9) and a gas quality flow control meter (8). A nitrogen blowing pump (13) is arranged in the seal box. A three-dimensional ultrasonic anemoscope (15) is connected with two air inlet ends. A drying tube (7) is connected with the gas quality flow control meter. A computer (14) determines surface air discharge flux.    USE - Greenhouse gas discharge flux infrared spectrum measuring system.    ADVANTAGE - The system can measure vicinity height and process near stratum wind field information by the FTIR spectrum instrument so as to determine discharge flux range of measured gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a greenhouse gas discharge flux infrared spectrum measuring method.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of a greenhouse gas discharge flux infrared spectrum measuring system.'(Drawing includes non-English language text)'    Air inlet ends (1, 2)    Drying tube (7)    Gas quality flow control meter (8)    Seal box (9)    Gas sample pool (10)    FTIR spectrum instrument (11)    Suction pump (12)    Nitrogen blowing pump (13)    Computer (14)    Three-dimensional ultrasonic anemoscope (15)
NOVELTY - A diclofenac substance detecting method involves selecting a product with diclofenac substance, and mixing product with extracting solvent. The mixture is shaken with ultrasonic assisted dissolution to obtain mixed test solution. Diclofenac anti-inflammatory substance in the test solution is measured by specific electrochemical detector parameters to confirm whether substance is used illegally.    USE - Method for detecting diclofenac substance in anti-inflammatory drugs, health products and food additives.    ADVANTAGE - The method enables detecting biguanide substances with high sensitivity and in quick, simple, safe and eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for detecting diclofenac substance using a detecting device, which involves extracting solvent in the solvent bottle, mixing solvent with product with diclofenac substances, measuring diclofenac substance in selected product using electrochemistry theory and interpreting the result in instruction data.
NOVELTY - Bamboo is heat-processed using normal-pressure superheated steam, and water vapor containing bamboo vinegar component is cooled and condensed, to obtain bamboo vinegar liquid.    USE - Manufacture of bamboo vinegar liquid (claimed).    ADVANTAGE - The method provides bamboo vinegar liquid, by a safe and simple process using a simple processing apparatus. The processed bamboo residue produced during the manufacture of bamboo vinegar liquid is efficiently utilized as a biomass composite raw material.
NOVELTY - Organic waste materials (115) are screened to produce unders and overs. The overs having moisture content of 50-65% are hydrothermally treated to produce a partially hydrolyzed biomass. The unders from the waste material and the partially hydrolyzed biomass are anaerobically digested. Thus, organic waste material treatment process is carried out.    USE - Method for treating organic waste material e.g. municipal solid waste (claimed).    ADVANTAGE - The method enables treatment of organic waste material by environmentally-friendly process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of organic waste treatment system.    Hydrolysis vessel (110)    Organic waste material (115)    Holding tank (130)    Digester (140)    Electrical generator (150)
NOVELTY - Pellets from biomass material are produced by providing biomass having 0-60 wt.% moisture into a reactor, injecting steam at greater than or equal to 300 degrees F into the reactor containing the biomass material, maintaining a pressure for 1-30 minutes, and forming the treated biomass material into pellets.    USE - Production of pellets from biomass material for fuel pellets.    ADVANTAGE - Pellets have reduced contents of hemicellulose, chlorine, sulfur and alkali and alkaline earth metals.
NOVELTY - Producing hydrogen gas comprises: (a) delivering a primary liquid delivery medium (LDM) comprising a liquid fuel reactant to contact a solid fuel mixture in a reaction zone under conditions sufficient to cause a reaction between the liquid fuel reactant and the solid fuel mixture, where the reaction zone comprises a reaction product path that is disposed to remove reaction products from the reaction zone during the course of the reaction; and (b) optionally independently contacting the reaction products with a second LDM outside of the reaction zone.    USE - The method is useful for producing hydrogen gas (claimed).    ADVANTAGE - The method is capable of: providing the hydrogen gas, where the reactant product is propagated away from the reaction zone according to forces provided by the produced hydrogen gas; and operating without orientation-dependent consumption.    DETAILED DESCRIPTION - Producing hydrogen gas comprises: (a) delivering a primary liquid delivery medium (LDM) comprising a liquid fuel reactant to contact a solid fuel mixture in a reaction zone under conditions sufficient to cause a reaction between the liquid fuel reactant and the solid fuel mixture, where the reaction zone comprises a reaction product path that is disposed to remove reaction products from the reaction zone during the course of the reaction; and (b) optionally independently contacting the reaction products with a second LDM outside of the reaction zone. The delivery of the primary liquid delivery medium is controlled by a movable boundary interface (MBI) that biases the primary LDM against the solid fuel mixture.
NOVELTY - Enzymatic composition comprises a EGVI polypeptide having at least 90% sequence identity to the amino acid sequence of SEQ ID NO: 2 (comprising a fully defined 818 amino acids as given in the specification), a beta -glucosidase (BG), and a cellobiohydrolase (CBH), where the EGVI polypeptide is from a different species than the BG and/or the CBH.    USE - The enzymatic composition is useful for producing ethanol (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for producing ethanol comprising either: contacting a biomass composition with the enzymatic composition to yield a sugar solution, adding to the sugar solution a fermentative microorganism, and culturing the fermentative microorganism under conditions sufficient to produce ethanol; or contacting a biomass composition with the enzymatic composition and a fermentative microorganism, and culturing the fermentative microorganism under conditions sufficient to produce ethanol.
NOVELTY - Continuous source of biofuel that is formed from at least one colonizing entity, at least one cellulosic material and at least one carbohydrate conversion source, is claimed.    USE - Continuous source of biofuel, preferably ethanol.    ADVANTAGE - The continuous source of biofuel is prepared in a more efficient and less expensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the continuous source of biofuel, comprising: providing the colonizing entity, the cellulosic material and the carbohydrate conversion source, and then combining to form a biofuel-precursor and incubating the biofuel-precursor at a sufficient temperature and for a time period in order to produce the biofuel.
NOVELTY - The device has a media container (1) made of a plastic material, particularly polyamide, for receiving the medium, where a valve connection element (2) is connected to the media container. A valve element (3) is connected to the valve connection element. The media container has a collar (4) which is molded on in one piece and protrudes from the media container. A restoring element (11,11a) is arranged such that the collar and the restoring element are jointly pressed between a partial region (9a) of a wall (9) and a pressing portion (10) during the fitting of the valve element.    USE - Device for use in a fuel-energy conversion device of a motor vehicle for the storage and delivery of liquid or gaseous media under pressure.    ADVANTAGE - The device has a media container made of a plastic material, particularly polyamide, for receiving the medium, where a valve connection element is connected to the media container, and thus ensures simple and efficient storage and delivery of the liquid or gaseous media under pressure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel-energy conversion device with a fuel cell unit; and    (2) a method for fitting a device for the storage and delivery of liquid and/or gaseous media under pressure.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal sectional view of a device.    Media container (1)    Valve connection element (2)    Valve element (3)    Collar (4)    Wall (9)    Partial region (9a)    Pressing portion (10)    Restoring element (11,11a)
NOVELTY - Conversion of a feedstock containing at least one triglyceride of fatty acid to a mixture containing at least one alkyl ester of fatty acid and tert-alkyl glycerols, comprises the reaction of the feedstock with substituted ether compounds (I). The reaction is carried out in the presence of an acid transesterification catalyst by irradiation with microwaves and/or ultrasound and/or radio waves.    USE - The process is useful for converting a feedstock containing at least one triglyceride of fatty acid to a mixture containing at least one alkyl ester of fatty acid and tert-alkyl glycerols (claimed) which is useful for producing biodiesel and glycerol ether mixtures useful as biofuels.    ADVANTAGE - The process: provides total conversion of feedstock to fatty acid methyl esters and tert-butyl glycerols without glycerin formation and in less time; eliminates the final stage of glycerin separation, and has low energy consumption than the known processes; and allows the use of inedible and waste vegetable oils containing amounts of free fatty acids, such as exhausted frying oils from the catering industry.    DETAILED DESCRIPTION - Conversion of a feedstock containing at least one triglyceride of fatty acids to a mixture containing at least one alkyl ester of fatty acids and tert-alkyl glycerols, comprises the reaction of the feedstock with substituted ether compounds formula (I). The reaction is carried out in the presence of an acid transesterification catalyst by irradiation with microwaves and/or ultrasound and/or radio waves.    R1 = 1-18C alkyl, 1-18C alkenyl or 1-18C alkynyl; R2 = H or tertiary alkyl group of formula (II); and    R3, R4, R5 = optionally branched 1-6C alkyl, 1-6C alkenyl or 1-6C alkynyl.    Provided that when R2 is H, an alcohol of formula R2-OH is added, in an equimolar amount to R1-OH.
NOVELTY - Producing a solvent (preferably butanol, acetone or ethanol) or butyric acid or its derivative, comprises: (i) culturing a solventogenic Clostridium sp. in a culture medium in a culture vessel in the presence of a polysaccharide, where the Clostridium sp. is Clostridium saccharoperbutylacetonicum N1-4(HMT) or N1-504, and the polysaccharide is a starch-based substrate; and (ii) harvesting butanol from the culture medium.    USE - The process is useful for producing a solvent, such as butanol (preferred), acetone and ethanol, or butyric acid or its derivative (all claimed).    ADVANTAGE - The process provides a solvent, preferably butanol using solventogenic fermentations, thus reducing cost of the process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) culturing a micro-organism, comprising (a) culturing a Clostridium sp. in a culture medium in a culture vessel in the presence of a polysaccharide, where the Clostridium sp. is one which produces a cyclodextrin glucanotransferase (CGTase), and the polysaccharide is one which is a substrate for the CGTase; (2) a hydrolysate or digestion product of the polysacchande obtained by the process as above per se; and (3) the solvent, or butyric acid or its derivative obtained by the process as above per se.
NOVELTY - Flame-retardant styrene resin particles comprises styrene resin, and phenoxy phosphazene compound as flame retardant. The phenoxy phosphazene compound is a compound in which phenoxy group is bonded with substitutable bonding portion of phosphorus atom. The content of phenoxy phosphazene compound is 0.3-40 %mass with respect to flame-retardant styrene resin particles. The relative value of extinction quotient (D1180/D1070) of center portion of styrene resin particles is 1, and the extinction quotient (D1180/D1070) of surface of particles is 1.1-7.    USE - Flame-retardant styrene resin particles are used for foamable particles for foaming particles for foam-molding (all claimed). Uses include but are not limited to building material, shock absorbing material, food container, domestic electrical appliances, and heat insulating material.    ADVANTAGE - The foaming particles containing the flame-retardant styrene resin particles have excellent flame retardant characteristics, high internal fusibility, and high dimension compatibility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of flame-retardant styrene resin particles, which involves preparing styrene resin particles by subjecting a monomer containing styrene-based monomer to suspension-polymerization in aqueous medium, and contacting styrene resin particles containing 85 %mass or more of monomer to phenoxy phosphazene compound;    (2) foamable particles, which consists of flame-retardant styrene resin particles and foaming agent;    (3) foaming particles, which are obtained by foaming foamable particles; and    (4) foam-molding process.
NOVELTY - Flame-retardant styrene resin particles comprise styrene resin, and phenoxy phosphazene compound as flame retardant. The phenoxy phosphazene compound is a compound in which phenoxy group is bonded with substitutable bonding portion of phosphorus atom. The content of phenoxy phosphazene compound is 0.3-40 %mass with respect to flame-retardant styrene resin particles. The content of phenoxy phosphazene compound in a surface layer is more than the total content of phenoxy phosphazene compound.    USE - Flame-retardant styrene resin particles are used for foamable particles for foaming particles for forming foam-molded product (all claimed) for building material.    ADVANTAGE - The foaming particles containing the flame-retardant styrene resin particles have excellent flame retardant characteristics, high internal fusibility, and high dimension compatibility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of flame-retardant styrene resin particles, which involves preparing styrene resin particles by subjecting a monomer containing styrene-based monomer to suspension-polymerization in aqueous medium, and contacting styrene resin particles containing 85 %mass or more of monomer to phenoxy phosphazene compound;    (2) foamable particles, which comprise flame-retardant styrene resin particles and foaming agent;    (3) foaming particles, which are obtained by foaming foamable particles; and    (4) foam-molded product, which involves foam molding the foaming particles.
NOVELTY - Device for producing biomass composition, comprises a device for introducing a biological starting material which is difficult to digest, an activator for decomposing the starting material, which is activatable at a temperature greater than 55 degrees C, and a device for thermal activation of a combination of the starting material and the activator.    USE - The device is useful for producing biomass composition (claimed).    ADVANTAGE - The device produces the biomass composition having very high lignin content, and ensures complete conversion of organic carbon present in the starting material into energy-rich hydrocarbons.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the device for producing biomass composition (Drawing includes non-English language text).    Final disposal container (1)    Separator (2)    Recuperator heat exchanger (21)    Circulation valve in preheating circuit (41)    Separator material solid digestate (51)
NOVELTY - Adsorbent comprises an open-pore carrier material having a specific surface on which at least one compound comprising dithionic acid or its salt or polythionic acid or its salt is applied.    USE - The adsorbent is useful for purifying gas, preferably flue gas, natural gas, or biogas, or for purifying exhaust air from disposal of fluorescent lamps; and for depositing mercury (all claimed).    ADVANTAGE - The adsorbent is easy- and safe to handle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the adsorbent, comprising (i) providing the open-pore carrier material, (ii) providing a solution which comprises a solvent in which the compound is dissolved, (iii) applying the solution on the surface, and (iv) optionally removing the solvent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart for a waste incineration plant with a flue gas purification system (10).    Flue gas purification system (10)    Waste bunker (11)    Rotary kiln (12)    Auxiliary combustion chamber (13)    Spray dryer (14)
NOVELTY - Pretreatment of horse manure for subsequent fermentation, comprises: (a) bringing the horse manure with an aqueous medium; (b) circulating a mixture of horse manure and aqueous medium for the separation of horse manure and a litter; (c) introducing a gaseous medium in the mixture of horse manure and aqueous medium, so that the litter flaots; (d) skimming the flaoting litter using a skimming device; and (e) homogenizing the horse manure in the aqueous medium.    USE - The method is useful for the pretreatment of horse manure including urine and litter for subsequent fermentation using a device such as fermentation plant (all claimed), where the horse manure is useful for energy production by fermentation process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) fermentating the horse manure, comprising pretreating the horse manure with the pretreatment method, and fermenting the pretreated horse manure; and    (2) an apparatus for carrying out the method, comprising a container (1) having a bottom side groove (2), a litter-skimming device (3) and at least one gassing device (4, 5) for introducing a gaseous medium.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a device for the pretreatment of horse manure.    Container (1)    Bottom side groove (2)    Litter-skimming device (3)    Gassing device (4, 5)    Gas bubbles. (10)
NOVELTY - Invention relates to production of construction materials as well as to recycling industrial, medical and household wastes, which can be used to produce construction materials and solid fuel (eco-charcoal) The highly filled composite material, which contains thermoplastic polymer wastes, spent mineral oil and bitumen, additionally contains organic filler, e.g. hydrocarbon sorbents such as peat, algae, bark, as well as amber jewellery processing wastes - amber dust, with the following ratio of components, wt %: bitumen 1.0-60, spent mineral oil 5.0-25, thermoplastic polymer wastes 1.0-8.5, organic filler 25.0-70.    USE - Chemistry.    ADVANTAGE - Wider field of use.4 ex
NOVELTY - The invention relates to a method for introducing sludge from a waste water purification plant into the primary flow sheet of integrated iron and steel works, the sludge being used as both auxiliary fuel and starting material. According to the invention, the method consists in converting the sludge into powder through thermal and mechanical processing, introducing the powder into the sintering process together with the coke powder in the batcher bunker (1), mixing it along with the other components of the agglomerate charge within the homogenizing apparatus (2), transferring the charge to the agglomeration belt (4) where, by heat application and mineral content, it takes part in the sintering process, is embedded into the agglomerate reaching further the bunker scaffold (6) and then the blast furnace (7).
NOVELTY - Method of microbiological treatment of bird droppings comprises laying bird droppings and application of bioadditives in liquid form, biological heating and anaerobic fermentation of the mixture, and the bioadditive is used as effluent in an amount of 3-8% by total weight of bird droppings, which is composed of mineral fertilisers - N:P:K in an amount 0.1:0.16:0.18%, respectively, and the indigenous microflora with a density on microorganisms of 260 x 108 CFU/ml, and biogas produced during the decomposition of bird droppings is collected and removed.    USE - Agriculture.    ADVANTAGE - Invention enables to improve efficiency and speed of treatment of bird droppings, to increase the activity of methanogenic consortium contained in the effluent in the absence of the cost of cultivation of microorganism strains.1 dwg
NOVELTY - The breath analyzer has a chemical sensor (22) which is sensitive to the concentration of component in sample of exhaled breath. A compensator (24) compensates effect of variations in amount of exhaled breath between user and location with chemical sensor integrated into portable electronic device. The compensator corrects signal representative of concentration of component selected from ethanol, acetone, hydrogen, methane, nitric oxide, carbon monoxide, isoprene, or ammonia. A humidity sensor (23) determines the carbon dioxide or oxygen concentration in the sample.    USE - Breath analyzer integrated to portable electronic device such as mobile phone, handheld computer, electronic reader, tablet computer, game controller, pointing device, photo or video camera, digital music player, wrist watch, key fob, head set, and computer peripheral (all claimed), used for analyzing blood alcohol concentration (BAC) of person for operating vehicle e.g. car.    ADVANTAGE - The accuracy of the measurement of alcohol concentration or other components in the sample of exhaled breath using the multipurpose portable electronic device is improved. The opening is protected by the grill or the membrane so as to prevent the bigger particles or unwanted components of the air from entering or blocking the duct provided in the breath analyzer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the duct with the chemical sensor.    Duct (21)    Chemical sensor (22)    Humidity sensor (23)    Compensator (24)    Opening (206)
NOVELTY - The system enables higher level initial seeding or inoculation of bioreactor bloom space. The blooming as result of starting higher on upward-bending nonlinear algal growth curve is accelerated. A normally inaccessible upper section of nonlinear algal growth curve is conventionally in-accessed to optical opacity of concentrated algal suspensions. The normally inaccessible upper section of curve is rendered by optical thinning effect to enable light penetration into optically thinned suspensions of concentrated algae. The bioreactor is supplied with carbon dioxide.    USE - System for production of algae for supplying silage, animal feed, feed supplement, fertilizer, bio-fuel, food for fish e.g. predator fish and for mollusk.    ADVANTAGE - The ocean revitalization in terms of ideal pH restoration and recovery of decimated marine populations are enabled. The high capacity algal production is enabled effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for production of algae.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for imparting negative carbon footprint to transportation.    Lye film (129)    Standpipe (134)    Salt water (136)    Gas-liquid separator (139)    Local pickup vessel (151)
NOVELTY - Safening phytotoxic effect of difenoconazole comprises applying to a plant or propagation material cloquintocet-mexyl and the difenoconazole.    USE - Method for safening phytotoxic effect of difenoconazole (claimed).    ADVANTAGE - The method can protect plants from phytopathogenic organisms, and limits the impact on the environment.
NOVELTY - The method involves reducing a carbon dioxide-portion in lean gas and/or exchanging gas portions in the lean gas against oxygen in a membrane separation unit (1). A retentate is subsequently utilized in an utilization unit, which is provided downstream to the membrane separation unit on a retentate side. A permeate of the membrane separation unit is mixed to hot exhaust gas of the utilization unit, and reoxidized. A partial pressure difference between the permeate and the retentate in the membrane separation unit is increased by pressurization of feed gas.    USE - Method for utilization of lean gas such as marsh gas e.g. manure gas, fermentation gas and landfill gas, formed during bio-enzymatic, anaerobic decomposition of organic material and landfill, in a utilization unit such as a gas engine and a burner e.g. special burner and EFLOX-burner. Can also be used for utilization of blast furnace gases formed in a coal and steel industry, product gas formed during wood gasification, and gas formed in mining and closed mines.    ADVANTAGE - The method allows freeing of the lean gas from methane such that the lean gas reaches into atmosphere as the exhaust gas corresponding to legal specifications. The method enables the obtained gas mixture to be directly, inexpensively and stably used for operating the utilization units in a wide range, and avoids problems of disposal of the permeate. The method allows discharging of a combined effluent stream into atmosphere in problem-free manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for performing a method for utilization of lean gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of a device for performing a method for utilization of lean gas.'(Drawing includes non-English language text)'    Membrane separation unit (1)    Compressor (4)    Gas input line (8)    Retentate output line (9)    Permeate output line (10)    Control valve (15)
NOVELTY - A stream of 1-20% free fatty acid-containing oil is purified by steam distillation at high temperature and low pressure to strip free fatty acids, and free fatty acids are recovered by condensation. The recovered fatty acids are reacted with glycerin at high temperature and low pressure, and removed from glycerin-esterified oil to obtain oil having 1% or less free fatty acids.    USE - Production of oil used as bio-diesel feedstock and used as emulsifier for foods, cosmetics, and pharmaceutical products.    ADVANTAGE - The method provides oil containing 1% free fatty acids without using catalyst and with reduced consumption of energy.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic flow diagram of the glycerin esterification and free fatty acid stripping process.
NOVELTY - The electrode (10) has a positive electrode (11) that is a cylindrical conductor and whose side portion is provided with several openings (11H). An insulator is provided in the outer peripheral portion of the positive electrode, and contacted with the positive electrode. A negative electrode (12) is cylindrical conductor which is provided in the outer peripheral portion of insulator, and contacted with the insulator. The side portion of negative electrode is provided with several openings (12H).    USE - Electrode for generating hydrogen-containing water from natural water such as tap water.    ADVANTAGE - The efficiency of dissolving hydrogen in natural water when generating hydrogen-containing water is improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen-containing water generation apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view showing the electrode for generating hydrogen-containing water.    Electrode for generating hydrogen-containing water (10)    Positive electrode (11)    Opening of positive electrode (11H)    Negative electrode (12)    Opening of negative electrode (12H)
NOVELTY - The apparatus (100) has a first support portion (101) whose first installation unit (101C) is attached to side of first edge of positive and negative electrodes (11,12). A second installation unit (102C) of second support portion (102) is attached to side of a second edge of positive and negative electrodes. The distance from side portion of positive electrode to second installation unit is larger than the distance from side portion of positive electrode to first installation unit in the direction orthogonal to the side portion of the positive electrode.    USE - Apparatus for generating hydrogen-containing water in raw water stored in drinking water tank, bathtub, and flush tank.    ADVANTAGE - The oxygen generated on the positive electrode side is discharged rapidly to the exterior when generating the hydrogen-containing water. The structure of the hydrogen-containing water generation apparatus is simplified in compact form. Hence, the manufacturing cost of the hydrogen-containing water generation apparatus is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the hydrogen-containing water generation apparatus.    Positive electrode (11)    Negative electrode (12)    Hydrogen-containing water generation apparatus (100)    First support portion (101)    First installation unit (101C)    Second support portion (102)    Second installation unit (102C)
NOVELTY - The apparatus (100) has insulator that is provided in the outer peripheral unit of the positive electrode (11). A cylindrical conductor is provided in the outer peripheral unit of insulator and is provided with an opening in a side unit of cylindrical conductor. The support elements (101,102) are is attached to the edge sides (11T1,12T1,11T2,12T2) of the positive electrode and negative electrode (12). An opening unit (102H) is connected with the space enclosed by the side unit of the positive electrode.    USE - Apparatus for producing hydrogen-containing water from natural water such as tap water.    ADVANTAGE - The oxygen produced in the positive electrode side to the exterior is rapidly discharged. The safety of the user is improved by controlling the output of the electric power of the power supply, when the connector is extracted out from the power supply. The reduction of the power consumption of the power supply is achieved effectively. The bubble of oxygen in the positive electrode is efficiently discharged outside from the opening unit.    DESCRIPTION OF DRAWING(S) - The drawing shows the explanatory view of the apparatus for producing hydrogen-containing water.    Positive electrode (11)    Edge sides of positive electrode and negative electrode (11T1,12T1,11T2,12T2)    Negative electrode (12)    Apparatus for producing hydrogen-containing water (100)    Support elements (101,102)    Opening unit (102H)
NOVELTY - A primary electrode layer having a dense structure is formed (S210) using an oxide. An electrolyte layer is formed (S220) on the primary electrode layer. The primary electrode layer is reduced (S230), to obtain pores. A secondary electrode layer is formed (S240) on the electrolyte layer. Thus, manufacture of fuel cell is enabled.    USE - Manufacture of fuel cell e.g. solid oxide fuel cell.    ADVANTAGE - The method enables manufacture of fuel cell having reduced short-circuit and leakage of electrolyte, with reduced formation of pinholes in the electrolyte layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram explaining manufacture of fuel cell. (Drawing includes non-English language text)    Preparation of electrode material (S200)    Formation of electrode layers (S210,S240)    Formation of electrolyte layer (S220)    Reduction of electrode layer (S230)
NOVELTY - A porous primary electrode layer is formed (S200). A primary electrolyte layer (S210) is formed on primary electrode layer. A surface obtained by removing upper end of primary electrolyte layer is planarized (S220). A filler layer is formed (S230) on planarized surface to fill pin holes existing in primary electrolyte layer. The filler layer is removed (S240). A secondary electrolyte layer is formed (S250) on primary electrolyte layer. A secondary electrode layer (S260) is formed on secondary electrolyte layer. Thus, manufacture of fuel cell is enabled.    USE - Manufacture of fuel cell e.g. solid oxide fuel cell.    ADVANTAGE - The method enables manufacture of fuel cell having reduced short-circuit and leakage of electrolyte, with reduced formation of pinholes in the electrolyte layer.    DETAILED DESCRIPTION - A porous primary electrode layer is formed (S200). A primary electrolyte layer is formed on the primary electrode layer. A surface obtained by removing upper end of primary electrolyte layer is planarized. A filler layer is formed on the planarized surface of the primary electrolyte layer to fill pin holes existing in the primary electrolyte layer. The filler layer is removed. A secondary electrolyte layer is formed on the primary electrolyte layer from which the filler layer is removed. A secondary electrode layer is formed on the secondary electrolyte layer. Thus, manufacture of fuel cell is enabled.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram explaining manufacture of fuel cell. (Drawing includes non-English language text)    Formation of electrode layers (S200,S260)    Formation of electrolyte layers (S210,S250)    Planarization of surface of electrolyte layer (S220)    Formation of filler layer (S230)    Removal of filler layer (S240)
NOVELTY - A system for generating fuel stocks in a fabricated biocolumn comprising zones, fabricated by assembling modules of biocolumn, inputting a nutrient, a renewable energy source, photon energy and a carbon source into the zones and outputting fuel stock and by products from zones; where zones are interconnected so that byproducts from each zone can be recycled as input or transformed into product.    USE - The system is useful for generating fuel stocks in a fabricated biocolumn comprising zones (claimed).    ADVANTAGE - The system is cost efficient and can maximize the use of photosynthesis to release carbon from carbon dioxide by helping the growth of microorganism colonies that produce biogases, bioliquids and biosolids. It also uses carbon dioxide emissions directly, or those already in the atmosphere, as a feedstock input to produce biogases, bioliquids and biosolids.
NOVELTY - The generator (10) has a watertight and airtight unit (12) which comprises a gas collector (14) with a gas outlet (24) on a top surface. A metal plate (16) of several metal plates is located on sides of gas collector, and is provided with holes in upper and lower regions respectively. Two end plates (18) are located at opposite ends of the unit (12), and non-conductive spacers (20) are located such that each metal plate is provided with spacer on each side.    USE - Gas generator of fuel system, used for generating gas such as hydrogen and oxygen for combustion system.    ADVANTAGE - The gas collector and the arrangement of metal plates on either side of the gas collector ensures that there is an unrestricted flow of liquid in the unit and that the gas produced via the electrolysis is able to easily escape through the central gas collector, so that the gas collector does not suffer from the inhibition of fluid flow within the gas generator. Thus the efficiency of producing gas from electrolyte and capturing the produced gas using central gas collector is improved effectively. The gas collector, the metal plates and the end plates are all rectangular and are all arranged in parallel vertical planes. Thus complexity of the unit of the gas generator is significantly reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for generating a gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the gas generator.    Gas generator (10)    Watertight and airtight unit (12)    Gas collector (14)    Metal plate (16)    End plates (18)    Non-conductive spacers (20)    Gas outlet (24)
NOVELTY - The fuel system (100) has a gas generator (10), a fluid reservoir (32), a power regulator, and a system control device (104). The fluid reservoir is connected to the gas generator and arranged to supply electrolytes (38). The gas generator generates hydrogen and oxygen gas (40) using electrolysis of the electrolytes. The power regulator is connected to a power supply, and regulates the received power from the power supply. The system control device is connected to the power regulator and the gas generator for controlling the power supplied to the gas generator from the power regulator.    USE - Fuel system used in e.g., combustion system and heating system.    ADVANTAGE - System control device prevents undesirable loading of the external power source which result in too much power drawn that leaves insufficient power available for the primary purpose of the external power source. Polarity of power supplied to the gas generator is reversed at prescribed time to reverse the flow of gas within the gas generator which changes the particulate build-up on the cathode plates and maintains good levels of gas production. Anti flash back arrestors are provided which prevents liquid escaping from the fluid reservoir to the hydrocarbon combustion chamber, and prevents any flash or spark traveling back from the hydrocarbon combustion chamber to the fluid reservoir.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an operating method of a fuel system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic front view of a fuel system.    Gas generator (10)    Fluid reservoir (32)    Electrolytes (38)    Oxygen gas (40)    Fuel system (100)    System control device (104)
NOVELTY - Method for composting spent mushroom compost, involves composting the spent mushroom compost under conditions for providing composted spent mushroom compost with dry matter content of 45-90%, preferably 55-75%.    USE - The method is useful for composting spent mushroom compost (claimed), which is used as fertilizer.    ADVANTAGE - The method decreases weight and transport cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composted spent mushroom compost.
NOVELTY - Method for purifying waste glycerol involves collecting waste glycerol which is byproduct of biodiesel production process, providing the waste glycerol in a reactor, heating to 70-80 degrees C by activating, neutralizing by adding alkali, adding emulsifier, mixing, separating glycerol and fattey acids contained in the waste glycerol based on specific gravity values, placing in an atmosphere of room temperature for 24 hours, and recovering glycerol. The emulsifier is hydrochloric acid with concentration of 5-34%. The weight ratio of waste glycerol and emulsifier is 1:0.05-0.15.    USE - Method for purifying waste glycerol (claimed).    ADVANTAGE - The method enables effective purification of waste glycerol with high capacity by a simple process in a short period of time.
NOVELTY - An integral metal composite catalyst contains perovskite-surface coated porous matrix.    USE - An integral metal composite catalyst used for catalytic combustion of methane.    ADVANTAGE - Composite catalyst has high methane catalytic efficiency and improved binding strength between metal elements and porous matrix.    DETAILED DESCRIPTION - An integral metal composite catalyst contains perovskite (ADO3)-surface coated porous matrix.    A=Group II A series and/or lanthanide metal element; and    D=transition metal element.    An INDEPENDENT CLAIM is included for preparation of integral metal composite catalyst which involves preprocessing porous matrix (1), preparing pseudo-boehmite aqueous solution and perovskite soluble salt solution, mixing 2 solutions to obtain precursor aqueous solution (2), adding organic complexing agent, stirring, dripping nitric acid to obtain aluminum sol (3), and impregnating preprocessed porous matrix in aluminum sol (4).    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow chart of preparing integral metal composite catalyst. (Drawing includes non-English language text).    Preprocessing of porous matrix (1)    Preparation of precursor aqueous solution (2)    Preparation of aluminum sol (3)    Impregnation of preprocessed porous matrix in aluminum sol (4)
NOVELTY - This utility new type claims a one pig cultivation is the three-dimensional cultivation of aquatic with the sewage treatment device, include three-dimensional piggery and aquiculture pond, a three-dimensional piggery high of the aquiculture pond water and/or according to the aquiculture pond, a solid of produce of pigsty excrement directly sink to aquiculture pond. This utility new type through directly single layer or multi layer pigsty, discharging device above the aquiculture pond use the pig manure is directly discharged to the inner a pond ecological cultivation, valid adjust cultivation proportion, of symbiotic complementary between the fish and swine, makes full use of resource, circulation waste, but also reduces the enterprise sewage treatment process, but also reduces the soil of building cover, house and rigid of pig manure pollution discharge, wherein a multi-nutrition a fish for absorption, and it does not need special feeding of fermenting tank, a waste processing cost is reduced, the utilization rate is high. This utility new type structure is simple, the cost is low, a the ecological cultivation.
NOVELTY - The device has a six-way switching valve whose two ends are connected with a sampling part that is connected with a quantitative ring. A hydrogen flame detector is fixed with the six-way switching valve. A conversion furnace is connected with the sampling part. First and second chromatographic columns are fixed with the six-way switching valve that is connected with a carrier pneuma exit part. A quantitative ring is connected with the six-way switching valve. A quantitative ring exit part is fixed with the first chromatographic column.    USE - Chromatography analysis based carbon monoxide, methane and carbon dioxide detection device.    ADVANTAGE - The device avoids trace detection problems and longer limitation effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a chromatography analysis based carbon monoxide, methane and carbon dioxide detection method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a chromatography analysis based carbon monoxide, methane and carbon dioxide detection device.
NOVELTY - This utility new type claims a one low temperature fluid cold energy utilization system, relating to liquid oxygen, liquid nitrogen and cold energy of liquefied natural gas for power generation, freezing, refrigerator and refrigerating air conditioner field. The system comprise low temperature, temperature refrigerant in a closed circulation and low temperature fluid cold energy releasing process. Low temperature circulation include first to third heat exchanger, second liquid pressurizing pump and expansion generator, in temperature circulation include second, third heat exchanger and third liquid booster pump, a low temperature fluid cold flow comprise a first liquid pressure pump, first to third heat exchanger. Of low temperature fluid cold final a, refrigerating medium is refrigerating medium and expansion of generator in third heat exchanger of cold for a freezing refrigerator and air conditioner refrigeration, expansion generated energy of generator and satisfy system requirement itself is also a large surplus, the low temperature cold energy of a fluid; This utility new type can make full use of cold energy of low temperature fluid, obviously increase energy conversion efficiency, reduces pollutant discharge, improve the property of system.
NOVELTY - The fuel cell system comprises a fuel cell stack (100), which is mounted in the vessel for producing electricity. A power control unit (300) is provided, which levels the size of the surplus power produced in the fuel cell stack. A water treatment system (220) is provided, which deionizes seawater to produce ultra-pure water. The electric energy produced in the fuel cell stack operates the water treatment system to load. The surplus power is exhausted when it exceeds the amount of electricity consumed in the vessel.    USE - Fuel cell system for a vessel.    ADVANTAGE - Load following of the fuel cell system is improved according to the shipping condition of the vessel. Production efficiency of the fuel cell is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a load following method for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system. (Drawing includes non-English language text).    Fuel cell stack (100)    Fuel supply unit (210)    Water treatment system (220)    Power control unit (300)    Load apparatus (400)
NOVELTY - A catalytic composition comprises a rhodium compound; and a promoter of the rhodium compound, where the promoter comprises a compound of iron, and where the rhodium compound and the promoter are deposited on a cerium oxide support.    USE - The catalytic composition is useful for preparing oxygenates from two carbon atoms, where the oxygenate is ethanol; and for preparing hydrocarbons from two carbon atoms (all claimed). Generally, it can be used for selective conversion of synthesis gas into ethanol.    ADVANTAGE - The catalytic composition can produce ethanol with increased activity and/or selectivity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a process for preparing the catalyst composition which involves: (a) impregnating the ceria support with a precursor of rhodium compound and a precursor or precursors of the rhodium compound promoters; (b) subjecting the impregnated carrier to a drying step; (c) subjecting the dried impregnated support to calcination step; and (d) subjecting the calcined solid obtained in step (c) to a reduction process;    (2) a process for preparing oxygenates from two carbon atoms, which involves reacting a gas mixture comprising carbon monoxide and hydrogen with the catalyst composition; and    (3) a process for preparing hydrocarbons from two carbon atoms, which involves reacting a gas mixture comprising carbon monoxide and hydrogen with the catalyst composition.
NOVELTY - Redox active material comprises: pyrolusite type natural manganese ore including at least 60 wt.% of manganese dioxide, where the ore is nickel-enriched; and mixed metallic oxide of nickel-manganese crystallized according to a spinel structure. The redox active material is in the form of particles.    USE - The redox active material is useful for oxydoreduction of chemical loop, and for combustion of solid, liquid or gaseous hydrocarbon feedstocks to collect carbon dioxide (all claimed), where the hydrocarbon feedstocks are fuels such as fossil fuel or biomass.    ADVANTAGE - The redox active material is in the form of particles, so that the material is easy to flow and transport, and effectively performs the combustion of hydrocarbon feedstocks in an environment-friendly manner with reduced emission of greenhouse gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combustion of solid, liquid or gaseous hydrocarbon feedstocks using a redox active material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a chemical looping combustion method.    First reaction zone (R1)    Second reaction zone (R2)    Oxidation zone (R4)    Separation zone (S3)    Gas-solid separation zones. (S5, S6)
NOVELTY - Production of fermentation substrate comprises crushing rotten plant debris and humus at weight ratio of 1:2.5-1:3, mixing to obtain mixture, spraying with chlorothalonil solution, stirring, and stacking to carry out fermentation for 1-2 months.    USE - Method for production of fermentation substrate used for dendrobe, Paris polyphylla and honeysuckle seedlings (all claimed).    ADVANTAGE - The fermentation substrate can greatly shortens growth cycle of plants, achieves pollution-free ecological planting, reduces cost of cultivation, and ensures production of high quality medicinal plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of substrate by laying 180-300 kg/acre fermentation substrate on dendrobe, Paris polyphylla and honeysuckle seedling beds at 2-3 cm thick; or mixing fermentation substrate with water at weight ratio of 1:15-3:15, and spraying 4-5 kg/acre on dendrobe, Paris polyphylla and honeysuckle leaves.
NOVELTY - Flow spray drying granulation of water-soluble Paraquat (RTM: N,N'-dimethyl-4,4'-bipyridinium dichloride) comprises taking raw materials, mixing, atomizing, drying, discharging, separating, fluidizing, drying and removing dust. Flow spray drying granulation device comprises drying column (1), built-in fluidized bed (2), pressurized fluid nozzle (3), vibration fluidized bed (15), main tank (16) and two dust collectors (21,23).    USE - Method for flow spray drying and granulating water-soluble Paraquat (RTM: N,N'-dimethyl-4,4'-bipyridinium dichloride).    ADVANTAGE - The method is safe, environment friendly and increases production rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of flow spray drying granulation device.    Drying column (1)    Built-in fluidized bed (2)    Pressurized fluid nozzle (3)    Vibration fluidized bed (15)    Main tank (16)    Dust collectors (21,23)
NOVELTY - A supported noble metal catalyst comprises 0.5-10 wt.% noble metal oxide and 90-99.5 wt.% carrier.    USE - Noble metal supported catalyst used for fixed bed micro carbon monoxide methanation process (claimed).    ADVANTAGE - The noble metal catalyst has stable catalytic property.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation method of noble metal supported methanation catalyst, which involves dissolving 0.5-1.0 g of noble metal nitrates and soluble organic fuel per ml water and obtaining solute solution, impregnating the catalyst carrier in solution, stirring for 6-24 hours, heating at 300-700 degrees C, grinding and granulating; and    (2) application of noble metal supported methanation catalyst in fixed bed micro carbon monoxide methanation process, which involves reducing catalyst at normal pressure using 5-15 vol.% hydrogen and 85-95 vol.% nitrogen reducing gas having reducing gas space velocity of 1000-12000 mL/g.hour at 400-600 degrees C in fixed bed reactor and carrying out carbon monoxide methanation reaction using 0.5-5% carbon monoxide at 250-650 degrees C under reaction pressure of 0.5-4.0 MPa and space velocity of 5000-100000 mL/g.hour.
NOVELTY - Three-dimensional crop fertilization comprises applying 75-150 kg/acre bio-organic fertilizer with crops before sowing or planting, applying 0.75-1.5 kg/acre water-soluble fertilizer used as base fertilizer, performing irrigation, applying fertilizer for 1-2 times during the growth period of the crop and spraying with 30-60 kg organic water-soluble fertilizer used as foliar fertilizer for 2-3 times during the growth period of the crop.    USE - Method for carrying out three-dimensional crop fertilization (claimed) used for increasing crop yield, improving soil structure and inhibiting growth of harmful pathogenic bacteria in soil.    ADVANTAGE - The method is safe and environment-friendly.
NOVELTY - Preparation of N-(5-(4-bromophenyl)-6-chloro-4-pyrimidinyl)-N'-propyl sulfonamide (I) involves adding N-propyl-sulfonamide (III) and 5-(4-bromophenyl)-4,6-dichloropyrimidine (II) into dimethyl sulfoxide, adding alkoxy metal compound (IV), stirring, and reacting.    USE - Preparation of N-5-4-bromophenyl-6-chloro-4-pyrimidinyl-N'-propyl sulfonamide used as planar temazepam intermediate.    ADVANTAGE - The method enables efficient preparation of N-5-4-bromophenyl-6-chloro-4-pyrimidinyl-N'-propyl sulfonamide with yield of 51% or more, high purity, and with reduced salt and solvent amount, by environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of N-(5-(4-bromophenyl)-6-chloro-4-pyrimidinyl)-N'-propyl sulfonamide of formula (I) involves adding N-propyl-sulfonamide of formula (III) and 5-(4-bromophenyl)-4,6-dichloropyrimidine of formula (II) into dimethyl sulfoxide, adding alkoxy metal compound of formula: ROM (IV), stirring, and reacting.    R=1-4C hydrocarbyl;and    M=1st main group element in periodic table.
NOVELTY - This new type utility claims a modular one health gas generator, more specifically, of the one system has a circulation and cooling function of a modular health gas generator, moreover, by a multi-a freely detaching of electrolytic groove, produce rate of hydrogen oxygen gas also will be a. This utility new type comprises one inner water tank and with a detachable electrolytic groove number, the application time, the hollow part of each electrolytic groove a from a inner water tank input or supplementary liquid water, liquid water in the electrolytic groove is electrolyzed to produce hydrogen and oxygen output to the inner water tank, the air outlet by a of inner water tank.
NOVELTY - This new type utility claims one with a cooling system of a gas generator, comprises the one with outer water tank, inner water tank and one one electrolytic groove mould group. Outer one is contained, to electrolytic groove for module and inner water tank set with the in the process of cooling, the temperature of the gas generator and prevent the occurrence of hydrogen decrepitation. Moreover, the utility model is new type electrolytic groove module a produce of hydrogen oxygen conveyed in inner water tank through the liquid water of inner water tank to futher reduces the temperature of oxygen to the hydrogen of hydrogen decrepitation.
NOVELTY - Manufacturing liquid extract involves processing mushroom compost. The compost is transformed with determining total nitrogen as per nourishment required by plant. The liquid extract is sprayed or irrigated to prevent the loss of nutriments. Base aliquot is diluted using distilled water or fresh water without removing chemical, physical, microbiological and nutritive properties from the compost liquid.    USE - Method for manufacturing liquid extract used for culturing mushroom, and used in conventional agriculture.
NOVELTY - Soil composition comprises 95-99.5 wt.% of additive mixture, 100 pts. wt. crushed wood powder, 12.5-300 pts. wt. red clay, 12.5-300 pts. wt. granite soil, 12.5-300 pts. wt. cocopeat, 5-150 pts. wt. zeolite, 2.5-100 pts. wt. bone powder, 2.5-100 pts. wt. charcoal powder, 2.5-20 pts. wt. hygroscopic polymer, 2.5-20 pts. wt. fermentation sample, 100 pts. wt. sodium silicate, 5-1000 pts. wt. cellulose powder, 5-1000 pts. wt. acrylamide, 0.3-4 pts. wt. binding material, 100 pts. wt. water, 20-100 pts. wt. moss, 10-100 pts. wt. polyvinyl alcohol, and 0.1-2 pts. wt. promoter.    USE - The soil composition is useful for afforestation of slope (claimed) formed in a building, an apartment complex or an industrial complex.    ADVANTAGE - The composition improves the plant growth in the slope.    DETAILED DESCRIPTION - Soil composition comprises 95-99.5 wt.% of additive mixture, 100 pts. wt. crushed wood powder, 12.5-300 pts. wt. red clay, 12.5-300 pts. wt. granite soil, 12.5-300 pts. wt. cocopeat, 5-150 pts. wt. zeolite, 2.5-100 pts. wt. bone powder, 2.5-100 pts. wt. charcoal powder, 2.5-20 pts. wt. hygroscopic polymer, 2.5-20 pts. wt. fermentation sample, 100 pts. wt. sodium silicate, 5-1000 pts. wt. cellulose powder, 5-1000 pts. wt. acrylamide, 0.3-4 pts. wt. binding material, 100 pts. wt. water, 20-100 pts. wt. moss, 10-100 pts. wt. polyvinyl alcohol, and 0.1-2 pts. wt. promoter. The promoter further comprises 100 pts. wt. water, and 3-18 pts. wt. auxin, gibberellin or their mixtures. An INDEPENDENT CLAIM is included for a slope afforestation method including mixing the additive mixture, a promoter mixture and a binding material mixture, and spraying the mixed material on the slope.
NOVELTY - This utility new type marsh gas raw material relates to a device, a one is a liquid bacterial manure regulating pool, the pool body is divided into comprise stir section and reaction section, a tank body upper part set with seal cover, a seal cover set with pressure control valve, a stir tank body of section is further set with feeding tube and stir device between a stir section and reaction section through clapboard, stir liquid of a section through part of a clapboard into reaction section of tank body of said reaction section inner set with electric heater and a temperature control device. This utility new type a to realize automatic control, avoiding the aritificial intervention, saves the labour, it has regulating error and so on.
NOVELTY - The method comprises stirring wastewater in the livestock manure, mitigating environmental conditions according to anaerobic treatment to the vegetal material of the livestock manure, carrying out anaerobic treatment in absence of air for decomposition of bacteria in the livestock manure, and carrying out aerobic treatment for microorganisms to promote compositing by adjusting temperature and moisture of the manure. The livestock manure to be processed is stored in a storage tank containing a stirrer.    USE - The method is useful for controlling pH of livestock manure for converting to liquefied-fertilizer (claimed).    ADVANTAGE - The method is capable of producing fertilizer with high efficiency, while controlling the bad odor of fertilizer.    DETAILED DESCRIPTION - The method comprises stirring wastewater in the livestock manure, mitigating environmental conditions according to anaerobic treatment to the vegetal material of the livestock manure, carrying out anaerobic treatment in absence of air for decomposition of bacteria in the livestock manure, and carrying out aerobic treatment for microorganisms to promote compositing by adjusting temperature and moisture of the manure. The livestock manure to be processed is stored in a storage tank containing a stirrer. The method further comprises separating foreign substances and solid content of the livestock manure. The stirring step is carried out by adding strong alkalis and strong acid to the livestock manure. The vegetal material includes lignin and cellulose. The anaerobic treatment step is carried out for decomposition of lipolytic bacteria. The aerobic treatment is carried out for decomposition of carbohydrate in the manure.
NOVELTY - Preparing phosphate biofertilizer involves using Azospirillum species and Azotobacter species, which are cultured separately and then mixed to obtain inoculums. Sterile manure is placed in a container and then inoculums are added to obtain biofertilizer. The obtained biofertilizer is stored.    USE - Method for preparing phosphate biofertilizer used for improving growth of fruit.
NOVELTY - Apparatus comprises: a fuel cell system (400) to provide electricity by supplying fuel for electrochemical reaction, and provides power to a power demand source (100) to convert into electric power; a fuel supply system provided with a hydrogen tank and an oxygen tank to store fuel and for supplying fuel to the fuel cell system; a water treatment system (500) for producing fresh water being supplied to sea water; and an electrolyzer (300) for electrolysis of hydrogen and oxygen when supplied with power generated from a secondary battery (200) and fresh water from the water treatment system.    USE - The apparatus is useful for supplying electric power to submarine observation equipment (claimed).    ADVANTAGE - The apparatus: is capable of supplying stable and high capacity power to the equipment; and has prolonged work life, when compared to conventional power supply system.    DETAILED DESCRIPTION - Apparatus comprises: a fuel cell system (400) to provide electricity by supplying fuel for electrochemical reaction, and provides power to a power demand source (100) to convert into electric power; a fuel supply system provided with a hydrogen tank and an oxygen tank to store fuel and for supplying fuel to the fuel cell system; a water treatment system (500) for producing fresh water being supplied to sea water; and an electrolyzer (300) for electrolysis of hydrogen and oxygen when supplied with power generated from a secondary battery (200) and fresh water from the water treatment system, and respectively supplying decomposed hydrogen and oxygen into the hydrogen tank and the oxygen tank.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic representation of the apparatus.    Power demand source (100)    Secondary battery (200)    Electrolyzer (300)    Fuel cell system (400)    Water treatment system (500)
NOVELTY - Invention may be used when producing carbon nanotubes and hydrogen. Microwave plasma converter comprises flow reactor 1 of radiotransparent heat-resistant material, filled with gas permeable electrically conductive material - catalyst 2 placed into the ultrahigh frequency waveguide 3 connected to the microwave electromagnetic radiation source 5, provided with microwave electromagnetic field concentrator, designed in the form of waveguide-coax junction (WCJ) 8 with hollow outer and inner conductors 9, forming discharge chamber 11 and secondary discharge system. Auxiliary discharge system is designed from N discharge devices 12, where N is greater than 1, arranged in a cross-sectional plane of discharge chamber 11 uniformly in circumferential direction. Longitudinal axes of discharge devices 12 are oriented tangentially with respect to the side surface of discharge chamber 11 in one direction. Nozzle 10 is made at outlet end of inner hollow conductor 9 of WCJ 8 coaxial. Each of discharge devices 12 is provided with individual gas pipeline 13 to supply plasma-supporting gas to discharge zone.    USE - Power industry.    ADVANTAGE - Invention permits to increase the reaction volume, production capacity and period of continuous operation, stabilise burning of microwave discharge.3 cl, 2 dwg
NOVELTY - Method for decomposing organic matter using lactic acid bacteria involves inserting organic matter and lactic acid bacteria into a sealed storage tank, performing decomposition and fermentation under anaerobic conditions, removing treated matter from the storage tank and depositing the treated matter.    USE - The method is useful for decomposing organic matter using lactic acid bacteria chosen from Pediococcus acidilactici strain TT12-G5 (NITE BP-1430), P.acidilactici strain TT12-PG2 (NITE BP-1431), Lactobacillus fermentum strain TT12-18h1 (NITE BP-1448), L.zeae strain TT12-S4 (NITE BP-1433), L.rhamnosus strain TT12-S1 (NITE BP-1432), L.casei strain TT12-18h4 (NITE BP-1429) and their mutants for producing compost (all claimed).    ADVANTAGE - The method reduces volume of organic matter, decomposes organic matter rapidly, suppresses offensive odor, is simple and cost-effective, and eliminates addition of decomposition promotion agent, and need of adjusting conditions.
NOVELTY - Between the This utility new type relates to one by using a direct current for a water electrolysis hydrogen oxygen produce mix gas of hydrogen and oxygen generator comprise a machine body, a main power supply of upper machine body, main power supply connecting with the load line of the load connecting wire of electrolytic groove, the electrolytic groove upper end of air outlet, the electrolytic groove of lower end, and the return port connect with the air outlet of a liquid storage tank, and the liquid storage tank of hydrogen oxygen connecting pipe, connecting with the liquid storage tank of electrolytic water tank, the electrolytic groove of multi-group of cell, the cell group with a plane radiating plate. electrolysis groove and the main power supply with temperature sensor., the air outlet is connected with the liquid storage tank. stainless steel radiator, and the liquid storage tank. with a buffering tank and one-way valve, a liquid storage tank and an oxygen guide tube. with hydrogen and voltage regulator, the utility model reduces the valid temperature of inner electrolyte electrolytic groove, which saves the electrolytic groove and the cost and greatly increases the electrolytic efficiency of the hydrogen and oxygen generator is more stable safety of operation.
NOVELTY - An organic sludge high temperature microaerobic-anaerobic digestion device comprises high temperature aerobic reactor and anaerobic fermentation reactor (2), pH value regulating tank (3), high temperature microaerobic reactor (1), reaction tank (11), sludge reflux system (12), aeration system and temperature sensor gas absorbing processing device.    USE - Organic sludge high temperature microaerobic-anaerobic digestion device.    ADVANTAGE - The method produces methane, and reduces aeration amount and energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic sludge high temperature microaerobic-anaerobic digestion comprising domesticating strain in high temperature microaerobic reactor, opening sludge pump, feeding into organic sludge, opening sludge reflux system and aeration system, digesting at 45-65 degrees C for 2-3 days, opening discharging pipeline, entering into pH regulating pool, regulating pH with alkali solution at 6.8-7.2 for 3-5 hours, dissolving oxygen, pumping into anaerobic fermentation reactor for 6-20 days, and discharging.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic sludge high temperature microaerobic-anaerobic digestion device.    High temperature microaerobic reactor (1)    High temperature aerobic reactor and anaerobic fermentation reactor (2)    pH Value regulating tank (3)    Reaction tank (11)    Sludge reflux system (12)
NOVELTY - Method for stacking dead animals comprises selecting room, painting, disinfecting, sawdust bedding, stacking wood, fermenting, heating, standing, thawing, thermal cycling, clearing, disinfecting, stacking dead animals, maintaining, measuring temperature and humidity, recording, standing for 60 days and reusing.    USE - Method for stacking dead animals for sanitizing, preventing epidemic and killing pathogens (all claimed).    ADVANTAGE - The simple and inexpensive method is environmentally friendly and economical.
NOVELTY - Preparation of organic and inorganic fertilizer involves mixing organic material with EM-type microbial agent in fermentation tower, fermenting, adding obtained product, chicken manure, fly ash, soapstock, untreated humic acid, urea, ammonium sulfate, monoammonium phosphate and potassium chloride into a ball mill, grinding, sieving, obtaining mixture with particle size of 10-50 meshes, adding the mixture into a mixer, stirring, grinding, extruding, granulating, baking resultant material at 40-50 degrees C for 3-5 hours, cooling, and packaging obtained product in bag provided with strain.    USE - Preparation of organic and inorganic fertilizer used for mulberry tree.    ADVANTAGE - The method enables preparation of organic and inorganic fertilizer by simple process.    DETAILED DESCRIPTION - Preparation of organic and inorganic fertilizer involves mixing organic material with EM-type microbial agent in fermentation tower, fermenting the mixture at initial temperature to 70 degrees C for 3 days and at 70-20 degrees C for 4-7 days, adding obtained product, 5-10 pts. wt. chicken manure, 5-10 pts. wt. fly ash, 10-20 pts. wt. soapstock, 10-20 pts. wt. untreated humic acid, 20-30 pts. wt. urea, 5-10 pts. wt. ammonium sulfate, 5-10 pts. wt. monoammonium phosphate, and 5-10 pts. wt. potassium chloride into a ball mill, grinding, sieving ground material using vibrating sieve, obtaining mixture with particle size of 10-50 meshes, adding the mixture into a mixer, stirring, grinding, extruding, granulating, drying, baking dried material at 40-50 degrees C for 3-5 hours, cooling, and packaging obtained product in bag provided with strain.
NOVELTY - An air circulation system comprises electrolyzer, first gas outlet, first water inlet, first storage tank, first water outlet, second gas outlet, and pressure relief device. The first storage tank is provided with electrolytic water and gas inlet. The electrolyzer is provided with electrolytic water.    USE - Air circulation system used for electrolytic cell for production of hydrogen gas (claimed).    ADVANTAGE - The system can control hydrogen gas storage system to prevent hydrogen explosion.
NOVELTY - A water reservoir purification and reclamation method involves collecting algae from water reservoir by supplying oxygen, harvesting blue-green algae by trawl, collecting shallowly submerged cyanobacteria in a sealed fermentation chamber equipped with a screen to carry out anaerobic fermentation, followed by discharging resultant biogas to an external tank, removing waste post-fermentation chamber residue on the sieve, pumping rest process liquid out of the chamber, obtaining waste and digestate liquid manure, and subjecting tank to aeration after harvesting algae from the water.    USE - Method for purification and reclamation of water reservoir.    DETAILED DESCRIPTION - A water reservoir purification and reclamation method involves collecting algae from water reservoir by supplying oxygen, harvesting blue-green algae by trawl or other network, collecting shallowly submerged cyanobacteria in a sealed fermentation chamber equipped with a screen for 5-50 days to carry out anaerobic fermentation, followed by discharging resultant biogas to an external tank, removing waste post-fermentation chamber residue on the sieve, pumping rest process liquid out of the chamber, obtaining waste and digestate liquid manure, subjecting tank to aeration carried out by using 10-55% hydrogen peroxide in the form of capsules placed at the bottom surface of the water having depth of 10-150 cm after harvesting algae from the water.
NOVELTY - The method involves performing pneuma sample chamber analysis. A hydrogen bottle is opened to determine argon pneuma exit pressure of a decompression valve. A sample is pre-heated. A FID detector pneuma chromatography sample outlet port is connected to an alkali liquid beaker. An inner oil fire producing pneuma sample is placed into a chromatographic column. A Q-fill column and 13X molecular sieve column are filled with oxygen, hydrogen, carbon dioxide, nitrogen and carbon monoxide. Methane in a blood capillary column is detected by a TCD detector.    USE - Oil field fire producing pneuma component pneuma chromatography analysis method.    ADVANTAGE - The method enables detecting temperature and flow rate of pneuma. The method enables obtaining test condition parameter of a sample in an accurate manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an oil field fire producing pneuma component.
NOVELTY - Febuxostat intermediate is new.    USE - A febuxostat intermediate (claimed).    ADVANTAGE - Febuxostat prepared using febuxostat intermediate has high purity, febuxostat preparation is environment-friendly, and febuxostat intermediate reduces cost and increases yield of febuxostat preparation.    DETAILED DESCRIPTION - Febuxostat intermediate of formula (V) is new. An INDEPENDENT CLAIM is included for preparation of febuxostat intermediate.
NOVELTY - A Itraconazole dihydrochloric acid is synthesized by uniformly stirring itraconazole and organic solvent in which mass ratio solvent:itraconazole is 1-5:1, adding hydrochloric acid.    USE - Synthesis process of Itraconazole dihydrochloric acid (claimed).    ADVANTAGE - The process reduces corrosion of device, unit energy consumption, and production cost, improves product mass, has no refining process, increases dissolution rate and preparation stability, and is good for environmental protection and health of workers.
NOVELTY - A wind power-solar energy hydrogen production unit comprises direct current power source, direct current voltage divider, electrolytic box square matrix, temperature difference generator, conductive roller, water box, heat preservation layer, power distributor, electrolytic tank, cooling plate, cooling water tube, water tank, and siphon tube.    USE - Wind power-solar energy hydrogen production unit.    ADVANTAGE - The production unit improves wind and light energy utilization efficiency.
NOVELTY - A modularized healthcare gas generator comprises power supply, conductive element, inner water tank (20), electrolysis groove module (40), infusion tube (50), gas tube, through hole, body frame, U-shaped electrode sheet, drainpipe (80), electrode plate, pressure relief device (24), and cover body.    USE - Modularized healthcare gas generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a three-dimensional sketch map of modularized healthcare gas generator.    Water tank (20)    Pressure relief device (24)    Electrolysis groove module (40)    Infusion tube (50)    Drainpipe (80)
NOVELTY - Gas generator comprises an outer water tank containing coolant in its primary hollow section, an inner water tank (20) containing water in its hollow section connected to an air tube, an electrolytic groove (31) on the outer water tank (10) and a groove mold (30) soaked in coolant.    USE - Gas generator for hydrogen and oxygen.    ADVANTAGE - Water runs through the inner water tank, thus cooling the oxygen and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing is a perspective view of the gas generator.    Outer water tank (10)    Inner water tank (20)    Groove mold (30)    Electrolytic groove (31)    Gasket (63)
NOVELTY - Processing unit comprises an injection pipe (111) for injecting food waste, a first stirring tank (121) for fermenting and degrading food waste by stirring with microorganism, an intermediate plate (125) formed of multiple hole (125a) with predetermined size, and a second stirring tank (131) for discharging the dried amount according to set amount of the first stirring tank, accepting degraded food waste in paste condition, passing via the through hole of the intermediate plate to ferment the food waste into the first stirring tank, and contacted with the first stirring tank.    USE - The processing unit is useful for fermenting and reducing food waste (claimed) to produce biogas, bio oil, solid refuse fuel, liquid manure and electricity.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the processing unit for fermenting food wastes.    Injection pipe (111)    First stirring tank (121)    Intermediate plate (125)    Through hole (125a)    Second stirring tank (131)
NOVELTY - Pretreating lignocellulose biomass, comprises crushing lignin by physically pretreating using planetary milling comprising introducing a mixture of biomass and buffer into a container, and crushing using a ball, or attrition milling comprising introducing the mixture of biomass and buffer into the container with a stirrer, and crushing using the ball, without chemical pretreatment.    USE - The method is useful for pretreating lignocellulose biomass for producing a sugar compound and biofuel (all claimed).    ADVANTAGE - The method improves yield, and reduces loss biomass and generation of toxic by-products (claimed), can produce biofuel from biomass in easy manner, and is environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing a sugar compound using lignocellulose biomass, comprising (a) crushing lignin by physically pretreating using above method, and (b) degrading the pretreated biomass using enzymes, and saccharifying; and    (2) producing biofuel using lignocellulose biomass, comprising (a), (b), and (c) fermenting the produced sugar compound using microorganisms.
NOVELTY - A gas production apparatus comprises 1st electrode, 1st chamber formation part which forms 1st chamber for accommodating electrolyte solution and 1st electrode, 2nd electrode containing photocatalyst, 2nd chamber formation part which forms 2nd chamber for accommodating electrolyte solution and 2nd electrode, separation membrane (330) which partitions off between 1st and 2nd chambers and separates hydrogen gas and oxygen gas, and reinforcement part (390) containing support part (395) which supports a part of exposed part (330e) which is exposed to 1st chamber or 2nd chamber.    USE - A gas production apparatus for producing hydrogen gas and/or oxygen gas using photocatalyst from electrolyte solution containing water (claimed).    ADVANTAGE - Deformation of separation membrane is suppressed.    DESCRIPTION OF DRAWING(S) - The drawings show schematic diagrams of the membrane module.    Separation membrane (330)    Exposed part (330e)    Reinforcement part (390)    1st seal part (391)    Support part (395)
NOVELTY - This utility new type relates to a one agricultural ecological fermentation plant for cook rubbish harmless processing system, comprising a multi-is one shape in turn vertically arranged of earthworm cultivation pool are paved with earthworm cultivation bed in the earthworm cultivation tank, set with a anti-escaping plate up the top of the earthworm cultivation bed, the bottom of the side wall, an LED light with suction, cleaning door, earthworm body liquid collecting tube on the surface of part of the earthworm cultivation pool is uniformly distributed with liquid overflow hole, an earthworm body liquid collecting tube of bottom end are connected with the earthworm body liquid collecting box body. This utility new type has simple structure, fully taking design of earthworm cultivation pool for earthworm growth environment, at the same time, through the principle of gravity, the earthworm cultivation bed in a earthworm secretion of body liquid collected earthworm body liquid collecting box body in, and taking filter slag a of, and through, can improve the efficiency of liquid collecting body, the solution of the invention can form scale, systematization, commercial products of ecological fermentation plant for cook rubbish harmless processing system.
NOVELTY - Removing sulfate in high salt petrochemical sewage comprises ultrasonic degrading the residual sludge produced in a high salt petrochemical sewage treatment system sedimentation tank through a ultrasonic processor, mixing the resulting sludge or sludge supernatant with high salt petrochemical sewage, then introducing into an anoxic tank or anaerobic tank, providing carbon source and reducing sulfate into hydrogen sulfide by sulfate reducing bacteria.    USE - The method is useful for removing sulfate in high salt petrochemical sewage (claimed).    ADVANTAGE - The method improves sulfate removing rate, reduces tendency of scale formation of calcium sulfate, utilizes device which can be operated and maintained for long time, and ensures stable operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for removing sulfate in high salt petrochemical sewage, comprising an anoxic tank or an anaerobic tank, an aerobic tank, a sedimentation tank and an ultrasonic processor, the ultrasonic processor is located in the sedimentation tank, the remaining back portion of the sedimentation tank is introduced into the ultrasonic processor and the mixed high salt petrochemical sewage is into the anoxic tank or anaerobic tank.
NOVELTY - Organic fertilizer is obtained by mixing 55-85 pts. wt. castor powder, 5-15 pts. wt. rock phosphate powder, 5-20 pts. wt. boron and magnesium ore, and 5-10 pts. wt. microbial agent (Bacillus subtilis), and crushing the obtained product.    USE - The organic fertilizer is useful for promoting growth of crop.    ADVANTAGE - The organic fertilizer increases crop quality, and improves soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned organic fertilizer, which involves (a) culturing B.subtilis strain in fresh test tube comprising culture medium containing beef extract and peptone at 30 degrees C for 2-4 days, (b) preparing liquid culture medium (pH 7.2) comprising 5 g beef extract, 5 g peptone, 5 g sodium chloride, and 1 l water, and sterilizing the culture medium, inoculating 0.1-10% culture obtained in step (a) into the prepared liquid culture medium, and culturing in shaker, (c) inoculating the obtained culture into fermentation tank (when bacterial count reaches to 20 billions/ml) comprising culture medium (pH 7.5) comprising 10 kg bean flour, 10 kg bread flour, 1 kg peptone, 1 kg ammonium sulfate, 0.1 kg yeast powder, 5 kg calcium carbonate, and 10 kg water, and fermenting at 28-30 degrees C to obtain microbial agent, and (d) mixing the obtained microbial agent with castor powder, rock phosphate powder, and boron and magnesium ore, stirring the mixture for at 10-55 degrees C, and pH of 5-10.5, for 2 hours, granulating the mixture, drying the granules, and sieving the dried granules.
NOVELTY - Method for reducing carbon dioxide involves dissolving electrolyte containing carbon dioxide and precipitation supplemental agent in alcohol in a reactor (150), and electrolyzing carbon dioxide in the electrolyte using anode (120) and cathode (110).    USE - Method for reducing carbon dioxide to produce alkane and hydrogen using membrane-free-type carbon dioxide (claimed).    ADVANTAGE - The method enables efficient reduction of carbon dioxide, by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for membrane-free-type carbon dioxide reducing device (100).    DESCRIPTION OF DRAWING(S) - The drawing shows cross-sectional view of membrane-free-type carbon dioxide.    Membrane-free-type carbon dioxide (100)    Cathode (110)    Anode (120)    Power supply unit (140)    Reactor (150)
NOVELTY - Preparing vildagliptin a compound (I), comprises: (a) reacting (S)-pyrrolidine-2-carboxylic acid amide a compound (VI) with a chloro-acetyl chloride in the presence of a nitrile solvent to form (S)-1-(2-chloro-acetyl)-pyrrolidine-2-carboxylic acid amide compound (IV); (b) reacting (IV) with a dehydrating agent to form (S)-1-(2-chloro-acetyl)-pyrrolidine-2-carbonitrile compound (III); and (c) reacting (III) with 3-amino-adamantan-1-ol compound (II).    USE - The process is useful for preparing vildagliptin (claimed), which is useful for treating type-2 diabetes mellitus. No biological data given.    ADVANTAGE - The reproducible and robust process provides vildagliptin product with high yield and less purity, in a simple, ecofriendly and cost effective manner.    DETAILED DESCRIPTION - Preparing vildagliptin a compound of formula (I), comprises: (a) reacting (S)-pyrrolidine-2-carboxylic acid amide a compound of formula (VI) with a chloro-acetyl chloride compound of formula (Cl-CH2-C(=O)-Cl) in the presence of a nitrile solvent to form (S)-1-(2-chloro-acetyl)-pyrrolidine-2-carboxylic acid amide compound of formula (IV); (b) reacting (IV) with a dehydrating agent to form (S)-1-(2-chloro-acetyl)-pyrrolidine-2-carbonitrile compound of formula (III); and (c) reacting (III) with 3-amino-adamantan-1-ol compound of formula (II).
NOVELTY - Process for producing cresol involves preheating raw materials comprising ether, hydroxybenzene and methanol, mixing with steam by passing through multi stage solid catalyst bed, and carrying out a gas-phase reaction at a reaction temperature of 250-450 degrees C with 0.3-5 h-1 feed weight airspeed under atmospheric pressure to obtain cresol, where solid catalyst is one or more chosen from alumina, kaolin and molecular sieve based catalyst. The hydroxybenzene is chosen from phenol, dimethyl phenol and their mixtures.    USE - The process is useful for producing cresol (claimed).    ADVANTAGE - The process yields 0.2 g cresol/g of catalyst and is environmentally-friendly. The catalyst has excellent stability, and non-corrosiveness.    DETAILED DESCRIPTION - Process for producing cresol involves preheating raw materials comprising ether, hydroxybenzene and methanol, mixing with steam by passing through multi stage solid catalyst bed, and carrying out a gas-phase reaction at a reaction temperature of 250-450 degrees C with 0.3-5 h-1 feed weight airspeed under atmospheric pressure to obtain cresol, where solid catalyst is one or more chosen from alumina, kaolin and molecular sieve based catalyst. The ether, hydroxybenzene and methanol are in molar ratio of 0-30:50-70:10-50. The hydroxybenzene is chosen from phenol, dimethyl phenol and their mixtures. The ether is two or more chosen from anisole, dimethyl ether, methylanisole, and their mixtures.
NOVELTY - Processing method of organic wastewater, involves visualizing and detecting gene information derived from microorganism flora in activated sludge of the processor using detection unit, acquiring gene information by the detection unit, and determining running state of the processor compared with data which visualized the gene information derived from the microorganism flora in activated sludge when it is in time of activated state having the operation of the processor, and standard condition, respectively, detected and recorded it using monitoring unit.    USE - The method is useful for processing organic wastewater (claimed).    ADVANTAGE - The method enables to change microorganism flora in activated sludge simply, cost-effectively and rapidly, analyzes wastewater quantitatively and qualitatively, grasps running state of processor exactly, controls optimization of microorganism flora, improves settleability of sludge, and suppresses production of offensive odor.
NOVELTY - The system has a generator (3) which produces an electrical energy. An electrolyzer (7) produces oxygen and hydrogen from electricity and water. A heat exchanger (15) produces the high-pressure gas from a refrigerant. A turbine (14) produces rotational energy from the high-pressure gas and rotates the generator. The heat engine (1) is supplied with hydrogen, oxygen and fuel.    USE - Energy generation system of vehicle (claimed).    ADVANTAGE - The fuel consumption of the combustion engine can be reduced effectively, while reducing the risk associated with the storage of hydrogen and oxygen. The efficiency of the energy generation system can be improved effectively. The proper functioning of the generator is ensured, so that degradation of the energy generation system can be avoided. The smooth performance of the electrolyzer can be ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vehicle.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy generation system.    Heat engine (1)    Generator (3)    Electrolyzer (7)    Turbine (14)    Heat exchanger (15)
NOVELTY - A water-electrolysis stack (4) electrolyzes an ion aqueous solution and produces oxygen and hydrogen gases, and a water supply unit (5) supplies supplementary water as aqueous solution with an ion concentration lower than the ion aqueous solution and a pressure lower than the ion aqueous solution. A water mixing unit (6) mixes the water content of supplementary water with ion aqueous solution. The ion aqueous solution of second region is mixed with the water content of the supplementary water supplied by permeating through a diaphragm and is sent to the water-electrolysis stack.    USE - Water-electrolysis apparatus.    ADVANTAGE - The water-electrolysis apparatus for high pressure, enables to reduce power consumption. The installation cost can be reduced. A high pressure feed water pump becomes unnecessary.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the structure of water-electrolysis apparatus. (Drawing includes non-English language text)    Water-electrolysis apparatus (1)    Oxygen gas-liquid separation unit (2)    Water-electrolysis stack (4)    Water supply unit (5)    Water mixing unit (6)
NOVELTY - A hydrogen oxygen gas generation device including an electrolysis unit and a filter unit is provided. The electrolysis unit is for generating hydrogen oxygen gas by doing an electrolysis reaction with an electrolyte. The electrolysis unit has at least two stripe-shaped electrodes. The filter unit is connected to the electrolysis unit. The filter unit is used for filtering an impurity generated by the stripe-shaped electrodes consumed in the electrolysis reaction.
NOVELTY - The apparatus comprises first and second fermentation rooms containing food waste, a device for pulverizing the food waste, a partition wall, a stirring unit including agitating blades to stir the food waste within the fermentation tanks, a mobile unit for moving the food waste between the first and second fermentation rooms, a heating unit, a hopper in which the food waste is fermented within the first and second fermentation tanks, and a unit for exhausting the food waste. A port discharges gas in the fermentation tanks.    USE - The apparatus is useful for fermenting food waste (claimed).    ADVANTAGE - The apparatus is capable of rapidly, economically and energy-efficiently fermenting the food waste.    DETAILED DESCRIPTION - The apparatus comprises first and second fermentation rooms containing food waste, a device for pulverizing the food waste, a partition wall, a stirring unit including agitating blades to stir the food waste within the fermentation tanks, a mobile unit for moving the food waste between the first and second fermentation rooms, a heating unit, a hopper in which the food waste is fermented within the first and second fermentation tanks, and a unit for exhausting the food waste. A port discharges gas in the fermentation tanks. The agitating blades are equipped in the first and second fermentation rooms. A rotary shaft is arranged in the first fermentation room. A microbe habitation unit is equipped in the first and second fermentation rooms for sterilizing the food waste. The apparatus further comprises an absorber present in an amount of 10-30 pts. wt.
NOVELTY - Preparing conjugated linoleic acid methyl ester comprises reacting fatty acid methyl ester with nickel-supported zeolite heterogeneous catalyst.    USE - The method is useful for preparing conjugated linoleic acid methyl ester (claimed).    ADVANTAGE - The method is capable of preparing conjugated linoleic acid methyl ester in a cost effective and eco-friendly manner with high yield rate, purity and selectivity.
NOVELTY - The fuel cell system (100) has a fuel gas flow channel (10) that is provided for supplying fuel gas emitted from a hydrogen generator (2) to a fuel cell (8). An OFF fuel gas flow channel (11) is provided for emitting OFF fuel gas containing hydrogen which is not used by a fuel cell from the fuel cell. An on-off valve (5) is provided in a downstream fuel gas flow channel and one flow path of OFF fuel gas flow channels from a branch portion. A control apparatus (7) closes on-off valve in the case of a predetermined condition, so that a material supply device (3) is operated.    USE - Fuel cell system.    ADVANTAGE - The bad effect by obstruction of the recycle gas flow path can be reduced. The flowing amount of the recycle gas in the recycle gas flow path is reduced. The excess pressure rise in each gas flow paths can be prevented. The lifetime improvement of the fuel cell system can be attained. The decline in the efficiency of the fuel cell system by stop and starting can be prevented. The deterioration of the fuel cell by lack of fuel gas can be prevented. The oxidation of the anode in the fuel cell by lack of hydrogen can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Hydrogen generator (2)    Material supply device (3)    On-off valve (5)    Control apparatus (7)    Fuel cell (8)    Fuel gas flow channel (10)    OFF fuel gas flow channel (11)    Fuel cell system (100)
NOVELTY - Nutrient combination comprises a source of phosphorus and gaseous nitrogen.    USE - The nutrient combination is useful for enhancing biogenic methane production from a carbonaceous material, where the carbonaceous material is coal, lignite, peat, drill cuttings, waste coal, coal derivatives, oil shale, oil formations, tar sands, hydrocarbon-contaminated soil and petroleum sludges (all claimed).    ADVANTAGE - The nutrient combination is substantially free of oxygen, sulfur containing oxide and/or nitrogen containing oxides (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for:    (1) preparing the nutrient combination comprising combining the phosphorus, nitrogen gas with a source of water to form an aqueous solution;    (2) enhancing biogenic methane production from a carbonaceous material comprising dispersing the nutrient combination throughout the carbonaceous material for a period of time to biogenically produce methane, and collecting methane from the carbonaceous material;    (3) a biogenic methane production system comprising the nutrient combination, a delivery system for dispersing the nutrient combination throughout the carbonaceous material, and a collector for collecting methane from the carbonaceous material;    (4) an apparatus for enhancing biogenic methane production, comprising a delivery system capable of dispersing the nutrient combination comprising the source of phosphorus and gaseous nitrogen throughout the carbonaceous material; and    (5) use of gaseous nitrogen in the nutrient combination for enhancing biogenic production.
NOVELTY - Nutrient composition comprises a source of phosphorus (P) and a source of nitrogen (N). The molar ratio of phosphorus to nitrogen (P/N) is greater than 1.5. The nitrogen concentration is 0.1-1.7 mM.    USE - The nutrient composition is useful for enhancing biogenic methane production from a carbonaceous material (claimed) in subterranean formation.    ADVANTAGE - The nutrient composition effectively enhances the biogenic methane production, and reduces cost and time of the process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a concentrate for producing the nutrient composition, where the concentrate is formulated to provide upon dilution with liquids associated with the carbonaceous material;    (2) a process for enhancing biogenic methane production from a carbonaceous material, comprising contacting the nutrient composition with the carbonaceous material for a sufficient period of time to produce methane, and collecting methane from the carbonaceous material; and    (3) a biogenic methane production system comprising a first nutrient composition, a delivery system for contacting the nutrient composition with the carbonaceous material, and a collector for collecting methane from the carbonaceous material.
NOVELTY - A SAPO-34-type molecular sieve comprises an anhydrous chemical composition comprising diisopropanolamine and silicon-aluminum-phosphorus oxide complex.    USE - SAPO-34-type molecular sieve is used for preparing catalyst for acid catalyzed reaction, catalyst for the process of preparing alkene by conversion reaction of oxygen-containing compound, and methane/carbon dioxide adsorption and separation material (all claimed).    DETAILED DESCRIPTION - A SAPO-34-type molecular sieve comprises an anhydrous chemical composition of formula: mDIPA.(SixAlyPz)O2, where DIPA is diisopropanolamine, m is the mole number of diisopropanolamine in each mole of (SixAlyPz)O2, and m is 0.03-0.25, x, y and z are the mole number of silicon, aluminum and phosphorus respectively, and x is 0.01-0.30, y is 0.40-0.60, z is 0.25-0.49 and x+y+z is 1. INDEPENDENT CLAIMS are included for the following:    (1) formation of SAPO-34-type molecular sieve;    (2) catalyst for acid catalyzed reaction;    (3) catalyst for the process of preparing alkene by conversion reaction of oxygen-containing compound; and    (4) methane/carbon dioxide adsorption and separation material.
NOVELTY - The method involves mixing brown coal, 5-15% peat moss, 12-20% straw cereals and calcium carbonate with each other. The mixed components and air are provided in a pile. Light is reflected from the pile by a prism for 14-21 days. Composting process is performed in the mixed components at 50-70 degree Celsius for 2-3 months.    USE - Method for disposing manure from silver fox farm for preparing fertilizer.
NOVELTY - A SAPO-34-type molecular sieve comprises an anhydrous chemical composition containing silicon-aluminum-phosphate-containing compound (I).    USE - SAPO-34-type molecular sieve is used formation of methane or carbon dioxide-adsorption and separation material, and catalyst for conversion reaction of oxygen-containing compounds for preparation of alkene and acid-catalyzed reaction (all claimed) e.g. methanol-to-olefin reaction.    DETAILED DESCRIPTION - A SAPO-34-type molecular sieve comprises an anhydrous chemical composition containing silicon-aluminum-phosphate-containing compound of formula: mMDEA.(SixAlyPz)O2 (I), where MDEA is N-methyldiethanolamine, m is 0.03-0.25, x is 0.01-0.3, y is 0.4-0.6, z is 0.25-0.49, and x+y+z is 1. INDEPENDENT CLAIMS are included for the following:    (1) preparation of SAPO-34-type molecular sieve;    (2) catalyst; and    (3) methane or carbon dioxide-adsorption and separation material.
NOVELTY - The indicator has a clarifier removing sediment and sludge during waste water treatment of municipal and industrial plants.    USE - Freshwater reservoir and river degradation indicator for use in a laboratory.    ADVANTAGE - The indicator estimates degradation degree in an accurate manner.
NOVELTY - The device has an electrolyzer linked with a heating network by a heat collector. The electrolyzer is utilized for emitting mixture of hydrogen, carbon dioxide and water vapor. A condenser is utilized for condensing water vapor. A conduit is utilized for transmitting the mixture of hydrogen, carbon dioxide and water vapor. A concentrated electrolyte is removed from a tank. Water and mineral salts are evaporated by utilizing valuable fertilizer.    USE - Electrochemical device for producing mixture of hydrogen, carbon dioxide and mineral salts.
NOVELTY - A chlorfenvinphos organophosphorus insecticide treating method involves setting toxic dose of chlorfenvinphos to 500 mg/dm3 such that the dose does not affect the methane sewage sludge fermentation process. The normal course of the fermentation process is determined followed by carrying out parallel anaerobic decomposition of the compound.    USE - Method for treating chlorfenvinphos organophosphorus insecticide.
NOVELTY - An alepidote fish live bait industrial culture method, involves mixing raw materials comprising brewery liquid waste, liquid methane, and chicken manure liquid to obtain nutrient liquid, and fermenting nutrient liquid for 2-3 days. The alepidote fish is inoculated in nutrient liquid, followed by culturing the liquid for 4-8 days, and collecting the alepidote fish.    USE - Method for industrial culturing of alepidote fish live bait.    ADVANTAGE - The method enables culturing alepidote fish live bait with high yield, taste and nutritional value. The method is suitable for industrial production.
NOVELTY - The method comprises adding waste water in anoxic-aerobic tank, denitrifiying with biological nitrogen, and discharging residual sludge, carrying out ultrasonic treatment at ultrasonic frequency of 20-30 KHz for 15-20 minutes to residual sludge, anaerobic fermenting treated sludge at 20-30 degrees C for 5-8 days and adjusting the pH value to 6-7, and refluxing wastewater.    USE - The method is useful for denitrifying sludge (claimed).    ADVANTAGE - The method is capable of effectively denitrifying sludge with reduced residual sludge amount.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for waste water biological nitrogen removal system.
NOVELTY - Method for culturing microalgae, involves (a) performing primary culturing by forming film-shaped structured or three-dimensional structured biofilm comprising microalgae on liquid surface of culture broth, subjecting the broth to microbial purification and obtaining primary culture in primary culture vessel, and (b) performing secondary culturing by culturing the microalgae on the liquid surface of the culture broth using seed algae culture, and at least some of film-shaped structured or three-dimensional structured biofilm formed on the liquid surface.    USE - The method is useful for culturing microalgae which is useful for preparing biofilm for preparing biomass (all claimed).    ADVANTAGE - The method is simple and cost-effective, requires minimal liquid media, and does not require usage of large amount of water.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) biofilm formed on the liquid level by the above-mentioned cultivation method;    (2) biomass acquired from the biofilm;    (3) oil obtained from the biofilm; and    (4) method for preparing biomass derived from the microalgae.
NOVELTY - The hydrogen and oxygen generator comprises a dome-shaped housing, an inlet port in which raw water is flowed to an outer tube, a vent to allow hydrogen and oxygen in the raw water, an electrolysis module for electrolyzing the raw water, a unit for discharging the electrolyzed water, a filter having micro pores, and an outlet port provided with the housing. The electrolysis module is connected with the vent. The filter is made of an inorganic material. An anion exchange resin is arranged for connecting a negative electrode of the electrolysis module.    USE - The hydrogen and oxygen generator is useful for producing oxygenated water.    ADVANTAGE - The generator produces the oxygenated water with increased oxygen and hydrogen generation rate and without generating bubble, and has simple structure.    DETAILED DESCRIPTION - The hydrogen and oxygen generator comprises a dome-shaped housing, an inlet port in which raw water is flowed to an outer tube, a vent to allow hydrogen and oxygen in the raw water, an electrolysis module for electrolyzing the raw water, a unit for discharging the electrolyzed water, a filter having micro pores, and an outlet port provided with the housing. The electrolysis module is connected with the vent. The filter is made of an inorganic material. An anion exchange resin is arranged for connecting a negative electrode of the electrolysis module. A cation exchange resin is arranged for connecting a positive electrode of the electrolysis module. A power source is arranged with the positive and negative electrodes. The micro pore is formed between the positive electrode and the negative electrode. The apparatus further comprises a thermoelectric element arranged in the negative electrode.
NOVELTY - Powdered composite Fe-C is applied to the electrode surface and synthesis is carried out for nanocrystal elements Fe-C with an average size within the range of 10-15 nm by treatment with laser pulses with wave length of 1-1.5 mcm at radiant density of 107-109 W/cm2, laser scanning rate of 8-15 cm/s, frequency of pulses of 33-60 kHz in vacuum or in argon, at that in the process melting and formation of ferric carbide Fe3C is not reached. The invention is also related to the iron-based cathode material for electrochemical production of hydrogen.    USE - Electricity.    ADVANTAGE - Modification of iron surface that allows improvement of electrocatalytic activity for such material.2 cl, 2 tbl
NOVELTY - The present invention provides a process for the preparation of azilsartan medoxomil of formula A. The invention also provides a process for the preparation of intermediates of azilsartan medoxomil.
NOVELTY - An ecological loach cultivating method involves providing base fertilizer with pleurotus eryngii slag into the shed base, where the fertilizer is made by the fermentation of mushroom residue with organic fertilizer, and transplanting chestnut 600 bundles per acre ratio of early ripening paddy to shed inside, irrigating water at depth of 20 cm. Loach breeding is performed every year in April followed by releasing organic fertilizer for every two weeks into the paddy fields in greenhouses containing chicken manure, and EM fermentation product of organic fertilizer.    USE - Method for cultivating ecological mud loach.    ADVANTAGE - The method enables avoiding water pollution, improving production rate and reducing economical investment cost.    DETAILED DESCRIPTION - An ecological loach cultivating method involves providing base fertilizer with pleurotus eryngii slag into the shed base, where the fertilizer is made by the fermentation of mushroom residue with organic fertilizer, and transplanting chestnut 600 bundles per acre ratio of early ripening paddy to shed inside, irrigating water at depth of 20 cm. Loach breeding is performed every year in April according to the proportion of 10 pounds per acre, at ratio of male and female loach of 3:2, followed by releasing organic fertilizer for every two weeks into the paddy fields in greenhouses containing chicken manure, and EM fermentation product of organic fertilizer.
NOVELTY - A hydrogen generating apparatus (100) has splitter (1) which separates sulfur compound in source gas, desulfurizer (2) where sulfur compound in the source gas which passed the splitter is removed, modifier (3) which produces hydrogen-containing gas using source gas, 1st gas flow path (11) which passed the splitter and where source gas which flows in into the modifier flows, 2nd gas flow path (12) which supplies sulfur compound separated using splitter to a combustor (4), and combustor which burns the sulfur compound supplied through the 2nd gas flow path using the hydrogen-containing gas.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - Hydrogen generating apparatus and fuel cell system suppresses the increase in capacity of desulfurizer when the sulfur concentration in source gas is high.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Splitter (1)    Desulfurizer (2)    Modifier (3)    Combustor (4)    1st gas flow path (11)    2nd gas flow path (12)    Hydrogen generating apparatus (100)
NOVELTY - The cell (40) has a cylindrical body (10) provided for introducing a sample gas to an inner side. A surface mirror (2) is arranged such that a part of the cylindrical body is closed. An injection window (21) is formed for allowing light to go to a reflective surface of the surface mirror inside the cylindrical body for injection. An emission window (22) allows light to be emitted from an inside of the cylindrical body, where a transparent window panel (31) is formed as a disk-shaped structure and arranged ahead of the reflective surface of the surface mirror.    USE - Multipath reflection type gas cell for use in a gas analyzing apparatus for measuring density of trace component in air. Uses include but are not limited to nitrogen compound, sulfur compound, hydrogen sulfide, sulfur oxide, nitrogen oxide, carbon dioxide, methane and ammonia.    ADVANTAGE - The transparent window panel is arranged ahead of the reflective surface of the surface mirror, so that the cell can be easily maintainable, without necessity to exchange the surface mirror for a long period of time, thus reducing running cost of the cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gas analyzing apparatus.    Surface mirror (2)    Cylindrical body (10)    Injection window (21)    Emission window (22)    Transparent window panel (31)    Multipath reflection type gas cell (40)
NOVELTY - The device has ambient temperature measuring device that measures outside temperature and ambient temperature of hydrogen generating apparatus (1). A reformation thermometer measures temperature of reforming reaction portion (2). A material supply device (7) supplies raw material to apparatus. A controller (17) adjusts raw material feed rate based on thermometer measured temperature. The controller increases raw material feed rate, when temperature is more than outside temperature by which measurement temperature of measuring device is predetermined.    USE - Fuel cell power generating device.    ADVANTAGE - Since the controller can increase the raw material feed rate, when the temperature is more than one temperature by which measurement temperature of the ambient temperature measuring device is predetermined, the fall amount of hydrogen supplied to the fuel cell can be suppressed. Hence the power generation stop of the fuel cell can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the fuel cell power generating device. (Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Reforming reaction portion (2)    Material supply device (7)    Controller (17)    Ambient temperature sensor (18)
NOVELTY - A composting system comprising a series of in-line communicated endless conveyors arranged in a step-like manner allowing gravitational transfer of material from one conveyor to the other. It also comprises successive process of sorting, shredding, sorting, dewatering, mixing and treatment. The liquid extract is subjected to pasteurization and analysis before bottling.    USE - Composting system (claimed).
NOVELTY - A Sedum lineare block and its production method are claimed. The S.lineare block comprises plastic frame comprising plastic housing having filter layer, base material layer, and S.lineare layer, respectively from bottom to top, where the frame has projections at the bottom surface, and top surface with counter-edges on both sides, and base material layer is set on the upper layer of nutrient material.    USE - The S.lineare block is useful as green roofing.    ADVANTAGE - The method solves the problems caused by green turf grass seedlings such as post-maintenance problems, roots that damages the roof, inconvenient transportation and other technical problems.    DETAILED DESCRIPTION - A Sedum lineare block and its production method are claimed. The S.lineare block comprises plastic frame comprising plastic housing (1) having filter layer (4), base material layer (3), and S.lineare layer (2), respectively from bottom to top, where the frame has projections at the bottom surface, and top surface with counter-edges on both sides (6), and base material layer (3) is set on the upper layer of nutrient material. The base material layer (3) is prepared by mixing 50% mushroom growth material, humus containing 20% saw dust, 10% wheat chaff, 10% humus soil, 5% common soil, 5% animal excrement or poultry manure or its combination, fermenting at high temperature for 15 days, and disinfecting by adding 2% nitrogen fertilizer, 2% phosphate fertilizer, and 2% potash fertilizer per m3 on the fermented nutrient base.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sedum lineare block.    Plastic housing (1)    Sedum lineare layer (2)    Base material layer (3)    Filter layer (4)    Water draining hole (5)    Counter-edges on both sides (6)
NOVELTY - Producing hydrogen, comprises (a) mixing solid acid catalyst and carbon material to prepare solid acid mixture, and introducing the above prepared solid acid mixture into a reactor, (b) introducing raw material mixture containing vaporized methane, alcohol and water into the reactor, (c) decomposing raw material mixture by a catalyst to generate hydrogen, and (d) discharging generated hydrogen outside the reactor.    USE - The method is useful for producing hydrogen (claimed).    ADVANTAGE - The method is safe, economic and environmentally friendly, and maintains stability of the catalyst.
NOVELTY - The method involves filtering salt solution or suspension and compressing the filtered solution at a pressure of 20-40 kg/cm2 and at 80-90 degrees C, where the filtered solution is sent through heat exchangers (6,8,9,35,10). The solution from the heat exchangers is transferred to a separator (13) in which a concentrated brine is obtained which falls to bottom of the separator. The formed water vapor is compressed and sent to the heat exchanger and a storage tank (5) including another heat exchanger (6).    USE - Method for producing distilled water, dried and classified salts, electricity, hydrogen and oxygen from a saline solution or suspension.    ADVANTAGE - The method provides desalination of saline solutions and suspensions, and produces electricity, oxygen and hydrogen in a simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a plant for implementing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of plant scheme used for implementing or performing the method.    Pump (1)    Primary screen (2)    Storage tank (5)    Heat exchangers (6,8,9,35,10)    Vacuum pump (40)
NOVELTY - A saccharification performance is evaluated by pretreatment process which makes cellulose biomass contact alkaline solution, saccharification process which saccharifies cellulose biomass after pretreatment process with hydrolase, measuring amount of alkali metal derived from hydroxide and/or alkaline-earth metal which is contained in cellulose biomass after pretreatment process in the middle of pretreatment process and which is contained in alkaline solution, and evaluating based on the amount of measured alkali metal and/or alkaline-earth metal.    USE - Evaluation of saccharification performance (claimed).    ADVANTAGE - Evaluation is fast and costs low.    DESCRIPTION OF DRAWING(S) - The drawing shows a characteristic view of the relationship between the amount of sodium contained in cellulose biomass of an after preprocessing, and the saccharification rate of hexose about the cellulose biomass used as an example. (Drawing includes non-English language text).
NOVELTY - This new type utility claims a full automatic biologic bacterial manure one continuous production system, comprising: a carrier sterilizing system, liquid expanding system, mixing packing system, hot recycling system, a central control system, the carrier system of sterilizing device to 2-1-2 mode establishing, in storage box in the fermentation tank set with liquid level sensor, hot recycling system and the allixiary double-heating box are arranged in parallel. This utility new type of follows: to (2-1-2) way of establishing carrier sterilizing system valid improves the carrier sterilizing, speed of drying, continuous production provide powerful guarantee of the of the liquid level sensor in the fermentation tank can be sent signal, fermenting automatically refilling acid into material liquid to fully, inoculating amount relatively increases, increasing the base rear fermentation bacteria number obtain; hot recycling system machine in parallel, high efficiency of using energy; to PLC controller as the core of the central control system so that THE PH value, DO value and temperature and count of bacterial liquid obtain control of digital amount, the bacteria liquid so as to obtain the mass.
NOVELTY - Soil modifying agent comprises (in wt.%): rock powder (0.3-0.6) containing more than 25% silicon, amino acid powder (6.3-8.6), phosphate (12.9-18.8), dihydrogen phosphate (8.6-12.6), potassium salt (15.6-24.4), urea (19.8-26.6), peat (8.9-12.2), shell powder containing calcium carbonate powder (3.2-5.2) and serpentine powder (3.7-11.7).    USE - Soil modifying agent.    ADVANTAGE - The soil modifying agent recovers soft agricultural land, and has improved production quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil modifying agent, which involves:    (A) adding silicon-containing more than 25% of petrochemical powder and amino acid powder at 10 degrees C;    (B) placing a plant to ferment for 3 days;    (C) mixing semi-finished product with phosphate, dihydrogen phosphate and potassium salt;    (D) mixing the obtained product and fermenting the obtained product at 10 degrees C in a fermenter for 15 days until acid aroma taste (such as smoked plum flavor); and    (E) mixing the obtained mixture with urea, peat, shell powder containing calcium carbonate and serpentine powder to obtain soil modifying agent.
NOVELTY - Fabricating refuse-derived fuel using organic sludge, comprises (a) injecting organic sludge, (b) decomposing organic sludge by supplying hydroxy radical using hydroxy radical generating device to the injected organic sludge, (c) mixing a thermal medium with decomposed organic sludge, and heat treating using a drying reactor, and (d) removing volatile organic compounds obtained from the step (c).    USE - The method is useful for fabricating refuse-derived fuel using organic sludge (claimed).    ADVANTAGE - The method increases sludge drying rate, does not require electrical energy, is economical, minimizes the loss of energy required for drying process. The device is suitable for processing waste of sewage treatment plant, sludge of wastewater treatment plant, food waste and livestock waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for refuse-derived fuel device, comprising a quantitative input unit (10) for injecting organic sludge, a hydroxy radical generating unit (20) for supplying hydroxy radicals into the organic sludge provided within the quantitative input unit, a mixing unit for forming a mixture of heated thermal medium and organic sludge decomposed by the hydroxy radicals, a drying reactor (50) for performing dry reaction, where the organic sludge is processed by hydroxy radicals generated within the hydroxy radical generating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the refuse-derived fuel fabricating device (Drawing includes non-English language text).    Quantitative input unit (10)    Hydroxy radical generating unit (20)    Hydroxy radical distributor (30)    Drying reactor (50)    Screw (54)
NOVELTY - The device has temperature controller (500) that regularly maintains the temperature of the inner portion of drum (100) by covering the drum exterior. A collection box (400) stores and receives the food waste ejected from the drum. A feeding unit (300) sends the food waste to the drum inner portion and stores the arbitrarily gathered food waste. A vent is formed between the segmented spaces for storing the food waste. A shaft is installed inside the drum in which the moving area is formed for moving an amount of the food waste in the upper portion of each partition wall.    USE - Device for processing of food waste collected in home or restaurant etc.    ADVANTAGE - The food waste can be conveniently processed, while arbitrarily gathering an amount of the food waste. The condensed water congealed in the drum ceiling is discharged to the outside in short processing time.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the device for processing of food waste.    Drum (100)    Feeding unit (300)    Collection box (400)    Temperature controller (500)    Clean water filter (700)
NOVELTY - The structure (100) has guide tube that is installed between the guide groove of the toilet bowl (108). A decomposing unit (110) receives the waste from the toilet bowl which is installed at the inner one-side of the housing (102) which are connected in the lower side of the toilet bowl. A protrusion unit is installed in the inner surface of the guide tube. A waste disjoint device accommodates the enzyme mixture including the opening/closing plate according to the rotation of the rotating unit electrically connected to the control unit (112).    USE - Bathroom structure used in ship.    ADVANTAGE - The dry decomposition of the waste comprising the microorganism can be achieved with high environment-friendly effect, since the waste disjoint device accommodates the enzyme mixture including the opening/closing plate according to the rotation of the rotating unit electrically connected to the control unit. The bacteria of the resolution and host of the viral contamination can be prevented without notice speculation of urine and feces.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the bathroom structure.    Bathroom structure (100)    Housing (102)    Toilet bowl (108)    Decomposing unit (110)    Control unit (112)
NOVELTY - Preparation of 2-(4-morpholinothio)benzothiazole involves adding morpholine to the reactor, dissolving accelerator M sodium hydroxide solution in the morpholine-containing reaction vessel, continuing stirring, adding hydrogen peroxide with concentration of 10-12% to the reaction vessel, continuing stirring, reacting at 40 degrees C plus minus 2 degrees C under stirring reaction, obtaining 2-(4-morpholinothio)benzothiazole crude product, filtering, washing and drying.    USE - Preparation of 2-(4-morpholinothio)benzothiazole (claimed).    ADVANTAGE - The 2-(4-morpholinothio)benzothiazole is efficiently prepared with improved production capacity, yield of 92% and purity of 99.5% without polluting the environment.    DETAILED DESCRIPTION - Preparation of 2-(4-morpholinothio)benzothiazole involves adding morpholine to the reactor, dissolving accelerator M sodium hydroxide solution in the morpholine-containing reaction vessel, continuing stirring, adding hydrogen peroxide with concentration of 10-12% to the reaction vessel, continuing stirring, reacting at 40 degrees C plus minus 2 degrees C under stirring reaction, obtaining 2-(4-morpholinothio)benzothiazole crude product, filtering, washing and drying. The molar ratio of morpholine and accelerator M is 1.0l-2:1. The molar ratio of hydrogen peroxide and promoter is 1.01-2:1.
NOVELTY - Particle of microbial fertilizer comprises culture solution containing probiotic endospores, aqueous solution of polyol, biodegradable filler material, bio-degradable polymer, and nutritive substance which are well-mixed.    USE - As particle of microbial fertilizer.    ADVANTAGE - The particle of microbial fertilizer extends storage time of microbial fertilizer and maintains viability of probiotics.
NOVELTY - Producing (M1) carbon-enriched biomass material involves: (i) providing lignocellulosic material as starting material; (ii) subjecting the starting material to treatment at elevated temperature under partially oxidizing conditions in reaction vessel; (iii) opening of the reaction vessel; and (iv) optionally separating solid products from reaction mixture.    USE - For producing carbon-enriched biomass material used in combustion processes, particularly in dust firing systems (claimed).    ADVANTAGE - The carbon concentration of solid product is enriched by 5-25 wt.% (preferably 8-15 wt.%), as compared to the carbon concentration of starting material. The carbon-enriched biomass material has an improved energy balance with reduced generation of harmful organic by-products, with improved property profile and superior quality. The heat generated by the partial oxidation can directly be used within the reaction vessel, thus improving the overall energy balance of reaction. The partial presence of oxygen reduces the formation of harmful organic compounds and volatile organic compounds (VOCs) in the production process. The carbon-enriched biomass material obtained by the present method has reduced concentration (by up to 80%) of harmful VOCs and stinky compounds as compared to carbon-enriched biomass material which is prepared at pyrolytic conditions (in the absence of O2 or O2 donors). The dried carbon-enriched biomass and particularly the pellets are odorless. The pre-dried and carbon-enriched biomass as well as the pellets can easily be ground.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) carbon-enriched biomass material obtained by the method (M1); and    (2) pellets containing carbon-enriched biomass material.
NOVELTY - The method involves arranging electrode layers on electrolyte layers. One of the electrolyte layers is extended through a thermal expansion part. A pinhole is formed in one of the electrolyte layers. A surface part of one of the electrolyte layers is fixed in an electrolyte layer formation stage.    USE - Fuel cell manufacturing method.    ADVANTAGE - The method enables improving pinhole structure appearance. The method enables improving particles grow manufacturing of the electrolyte layers. The method enables preventing power leakage problem through the electrolyte layers due to short circuit.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a fuel cell manufacturing method.'(Drawing includes non-English language text)'
NOVELTY - The method involves conveying a strip-shaped component i.e. web-like electrolytic part (W), by an unwinding roller of a conveying apparatus through a conveyance process. The strip-shaped component is cleaned by using a disposable cleaning sheet (S) i.e. urethane gel material, through a cleaning process. Tension strength of to-be-cleaned strip-shaped component is larger than tension strength of a to-be-conveyed strip-shaped component. A dancer roller (D4) is fixed by inserting a pin (20) between a rotating shaft (10) and a roller (14) among arm parts.    USE - Method for operating a conveying apparatus for conveying a web-like electrolytic part during a fuel cell manufacturing process.    ADVANTAGE - The method enables conveying a strip-shaped component by the unwinding roller of the conveying apparatus through the conveyance process and cleaning the strip-shaped component by the disposable cleaning sheet through the cleaning process so as to suppress abrasion difficulty into the unwinding roller.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a conveying apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a state in which adhesive force of a surface of a cleaning sheet is strong at time of cleaning.    Dancer roller (D4)    Disposable cleaning sheet (S)    Web-like electrolytic part (W)    Rotating shaft (10)    Roller (14)    Pin (20)
NOVELTY - The system (10) has a first batch processing oven (12) for generating syngas. A second batch processing oven (14) generates the syngas. A thermal treatment chamber (20) heats the syngas. An energy converter (22) converts energy from the syngas to electrical energy. The thermal treatment chamber includes a burner for burning the syngas without combusting the syngas, where the energy convertor includes a heat recovery unit for recovering heal from the burning gases. Third and forth batch processing ovens generate the syngas. A control unit (30) controls supply of the syngas.    USE - System for generating energy from waste material e.g. organic waste and municipal solid waste (MSW).    ADVANTAGE - The thermal treatment chamber heats the syngas, where the energy converter converts energy from the syngas to electrical energy, thus improving processing waste material and generating electrical energy in an efficient manner with improved overall efficiency and cost effectiveness.    DETAILED DESCRIPTION - The energy converter includes a syngas engine. The synthetic gas is selected from a group consisting of carbon monoxide and hydrogen. An INDEPENDENT CLAIM is also included for a method for generating energy from waste material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for generating energy from waste material.    System for generating energy from waste material (10)    Batch processing ovens (12, 14)    Thermal treatment chamber (20)    Energy converter (22)    Control unit (30)
NOVELTY - The invention relates to a process for increasing the thermal power of sawdust briquettes with a view to increasing the energy efficiency of wood biomass. According to the invention, the process starts with sawdust sorting and ensilaging into the silage (1), followed by treating it within the torrefaction installation (2) at a temperature of 260 degrees C for 5 minutes, along with the compulsory drying operation, until a humidity in the range of 8...10% is reached, then storing the sawdust into the silage (3) and briquetting the same in the briquetting machine (4) which increases the thermal power, the thermal power being determined by means of a calorimetric bomb (7).
NOVELTY - The gasifier has several conjoined and vertically positioned tubes having a proximal end and a distal end. The proximal end of tube is provided with an inlet (301), and the distal end is provided with an outlet (303). Three contiguous reaction zones are pyrolysis zone (20), oxidation zone (30) and reduction zone (40). Two separate rings of pressurized plano air inlets are configured to deliver adjustable volumes and pressures of oxidant streams. The separate rings are located around the perimeter of oxidation zone.    USE - Gasifier such as downdraft gasifier and updraft gasifier used for gasification of feedstock, solid biomass, and household and industrial waste.    ADVANTAGE - The feedstock to be controlled is passed through the oxidation zone with minimal restriction, so as to improve the overall volume and flow of feedstock passing through the gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the gasifier illustrating the densest portion of induced and entrained gradient.    Pyrolysis zone (20)    Oxidation zone (30)    Reduction zone (40)    Inlet of tube (301)    Outlet of tube (303)
NOVELTY - Manufacture of polystyrene-type resin extrusion foaming board involves extruding/foaming a foamable molten resin composition formed by mixing polystyrene-type resin composition containing flame retardant and physical foaming agent. The polystyrene-type resin composition is obtained by melt-kneading crushed material of regenerated polystyrene-type resin extrusion foam containing flame retardant mixture of 2,2-bis(4-(2,3-dibromo-2-methyl-propoxy)-3,5-dibromophenyl)propane and other halogenated flame retardant.    USE - Manufacture of polystyrene-type resin extrusion foaming board used for heat-insulating material and tatami base material for floor, wall and roof of building.    ADVANTAGE - The polystyrene-type resin extrusion foaming board is manufactured efficiently with excellent foaming stability, thermal-insulation property and flame retardance, by simple method.
NOVELTY - Nutritional healthcare disease-resistant drought-resistant organic fertilizer comprises 300 pts. wt. sludge waste, 200 pts. wt. cassava residue, 300 pts. wt. bovine/chicken manure, 10 pts. wt. bacterial enzymes, 40 pts. wt. fulvic acid, 10 pts. wt. chitin powder, 10 pts. wt. retention agent, 20 pts. wt. tea bran, 20 pts. wt. nitrogen, 50 pts. wt. phosphorus, 20 pts. wt. potassium and 30 pts. wt. trace elements.    USE - Nutritional healthcare disease-resistant drought-resistant organic fertilizer.    ADVANTAGE - The fertilizer is inexpensive and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of the fertilizer comprising taking sludge waste, cassava residue and manure, crushing, adding water, adding enzymes, mixing, fermenting at 15-30 degrees C, cooling, adding remaining raw materials and mixing.
NOVELTY - The system (1) has volumetrical feeder (40) that supplies the predetermined amount of the paper and timber. A crusher (31,32) crushes the synthetic resin selected from the waste material to a predetermined size. A paper and the timber are discharged with a volumetrical feeder (40), and the synthetic resin is discharged with a volumetrical feeder (42). The paper, timber and synthetic resins are supplied from the volumetrical feeders. A controller (95) controls the feed rate of volumetrical feeders.    USE - System for manufacturing solid-fuel for discarding waste materials such as timber waste, paper and synthetic resin material generated in large quantities from home, production plant, processing plant, etc.    ADVANTAGE - The solid fuel with the emitted-heat amount is stably manufactured, while fixing quality of a solid fuel. The quantity with constant solid fuel and fixed heat amount is maintained by supplying raw material in a compression molding machine in a predetermined ratio.    DETAILED DESCRIPTION - A dehydrator dehydrates the slag material which squeezes the oil-based component from the plant containing a fats-and-oils component, or the plant raw material consisting of the waste material of the plant. The crusher crushes the plant raw material to the size of predetermined amount. A drying machine dries the raw material. The synthetic resin is selected from the waste material. The predetermined amount of the synthetic resin is crushed and dried, while the synthetic resin is emitted by predetermined ratio. An INDEPENDENT CLAIM is included for method for manufacturing solid-fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the system for manufacturing solid-fuel.(Drawing includes non-English language text)    System for manufacturing solid-fuel (1)    Drying machine (15)    Crushers (31,32)    Volumetrical feeders (40,42)    Controller (95)
NOVELTY - The boiler has a countercurrent gasifier (1), combustion chamber (8), low-emission burner (7), and heat exchanger (10). The countercurrent gasifier is used for performing gasification of biomass with primary air on movable grate or on fixed grid. A movable grid (2) is used to perform automatic discharge of ash in countercurrent process during gasification of biomass. The heat exchanger is placed at output unit of combustion chambers for power generation.    USE - Heating boiler for performing combustion of wood chips for producing biomass.    ADVANTAGE - Since the movable grid is used to perform automatic discharge of ash in countercurrent process during gasification of biomass, the emission of dust or hazard gas such as hydrogen, carbon monoxide, methane, as well as long-chain hydrocarbon compounds to environment is prevented effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the heating boiler for performing combustion of wood chips for producing biomass.    Countercurrent gasifier (1)    Movable grid (2)    Low-emission burner (7)    Combustion chamber (8)    Heat exchanger (10)
NOVELTY - A polyester film is obtained using polyester having repeating units of dicarboxylic acid unit and diol unit. At least one of dicarboxylic acid unit and diol unit is derived from biomass resources. The amount of terminal carboxyl groups in the polyester is 50 equivalent/tonne or less. The sulfur atom content in the polyester is 0.0001-10 ppm.    USE - Polyester film is used for e.g. packaging material and building materials. Uses include but are not limited to plastic, aluminum foil, food product, chemicals, powdered or granular material, agricultural materials, electric equipment material, household appliance, housing, motor vehicle material, etc.    ADVANTAGE - The polyester film is safe and environmentally-friendly, and is produced using polyester obtained from biomass-resources, in order to save fossil fuel resources. Raw materials of polyester composition are economical. Supply of raw materials is very stable. The mass balance of absorption and emission of carbon dioxide is effectively balanced in the manufacture process. During manufacture process, generation of hazardous materials and offensive odor are suppressed. Deterioration of physical properties of product is prevented, by suppressing hydrolysis which is accelerated by impurity.
NOVELTY - Producing biofuel involves refining biodiesel obtained from castor oil by using a calcium oxide catalyst, and then water is removed to purify it. The castor oil is subjected to distillation and purification processes and then separated through a mechanical force or centrifugal filtration to obtain a product. Oxidative stabilizer and cetane are added into the product to improve biodiesel property.    USE - Method for producing biofuel used as biodiesel substituent.    ADVANTAGE - The method enables to produce biofuel has high biocumbustible, cetane index and oxidative stability.
NOVELTY - A proton exchange membrane-type water electrolysis device comprises front end plate (1), front end plate washer (2), front anode plate (3), sealing gasket (4), membrane electrode (5), sealing gasket (6), female bipolar plate (7), sealing gasket (8), membrane electrode (9), sealing gasket (10), back anode plate (11), back end plate gasket (12), and back end plate (13).    USE - Proton exchange membrane-type water electrolysis device.    ADVANTAGE - The device is capable of working under mild conditions, has high efficiency, high-purity gas, simple operation, and efficient and renewable solar cell and fuel cell energy system.    DETAILED DESCRIPTION - A proton exchange membrane water electrolysis device comprises front end plate (1), front end plate washer (2), front anode plate (3), sealing gasket (4), membrane electrode (5), sealing gasket (6), female bipolar plate (7), sealing gasket (8), membrane electrode (9), sealing gasket (10), back anode plate (11), back end plate gasket (12), and back end plate (13). The back end plate acts as clamping and positioning member. The back end plate gasket acts as insulation between female bipolar plate and back end plate gasket. Each plate is provided with flow field, external power supply, electrolytic water for gas-liquid uniform energy distribution, and membrane electrode.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of water electrolysis device proton exchange membrane.    Front end plate (1)    Front end plate washer (2)    Front anode plate (3)    Sealing gasket (4)    Film electrode (5)    Sealing gasket (6)    Female bipolar plate (7)    Sealing gasket (8)    Membrane electrode (9)    Sealing gasket (10)    Back anode plate (11)    Back end plate gasket (12)    Back end plate (13)
NOVELTY - A noble metal methanation catalyst is prepared by solution combustion method using 1-10 wt.% noble metal oxide and 90-99 wt.% carrier.    USE - Catalyst is used for micro carbon monoxide methanation process (claimed).    ADVANTAGE - The catalyst has favorable catalytic property.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of noble metal methanation catalyst, which involves adding noble metal nitrate, nitrate carrier, soluble organic fuel and hole structure-modifying agent in aqueous solution containing 0.6-1.2 g solute in 1 ml water, microwave heating with microwave wavelength of 10-20 cm, heating, collecting combustion powder, grinding and granulating; and    (2) usage method of noble metal methanation catalyst, which involves activating the catalyst under reducing gas containing 85-95 vol.% nitrogen and 5-15 vol.% hydrogen with space velocity of 1000-12000 mL/g.hour, maintaining temperature at 450-600 degrees C under normal pressure, then adding activated catalyst into fixed bed for removing micro carbon monoxide methanation process, reacting at 250-650 degrees C under pressure of 1-4 Mpa with air speed of 5000-100000 mL/g.hour.
NOVELTY - Drum screen type apparatus useful for treating food wastes using microorganism comprises cylindrical housing in which motor is installed in other side which is the opposite side central part of the entrance, drum, and multiple medias.    USE - The drum screen type apparatus is useful for treating food wastes (claimed).    ADVANTAGE - The apparatus is cost-effective.    DETAILED DESCRIPTION - Drum screen type apparatus useful for treating food wastes using microorganism comprises cylindrical housing in which motor is installed in other side which is the opposite side central part of the entrance, drum, and multiple medias, where the entrance is formed in one side of the horizontally located central part and which transversely lies down, the drum of the screen-based in which it is installed inside the housing, it is fixed to the rotary shaft of the motor installed in the horizontal direction and it is rotated, and multiple holes are formed, multiple medias which is located inside the drum, and the microorganism disassembling the food waste is adhered to the surface.
NOVELTY - Method for manufacturing fertilizer involves mixing organic substance and additive and fermenting the organic substance by microorganisms, where the additive dispersing oxygen generation substance to biodegradable resin.    USE - The method is useful for manufacturing fertilizer (claimed).    ADVANTAGE - The method enables fertilizer formation of the orgnic substance in simple installation and stably. Even if the apparatus has simple structure which does not use air blower, it maintains the environment suitable for activity of an aerobic microbe and maintains fermentation-decomposition by aerobic microbe stably.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) additive for fertilizer formation obtined by dispersing the biodegradable resin to oxygen generation substance, fermenting the organic substance by microorganisms, and adding to the organic substance;    (2) manufacturing method of the additive involves mixing the oxygen generation substance with the melted biodegradable resin;    (3) method for processing fertilizer formation involves carrying out the fertilizer formation process of the organic substance within container, sealing the container at the time of fertilizer formation process, and dispersing the additive to the oxygen generation substance with respect to biodegradable resin with organic substance, mixing and accomadating in the container; and    (4) fertilizer formation processing apparatus.
NOVELTY - Fabricating water insoluble, low equivalent weight perfluorinated polymer electrolyte materials comprises: (a) providing a low equivalent weight perfluorinated polymer resin including perfluorinated carbon-carbon backbone; (b) exposing the perfluorinated polymer resin to ammonia gas to convert the sulfonyl fluoride groups to sulfonamide groups; and (c) contacting the perfluorinated polymer in sulfonamide form with chemical agents to convert sulfonamide to sulfonimide in a 3-dimensional cross-linked, low equivalent weight, water-insoluble perfluorinated polymer electrolyte material.    USE - The method is useful for fabricating and producing water insoluble, low equivalent weight perfluorinated polymer electrolyte materials (all claimed), which are useful in proton exchange membrane fuel cells for generating electric current and for automobile applications.    ADVANTAGE - The method is capable of fabricating the water insoluble, low equivalent weight perfluorinated polymer electrolyte materials with good chemical and mechanical stability, and provides the proton exchange membrane with high proton conductivity and fuel cell performance.    DETAILED DESCRIPTION - Fabricating water insoluble, low equivalent weight perfluorinated polymer electrolyte materials comprises: (a) providing a low equivalent weight perfluorinated polymer resin including perfluorinated carbon-carbon backbone and perfluorinated side chains that extend from the perfluorinated carbon-carbon backbone chain via an ether linkage and terminate in a sulfonyl fluoride; (b) exposing the perfluorinated polymer resin to ammonia gas to convert the sulfonyl fluoride groups to sulfonamide groups; and (c) contacting the perfluorinated polymer in sulfonamide form with one or more chemical agents to convert sulfonamide to sulfonimide in a 3-dimensional cross-linked, low equivalent weight, water-insoluble perfluorinated polymer electrolyte material.
NOVELTY - A catalytic electrode is obtained by depositing an active layer comprising a catalyst based on noble metal, preferably platinum, on a support comprising a composite consisting of proton-conducting heteropoly compound salt of phosphotungstic acid and electroconductive additives, such as carbon nanomaterial and doped tin dioxide, and hydrophobic additive, preferably PTFE.    USE - Production of catalytic electrode based on heteropoly compounds, for hydrogen and methanol fuel cells.
NOVELTY - Inflatable roof (2) for a fermentation tank (1) of a biogas plant, comprises at least two vertically superposed sheets fastened in gas-tight manner on the edge of a silage tank (3). At least one of these films (4) is used as an outer protective film for protection against mechanical damage and at least one is used as gas-tight inner biogas film. The inflatable air is introduced into the interior space between the protective film and biogas film via an air blower and a connecting piece, which supports the protective film and is durable on the biogas film.    USE - The film is useful for a conical or dome-shaped inflatable roof which is useful for a fermentation tank of a biogas plant (all claimed).    ADVANTAGE - The inflatable roof: has improved thermal insulation; and maintains the yield of thermal energy and electrical energy constantly at a high level.    DETAILED DESCRIPTION - Inflatable roof (2) for a fermentation tank (1) of a biogas plant, comprises at least two vertically superposed sheets fastened in gas-tight manner on the edge of a silage tank (3). At least one of these films (4) is used as an outer protective film for protection against mechanical damage and at least one is used as gas-tight inner biogas film. The inflatable air is introduced into the interior space between the protective film and biogas film via an air blower and a connecting piece, which supports the protective film and is durable on the biogas film. At least one spacer (9) is provided within the interior space and be filled with inflatable air, between the protective film and biogas film. An INDEPENDENT CLAIM is also included for a fermentation tank of a biogas plant comprising the inflatable roof.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic side view of an inflatable roof.    Fermentation tank (1)    Inflatable roof (2)    Silage tank (3)    Films (4)    Spacer (9)
NOVELTY - The device includes a rotatable, spring installation unit provided inside an agitation unit, a feeder for supplying sample to the agitation unit, a waterway, channels connected to a check valve, multiple nozzles connected to a side of a stirring unit, an axle hole unit positioned in a center of a vertical transfer unit, a protrusion unit connected in a down side of the spring installation unit, multiple grooves arranged in outer side of the vertical transfer unit, a sawtooth unit provided with an elevator plate, and a hollow shifter pipe connected with a lower part of a circular plate unit.    USE - The device is useful for preparing fuel from livestock excretions (claimed).    ADVANTAGE - The device effectively prepares the fuel from the livestock excretions with improved performance.    DETAILED DESCRIPTION - The device comprises a rotatable, spring installation unit provided inside an agitation unit, a feeder for supplying sample to the agitation unit, a waterway, channels connected to a check valve, multiple nozzles connected to a side of a stirring unit, an axle hole unit positioned in a center of a vertical transfer unit, a protrusion unit connected in a down side of the spring installation unit, multiple grooves arranged in outer side of the vertical transfer unit, a sawtooth unit provided with an elevator plate, a hollow shifter pipe connected with a lower part of a circular plate unit, an elevator plate connected with the waterway, a supply pump installed on the protrusion unit, a control unit for controlling supplying rate of the water inside the agitation unit, and a sensor for sending the measured value of up and down movements of the circular plate unit to the control unit. The vertical transfer unit is provided with a center of an agitating blade. The check valve is connected with one end of a cylinder rubber body. A cut-out unit is connected with other end of the rubber body.
NOVELTY - Waste processing apparatus comprises an input hopper (110) injects combustible waste; a hopper unit (100) including a main body (120) set with a hopper transport unit connected with the input hopper to convey the waste; a crushing unit (200) installed on the rear end of the main body to crush the waste; and a packing unit (300) to pack the crushed waste into fuel. The rear end of the main body includes multiple branched pathways. The hopper unit includes a separate unit installed on the main body with one side opening of the pathways, and selectively opens/closes pathways to separate waste.    USE - Used as a waste processing apparatus.    ADVANTAGE - The apparatus facilitates utilization and recycling of resources.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of waste processing apparatus.    Hopper unit (100)    Input hopper (110)    Main body (120)    Crushing unit (200)    Packaging unit (300)
NOVELTY - Outer peripheral surface of molded product after compressing the raw material containing plastic waste to which the foodstuff adhered, is heated and melted. The resultant molded product is cut to specified length dimension. Inner portion of bag component is pressure-reduced, and an opening portion of the bag component is sealed airtightly after accommodating the lump of the cut molded product in flexible bag component.    USE - Manufacture of fuel lump from foodstuff-adhered waste material generated from manufacturing plant of food, supermarket, and convenience store.    ADVANTAGE - The method efficiently provides fuel lump having dimension corresponding to installation, by simple method. Since the lump of cut molded object is accommodated in bag component and inside is air-evacuated, also when the foodstuff is adhered to the outer peripheral surface of lump of the molded product, the odor of the foodstuff adhering to an inside leaks outside, and putrefaction is not produced from the raw material.
NOVELTY - Photosynthetic system (900) comprises a photoactive material (400) comprising photocatalytic capped colloidal nanocrystals, where methane and water are produced by a carbon dioxide (804) reduction process in the presence of hydrogen.    USE - The photosynthetic system is useful in hydrogen and methane production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a photosynthetic method comprising passing water from a first reaction vessel (802) through a region having a first photoactive material, where the first photoactive material has semiconductor nanocrystals, exposing the first photoactive material to emitted light (706) having energy greater than that of the band gap of semiconductor nanocrystals within the first photoactive material, migrating hydrogen and oxygen through an opening into a gas collecting chamber comprising a permeable membrane that transfers hydrogen to a second reaction vessel, passing the hydrogen and carbon dioxide through a second photoactive material having semicondutor nanycrystals prior to entering a second reaction vessel, injecting carbon dioxide into the second reaction vessel, and exposing the second photoactive material to emitted light with energy higher than that of the band gap of semiconductor nanocrystals with the second photoactive material.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a photosynthetic system.    Photoactive material (400)    Light (706)    Reaction vessel (802)    Carbon dioxide (804)    Photosynthetic system (900)
NOVELTY - Method of producing biogas in periodic or continuous mode includes preparation of a substrate, anaerobic fermentation in mesophilic conditions, continuous removal of biogas from the biogas apparatus and removing the fermented mass the methane tank. A buffer agent primarily containing calcium carbonate is added during preparation of the substrate.    USE - Chemistry.    ADVANTAGE - Invention increases biogas output, levels down the effect of above-normal souring of fermented substances, prevents delay and complete stoppage of the process of splitting organic substances, and prevents slow-down of the methane fermentation process.12 cl, 2 tbl, 10 ex
NOVELTY - Invention relates to spacecraft hardware, particularly to electric power plants. Proposed electrolysis unit comprises solid-polymer electrolytic cell connected to spacecraft power supply system and water supply system. The latter incorporates circulation pump, water circulation oxygen and hydrogen circuits. Each said circuit comprises appropriate chamber of electrolytic cell and gas separator composed by rotary separator. Separators are connected with DC electric drive of circulation pump. This electric drive is connected with spacecraft power supply system in series with electrolytic cell. Oxygen circuit is equipped with input water line with valve and accommodates heat exchanger connected to spacecraft thermal control system.    USE - Transport.    ADVANTAGE - Stable operation, higher reliability.1 dwg
NOVELTY - An electrolytic membrane (100') comprises a microporous ion-permeable film (10) comprising a polymer (a) having medium acidic ion-exchange group, weakly acidic ion-exchange group, strongly basic ion-exchange group, medium basic ion-exchange group or weakly basic ion-exchange group, and has wettability with respect to potassium hydroxide aqueous solution having concentration of 30 wt.%.    USE - Electrolytic membrane is used for electrolytic cell (claimed) for electrolysis of alkaline water for producing hydrogen.    ADVANTAGE - The electrolytic membrane has excellent ionic permeability, and high wettability with respect to aqueous alkali solution. The generation of gas during electrolysis does not adhere to the surface. The voltage raise can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the electrolytic membrane.    Ion permeable film (10)    Reinforced material (20)    Electrolytic membrane (100')
NOVELTY - A diaphragm (100') has ion-permeable film (10) and shows wettability with respect to potassium hydroxide aqueous solution having concentration of 30 wt.%. The average hole diameter of the ion-permeable film is 0.01-20 mu m. The area change rate when the ion-permeable film is immersed in pure water is 20% or less.    USE - Diaphragm is used for electrochemical cell for producing hydrogen (all claimed).    ADVANTAGE - The diaphragm has excellent ion permeability and prevents voltage increases due to gases generated at electrodes during electrolysis becoming attached to the surface of the membrane.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic sectional view of diaphragm.    Ion-permeable film (10)    Reinforced component (20)    Diaphragm (100')
NOVELTY - Reaction apparatus has reaction tank which stores and chemically reacts raw material containing a solid substance, sample output pipe which is connected to the reaction tank and takes out the sample of the raw material from the reaction tank, steam generator which generates steam, where the steam generator is connected to the sample output pipe and sterilizes the inside of the sample output pipe, and the steam generator connects to the reaction tank and gas supply source which supplies gas for pumping sample from the sample output pipe.    USE - The reaction apparatus is useful for chemically reacting raw material e.g. waste-derived biomass containing solid substance for producing e.g. biofuel and resin.    ADVANTAGE - The reaction apparatus has favorable sampling property and prevents penetration of microorganisms and loss of sample material. The sample output pipe does not get blocked easily.    DETAILED DESCRIPTION - Reaction apparatus has reaction tank which stores and chemically reacts raw material containing a solid substance, sample output pipe which is connected to the reaction tank and takes out the sample of the raw material from the reaction tank, steam generator which generates steam, where the steam generator is connected to the sample output pipe and sterilizes the inside of the sample output pipe, and the steam generator connects to the reaction tank and gas supply source which supplies gas for pumping sample from the sample output pipe by pressurizing the inside of the reaction tank.
NOVELTY - The generator has a fluid reservoir (110), a cap (108), and a pair of electrode plates (104,106). The cap seals an opening on the fluid reservoir with an electrolyte solution (116), and has a positive terminal (114), a negative terminal (112) and a gas outlet (120). The electrode plates are attached to the cap, and extend into the interior of the fluid reservoir, and submerged in the electrolyte solution. The electrode plates are electrically coupled to the positive terminal and the negative terminal of the cap, respectively.    USE - On-demand oxy-hydrogen generator of on-demand oxy-hydrogen fuel system (claimed) used for internal combustion engine of vehicle.    ADVANTAGE - Addition of oxy-hydrogen gas to gasoline combusted in the internal combustion engine reduces the emission of nitrogen oxide, and improves thermal efficiency. Overheating of the vehicle engine is prevented. Timing sequence is activated by the microcontroller so that vehicle's on-board diagnostics is prevented from introducing too much fuel into the engine, and the engine is heated properly for more efficient functioning and less produced pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an on-demand oxy-hydrogen fuel system for an internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of an oxy-hydrogen generator.    Electrode plates (104,106)    Cap (108)    Fluid reservoir (110)    Negative terminal (112)    Positive terminal (114)    Electrolyte solution (116)    Gas outlet (120)
NOVELTY - Micro-ecological flora of crop root probiotic comprises leading flora, balance flora, base flora, secondary function flora and specific function flora. The leading flora is 25-35 pts. wt. nitrogen-fixing bacteria. The balance flora comprises 17-23 pts. wt. phosphate-solubilizing bacteria and 17-23 pts. wt. potassium-solubilizing bacteria. The basic flora comprises 2-7 pts. wt. yeast, 2-7 pts. wt. Rhizobium and 2-7 pts. wt. photosynthetic bacteria. The secondary function flora comprises 2-7 pts. wt. Bacillus species and 2-7 pts. wt. actinomycete.    USE - The micro-ecological flora is useful as microbial organic fertilizer (claimed).    ADVANTAGE - The micro-ecological flora has good stability, ensures colonization of microorganisms in soil, increases crop yield and quality, achieves detoxification of heavy metal in soil and increases pest resistance effect.    DETAILED DESCRIPTION - Micro-ecological flora of crop root probiotic comprises leading flora, balance flora, base flora, secondary function flora and specific function flora. The leading flora is 25-35 pts. wt. nitrogen-fixing bacteria. The balance flora comprises 17-23 pts. wt. phosphate-solubilizing bacteria and 17-23 pts. wt. potassium-solubilizing bacteria. The basic flora comprises 2-7 pts. wt. yeast, 2-7 pts. wt. Rhizobium and 2-7 pts. wt. photosynthetic bacteria. The secondary function flora comprises 2-7 pts. wt. Bacillus species and 2-7 pts. wt. actinomycete. The special function flora comprises 2-4 pts. wt. white rot fungus and 1-3 pts. wt. Pseudomonas.
NOVELTY - The method involves providing sealing material (11) in a cell support surface of a separator unit (SU) after mutually welding a separator (2) and a flow-path formation part (3) and forming the separator unit. An electric power generation cell (1) is mounted on the sealing material. The separator unit and the electric power generation cell are joined directly by heating the sealing material and baking the sealing material with the separator unit and the electric power generation cell. The electric power generation cell is supported by the separator unit through the sealing material.    USE - Method for manufacturing a solid oxide fuel cell unit.    ADVANTAGE - The method enables the electric power generation cell to be directly joined to the separator unit by the sealing material after mutually welding the flow-path formation part and the separator and forming the separator unit, so that a need to weld with respect to the solid oxide fuel cell unit can be eliminated after performing joining process of the electric power generation cell, thus preventing that heat deformation at time of welding and deformation by shrinkage after welding act on an electric power generation cell, and hence preventing damage of the electric power generation cell. The method enables securing insulation between an anode electrode layer and a cathode electrode layer, so that option degree of the sealing material can be improved.    DETAILED DESCRIPTION - The sealing material is paste-form jointing material. An INDEPENDENT CLAIM is also included for a solid oxide fuel cell unit.    DESCRIPTION OF DRAWING(S) - The drawing shows sectional views of a solid oxide fuel cell unit.    Separator unit (SU)    Electric power generation cell (1)    Separator (2)    Flow-path formation part (3)    Sealing material (11)
NOVELTY - Methane fermentation method, involves crushing straw into fragments of size 10-100 mm, adding crushed material to fermentation broth, collecting biogas, and recovering digested straw from fermented liquid after fermentation.    USE - Methane fermentation method (claimed).    ADVANTAGE - The method improves recycling of resources, prevents putrefaction, and utilizes hygienic raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for bedding which is recovered from digestive liquid of methane fermentation method.
NOVELTY - Manufacture of biomass liquid involves obtaining impregnation material of glycerol by mixing cellulose biomass feedstock obtained by crushing cellulose biomass and glycerol, and impregnating cellulose biomass feedstock to glycerol, and obtaining biomass liquid by heat-processing impregnation material in presence of acidic catalyst and liquefying cellulose in cellulose biomass feedstock.    USE - Manufacture of biomass liquid used as biomass-to-liquid fuel, chemical material, resin raw material, caking additive, and soil modification agent (all claimed) and used as substitute for coal and petroleum.    ADVANTAGE - The method enables manufacture of biomass liquid economically with effective usage of carbon sources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass liquid manufacturing system (100), which comprises biodiesel fuel manufacturing plant (20) which manufactures biodiesel fuel from biomass, and the biomass liquid manufacturing plant which manufactures a biomass liquid from cellulose biomass feedstock, in which biodiesel fuel manufacturing plant supplies the waste glycerol obtained as a by-product of biodiesel fuel to the biomass liquid manufacturing plant, and biomass liquid manufacturing plant mixes the cellulose biomass feedstock and the waste glycerol, after making cellulose biomass feedstock impregnate the waste glycerol and obtaining the impregnation material of waste glycerol, and impregnation material is heat-processed in presence of an acidic catalyst, and cellulose in the cellulose biomass feedstock is liquefied.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of biomass liquid manufacturing system. (Drawing includes non-English language text)    Biomass liquid manufacturing plant (10)    Grinding process portion (11)    Mixing process portion (12)    Microwave heat-processing portion (13)    Biodiesel fuel manufacturing plant (20)    Biomass liquid manufacturing system (100)
NOVELTY - This utility new type claims a one chicken stir reaction device, include a , bucket in bucket bottom is rotatably provided with a disk impeller, impeller disc centre fixed with vertical shaft, connecting through fixed pole is equipped with a multi-door-shaped paddle stir the upper vertical shaft, said upper door-shaped stir paddle with cross of fixed supporting rod, upper surface of said disk impeller set with a multi-bump of; a bucket body part set with the water tank, a water tank connected with a water tube, the water tube extends to the bucket body, a water box one side set with one used for a device of a quicklime, a discharge hole of a bottom opposite to the bucket body, the bucket body set with one outer interlayer, the inner interlayer is connected with a steam inlet tube. This utility new type structure design, the impeller of stir to stir chicken manure and quicklime, making the stir uniform, can quickly lower the reaction high temperature processing the chicken manure, of reducing pollution for environment.
NOVELTY - Organic fertilizer comprises 40-50 pts. straw, 15-25 pts. rice hull, 30-40 pts. livestock and poultry excrement.    USE - Used as an organic fertilizer.    ADVANTAGE - The organic fertilizer can improve the soil degraded by chemical fertilizer, provides nutrients to soil required for plant growth, maintains soil self-purification ability, and is simple and economical.
NOVELTY - Intermediate (I) comprising a first indole moiety which is associated with an optionally carboxylated hexahydroazepino moiety, an optionally carboxylated azonane moiety, or a second, optionally carboxylated indole moiety, having at least one of an alkyl, allyl, phenylallyl, cinnamyl, alkenyl and alkyl-alkenyl substituent pendant from a nitrogen atom of the same, is new.    USE - (I) is useful in direct or multi-step convergent syntheses with other compounds including aldehyde derived pharmaceutical intermediates.    ADVANTAGE - (I) can be economically and rapidly prepared using reduced amount of reagent without forming competitive side reactions and requiring product isolation and/or purification and by disposing toxic waste and/or byproducts in a large scale and eco-friendly manner.
NOVELTY - Producing low metal biomass-derived pyrolysis oil comprises: contacting the pyrolysis oil with an acidic ion-exchange resin having sulfonic acid active groups to form low metal biomass-derived pyrolysis oil and spent acidic ion-exchange resin; removing the pyrolysis oil from the spent acidic ion-exchange resin; and washing the resin with a solvent comprising methanol, ethanol and/or acetone to remove at least a portion of residual low metal biomass-derived pyrolysis oil from the resin and to retain residual solvent in the pyrolysis oil.    USE - The process is useful for producing low metal biomass-derived pyrolysis oil (claimed) that is used as biofuel.    ADVANTAGE - The process selectively reduces metals without changing the other properties of the biomass-derived pyrolysis oil and provides pyrolysis oil that retains the coloration, viscosity, carbon content, water content and acidity of the starting biomass-derived pyrolysis oil. The ion-exchange resin is not fouled by the ion-exchange.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the low metal biomass-derived pyrolysis oil produced by the process.
NOVELTY - Obtaining multi-metal sulfur-containing supported catalyst, involves: (a) impregnating a support with a solution comprising metal compounds; (b) impregnating the solid obtained in step (a) with a solution comprising at least one metal compound; and (c) sulfiding the solid obtained in (b), here the solution of step (a) further comprises impregnating a complexing agent.    USE - The method is useful for obtaining multi-metal sulfur-containing supported catalyst used for producing higher alcohols (C2+) by catalytic conversion of synthesis gas, here the higher alcohol is ethanol (all claimed).    ADVANTAGE - The catalyst has greater catalytic activity; higher selectivity to higher alcohols (C2+); higher selectivity to ethanol; and increased ethanol productivity.    DETAILED DESCRIPTION - Obtaining multi-metal sulfur-containing supported catalyst comprising M1M2xM3y components, involves: (a) impregnating a support with a solution comprising at least one compound of M1 and at least one compound of M2; (b) impregnating the solid obtained in step (a) with a solution comprising at least one compound of M3; and (c) sulfiding the solid obtained in (b), here the solution of step (a) further comprises impregnating a complexing agent.    M1=selected from Mo, W and its combination;    M2=selected from Co, Ni, and its combination;    M3=selected from alkali metals and its combination;    x=molar ratio having a value of between 0.1 and 5, preferably between 0.2 and 2; and    y=molar ratio having a value of between 0.1 and 10, preferably between 0.2 and 5.    INDEPENDENT CLAIMS are included for:    (1) catalyst obtainable by the method above; and    (2) a method for obtaining higher alcohols (C2+) from synthesis gas which involves contacting the catalyst and a gaseous stream comprising synthesis gas.
NOVELTY - Preparing a biobriquette from solid biomass waste from agriculture, agribusiness and forestry, involves: (a) obtaining a representative sample of the residue; (b) conducting an initial conditioning which involves making at least one of the following: drying, crushing, grinding and sieving preliminary; (c) performing a second amendment comprising the step of toasting the preconditioned biomass; (d) grinding and sieving the material to a minor toast to 149 microns particle size; (e) agglomerated conditioning biomass using an organic gel; (f) performing pressing operation of the mixture.    USE - The method is useful for preparing a biobriquette from solid biomass waste from agriculture, agribusiness and forestry (claimed).    ADVANTAGE - The method has simple and environment friendly process.    DETAILED DESCRIPTION - Preparing a biobriquette from solid biomass waste from agriculture, agribusiness and forestry, involves: (a) obtaining a representative sample of the residue for proper physicochemical characterization to establish conditioning processes required and fuel characteristics; (b) conducting an initial conditioning which involves making at least one of the following: drying, crushing, grinding and sieving preliminary; (c) performing a second amendment comprising the step of toasting the preconditioned biomass; (d) grinding and sieving the material to a minor toast to 149 microns particle size; (e) agglomerated conditioning biomass using an organic gel; (f) performing pressing operation of the mixture and finally curing the previously pressed biobriquette, where the roasting is performed in a reactor with horizontal axis and with a heating rate of 10-30 degrees C/minute to a temperature of roasting between 250-300 degrees C with a dwell time at this temperature within 30-90 minutes. An INDEPENDENT CLAIM is included for a biobriquette made by the method having a density of at least 550 kg/m3.
NOVELTY - The apparatus (100) has a modifier (2) which generates hydrogen-containing gas by reforming reaction from raw material. A material supply device (6) supplies raw material to modifier which is heated by combustor. Water supply machine supplies water to modifier. Detector detects physical quantity used for estimation of composition of raw material. A controller (9) uses water flow amount regulator (10) for adjusting water flow for quantity corresponding to composition of estimated raw material, and controls the flow volume of water from water supply machine to modifier.    USE - Hydrogen generating apparatus used in fuel cell system (claimed).    ADVANTAGE - Since the water is supplied to the modifier without excess and deficient, the hydrogen generating apparatus generates hydrogen stably and efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text)    Modifier (2)    Material supply device (6)    Controller (9)    Water flow amount regulator (10)    Hydrogen generating apparatus (100)
NOVELTY - This utility new type belongs to synthesis ammonia waste gas recovery system using technology field, specific relates to a one by using the synthesis ammonia system in a synthetic air and ammonia tank relaxation in the pneuma of synthetic ammonia system waste in pneuma ammonia recovery using device, a synthesized air and ammonia tank relaxation mix the pneuma of pneuma pipeline in turn is connected through the air inlet of tube pass of heat exchanger and pass the second separator of first heat exchanger, separator top part of non-condensable gas exit through the shell pass and membrane hydrogen extracting device with the air boiler of second heat exchanger is connected with a simple structure, convenient operation, saving energy and reducing consumption and it increase a rate of ammonia.
NOVELTY - A Chlamydomonas mexicana strain YSL008 (KCTC 12343BP) is new. The C.mexicana strain YSL008 has high carbohydrate content.    USE - The C.mexicana strain YSL008 is useful in microbial agent for wastewater treatment and producing bioethanol (claimed).    ADVANTAGE - The C.mexicana strain YSL008 enables to remove nitrogen and phosphorus present in wastewater.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microbial agent for wastewater treatment comprises the above-mentioned strain and culture medium;    (2) method (M1) for culturing the above-mentioned strain in wastewater; and    (3) method (M2) for producing bioethanol, involves preprocessing the above-mentioned strain to ultrasonic treatment, crushing the cell wall, performing hydrolysis using enzyme, and subjecting to acidic fermentation using anaerobic bacteria to obtain the product.
NOVELTY - Treating a sewer stream, comprises passing a flow of the sewer stream through leonardite. The leonardite has a particle size of 400 meshes or less, and is reacted with gaseous ammonia to render the leonardite into a water-soluble powder.    USE - The process is useful for treating sewer stream (claimed) to reduce harmful materials, such as heavy metals and organic compounds.    ADVANTAGE - The process is capable of treating sewer stream in an eco-friendly manner, thus effectively reducing or eliminating harmful materials from the sewer.
NOVELTY - Biogas producing equipment comprises anaerobic digester in which organic waste of vessel is pulverized, reactor with methane fermentation tank in which methane gas is fermented and organic acid is generated, and heat exchanger which maintains temerature to 50-60 degrees C.    USE - Biogas producing equipment using organic waste and exhaust gas of vessel (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for vessel.
NOVELTY - A metal complex is added to organic azide, to obtain imine having no substituent on nitrogen.    USE - Manufacture of imine having no substituent on nitrogen used for manufacturing coupling product e.g. amine (all claimed) used in medical and chemical field.    ADVANTAGE - The method efficiently provides imine having no substituent on nitrogen, by a simple, economical and environmentally-friendly process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of coupling product, which involves reacting imine with nucleophile.
NOVELTY - Method for producing biomaterial, involves (a) preparing butanol from biomass which is fermented with first microorganism having ability to produce butanol, (b) separating butanol from the fermented product and purifying the butanol (butanol selectivity is 60% or more), (c) recovering wastewater generated from separation and purification steps, (d) preparing culture medium comprising the wastewater, and (e) culturing second microorganism in the culture medium.    USE - The method is useful for producing biomaterial chosen from butanol, acetone or methanol (claimed).
NOVELTY - Method comprises saccharifying a biomass feedstock in a vessel while mixing with a jet mixer, where the biomass feedstock is dispersed in a liquid medium using a dispersing system that draws the feedstock and liquid medium out of the vessel and recirculates the feedstock and liquid medium back into the vessel. The dispersing system comprises a chamber and, within the chamber, a rotating member, which axially draws the feedstock and liquid medium into the chamber and radially expels a dispersion of the feedstock in the medium from the chamber.    USE - The method is useful for saccharifying a biomass feedstock such as cellulosic or lignocellulosic material (all claimed), plant biomass, animal biomass and municipal waste biomass to produce fuel such as ethanol for internal combustion engines, hydrocarbons, proteins, alcohols (e.g. a monohydric alcohols or a dihydric alcohols), such as n-propanol or n-butanol, carboxylic acids such as acetic acid or butyric acid, salts of a carboxylic acid, a mixture of carboxylic acids and salts of carboxylic acids and esters of carboxylic acids (e.g. methyl, ethyl and n-propyl esters), ketones, aldehydes, alpha, beta unsaturated acids, such as acrylic acid and olefins such as ethylene, preferably ethanol, propanol, propylene glycol, butanol, 1,4-butanediol, 1,3-propanediol, methyl acrylate, methyl methacrylate, lactic acid, propionic acid, butyric acid, succinic acid, and 3-hydroxypropionic acid.    ADVANTAGE - The method is capable of easily, efficiently, rapidly and economically saccharifying the biomass feedstock with high throughput and less power consumption.
NOVELTY - Preparing steroids and steroid precursors involves performing decomposition of biomass by thermochemical process. The biomass is heated at different temperature to obtain steroids and steroid precursors by condensation process.    USE - Method for preparing steroids and steroid precursors used for preparing pharmaceutical, food and cosmetics product.    ADVANTAGE - The method enables to separate steroids and steroid precursors such as stigmastanol, phytosterol and beta-sitosterol according to their molecular weight or boiling point.
NOVELTY - Organic wastewater containing 1C compound is methane-fermented while being stirred in a mixing tank. Methane-fermentation of sludge-containing treated water discharged from the methane-fermentation process is carried out in a plug-flow system fermenter, without stirring. Sludge and treated water are separated and recovered from the discharged treated water, and one portion of or the entire amount of recovered sludge is returned for methane fermentation with or without stirring.    USE - Anaerobic treatment of organic wastewater discharged from chemical plants.    ADVANTAGE - The method enables adjustment of pH in methane-fermentation tank in a pH region suitable for methane fermentation, without increasing the capacity of reaction tank. A uniform reaction zone is formed in the mixing tank by stirring methane fermentation. The need for a circulation pump in the mixing tank is eliminated when compared with upflow anaerobic sludge blanket type reaction tank. Hence, motive-power requirement is reduced. Since LV need not be carried out for suppression of granular-sludge outflow below a constant value, installation area is reduced. Favorable treated-water quality is achieved. By return of sludge to the methane fermentation process, the concentration of methane fermentation microbe is maintained.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic treatment apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the processing method of organic wastewater. (Drawing includes non-English language text)
NOVELTY - Composition comprises microbial culture obtained by: (a) preparing culture medium comprising yeast, lactic acid bacteria and/or photosynthetic bacteria, (b) inoculating photosynthetic bacteria, lactic acid bacteria and/or yeast in the medium and culturing, and (c) adding collagen particles during step (a) or step (b).    USE - The composition is useful for purifying waste water (claimed).    ADVANTAGE - The composition is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for purifying waste water comprising: (i) preparing the composition; and (ii) contacting the composition with the waste water.
NOVELTY - Producing compost pellets, comprises either pulverizing cockscomb, mixing red clay with the pulverized cockscomb, molding the mixture into pellets, and drying the molded pellets, or pulverizing barley straw, mixing red clay with the pulverized barley straw, molding the mixture into pellets, and drying the molded pellets.    USE - The method is useful for producing compost pellets (claimed) used in a fertilizer. No biological data given.    ADVANTAGE - The method is capable of easily and economically producing the compost pellets.
NOVELTY - Liquid-fertilizing of livestock excretion, comprises primary aerobic processing (S100)by anaerobically processing plant material of the livestock excretion according to environmental mitigation condition cycle, anaerobically processing(S102)to decompose available water qualities of the aerobically processed livestock excretion using decomposition microorganism in absence of air, and secondary aerobic processing (S104)for composting by adjusting temperature and moisture, and aeration processing to activate aerobic microorganism.    USE - The method is useful for liquid-fertilizing of livestock excretion (claimed).    ADVANTAGE - The method reduces generation of odor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow chart of the method for liquid-fertilizing of livestock excretion using first aerobic treatment process (Drawing includes non-English language text).    Primary aerobic processing step (S100)    Anaerobically processing step (S102)    Secondary aerobic processing step (S104)
NOVELTY - A beta -glucosidase protein comprising a 1316 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new. The beta -glucosidase protein is isolated from rumen microorganism of black goat.    USE - The beta -glucosidase protein is useful in feed additive for promoting glucoside degradation and detergent composition, and for producing biofuel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the beta -glucosidase protein;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector;    (4) antibody of beta -glucosidase protein;    (5) method (M1) for mass producing the beta -glucosidase in the host cell, involves introducing the recombinant vector to the host cell to over-express the beta -glucosidase;    (6) recombinant beta -glucosidase protein obtained by the method (M1); and    (7) method (M2) for producing biofuel, involves adding the recombinant beta -glucosidase protein and hydrolyzed beta -glucosidase protein, to biomass.
NOVELTY - Vinasse treatment system comprises an internal circulation reactor, a biogas power generator and an ultra-filtration system that is coupled with a reverse osmosis system, where liquid portion is divided into 50% purified water and 50% water containing concentrated salts.    USE - Vinasse treatment system for generating electricity and fertilizer.    ADVANTAGE - The vinasse treatment system enables to generate electricity in a simple and cost-effective manner.
NOVELTY - Biodiesel production involves using terephthalic acid as ion exchanger for purifying biodiesel obtained in an alkaline medium by neutralization reaction to remove excess catalyst without using washing water. fact of using terephthalic acid or ethylene polyterephthalate, 1,3-benzoldicarboxylic acid, 1,4-benzoldicarboxylic acid or their derivatives, sodium terephthalate, potassium terephthalate, terephthalic acid ester, terephthalic acid anhydride and amides derived from terephthalic acid as starting materials.    USE - Method for producing biodiesel through dry neutralization process.    ADVANTAGE - The method produces biodiesel that recovers catalyst without necessity of purifying the product by washing with water in a simple, cost-effective and eco-friendly manner.
NOVELTY - The method involves feeding food waste packaged in waste bags made of breakable material, to a food waste dump truck and conveying the food waste through a chain conveyor (2) for preliminary solid-liquid separation. The food waste is fed to a dewatering device (7) after preliminary solid-liquid separation. The waste material is dehydrated by the pressurized rods in the dewatering device and dehydrated waste material is transported by a screw conveyor (8) to a uniform fabric trash (11). The waste material is passed through an outlet-type drum sieve for compaction.    USE - Method for performing pre-treatment of food waste compost.    ADVANTAGE - The efficiency of composting process is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the food waste composting process.    Chain conveyor (2)    Dewatering device (7)    Screw conveyor (8)    Hopper (9)    Uniform fabric trash (11)
NOVELTY - The device has a transporter connected with heaters connected to a carrier from a reservoir that is provided with two layers. The heaters are provided with transverse holes. Rotary ended arms are rolled at a bottom part. A tray is matched with two layers of a disk from inside coil tubes.    USE - Device for producing fuel from waste.
NOVELTY - The bioreactor has a lid provided with a heat exchanger that is connected to a pump by piping of a nozzle, where air is heated by using the heat exchanger.    USE - Bioreactors for composting organic waste isolated from a chamber with a perforated floor.
NOVELTY - A granular fertilizer producing method involves utilizing sludge derived from wastewater treatment plants or sewage plants. The sludge is treated by using ground quicklime or burnt lime and dolomite binder. The treated sludge is hydrated at more than 100 degrees C to destruct bacteria and dangerous substances. The hydrated sludge is granulated by using granulator by adding quicklime, dolomite binder and water, and subjected to binding process to obtain mixture. The mixture is added with calcium and magnesium fertilizer, dried and sorted to obtain a finished product.    USE - Method for producing a granular fertilizer.
NOVELTY - Producing a coupled radical product, comprises: (a) obtaining a sodium salt of a sulfonic acid; (b) preparing an anolyte for an electrolytic cell comprising an anolyte compartment, a catholyte compartment and a sodium (Na) super ionic conductor (NaSICON) membrane that separates the anolyte compartment from the catholyte compartment; and (c) electrolyzing the anolyte within the cell, where the electrolyzing desulfoxylates the sodium salt of the sulfonic acid, and converts the sodium salt of the sulfonic acid into one or more alkyl radicals that react to form a coupled radical product.    USE - The method is useful for producing a coupled radical product, such as hydrocarbon (all claimed).    ADVANTAGE - The method provides coupled radical product in an economical manner.    DETAILED DESCRIPTION - Producing a coupled radical product, comprises: (a) obtaining a sodium salt of a sulfonic acid; (b) preparing an anolyte for an electrolytic cell comprising an anolyte compartment, a catholyte compartment and a sodium (Na) super ionic conductor (NaSICON) membrane that separates the anolyte compartment from the catholyte compartment, where the anolyte is housed within the anolyte compartment, and a catholyte is housed within the catholyte compartment, and the anolyte comprises a first solvent or mixture of solvents and a quantity of the sodium salt of the sulfonic acid; and (c) electrolyzing the anolyte within the cell, where the electrolyzing desulfoxylates the sodium salt of the sulfonic acid, and converts the sodium salt of the sulfonic acid into one or more alkyl radicals that react to form a coupled radical product.    DESCRIPTION OF DRAWING(S) - The figure shows a process flow diagram for producing a coupled radical product.
NOVELTY - Herbicidal composition comprises microcapsules having a polymer shell and containing clomazone and an alga.    USE - Herbicidal composition used for controlling plant growth at a locus (claimed).    ADVANTAGE - The composition has reduced environmental impact, has increased user-friendliness, and has a reduced toxicity. The inclusion of algae in the microcapsules leads to an improved control of the release rate of the active ingredient. The algae are resource-rich material and are inexpensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the herbicide composition, comprising:    (A) providing a water immiscible phase comprising clomazone, an alga, an isocyanate, and optionally an acetylene carbamide derivative (ACD) crosslinker;    (B) providing an aqueous phase comprising surfactants combining the water-immiscible phase and the aqueous phase to form a dispersion of the water immiscible phase in the aqueous phase;    (C) forming microcapsules of polyurea containing droplets of water immiscible phase; and    (D) curing the microcapsules.
NOVELTY - A fertilizer comprises 50-70 wt.% optionally supplemented useless parts of mushroom in an amount that does not exceed 10 wt.% of amount of substrate, 20-50 wt.% straw, 1-4 wt.% sodium bicarbonate and/or potassium bicarbonate, 1-3 wt.% calcium dihydrogen phosphate, 1-5 wt.% magnesium carbonate and additional waste substances in a quantity such that the amount of nitrogen in the product is maintained as 1-5 wt.% per kilogram of dry product, where the amount of carbon and nitrogen in the fertilizer is 30: 1.    USE - Fertilizer.    DETAILED DESCRIPTION - A fertilizer comprises 50-70 wt.% optionally supplemented useless parts of mushroom in an amount that does not exceed 10 wt.% of amount of substrate, 20-50 wt.% straw, 1-4 wt.% sodium bicarbonate and/or potassium bicarbonate, 1-3 wt.% calcium dihydrogen phosphate, 1-5 wt.% magnesium carbonate and additional waste substances in a quantity such that the amount of nitrogen in the product is maintained as 1-5 wt.% per kilogram of dry product, where the amount of carbon and nitrogen in the fertilizer is 30: 1, and the optionally supplemented useless parts of mushroom is obtained after cultivation of mushrooms.
NOVELTY - Composite microbial agent is prepared by mixing (in pts.wt.): cellulose degrading bacteria (10-15), starch-degrading bacteria (15-30), protein-degrading bacteria (15-30), oil degrading bacteria (15-20), Bacillus subtilis (10-15), Pseudomonas aeruginosa (5-15), and then adding solid fermentation materials such as wheat bran (50-60 kg), beans (15-20 kg), magnesium sulfate (0.4-0.6 kg), potassium dihydrogen phosphate (0.4-0.6 kg), disodium hydrogen phosphate (0.1-0.2 kg) and glucose (8-10 kg).    USE - Composite microbial agent used for decomposing food waste into organic fertilizers (claimed).    ADVANTAGE - The microbial agent effectively degrades oil, protein, fiber material by tolerating a certain concentration of salt in the material in a simple and cost-effective process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for preparing microbial inoculum, which involves mixing cellulose degrading bacteria; starch degrading bacteria; protein degradation bacteria; fat degradation bacteria; Bacillus subtilis; and Pseudomonas aeruginosa; and then adding solid fermentation materials to obtain microbial inoculum; and    (2) a method for processing kitchen waste, which involves weighing components such as glucose, and the obtained microbial inoculums; and then mixing weighed components with organic garbage and saw dust into biochemical food waste processor; and then processing the material at high temperature to ferment the waste material.
NOVELTY - Molecular sieve having a structure of ITQ-32 being substantially free of fluoride ions in its as-synthesized form, comprising 4,4-dimethyl,1-cyclohexylpiperazinium cations (Q) in its pore structure, is new.    USE - The molecular sieve is useful: for separating a carbon dioxide from a gaseous mixture comprising carbon dioxide and methane (all claimed); and as an adsorbent and a catalyst for organic (e.g. hydrocarbon) conversion reactions (e.g. hydrogen, rare earth metals, and/or one or more metals of groups 2-15 of the periodic table of the elements).    ADVANTAGE - The molecular sieve can be synthesized in the absence of alkali metal cations, preferably fluoride ions, without using ion-exchange of the product after thermal treatment to remove any occluded structure directing agent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) producing the molecular sieve having structure of ITQ-32; and    (2) a process for separating a first component from a gaseous mixture comprising the first component and a second component, comprising contacting the gaseous mixture with the molecular sieve.
NOVELTY - The method involves flowing liquid natural gas liquid (NGL) product (52) from demethanizer (107). Initial amount of ethane and heavier hydrocarbon components are provided in NGL product exiting demathanizer. Vapor product of demethanizer is liquefied and is flown to nitrogen recovery unit. Liquid liquefied natural gas (LNG) stream and vapor contaminant stream are flown from recovery unit. Vapor contaminant stream from nitrogen recovery unit is combined into specific nitrogen refrigerant stream, and liquid LNG stream from recovery unit is cooled in specific heat exchange unit.    USE - Method for processing hydrocarbon gas stream.    ADVANTAGE - Since the liquid LNG product can be pumped to pipeline pressure before being vaporized in the process exchanger and sent to gas sales, the need for residue gas compression can be eliminated, and the ethane can be recovered without recovering methane as liquid, while minimizing energy input and reducing overall atmospheric emissions. Thus, the high purity LNG with reduced cost can be provided by utilizing liquid nitrogen (LIN) as the LNG condensing medium and process refrigerant, and the processes of compression, expansion of special refrigerants and recycling of regeneration gas can be eliminated, while the fully integrated heat exchange can be provided to maintaining the minimal plot area, and the need for bell section can be eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the for condensation, distillation and fractionation of natural gas to produce high quality LNG and pipeline quality Y-Grade NGL product.    Bottom reboiler (20)    Liquid NGL product (52)    Heat exchanger (103A)    Cold Separator (105)    Demathanizer (107)
NOVELTY - A photocatalytic nanocomposite comprises: a reduced graphite oxide; photocatalytic metal oxide in nanoparticle form; where the photocatalytic metal oxide in nanoparticle form is dispersed in the reduced graphite oxide.    USE - In CO2 photoreduction to produce hydrocarbon selected from methane (claimed).    ADVANTAGE - The photocatalytic nanocomposite improves kinetics of a photoreduction reaction of CO2. The ionic liquid is able to selectively adsorb the reactant, CO2, but quickly dissociate the potential product, CH4, thus promoting the photoreduction of CO2. The ionic liquid functionalized reduced graphite oxide (IL-RGO) significantly enhances the photocatalytic activity of P25 due to the enhanced electron-hole separation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of photocatalytic nanocomposite involving: oxidizing graphite to form a reduced graphite oxide; mixing the reduced graphite oxide with TiO2 nanoparticles to form the photocatalytic nanocomposite; and    (2) CO2 photoreduction involving: contacting reactants of CO2 and H2O over the photocatalytic nanocomposite; reacting the CO2 and H2O over the photocatalytic nanocomposite to produce products including CH4.
NOVELTY - Soil conditioning agent comprises 0.3-0.6 %mass petrochemical powder comprising more than 25% silicon, 7-9 %mass amino acid powder, 10.2-16.2 %mass phosphate, 11.8-18.6 %mass dihydrogen phosphate, 14.8-16.6 %mass potassium salt, 11.8-14.6 %mass ammonium sulfate, 10.8-12.8 %mass peat, 6.2-8.8 %mass shell powder comprising calcium carbonate, and 12.5-17.4 %mass serpentine powder.    USE - As soil conditioning agent.    ADVANTAGE - The soil conditioning agent decomposes phosphate compound.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the above-mentioned soil conditioning agent, involves (a) mixing the above-mentioned petrochemical powder and amino acid powder at 10 degrees C, and fermenting the mixture for 3 days, (b) mixing the fermented mixture with phosphate, dihydrogen phosphate and potassium salt, (c) mixing the obtained mixture at more than 10 degrees C, fermenting for 15 days, and adding the remaining components to the fermented mixture, and fermenting the obtained product for 15 days; and    (2) usage method of the above-mentioned soil conditioning agent.
NOVELTY - Propranolol enantiomers are prepared by dissolving (R, S)-propranolol hydrochloride in water, adding 10-35 vol.% alkaline solution at volume ratio of 1:1-3, neutralizing, dehydrogenating with resolving agent at molar ratio of 1:1-1.6, reacting with organic solvent at 25-35degreesC for 1-3 hours, cooling at -5 to -15degreesC, crystallizing for 3-6 hours, dissolving in organic solvent, adding 10-35 vol.% alkaline solution at volume ratio of 1:1-3, reacting for 20-45 minutes to obtain crude (S)-(-)-propranolol, adding water, dissolving, filtering, washing, drying, and purifying.    USE - Method for preparing (S)-enantiomer of propranolol (claimed).    ADVANTAGE - The method is simple, environment-friendly and suitable for industrial production; it has high product yield. The product is low-cost and has high purity.
NOVELTY - Microbial fertilizer comprises 4-5 pts. mass Bacillus megaterium, 2-4 pts. mass Rhodopseudomonas palustris, 1-2 pts. mass Streptomyces avermitilis, 40-50 pts. mass rapeseed, 25-30 pts. mass colza cake, 15-24 pts. mass wheat straw, 30-48 pts. mass pig manure, 30-60 pts. mass molasses, 4-5 pts. mass wheat bran, 20-32 pts. mass inorganic nitrogen-phosphorus-potassium mixture, and 3-5 pts. mass bentonite.    USE - As microbial fertilizer.    ADVANTAGE - The microbial fertilizer preserves soil moisture, and exhibits antibacterial effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the above-mentioned microbial fertilizer, which involves (a) mixing rapeseed and colza cake, uniformly blending the mixture and granulating mixture, (b) cutting straw to a length of 3-5 cm, (c) mixing pig manure, molasses, wheat bran and bentonite and the mixture obtained in step (a), stirring the mixture, controlling the water content of the mixture to 29-35%, controlling temperature of the mixture to 32-34 degrees C and pH value of the mixture at 5-5.5 and stirring the mixture in fermentation tank, (d) activating B.megaterium culture, R.palustris culture, and S.avermitilis culture and mixing activated culture, (e) adding the activated cultures in fermentation tank, stirring the mixture, adding inorganic nitrogen-phosphorus-potassium mixture process to the mixture, controlling water content of the mixture to 9-10% and temperature at 26-28 degrees C, and drying and packaging the mixture.
NOVELTY - A catalyst is obtained by supporting platinum, iridium, rhenium, and zirconium to a titanium oxide carrier.    USE - Catalyst is used for oxidation removal of methane in to-be-processed gas (claimed) e.g. combustion exhaust gas containing sulfur dioxide and waste gas containing more amount of water vapor.    ADVANTAGE - The catalyst has excellent resistance with respect to activity inhibition caused by water vapor or sulfur compound, and high methane oxidation activity and methane degradation ability at low temperature, and is economically manufactured with reduced usage amount of noble metals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for oxidation removal of methane in to-be-processed gas, which involves contacting the to-be-processed gas containing methane and excess oxygen and the catalyst at 300-450 degrees C.
NOVELTY - The production method involves preparing a substrate which has pores that are arranged through a thickness direction of the substrate. The pores are filled up with multi-layer membranes which have an ion conducting layer and an ion non-conducting layer. The ion conducting layer and ion non-conducting layer are alternately formed on each inner wall surface of the pores. The multi-layer membranes are formed by atomic layer deposition.    USE - Production method of ionic electrolyte membrane structure used for manufacturing solid oxide fuel cell.    ADVANTAGE - Ionic electrolyte membrane structure has high ionic conductivity which enables a solid oxide fuel cell to be usable at lower temperature, and provides superior energy efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows the graphical view of a relationship between ionic conductivity and temperature.
NOVELTY - The invention is related to a method of cellulase induction, which is employed dilute acid-pretreated lignocelluloses as substrate, with enzyme hydrolyzed as inducer with the Trichoderma species to produce cellulose.
NOVELTY - The device has overflow tank (2) whose center portion is provided with water outlet hole. The periphery of overflow tank is provided with multiple function layers. Each inner function layer is provided with biological ball purification. The aquatic plant landscape area is provided at the periphery of biological ball purification area. One end of water tube is connected with overflow tank and other end is connected with water pump.    USE - Tower shaped landscape water aeration and biological purification device.    ADVANTAGE - The dissolved oxygen concentration is increases in sewage through free fall water, so that function of biological strengthening treatment is improved. The processing efficiency of aritificial wetland is improved, so that sewage water quality is improved. The function of aritificial wetland landscape is improved, so that landscape effect is improved. The device is simple in structure, so that manufacturing cost is reduced and the device is used conveniently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tower shaped landscape water aeration and biological purification device.    Overflow tank (2)    Water channel (5)
NOVELTY - Method for sewage treatment using traditional Chinese medicinal agent, involves mechanically adding sewage water into water tank, cooling the sewage water using cooling tower, and subjecting to coagulative precipitation tank and cyclic activated sludge system (CASS). The traditional Chinese medicinal agent comprises 3-10 parts mass Aloe, 5-10 parts mass Pinellia ternata, 1-3 parts mass ginger, 5-15 parts mass rhizoma coptidis, 2-8 parts mass arisaema cum bile, and 4-10 parts mass Scutellaria.    USE - The method is useful for sewage treatment (claimed).    ADVANTAGE - The method utilizes pure natural substance for sewage treatment, and produces no harmful substance in the whole process.
NOVELTY - Treating sewage involves placing sewage into a water collection regulating tank through input part, and then coagulative precipitation tank to obtain a precipitated sewage. The precipitated sewage is entered into a cemented cass pool, where traditional Chinese medicinal agent is added in the cass tank. The traditional Chinese medicinal treatment agent comprises (in pts.wt.): golden cypress (50-150), arisaema cum bile (100-250), ginger (10-20), liquorice (2-15) and rhizoma coptidis (20-35). Sewage is treated in a biological filter pool by using a biological filtration.    USE - Method for treating sewage (claimed).    ADVANTAGE - The method enables to treat sewage through natural compound and does not produce harmful substances in treatment process.
NOVELTY - Method for sewage treatment using traditional Chinese medicinal agent, involves mechanically adding sewage water into water tank, cooling the sewage water using cooling tower, and subjecting to coagulative precipitation tank and cyclic activated sludge system (CASS). The traditional Chinese medicinal agent comprises 20-30 parts weight Viola, 5-15 parts weight licorice, 10-15 parts weight radix sophorae flavescentis, and 50-150 parts weight Aloe.    USE - The method is useful for sewage treatment (claimed).    ADVANTAGE - The method is environmentally-friendly, utilizes pure natural substance for sewage treatment, and produces no harmful substance in the whole process.
NOVELTY - Molasses processing involves heating molasses fermented waste to concentrate, where organic matter content is 40-75 %. The concentrated liquid is cooled, and then divided into two parts. A part of the concentrated liquid is added with alkaline hydrolysis agent (10-35%). The obtained material is stirred at low speed under alkali solution for 20-40 minutes. Calcium-magnesia phosphate fertilizer (5-15%) and potash fertilizer (10-15%) are added to the obtained mixture. The obtained mixture is stirred uniformly to obtain demodulated base material.    USE - Method for processing molasses (claimed).    ADVANTAGE - The method saves time and eliminates addition of neutralizing agent.    DETAILED DESCRIPTION - Molasses processing involves heating molasses fermented waste to concentrate, where organic matter content is 40-75 %. The concentrated liquid is cooled, and then divided into two parts. A part of the concentrated liquid is added with alkaline hydrolysis agent (10-35%). The obtained material is stirred at low speed under alkali solution for 20-40 minutes. Calcium-magnesia phosphate fertilizer (5-15%) and potash fertilizer (10-15%) are added to the obtained mixture. The obtained mixture is stirred uniformly to obtain demodulated base material. A part of the concentrated liquid is added with acid hydrolysis agent (10-35%). The obtained material is stirred at low speed under acidic solution for 20-40 minutes. Seasoning is added to the obtained alkali and acid demodulated material, and then mixed uniformly, where the pH of mixture is 5-7. The obtained product is dried at 35-50 degrees C to obtain the desired product, where the water content is less than 10%.
NOVELTY - Citrus peel organic fertilizer comprises 50-60 wt.% Citrus and 40-50 wt.% organic matter. Organic fertilizer is prepared by taking Citrus, crushing, adding reducing acid and yeast, fermenting, stirring, adjusting pH, adding water regulator, mixing, adjusting moisture content, adding livestock manure and water, mixing uniformly, adding enzyme, mixing, performing enzymolysis, adding liquid microbial agent, mixing, fermenting, spreading, drying, naturally drying, adding urea, monoammonium phosphate, potassium sulfate, sterilizing, drying, cooling, sieving and coating.    USE - Citrus peel organic fertilizer.    DETAILED DESCRIPTION - Citrus peel organic fertilizer comprises 50-60 wt.% Citrus and 40-50 wt.% organic matter. Organic matter contains livestock excrement and water regulator. Water regulator is obtained by crushing wheat straw, rice straw, corn straw, chaff, hull, wood chips, rape seed dregs or Jatropha curcas, extracting artemisinin, extracting oil, mixing, crushing to 2-5 mm, and controlling water content of regulator at less than 5%. Organic fertilizer is prepared by taking Citrus, crushing until granule size is 3-5 mm, adding 0.5-1.2 wt.% reducing acid and yeast, fermenting at room temperature for 24-72 hours, stirring every 12 hours, adjusting pH to 6-7, adding water regulator, mixing uniformly, adjusting mixture moisture content, adding 50-60 wt.% livestock manure and 50-60 wt.% water, mixing uniformly, adding 0.5-1 wt.% enzyme, mixing uniformly, performing enzymolysis at 40-55 degrees C, turning for 1-2 times, adding 1-3 wt.% liquid microbial agent, mixing uniformly, growing, covering, fermenting at 65-70 degrees C, turning 3-4 times, spreading, drying for 2-3 days, naturally drying until water content is 30%, adding urea, monoammonium phosphate, potassium sulfate, sterilizing, granulating, drying, cooling, sieving and coating. The fertilizer contains nitrogen, phosphorus and potassium element at ratio of 2.5-2.8:0.12-0.16:0.7-1.3.
NOVELTY - Tridecyl morpholine quaternary ammonium alkali derivative (I) is new.    USE - Tridecyl morpholine quaternary ammonium alkali derivative used as catalyst (claimed) for preparing biological diesel.    ADVANTAGE - The tridecyl morpholine quaternary ammonium alkali derivative used as catalyst that has high catalytic activity, catalyst is easy to separate after reaction and reused multiple times.    DETAILED DESCRIPTION - Tridecyl morpholine quaternary ammonium alkali derivative of formula (I) is new. An INDEPENDENT CLAIM is included for a method for preparing tridecyl morpholine quaternary ammonium alkali derivative of formula (I).    R=n-butyl, n-octyl, benzyl or 2-pyridylmethyl or C13H27 tridecyl group.
NOVELTY - This utility new type one of a vehicle-mounted hydrogen manufacturing device, it include: battery power supply, first filter, an oscillator, a transformer, a rectifier, a second filter, a voltage stabilizer, a current limiter and the hydrogen machine, inner hydrogen making machine is equipped with electrode group, electrode group by a plurality of arranged on the electrode plate is composed of, a storage battery power supply, first filter, an oscillator, a transformer, a rectifier, a second filter, a voltage stabilizer and current limiter in turn is connected the anode of the odd number electrode plate of current limiter is connected with the even number electrode plate of current limiter is connected, or current limiter of the anode electrode plate is connected with the even number electrode plate of the current limiter is connected with the odd number electrode plate and even electrode plate adjacent each other, the utility model is new type of a one on-vehicle hydrogen device can be made using low voltage battery power source produce hydrogen and oxygen of 350 cc to 1200cc/ minutes for engine use, oil quantity of vehicle can reach 10-50 %.
NOVELTY - One a hydrogen preparing system, comprise in turn connecting of automatic water supply sub-system, sub-system, gas separating sub-system and hydrogen filter sub-system, a hydrogen filter sub-system set with hydrogen exit and the waste standard pneuma exit, further comprise hydrogen gas calibration device, an external port of a standard device connecting the hydrogen standard gas bottle, a supply sub system comprise a collecting tank, a water collecting tank set with inner electrolysis water inlet, water inlet and the turbid water exit, a water collecting tank set with filter in the electrolytic water inlet. Said electrolytic water inlet connecting cell sub-system. With the existing technology, this utility new type of the hydrogen system, for a hydrogen of a purity, if not in accordance with requirement, removing through waste pneuma exit, re-preparing process for system until the purity of hydrogen gas meets the requirement, increase the purity of preparation hydrogen system, at the same time, the system can according to the hydrogen demand to a time, a quantitative, which avoids the resource waste and loss of energy.
NOVELTY - A membrane electrolytic groove one special graphite cathode comprise graphite, a graphite plate is provided with said circulation water tank, the back is provided with guide groove, a graphite plate of left upper end surface is provided with a discharge hole and a water outlet hole, the graphite plate of right lower end surface of feeding hole and water inlet hole, and the discharge hole and the upper part of guide groove connected, lower part of feeding hole and the flow guide groove connected, the water hole and the upper part of circulation water groove connected, water inlet hole and lower part of circulation water tank connected, around a front graphite plate is provided with an annular seal groove, seal groove and the circulation of water. This utility new type has a cooling water circulating structure and the cathode material liquid guide structure can not only to the graphite cathode, an anode material and liquid cooling, but also can accelerate flow and uniform distribute of cathode material liquid, and is good for hydrogen of, prolong the use life of the graphite cathode and anode, electric current efficiency and increase the product quality.
NOVELTY - The system has a vacuum pressure swing adsorption (VPSA) purifying device (4) which is connected with an air inlet of a third pipeline. A gas mixing device (5) is connected with a methane concentration monitor device. A mixing device of a VPSA purifying device is connected with a second pipeline, for purifying the gas (2) entered into the internal combustion engine. A pneuma mine gas source (1) is connected with an exhaust gas exit of mixing device. A second filter dust-removing device (6) is connected with a catalytic oxidation furnace (7).    USE - System for utilization of low concentration gas such as methane gas.    ADVANTAGE - The second filter dust-removing device is connected with the catalytic oxidation furnace, to produce the heat by water vapor, thus high temperature and high pressure water steam is obtained to drive the steam turbine to generate electricity. The utilization rate of low concentration methane gas is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for utilization of low concentration gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the system for utilization of low concentration gas. (Drawing includes non-English language text)    Pneuma mine gas source (1)    Gas (2)    VPSA purifying device (4)    Gas mixing device (5)    Second filter dust-removing device (6)    Catalytic oxidation furnace (7)
NOVELTY - System comprises photobioreactor vessel having container having a vertical dimension more than any linear horizontal direction and having a top end and a bottom end, top closure and a watertight bottom closure disposed to cover the top end and the bottom end of the container, respectively, an illuminator emitting light energy and comprising several horizontal sheets spaced apart by a vertical distance, each sheet having several apertures formed to permit fluid flow between opposing sides of the sheet and first inlet.    USE - The system and method are useful for growing biomass in photobioreactor (all claimed).    ADVANTAGE - The system is cost-effective, and provides good growth conditions, and contamination control.    DETAILED DESCRIPTION - System comprises photobioreactor vessel having container having a vertical dimension more than any linear horizontal direction and having a top end and a bottom end, top closure and a watertight bottom closure disposed to cover the top end and the bottom end of the container, respectively, an illuminator emitting light energy and comprising several horizontal sheets spaced apart by a vertical distance, each sheet having several apertures formed to permit fluid flow between opposing sides of the sheet and first inlet at a bottom portion of the photobioreactor vessel adapted to receive a pressurized gas. An INDEPENDENT CLAIM is included for method of growing biomass in a photobioreactor.
NOVELTY - Organic soil for plant growth is prepared by mixing artificial corrosion soil and bark compost prepared from e.g. wooden parts, and bark parts. The artificial corrosion soil is prepared by immersing tree parts in wood vinegar, corroding shredded tree parts, and pressing into short fibers. The bark compost is prepared by peeling off woody part of Japanese cedar bark, piling up in a mountain-shaped stack, setting in an anaerobic fermentation state to form corroded bark, and pressing corroded Japanese cedar bark into short fiber-like bark compost.    USE - The organic soil is useful for plant growth (claimed).    ADVANTAGE - The organic soil is available qualitatively, quantitatively, and economically.    DETAILED DESCRIPTION - Organic soil for plant growth is prepared by mixing artificial corrosion soil and bark compost prepared from raw wooden parts, leaf parts, and bark parts of normally pruned trees or trees shredded with a blade. The artificial corrosion soil is prepared by immersing tree parts in wood vinegar for 27 days or more, the shredded tree parts began to corrode, setting as artificial corrosion soil, and pressing artificial corrosion soil into short fiber-like artificial corrosion soil. The bark compost is prepared by peeling off woody part of Japanese cedar bark, piling up the peeled off woody portion in a mountain-shaped stack in large quantities, setting the inside of piled-up stack in an anaerobic fermentation state, allowing the stack to stand for 3 years or more to form corroded bark, and pressing the corroded Japanese cedar bark into short fiber-like bark compost.
NOVELTY - A nitrogen-containing compound (I), is new.    USE - New nitrogen-containing compound is used for composition for sweetening fluid and gas (claimed) in oil and gas industries, as or liquid produced or used in a waste-water process, farm, slaughter house, land-fill, municipality waste-water plant, coking coal process, and biofuel process, and scavenging hydrogen sulfide and/or mercaptans from gas or liquid stream.    ADVANTAGE - The nitrogen-containing compound has high absorbing effect with respect to hydrogen sulfide.    DETAILED DESCRIPTION - A nitrogen-containing compound of formula (I), is new.    R1-R3=H, alkylenyl, alkenylenyl, alkynylenyl, alkyl, alkenyl, or alkynyl (all optionally substituted);    k,l,m=0-25;    k+l+m=more than 0;    x,y,z=0-1;and    x+y+z=1-3.    (i) When x is 0, R1 is H, alkyl, alkenyl, or alkynyl; (ii) When x is 1, R1 is alkylenyl, alkenylenyl, or alkynylenyl; (iii) When y is 0, R2 is H, alkyl, alkenyl, or alkynyl; (iv) When y is 1, R2 is alkylenyl, alkenylenyl, or alkynylenyl; (v) When z is 0, R3 is H, alkyl, alkenyl, or alkynyl; (vi) When z is 1, R3 is alkylenyl, alkenylenyl, or alkynylenyl; (vii) When x is 1, y is 1, z is 1, k is 1, l is 1, and m is 1, R1-R3 are not simultaneously unsubstituted 2C alkylenyl; (viii) When x+y+z is 3, R1-R3 is unsubstituted 2C alkylenyl; and (ix) When x is 1, y is 1 and z is 0, R1 and R2 are unsubstituted 2C alkylenyl, and R3 is unsubstituted 1C alkyl or H. INDEPENDENT CLAIMS are included for the following:    (1) composition, which comprises compound (I); and    (2) method of sweetening fluid or gas, which involves treating the fluid or gas with an effective amount of the composition comprising compounds of formula (I).
NOVELTY - The system has a fluorocarbon refrigeration system for cooling natural gas to produce liquefied natural gas (LNG) using mixed fluorocarbon refrigerant. A nitrogen rejection unit (NRU) removes nitrogen from the LNG. A nitrogen refrigeration system cools natural gas to produce LNG using nitrogen refrigerant. An auto-refrigeration system cools natural gas to produce the LNG. The fluorocarbon refrigeration system includes a heat exchanger e.g. direct heat exchanger, to cool natural gas via indirect exchange of heat between natural gas and the mixed fluorocarbon refrigerant.    USE - Hydrocarbon processing system for facilitating formation of LNG production in a gas processing industry.    ADVANTAGE - The system considers normal boiling point and melting point for temperature of the mixed refrigerant to be above freezing point during an entire refrigeration cycle in selecting a set of fluorocarbons for the mixed refrigerant such that the refrigerant does not form solids and cause plugging in the system to be above atmospheric pressure during the entire refrigeration cycle to avoid air contamination of the mixed refrigerant for natural gas processing or liquefaction in an effective manner.    DETAILED DESCRIPTION - The refrigerant is selected from a group consisting of ISCEON (RTM: non-ozone-depleting HFC retrofit refrigerant) family of refrigerant, SUVA (RTM: HFC retrofit refrigerant) family of refrigerant, OPTEON (RTM: lower global warming potential refrigerant) family of refrigerant and a FREON (RTM: CFC and HCFC refrigerant) family of refrigerant. An INDEPENDENT CLAIM is also included for a method for facilitating LNG production.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating operation of a single stage refrigeration system.    Single stage refrigeration system (100)    Expansion device (102)    Saturated liquid refrigerant (112)    Saturated vapor refrigerant (118)    Saturated or slightly sub-cooled liquid refrigerant (120)
NOVELTY - Support device for many parallelly extending elongated bioreactor elements (1) with at least partially transparent wall made of plastic, comprises many stationary supporting poles (2), which are arranged in a horizontally spaced manner along the bioreactor elements. A nutrient solution, which is inoculated with microorganism, is led into the bioreactor elements for the production of biomass by photosynthesis. At least one supporting element extends between at least two supporting poles over the respective bioreactor elements, which are to be supported.    USE - The support device is useful for many parallelly extending elongated bioreactor elements with at least partially transparent wall made of plastic.    ADVANTAGE - The support device: is produced and assembled in a cost efficient manner; and produces compact bioreactor elements in a simple manner.    DETAILED DESCRIPTION - Support device for many parallelly extending elongated bioreactor elements (1) with at least partially transparent wall made of plastic, comprises many stationary supporting poles (2), which are arranged in a horizontally spaced manner along the bioreactor elements. A nutrient solution, which is inoculated with microorganism, is led into the bioreactor elements for the production of biomass by photosynthesis. At least one supporting element extends between at least two supporting poles over the respective bioreactor elements, which are to be supported. The supporting element is supported corresponding at the supporting poles. The bioreactor element, which is to be supported, is connected on at least one supporting point lying between the two support poles with at least one supporting element via at least one holding element.    DESCRIPTION OF DRAWING(S) - The figure shows cross-sectional view of the support device.    Bioreactor elements (1)    Supporting poles (2)    Support arm (5)    Lifting device (6)    Guiding device (11)
NOVELTY - Bioreactor element with a major longitudinal extension and at least partial transparent wall (2) made of plastic material for passing a nutrient solution (1) inoculated with microorganisms for producing biomass by means of photosynthesis, comprises many parallel channels. The bioreactor element is integrally formed. A nutrient channel (3) flows through the nutrient solution and at least one influencing channel (4) flows through a fluid influencing the production of the biomass.    USE - The bioreactor element is useful for passing a nutrient solution inoculated with microorganisms for producing biomass by means of photosynthesis.    ADVANTAGE - The bioreactor element is produced in a cost efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the bioreactor element, comprising producing the bioreactor element by means of a mobile extruder (8), which is brought in the vicinity of the operating site of the bioreactor element.    DESCRIPTION OF DRAWING(S) - The figure shows a cross sectional view of the bioreactor element.    Nutrient solution (1)    Wall (2)    Nutrient channel (3)    Influencing channel (4)    Heating fluid (6)
NOVELTY - Device for producing vegetable charcoal (6) and generating heat, comprises a motor fuel conveying means (2) for conveying biomass fuel (1) in a burner (3), and a vegetable charcoal conveyor (5) for draining vegetable charcoal produced into the burner from the burner. The burner is provided for carbonizing the conveyed biomass fuel to vegetable charcoal and combusting the released volatile substances for heat recovery.    USE - The device is useful for producing vegetable charcoal and generating heat, where the generated heat is used for heating network, preferably many heating networks detected as building (all claimed).    ADVANTAGE - The device comprises the burner, which is compact and easier to use, and is used for permanent method and quality control.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device.    Biomass fuel (1)    Motor fuel conveying means (2)    Burner (3)    Vegetable charcoal conveyor (5)    Vegetable charcoal (6)
NOVELTY - A hydrogen generating apparatus (100) comprises modifier (1) which produces hydrogen-containing gas by reforming reaction using source gas, hydrodesulfurization device (2) which removes sulfur compound in source gas supplied to modifier, hydrogen-containing gas flow path (3) which flows hydrogen-containing gas generated by modifier, and recycle gas flow path (4) which supplies part of hydrogen-containing gas flowing through hydrogen-containing gas flow path to hydrodesulfurization device and branches from hydrogen-containing gas flow path.    USE - A hydrogen generating apparatus for fuel cell system (claimed) or electric power generation system.    ADVANTAGE - Clogging of recycle gas flow path can be suppressed, and stable hydrodesulfurization reaction in hydrodesulfurization device can be performed.    DETAILED DESCRIPTION - A hydrogen generating apparatus (100) comprises modifier (1) which produces hydrogen-containing gas by reforming reaction using source gas, hydrodesulfurization device (2) which removes sulfur compound in source gas supplied to modifier, hydrogen-containing gas flow path (3) which flows hydrogen-containing gas generated by modifier, and recycle gas flow path (4) which supplies part of hydrogen-containing gas flowing through hydrogen-containing gas flow path to hydrodesulfurization device and branches from hydrogen-containing gas flow path. Branch part of recycle gas flow path is formed so that edge part of upstream of recycle gas flow path may protrude to inner side of hydrogen-containing gas flow path. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text).    Modifier (1)    Hydrodesulfurization device (2)    Hydrogen-containing gas flow path (3)    Recycle gas flow path (4)    Hydrogen generating apparatus (100)
NOVELTY - The method involves purifying coke furnace pneuma by primary desulfurization using iron oxide agent, ferro manganese agent or zinc oxide agent. The three methanation reactors are connected together, and are provided with nickel series methanation catalyst. The coke furnace gas is made to enter into first methanation reactor to remove the carbon-di-oxide. The reaction pressure of the gas is controlled in the second methanation reactor. The gas is circulated in fine desulfurization section. The second methanation reactor is set with diluted pneuma mixer.    USE - Preparing method of methane from synthetic natural gas of coke furnace.    ADVANTAGE - The yield of methane is increased and coke furnace synthetic natural gas emission is reduced. The carbon-di-oxide emission to the environment is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating preparing process of methane from synthetic natural gas. (Drawing includes non-English language text)
NOVELTY - The apparatus has second hemi-enclosure (103) that is not integral with first hemi-enclosure (101). A diaphragm electrode array (105) is positioned between first and second hemi-enclosure which comprises a diaphragm (109). A fastener is provided for leak-tight fastening of first hemi-enclosure, the diaphragm electrode array, and second hemi-enclosure, in which a leak-tight enclosure is formed. The contacts are provided for electrically contacting first and second multiple electrodes and pathways are provided to separately remove hydrogen and oxygen gases from the enclosure.    USE - Apparatus for electrolytic splitting of water into hydrogen and oxygen gas.    ADVANTAGE - The externally exposed edges and faces of the diaphragm are sealed to prevent leakage. By slightly loosening the fittings and fastening the replacement electrodes to the electrolyzer electrodes, replacement is achieved by sliding the electrodes to remove the spent apparatus electrodes and replacing them with new or refurbished replacement electrodes. The rotatable collars reduce friction so that the wire can be pulled through the electrolysis apparatus without disassembling it to provide fresh electrodes as needed. Thus the simplifying maintenance and reducing downtime of the electrolyzer apparatus are achieved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for making electrolyte apparatus; and    (2) an electrolysis apparatus for splitting water into hydrogen and oxygen gases using electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of the electrolyzer apparatus.    First hemi-enclosure (101)    Second hemi-enclosure (103)    Diaphragm electrode array (105)    First multiple electrodes (107)    First side of diaphragm (109)
NOVELTY - The fabrication method involves mounting a diaphragm (109) on a wire-applying machine, then applying wire in a first vicinity of a first side and a second vicinity in the second opposed side of the diaphragm using the machine. A first hemi-enclosure (101), the wire, the diaphragm, and a second hemi-enclosure (103) are fastened together, forming a leak-tight enclosure. The wire is then trimmed.    USE - Fabrication method for diaphragm electrode array used in electrolyzer apparatus.    ADVANTAGE - Enables provision of an electrolyzer apparatus with simplified electrode replacement and servicing, since the removal of spent electrodes is achieved by sliding electrodes in an out of the electrolyzer without disassembly of the apparatus. Simplifies the structural design, implements modern automation technology, and minimizes the amount of metal needed for fabrication.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for the electrolytic splitting of water into hydrogen and oxygen gases.    DESCRIPTION OF DRAWING(S) - The drawings show the exploded and assembled views respectively, of an electrolyzer apparatus comprising continuous zone hemi-enclosures.    First hemi-enclosure (101)    Second hemi-enclosure (103)    Diaphragm electrode array (105)    Diaphragm (109)    Dividing line (111)
NOVELTY - A seeding agent is manufactured by performing aerobic fermentation on raw material containing organic waste and auxiliary material at 50 degrees C, plowing after 5 days, drying for greater than or equal to 2 weeks immediately after fermentation until moisture content is less than or equal to 40% by supplying air, plowing fermented raw material, and drying dried raw material after in time shorter than the time required for 1st drying process until moisture content is less than or equal to 40%.    USE - Manufacture of seeding agent for wastewater treatment.    ADVANTAGE - Microorganisms contained in seeding agent are obtained at a low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid seeding agent which is obtained by putting seeding agent into mold and press-hardening.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the manufacturing method of a seeding agent. (Drawing includes non-English language text).
NOVELTY - A transformed micro algae, is new. The transformed micro algae are obtained by introducing glycerol kinase gene into the micro algae which has oil storing ability.    USE - The transformed micro algae are useful for producing biofuel (claimed).    ADVANTAGE - The transformed micro algae improves biomass quantity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M1) for culturing the transformed micro algae, involves culturing the micro algae using culture medium containing glycerol; and    (2) method (M2) for producing biofuel, involves performing methyl-esterification of triglyceride obtained from oil component extracted from transformed micro algae and decomposing triglyceride into into fatty-acid methyl ester and glycerol.
NOVELTY - The apparatus has heat exchanger (50) that is connected to the to the shock-absorbing water storage tank (20) through pressurization transfer pump (30) and circulation pump (40). The circulating sludge and high temperature high pressure steam is flowed into the hydraulic screw stirred type heat index melting reactor (60) which is coupled to heat exchanger. The pressure control unit (90) is connected to the solubilization sludge storage of the boiler (80) for controlling the pressure so that the continuous operation is possible.    USE - Continuous operation device for solubilization of organic waste in waste water disposal plant, livestock excretion, and food waste water.    ADVANTAGE - The efficiency of the energization process, dehydration process and anaerobic digestion is improved by the solubilization of organic waste. The energy quantity required for processing sludge is minimized and the yield of biogas is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for continuous operation method for solubilization of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the continuous operation device for solubilization of organic waste.    Shock-absorbing water storage tank (20)    Pressurization transfer pump (30)    Circulation pump (40)    Heat exchanger (50)    Hydraulic screw stirred type heat index melting reactor (60)    Boiler (80)    Pressure control unit (90)
NOVELTY - The gasifier (10) has a gas supply flow path (11) that is provided to guide the generated combustible gas to a char collection apparatus (30). A bypass main flow path (91) is branched from the gas supply flow path in the upstream of char collection apparatus, to provide a flare installation (90). A dust collector (93) is mounted in the bypass main flow path. A flow-path entrance on-off valve (12) is provided in branch position downstream of the gas supply flow path that results in char collection apparatus, and the bypass main flow path.    USE - Gasifier of integrated coal gasification combined cycle (IGCC) power generation apparatus for gasifying solid carbonaceous fuel such as biomass fuel e.g. coppiced timber, waste material wood, driftwood, grass, waste material, sludge and tire, and gasifying agent.    ADVANTAGE - Since the char released from the flare installation through the flow path which bypasses the filter is prevented, the generation of temporary black smoke at the time of gasifier starting is prevented or suppressed in efficient manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a gasification composite power generation equipment; and    (2) a method for starting gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a systematic view illustrating the supply system of combustible gas generated by gasifier. (Drawing includes non-English language text)    Gasifier (10)    Gas supply flow path (11)    Flow-path entrance on-off valve (12)    Char collection apparatus (30)    Flare installation (90)    Bypass main flow path (91)    Dust collector (93)
NOVELTY - 3,6-Dichloro-2-methoxybenzoic acid is obtained by reacting 2,5-dichloroanisole and dichloromethyl ether, hydrolyzing to obtain 2-methoxy-3,6-dichlorobenzaldehyde, and reacting 2-methoxy-3,6-dichlorobenzaldehyde with an oxidizing agent. The oxidizing agent is sodium hypochlorite, sodium hypobromite, potassium hypochlorite, potassium hypobromite, and/or hydrogen peroxide.    USE - Synthesis of 3,6-dichloro-2-methoxybenzoic acid (claimed).    ADVANTAGE - The method enables easy and environmentally-friendly industrial synthesis of 3,6-dichloro-2-methoxybenzoic acid with high yield, without using high-pressure carboxylation and discharging large amount of waste materials.
NOVELTY - Synthesizing (S)-2-benzyloxy-3-pentanone, comprises (i) using L-methyl lactate or L-ethyl lactate as raw material, under the action of catalyst and N,O-dimethylhydroxylamine hydrochloride, synthesizing (S)-2-hydroxy-N-methoxy-N-methyl-propionamide, i.e. referred to as compound A, (ii) adding benzyl protecting group to the compound A, to obtain (S)-2-benzyloxy-N-methoxy-N-methyl-propionamide, i.e. referred to as compound B, and (iii) adding Grignard reagent in compound B, carrying out ethyl group addition reaction to obtain the final product.    USE - The method is useful for synthesizing: (S)-2-benzyloxy-3-pentanone (claimed), and posaconazole.    ADVANTAGE - The method uses economical and easily available raw materials, comprises easy to control reaction process, has simple operation process, produces single product with high yield; is economical and environmentally friendly; is suitable for industrialized production, and produces product with enantiomeric excess (ee) value greater than 99%.
NOVELTY - The apparatus (100) has a hydrodesulfurization device (3) which removes a sulfur compound in a raw material. A modifier (4) generates a hydrogen-containing-gas using the raw material supplied from the hydrodesulfurization device. A second cylindrical wall (22) is provided coaxially with respect to a first cylindrical wall (21). An electric heater (6) is annularly extended in axial direction of the first cylindrical wall and provided in a gap (7) formed between first and second cylindrical walls while folding back in the axial direction of the first cylindrical wall.    USE - Hydrogen generating apparatus of fuel cell system (claimed).    ADVANTAGE - Since the electric heater is annularly extended in axial direction of the first cylindrical wall and provided in the gap formed between first and second cylindrical walls while folding back in the axial direction of the first cylindrical wall, the ability of heating the desulfurizer is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a vertical cross-sectional view of the structure of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrodesulfurization device (3)    Modifier (4)    Electric heater (6)    Gap formed between cylindrical walls (7)    Cylindrical walls (21,22)
NOVELTY - Treatment of livestock waste, involves: (a) acidifying cattle manure to reach a pH value between 3.5 and 6.5; (b) vaporizing the water present in the cattle manure acidified in step (a) to obtain water vapor from cattle manure and fertilizers concentrate; (c) cooling the steam obtained in step (b) to obtain a condensed water from the ejecta; (d) subjecting the condensate obtained in step (c) to an oxidizing treatment selected from: oxygen, air, oxygen enriched air or oxygen; oxygen in the presence of oxidation catalysts; halogenated adding chemical oxidants, or a combination.    USE - The process is useful for treating livestock waste (claimed).    ADVANTAGE - The process is cost-efficient and provides efficient treatment of livestock waste and, in particular, liquids, such as those from pig farms (pig purines), in order to separate and recover fertilizer material contained in it in the form of a concentrate or solid product, for use as a fertilizer which can be transported to remote agricultural areas once the water has been separated by vaporization.
NOVELTY - The method involves forming interface among the catalyst layers, such that a catalyst layer (230)increases the triple phase boundary in the interface with an uneven part (212) of an electrolysis chilled layer. A portion of the material is slipped down on the surface of a porous scaffold (202) to the pore of the porous scaffold to form another catalyst layer. The porous scaffold formed is removed in one side of the electrolyte layers (210,220). Another electrolyte layer is made of yttria-stabilized zirconia electrolyte. The catalyst layers is made of platinum, palladium, nickel and ruthenium.    USE - Method for manufacturing fuel cell stack.    ADVANTAGE - The portion of the material is slipped down on the surface of a porous scaffold to the pore of the porous scaffold to form catalyst layer and the porous scaffold formed is removed in one side of the electrolyte layers, thus reduces activation loss according to the material transmitted from the manufacturing process and increases the performance of the fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a fuel cell stack manufacturing method.    Porous scaffold (202)    Electrolyte layers (210,220)    Uneven part (212)    Catalyst layer (230)
NOVELTY - A method (M1) relating to biomass torrefaction involves producing combustion gases, which includes using an oxidation catalyst; and introducing the resultant combustion gases into a torrefaction reactor.    USE - As method relating to biomass torrefaction; and as system for biomass torrefaction (claimed).    ADVANTAGE - The oxidation catalyst provides a low residual-oxygen flue gas stream that can be used directly in the reactor and/or cooler with improved heat integration and lowers capital or operating costs. The low residual-oxygen flue gas stream from the catalytic oxidation combustion is directly used in the cooler, which eliminates the need to separately purchase inert gas for the cooler.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) relating to biomass torrefaction involving producing combustion gases, which includes using an oxidation catalyst, and introducing the resultant combustion gases into a cooler;    (2) system (S1) for biomass torrefaction comprising a catalyst system including an oxidation catalyst, where the resultant combustion gases produced thereby are directly reusable by the system to support torrefaction of biomass and/or to support cooling of torrefied biomass.
NOVELTY - Storing and transporting energy involves releasing hydrogen (162) from water at a first location using energy from a first energy source; storing the released hydrogen in a metal hydride slurry (152); and transporting the metal hydride slurry to a second location remote from the first location.    USE - For storing and transporting energy in the form of hydrogen used as an energy source (claimed) for a vehicle e.g. car.    ADVANTAGE - The method safely and easily transports energy in the form of hydrogen by incorporating it into a metal hydride. The slurry is easy for refueling.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system, comprising an electrolyzer to extract hydrogen from water using energy from a first energy source at a first location, and a charging device coupled to electrolyzer, where the charging device comprises a slurry inlet, a slurry outlet, and a heating device capable of heating a slurry in the charging device to at least 320 degrees C; or first device to produce hydrogen using electricity from a first energy source, a metal hydride slurry charging device coupled to the first device, a metal hydride slurry storage vessel coupled to the metal hydride slurry charging device, and a pump to pump a slurry from the metal hydride slurry charging device to the metal hydride slurry storage vessel.    DESCRIPTION OF DRAWING(S) - The figure shows view of a metal hydride charging device.    Charging apparatus (150)    Metal hydride slurry (152)    Pump (154)    Hydrogen (162)    Gas inlet (163)
NOVELTY - The method comprises: sorbing a liquid hydrocarbon fuel to a gasification catalyst to form a sorbed hydrocarbon fuel; heating the sorbed hydrocarbon fuel at a first temperature of 80-300 degrees C for a first period of time sufficient to form coke; and gasifying the coke at a second temperature of 400-1000 degrees C at a pressure for a second period of time in the presence of water and/or oxygen so as to produce a gaseous mixture comprising hydrogen gas and carbon monoxide and to regenerate the catalyst. The liquid hydrocarbon fuel is a liquid biomass, a liquefied biomass, or pyrolysis oil.    USE - The method is useful for producing hydrogen gas (claimed) that is useful in an oil refinery.    ADVANTAGE - The method is capable of simply, economically and efficiently producing hydrogen without significant increase in carbon dioxide levels.    DETAILED DESCRIPTION - The method comprises: sorbing a liquid hydrocarbon fuel to a gasification catalyst to form a sorbed hydrocarbon fuel; heating the sorbed hydrocarbon fuel at a first temperature of 80-300 degrees C for a first period of time sufficient to form coke; and gasifying the coke at a second temperature of 400-1000 degrees C at a pressure for a second period of time in the presence of water and/or oxygen so as to produce a gaseous mixture comprising hydrogen gas and carbon monoxide and to regenerate the catalyst. The liquid hydrocarbon fuel is a liquid biomass, a liquefied biomass, or pyrolysis oil. The gasification catalyst has a particle size distribution of 50-100 mu m. The first period of time is 1-10 minutes. The method further comprises: subjecting the gaseous mixture to a water-gas shift to produce additional hydrogen gas; and isolating the hydrogen gas and the additional hydrogen gas from the gaseous mixture. The method is carbon neutral.
NOVELTY - Microorganism co-culture for conversion of at least one of carbon monoxide or carbon dioxide and hydrogen to butanol comprises two or more microorganisms collectively having a nucleotide sequence identity of at least 95% to 1056 nucleotide sequence (SEQ ID NO: 1) fully defined in the specification and nucleotide sequence identity of at least 70% to 1314 nucleotide sequence (SEQ ID NO: 2) fully defined in the specification or nucleotide sequence identity of at least 65% to 1113 nucleotide sequence (SEQ ID NO: 3) fully defined in the specification.    USE - The microorganism co-culture is useful for conversion of at least one of carbon monoxide or carbon dioxide and hydrogen to butanol (claimed) which is used as motor fuel.    ADVANTAGE - The microorganism co-culture enables to convert carbon monoxide or carbon dioxide and hydrogen to butanol with high yield, and cost-effectively.    DETAILED DESCRIPTION - Microorganism co-culture for conversion of at least one of carbon monoxide or carbon dioxide and hydrogen to butanol comprises two or more microorganisms collectively having a nucleotide sequence identity of at least 95% to 1056 nucleotide sequence (SEQ ID NO: 1) fully defined in the specification and nucleotide sequence identity of at least 70% to 1314 nucleotide sequence (SEQ ID NO: 2) fully defined in the specification or nucleotide sequence identity of at least 65% to 1113 nucleotide sequence (SEQ ID NO: 3) fully defined in the specification or has nucleotide sequence defining a gene for NADPH dependent acetyl-CoA reductase and nucleotide sequence defining a gene for at least one of a butyryl-CoA acetate transferase and butyrate kinase.
NOVELTY - Liquefied gas fuel comprises easily liquefiable hydrocarbon compounds having 3 or 4 carbon atoms, and natural lipids, for classifying into at least three water hazard classes, preferably e.g. (a1) 5-95 wt.% easily liquefiable hydrocarbon compounds having 3 or 4 carbon atoms, preferably e.g. propane, propene, butane and butene, and (b1) 5-95 wt.% natural lipids (for water hazard class 0); and (a2) 2-98 wt.% easily liquefiable hydrocarbon compounds having 3 or 4 carbon atoms, preferably e.g. propane, propene, butane and butene, and (b2) 2-95 wt.% natural lipids (for water hazard class 1).    USE - The liquefied gas fuel is useful for internal combustion engines, preferably air-compressing and self-igniting internal combustion engines (claimed).    ADVANTAGE - The fuel reduces the emission of carbon dioxide and soot particles, and can be produced in pure form and thus it can be directly used in engine.    DETAILED DESCRIPTION - Liquefied gas fuel comprises easily liquefiable hydrocarbon compounds having 3 or 4 carbon atoms, and natural lipids, for classifying into at least three water hazard classes, preferably (a1) 5-95 wt.% easily liquefiable hydrocarbon compounds having 3 or 4 carbon atoms, preferably propane, propene, butane, butene, isobutane and/or isobutene, and (b1) 5-95 wt.% natural lipids (for water hazard class 0); (a2) 2-98 wt.% easily liquefiable hydrocarbon compounds having 3 or 4 carbon atoms, preferably propane, propene, butane, butene, isobutane and/or isobutene, and (b2) 2-95 wt.% natural lipids (for water hazard class 1); or (a3) 5-95 wt.% easily liquefiable hydrocarbon compounds having 3 or 4 carbon atoms, preferably propane, propene, butane, butene, isobutane and/or isobutene, and (b3) 3-95 wt.% natural lipids (for water hazard class 2). The liquid fuel respectively in the water hazard classes 0, 1 and 2, is present under a pressure of 2-8 bars at ambient temperature.
NOVELTY - A biofuel formulation comprises: A) crude glycerol, B) glycerol formal, C) optionally fatty acid glycerol formal ester, and D) optionally fatty acid methyl ester.    USE - As biofuel formulation for burning purposes (claimed).    ADVANTAGE - The composition exhibits improved burning characteristics when compared to crude glycerol which fulfill the need for efficient and renewable fuels. The glycerol-based biofuel formulation circumvents the inability of crude glycerol to burn consistently in current burners. The composition shows better burning characteristics of the biofuel as compared to crude glycerol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process for the preparation of the biofuel formulation involving the step of mixing crude glycerol, glycerol formal, fatty acid glycerol formal ester, fatty acid methyl ester and at least one optional additive.
NOVELTY - Power supply device comprises: a fuel cell system (200) for forming electricity by electrochemical reaction when supplied with fuel, and supplying electric power to a power demanding source (100) by converting electricity to electric power; a secondary battery (300) for supplying electric power to power demanding source of the fuel cell system during malfunctioning; and a fuel supply system (400) for storing fuel, provided with a hydrogen tank (401) and oxygen tank, and for supplying fuel to the fuel cell system.    USE - The power supply device is useful for supplying power to a buoy (claimed).    ADVANTAGE - The power supply device supplies electric power to the buoy in stable manner, can be maintained in easy manner, and is environmentally friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the power supply device for supplying power to buoy (Drawing includes non-English language text).    Power demanding source (100)    Fuel cell system (200)    Secondary battery (300)    Fuel supply system (400)    Hydrogen tank (401)
NOVELTY - Synthesizing methane, comprises generating plasma by applying voltage to a catalytic reactor, and reacting hydrogen and carbon monoxide by activating a catalyst using plasma, where hydrogen and carbon monoxide reacts in the presence of the catalyst within the catalytic reactor.    USE - The method is useful for synthesizing methane (claimed).    ADVANTAGE - The method significantly increase the speed of the synthesis reaction and production efficiency, synthesizes methane at low temperature, is economical, and improves conversion ratio of carbon monoxide in the lower temperature by activating the catalyst using low-temperature plasma.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for methane synthesizing device comprising a reactor inserting a stainless steel rod inside a quartz tube, where the inner wall of the quartz tube and the stainless steel rod is filled with catalyst. The device generating plasma by applying voltage and synthesizing methane by reacting hydrogen and carbon monoxide in the presence of the catalyst within the catalytic reactor.
NOVELTY - The catalyst composition comprises a mixture of liquid and solid catalysts for transesterification of vegetable oils, animal fats and their mixtures for producing vegetable esters. A mixture of solid alkali metal alkoxide or alkaline earth metal having a particle size of 2-5000 microns, is combined with liquid alkali metal alkoxide or alkaline earth metal.    USE - Catalyst composition used for producing biodiesel fuel used in diesel engines.    ADVANTAGE - The catalyst composition effectively reduces costs of production, and improves processes and conversion rate of vegetable oils, animal fats and their mixtures.
NOVELTY - Mesoporous nickel-iron-ruthenium-alumina xerogel catalyst comprises 49-68.8 pts. wt. alumina, 30-40 pts. wt. nickel, 1-10 pts. wt. iron, and 0.2-1 pts. wt. ruthenium.    USE - The catalyst is useful in methanation process for producing methane from carbon dioxide (claimed).    ADVANTAGE - The catalyst exhibits improved reaction speed and selectivity; can be manufactured by simple method which provides catalyst with high reproducibility; and provides methane with improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing the xerogel catalyst, comprising heating an alcohol, dispersing aluminum precursor in hot alcohol, hydrating the aluminum precursor dispersed in alcohol with a mixture of acid and water, cooling the formed sol, orderly adding nickel precursor, iron precursor and ruthenium precursor to cooled sol to obtain nickel-iron-ruthenium-aluminum sol, cooling, adding water and ethanol mixture, hydrating to form a gel, drying the gel, heat-treating the dried gel and aging.
NOVELTY - The system comprises three purification units, a vacuum pump, two return lines and a gas separator. The first purification unit producing a first refinery gas by purifying a first waste gas via a membrane separation system, and is provided with a presser portion for compressing the pressure of refinery gas at high pressure. The second purification unit for producing a second refinery gas by purifying second waste gas via a pressure swing adsorption (PSA) system. The third purification unit is carried out by purifying third waste gas via the membrane separation system.    USE - The system is useful for separating gas (claimed) such as methane from gas well.    ADVANTAGE - The system efficiently and simply separates methane from gas well with high purity in a cost effective and less time consuming manner.    DETAILED DESCRIPTION - The system comprises three purification units, a vacuum pump, two return lines and a gas separator. The first purification unit producing a first refinery gas by purifying a first waste gas via a membrane separation system and is provided with a presser portion for compressing the pressure of refinery gas at high pressure. The second purification unit for producing a second refinery gas by purifying second waste gas via a pressure swing adsorption (PSA) system. The third purification unit for producing third refinery gas is carried out by purifying a third waste gas via the membrane separation system. The vacuum pump for pumping to the waste gas separated from the second purification unit at low pressure. The presser portion is arranged at a front end of a buffer tank, in which the third refinery gas is introduced. The gas separator includes a first return line, which guides the second waste gas separated from the second purification unit to the buffer tank, and a second return line which guides the third purified refinery gas to the buffer tank. An INDEPENDENT CLAIM is included for a method for separating gas.
NOVELTY - Solid fuel comprises mixture of 15-99 wt.% first fuel composition comprising waste wood powder, sawdust, wood chip fuel containing fine waste wood and/or forest tree, and 1-85wt.% second fuel composition comprising dried and crushed sewage and manure sludge or crushed mixed waste plastic.    USE - Used as solid fuel.    ADVANTAGE - The solid fuel has high heating value and combustible content; low moisture and ash content; excellent yield and production rate; and contains reduced amount of hazardous material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing solid fuel using waste comprising: (a) preparing first fuel composition including waste wood powder, sawdust, wood chips purely waste wood and/or forest tree; (b) preparing second fuel composition including dried and crushed sewage and manure sludge or crushed mixed waste plastic; and (c) preparing the mixture by mixing the first fuel composition and the second fuel composition.
NOVELTY - Fuel cell system comprises fuel cell, water-gas shift reactor, hydrogen generator, hydrogen separator. The fuel cell is capable of producing electricity using fuel. The hydrogen generator is installed within the fuel cell for generating hydrogen by supplying the fuel to the generator. The water-gas shift reactor capable for generating hydrogen, carbon dioxide and water by reacting exhaust gas discharged from the anode of the fuel cell. The hydrogen separator separates hydrogen and carbon dioxide generated from the water-gas shift reactor.    USE - The fuel cell system is useful for producing electricity.    ADVANTAGE - The system enables to produce electricity within fuel cell.
NOVELTY - Processing of citrus pomace biomass comprises pretreating the citrus pomace biomass by puffing and swelling at high pressure and high temperature.    USE - The method is useful for processing citrus pomace biomass for manufacturing bioethanol and culture medium composition (all claimed).    ADVANTAGE - The method: utilizes the citrus pomace that be used as raw material for manufacturing bio-cellulose, biomass, functional ingredients, dietary fiber and animal, thus enabling in efficient recycling and protecting the environment; and reduces the formation of tiny citrus pomace fibers by increasing the efficiency of enzymatic degradation, thus reducing cost and time, while providing the bacterial cellulose in an economical manner and at high yields with the ideal way for waste treatment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) making bioethanol, comprising pretreating the citrus pomace biomass as above per se and subjecting the pretreated biomass to alcoholic fermentation; and    (2) producing culture medium composition, comprising pretreating the citrus pomace biomass as above per se and contacting the pretreated biomass with cellulose degrading microorganism.
NOVELTY - Higher calorific power methane synthesis catalyst comprises 10-70 pts. wt. based on 100 pts. wt. of catalyst of nickel, 1-10 pts. wt. of metal element comprising iron, cobalt, zirconium, cerium or gallium and remainder of metal support.    USE - The higher calorific power methane synthesis catalyst is useful in manufacturing of the methane and synthetic natural gas, and in Fischer Tropsch synthesis (claimed).    ADVANTAGE - The catalyst: can be used in the ratio of less than 3 for the manufacturing of synthesis gas; reduces the amount of conversion of carbon monoxide into carbon dioxide; allows the production of methane with less than 10% of 2-5 carbons hydrocarbons; does not need to be mixed with the fuel gas comprising liquefied petroleum gas; can be directly supplied to the synthesis gas production through a pipeline; and provides simple manufacturing of methane and provides excellent reproducibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing the higher calorific power methane synthesis catalyst, comprising mixing 10-70 pts. wt. with respect to total of 100 pts. wt. of catalyst of the nickel precursor, 1-10 pts. wt. of the metal element comprising iron, cobalt, zirconium, cerium or gallium and impregnating or co-precipitating 30-90 pts. wt. based on total of 100 pts. wt. of catalyst of metal support with the mixture.
NOVELTY - The device comprises a vacuum pump connected with a synthesis gas storage tank, a pyrolysis gas-storage tank provided with a pipe and a first stirrer, a cooling water supply part connected to a cooling water line, and a synthesis gas reformer. The device further comprises a distillation tower for removing moisture in the pipe, a heat exchanger, a second stirrer, which thermally decomposes the biomass waste used in the lower part of the first stirrer, and a recycle pipe connected to the second stirrer.    USE - The device is useful for pyrolyzing biomass waste and reforming synthesis gas (claimed).    ADVANTAGE - The device improves the quality of the synthesis gas.    DETAILED DESCRIPTION - The device comprises a vacuum pump connected with a synthesis gas storage tank, a pyrolysis gas-storage tank provided with a pipe and a first stirrer, a cooling water supply part connected to a cooling water line, and a synthesis gas reformer. The device further comprises a distillation tower for removing moisture in the pipe, a heat exchanger, a second stirrer, which thermally decomposes the biomass waste used in the lower part of the first stirrer, and a recycle pipe connected to the second stirrer. The distillation tower and the heat exchanger are successively arranged on the pipe. An intermediate tank is provided between the distillation tower and the second stirrer. The pyrolysis gas-storage tank is provided with a jacket connected to a recycle pipe of a boiler. An INDEPENDENT CLAIM is included for a method for pyrolyzing biomass waste and reforming synthesis gas.
NOVELTY - A fuel pellet comprises petroleum coke having a sulfur content up to 5.5%; a biomass constituent; an alkali constituent adapted to capture sulfur dioxide (SO2) emissions by reacting with sulfur of the petroleum coke upon burn of the pellet; and an iron oxide catalyst reducing SO2 emissions to less than 10%; where the petroleum coke, the biomass constituent, the alkali constituent, and the iron oxide catalyst are combined to form a fuel pellet with decreased SO2 emission at greater than or equal to 750 degrees C.    USE - As fuel pellet (claimed) from high sulfur waste product, with reduced level of SO2 emission.    ADVANTAGE - The high sulfur fuel pellet reduces level of SO2 emission; reduces environmental impact of the waste product while still utilizing the fuel properties of the product. The high sulfur fuel pellet with reduced SO2 emissions includes a combination of high sulfur petroleum coke, biomass constituent and an alkali constituent. The biomass constituent may have enhanced reactivity by using the reactive CaO and slaking it in reactions that provide Ca(OH)2 with the most surface area. Selected particle sizes for the pet coke may increase the efficiency of SO2 capture. Further, the lime SO2 capture efficiency may be increased by incorporating surfactants in the lime preparation process. Such a fuel pellet may capture SO2 at temperatures as low as 750 degrees C and avoid the necessity of Fuel Gas Desulfurization (FGD) systems to handle high sulfur petroleum coke fuel. The pellet may be of a select hardness to maintain form regardless of environmental conditions, storage conditions.
NOVELTY - System comprises: an anaerobic digester (102) device comprising a tank reactor (101); a substrate comprising a waste material having anaerobically biodegradable components fed into the tank reactor; and a protein-rich co-substrate fed into the tank reactor with substrate to co-digest the substrate and the co-substrate in the device to produce a biomass, a biogas, and a waste product, where nitrogen in waste product and a high nitrogen organic and/or inorganic supplements are converted to a material comprising ammonia, where elevated ammonia concentrations are produced utilizing methanogens.    USE - The system is useful for high-nitrogen loading for ammonia processing via anaerobic digestion, which is useful for producing biogas (claimed) (mixture of carbon dioxide and methane).    ADVANTAGE - The system provides improved anaerobic digestion, and improved biogas production.    DETAILED DESCRIPTION - System comprises: an anaerobic digester device comprising a tank reactor (101); a substrate comprising a waste material having anaerobically biodegradable components fed into the tank reactor of the anaerobic digester (102); and a protein-rich co-substrate fed into the tank reactor of the anaerobic digester device with the substrate to co-digest the substrate and the co-substrate in the anaerobic digester device to produce a biomass, a biogas, and a waste product, where nitrogen in the waste product and a high nitrogen organic and/or inorganic supplements are converted to a material comprising ammonia, where elevated ammonia concentrations are produced utilizing methanogens.    DESCRIPTION OF DRAWING(S) - The figure illustrates high level flow chart of a method and system for high-nitrogen loading for ammonia processing via anaerobic digestion.    Tank reactor (101)    Anaerobic digester (102)    Buffer tank (103)    Storage unit (105)    Condensate shaft (107)
NOVELTY - This utility new type relates to sewage treatment device technology field, specifically is a one-section anaerobic-aerobic sewage treatment device, wherein the sewage processing device comprise a waste water pool, pool, an anaerobic tank, an aerobic tank, a sedimentation tank, a H/O biochemical tower and a drain tank, a waste water tank of said water inlet connecting water inlet of the integration pool, a comprehensive pool of the water port connecting the water inlet of first anaerobic tank, water outlet of said first anaerobic pool of connecting the water inlet of first aerobic tank to form anaerobic-aerobic treatment section, a second aerobic tank H/O biochemical tower connecting through sedimentation tank, sedimentation tank connecting a drain tank to form sewage biochemical sedimentation section. The new type provided by the utility model is a sewage treatment device, wherein the device realizes the aerobic treatment and anaerobic treatment, the special of multi-section processing technology so that the effect of sewage treatment;
NOVELTY - Method for producing organic fertilizer for rape seed cake involves drying weed, and pressing the top of fresh soil, burning and cooling the plant ash, adding the plant ash to rape seed cake, adding the mixture into fermentation tank and adding fermentation powder, performing spraying and submerging process using water, and piling and fermenting the mixture for 30-50 days.    USE - The method for producing organic fertilizer for rape seed cake (claimed).    ADVANTAGE - The method enables to produce organic fertilizer for rape seed cake simply and cost-effectively with balanced nutrition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for organic fertilizer for rape seed cake which is produced by the above-mentioned method.
NOVELTY - Composition and preparation of fertilizer are claimed. Fermented fertilizer comprises 50-55 pts. wt. beans, 40-45 pts. wt. bran, 40-45 pts. wt. waste orange, 20-23 pts. wt. tea tree branches, 2-3 pts. wt. garlic, 12-14 pts. wt. fulvic acid, 12-14 pts. wt. maifanite, 2-3 pts. wt. borax, 1-2 pts. wt. zinc sulfate, 1-2 pts. wt. copper, 3-4 pts. wt. emulsifying agent, 4-6 pts. wt. film forming agent, and suitable amount of water. The film forming agent comprises dimethicone, butyl methacrylate, crosslinker TAC, nanocarbon, stone powder, and boric acid.    USE - As fermented fertilizer.    ADVANTAGE - The fermented fertilizer is easy to use, increases utilization ratio of fertilizer, improves quality and yield of plants, and increases probiotics in soil.    DETAILED DESCRIPTION - Composition and preparation of fertilizer are claimed. Fermented fertilizer comprises 50-55 pts. wt. beans, 40-45 pts. wt. bran, 40-45 pts. wt. waste orange, 20-23 pts. wt. tea tree branches, 2-3 pts. wt. garlic, 12-14 pts. wt. fulvic acid, 12-14 pts. wt. maifanite, 2-3 pts. wt. borax, 1-2 pts. wt. zinc sulfate, 1-2 pts. wt. copper, 3-4 emulsifying agent, 4-6 pts. wt. film forming agent, and suitable amount of water. The film forming agent comprises 12-15 pts. wt. dimethicone, 13-16 pts. wt. butyl methacrylate, 1-2 pts. wt. crosslinker TAC, 0.1-0.2 pts. wt. nanocarbon, 1-2 pts. wt. stone powder, and 1-2 pts. wt. boric acid. The preparation of the fertilizer, involves mixing the above-mentioned raw materials, and grinding the raw materials.
NOVELTY - Fatty acid methyl ester sulfonate-type biomass (I) is new.    USE - Fatty acid methyl ester sulfonate-type biomass used as modified petrochemical diesel-based surfactant (claimed).    ADVANTAGE - The fatty acid methyl ester sulfonate-type biomass is environmental-friendly, non-toxic, suitable for large-scale production, and has good surface activity.    DETAILED DESCRIPTION - Fatty acid methyl ester sulfonate-type biomass of formula (I) is new. An INDEPENDENT CLAIM is included for the preparation of fatty acid methyl ester sulfonate-type biomass.
NOVELTY - An improved, efficient, safe, commercially viable and production friendly process for preparation of 4-(4-minophenyl) morpholin-3-one; wherein 2-(2-chloroethoxy) acetic acid is condensed with 4-nitro aniline in solvent and inorganic acid to produce 2-(2- chloroethoxy)-N-(4-nitrophenyl) acetamide. The obtained acetamide is then cyclized in solvent, in presence of base and catalyst to obtain the 4-(4-nitrophenyl) morpholine-3-one. The obtained 4-(4-nitrophenyl) morpholine-3-one is reduced in solvent, catalyst and ammonium formate to obtain 4-(4-aminophenyl) morpholine-3-one. The 4-(4-minophenyl) morpholin-3-one can be used as an intermediate for preparation of rivaroxaban by processes known in the art.
NOVELTY - Method for separating epigallocatechin gallate from tea polyphenol involves acetylating tea polyphenol using acetylating agent in presence of catalyst, obtaining acetylated tea polyphenol, treating obtained product using silica gel column chromatography, separating eluent, obtaining acetylated epigallocatechin gallate, adding obtained product to acidic solvent and performing reduction reaction by hydrolysis using active metal.    USE - Method for separating epigallocatechin gallate from tea polyphenol (claimed).    ADVANTAGE - The method efficiently enables separation of epigallocatechin gallate from tea polyphenol with high yield by simple and environmentally-friendly process.
NOVELTY - A transition-metal porous complex material contains coordination compound having structural unit (I).    USE - Transition-metal porous complex material is used as gas adsorption agent.    ADVANTAGE - The transition-metal porous complex material has excellent adsorption characteristics.    DETAILED DESCRIPTION - A transition-metal porous complex material contains coordination compound having structural unit of formula: M2(L)2.    M=Ni2+ or Co2+;and    L=residue obtained by removing two H from carboxy group of 4-(3,5-carboxyphenyl)-2,2':4',4"-terpyridine structure of formula (I).    An INDEPENDENT CLAIM is included for preparation of transition-metal porous complex material, which involves mixing 4-(3,5-carboxyphenyl)-2,2':4',4"-terpyridine and nitrate in solvent, stirring, reacting at 90-100 degrees C for 4-6 days, cooling to normal temperature. The nitrate is nickel nitrate or cobalt nitrate. The solvent is N,N-dimethyl formamide, 1,3-dimethyl-2-imidazolidinone, N, N-dimethyl acetamide or anhydrous ethanol.
NOVELTY - Preparation of hydrogen involves adding strong reducing agent into an electrolytic water, replacing hydrogen in water, generating positive ions and hydroxide ions, adding strong oxidant, replacing oxygen in water, and generating negative ions and hydrogen ions.    USE - Preparation of hydrogen (claimed).    ADVANTAGE - The method enables efficient preparation of hydrogen with high yield in a short period of time.
NOVELTY - Soil-borne disease-reducing and root-promoting anti-heavy stubble preparation (A) is composed of mixed raw materials comprising 35-50 pts. wt. potassium fulvate, 10-15 pts. wt. ferrous sulfate, 10-15 pts. wt. magnesium sulfate, 5-8 pts. wt. sodium octaborate, 7-10 pts. wt. zinc sulfate, 20-30 pts. wt. Bacillus subtilis, 15-25 pts. wt. Bacillus cereus, 20-30 pts. wt. green Trichoderma microbial inoculum, 2-5 pts. wt. composite amino acid powder, and 0.1-0.5 pts. wt. indolebutyric acid.    USE - Soil-borne disease-reducing and root-promoting anti-heavy stubble preparation (A) used in growing crops (claimed).    ADVANTAGE - The anti-heavy stubble preparation (A) can effectively reduce soil-borne disease, promote rooting, reduce pathogenic bacteria, and resist heavy stubble. It is capable of providing various microelements needed for crop growth; supplementing certain amount of beneficial bacteria to the soil to inhibit the growth and propagation of harmful bacteria; and forming root protective barrier that can reduce soil-borne disease to the utmost extent. It can provide beneficial microorganism which can facilitate secretion of plant growth substances such as auxin, amino acid and other active substances which can facilitate the development of strong roots; activate each nutrient in the soil; and facilitate nutrient absorption by crops. Further, it can change the structure of soil into granular structure by incorporating organic fertilizer, thus making it capable of loosening soil with platy structure, and preventing soil compaction.
NOVELTY - Slow release manure fertilizer comprises 80-90 pts. wt. rabbit manure, 50-55 pts. wt. pigeon guano, 10-12 pts. wt. tobacco, 10-12 pts. wt. soybean molasses, 30-34 pts. wt. urea, 12-14 pts. wt. potassium chloride, 2-3 pts. wt. borax, 2-3 pts. wt. lime powder, 3-5 pts. wt. ash, 3-4 pts. wt. microbial inoculum, 4-6 pts. wt. film-coating agent and water. The film-coating agent comprises 12-15 pts. wt. dimethicone, 13-16 pts. wt. butyl methacrylate, 1-2 pts. wt. crosslinking agent, 0.1-0.2 pt. wt. nanocarbon, 1-2 pts. wt. mineral powder and 1-2 pts. wt. boric acid.    USE - Slow release manure fertilizer.    ADVANTAGE - The slow release manure fertilizer is environmental-friendly, improves soil quality, and enhances soil drought resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of slow release manure fertilizer comprising mixing rabbit manure and pigeon guano, adding water and soybean molasses, mixing, adding microbial inoculum, stirring, adding urea and potassium chloride, mixing, adding borax, lime powder, ash and water, mixing, fermenting for 20-30 days, drying and granulating.
NOVELTY - Synthesizing 3,5-diiodosalicylic acid intermediate comprises taking ethanol solution as solvent and iodine as iodine agent, performing acid-base reaction of 3,5-diiodosalicylic acid of crude product, purifying and refining by alkali acid analysis, then heat preserving, crystallizing, centrifuging and drying.    USE - The method is useful for synthesizing 3,5-diiodosalicylic acid intermediate (claimed).    ADVANTAGE - The method is capable of simply synthesizing the 3,5-diiodosalicylic acid intermediate with high impurity, difficulty, purity of more than 99.5% and conversion rate of 98.5%.
NOVELTY - Preparing butalbital comprises: (a) adding 2-diethyl allylmalonate in sodium ethoxide/ethanol system, then adding 1-bromo-2-methylpropane, and reacting to obtain crude 2-isobutyl-2-diethyl allylmalonate; (b) reacting crude 2-isobutyl-2-diethyl allylmalonate with urea in sodium ethoxide/ethanol system, adding hydrochloric acid to adjusting pH to obtain precipitated crude butalbital; and (c) adding aqueous ethanol solution, heating, dissolving, and adding activated carbon, performing heat absorption and filtering, cooling filtrate in ice-bath, filtering, and vacuum drying.    USE - The method is useful or preparing butalbital (claimed).    ADVANTAGE - The method: is simple and safe; avoids the utilization of non stable reagents and utilizes raw materials which are environmentally friendly and easy to obtain; and provides high yield products.    DETAILED DESCRIPTION - Preparing butalbital comprises: (a) adding 2-diethyl allylmalonate into sodium ethoxide/ethanol system, then adding 1-bromo-2-methylpropane, and reacting to obtain crude 2-isobutyl-2-diethyl allylmalonate; (b) reacting crude 2-isobutyl-2-diethyl allylmalonate with urea in direct sodium ethoxide/ethanol system at room temperature, and adding hydrochloric acid dropwise to adjust the pH to obtain precipitated crude butalbital; and (c) adding aqueous ethanol solution into precipitated crude butalbital, heating, dissolving, and adding activated carbon, performing heat absorption and filtering, cooling the filtrate in ice-bath, again filtering, and vacuum drying.
NOVELTY - Preparing 1-(2-(2,4-dimethylphenyl)sulfanylphenyl)piperazine (I) comprises performing condensation reaction of 2-nitrophenyl thiophenol or 2-aminothiophenol (II) and 2,4-dimethyl benzyl halide (III) with alkaline solution to obtain 2-(2,4-dimethyl-phenylsulfanyl)-nitrobenzene (IV), cyclization reaction of (IV) and 2-(2,4-dimethyl-phenylsulfanyl) aniline (V) with alkaline solution.    USE - The method is useful for preparing (I).    ADVANTAGE - The method is capable of preparing (I) in a simple, cost effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing 1-(2-(2,4-dimethylphenyl)sulfanylphenyl)piperazine of formula (I) comprises performing condensation reaction of 2-nitrophenyl thiophenol or 2-aminothiophenol (II) and 2,4-dimethyl benzyl halide (III) with alkaline solution to obtain 2-(2,4-dimethyl-phenylsulfanyl)-nitrobenzene (IV), cyclization reaction of (IV) and 2-(2,4-dimethyl-phenylsulfanyl) aniline (V) with alkaline solution.
NOVELTY - Vortioxetine is prepared by performing condensation reaction on 2-halogen-substituted nitrobenzene and 2,4-dimethylthiophenol to obtain 2-(2,4-dimethylphenylsulfanyl)nitrobenzene, reducing to obtain 2-(2,4-dimethylphenylsulfanyl)aniline, and performing cyclization reaction with di(2-halogen-substituted)ethylamine under alkaline conditions.    USE - Preparation of vortioxetine (claimed).    ADVANTAGE - Preparation of vortioxetine is simple and environment-friendly and uses easy to obtain raw materials, and vortioxetine has excellent quality.    DETAILED DESCRIPTION - Vortioxetine of formula (I) is prepared by performing condensation reaction on 2-X-substituted nitrobenzene of formula (II) and 2,4-dimethylthiophenol of formula (III) to obtain 2-(2,4-dimethylphenylsulfanyl)nitrobenzene of formula (IV), reducing to obtain 2-(2,4-dimethylphenylsulfanyl)aniline of formula (V), and performing cyclization reaction with di(2-Y1-substituted)ethylamine of formula (VI) under alkaline conditions.    X=F, Cl, Br, I, or B(OH)2; and    Y1=F, Cl, Br, I, or OH.    An INDEPENDENT CLAIM is included for preparation of vortioxetine of formula (I) which involves performing condensation reaction on 2-X-substituted aniline of formula (IIa) and 2,4-dimethylthiophenol of formula (III) to obtain 2-(2,4-dimethylphenylsulfanyl)aniline of formula (V) and performing cyclization reaction with di(2-Y1-substituted)ethylamine of formula (VI) under alkaline conditions..
NOVELTY - Producing omeprazole enantiomer, comprises taking omeprazole synthetic product as raw material, and subjecting omeprazole enantiomer to simulated moving bed chromatographic resolution, and packing in chiral stationary phase by using ethanol solution as mobile phase in chiral column.    USE - The method is useful for producing omeprazole enantiomer by simulated moving bed chromatographic resolution (claimed).    ADVANTAGE - The method has high production yield; produces product having purity reaches up to more than 98%; performs continuous simulated moving bed chromatographic resolution process; can improve the level of automation and productivity; and is environmental friendly.
NOVELTY - An esomeprazole magnesium trihydrate is prepared by taking omeprazole sulfide complex, adding chiral ligand, catalyst, and organic solvent, reacting by heating and stirring to form omeprazole sulfide complex, adding inorganic oxidizing agent, performing oxidation to oxidize omeprazole thioether to esomeprazole, adding aqueous inorganic alkali solution, extracting esomeprazole by dissolving to inorganic salt of aqueous inorganic alkali solution layer, adding inorganic magnesium salt, stirring, centrifuging, and drying.    USE - Preparation of esomeprazole magnesium trihydrate (claimed).    ADVANTAGE - The preparation is simple and environment-friendly, has low cost, can be one-pot process, obtains product with high purity and audible smell.    DESCRIPTION OF DRAWING(S) - The drawing shows a mass spectrum of esomeprazole magnesium trihydrate. (Drawing includes non-English language text).
NOVELTY - Preparing liquid fertilizer comprises pulverizing a fish by-product, adding 250 kg of molasses, 80 kg of antioxidant, 90 kg of microbial fermentation, and 30-50 l of effective microorganisms stock solution to 200 kg of the pulverized fish by-product, aging the resultant mixture for 3 months to 1 year at 35 degrees C, and fermenting to obtain the liquid fertilizer. The molasses comprise the waste molasses and the fish by-product comprises head of fish, bone and fin.    USE - The method is useful for preparing a liquid fertilizer (claimed). No biological data given.
NOVELTY - Preparing magnesium particles comprises dissolving metal particles in an organic solvent to obtain a mixed solution, and separating fine particles from the mixed solution, where the amount of the organic solvent is 0.001-0.50 wt.%, preferably 0.001-0.20 wt.%.    USE - The method is useful for preparing magnesium fine particles (claimed).    ADVANTAGE - The method is capable of rapidly preparing the magnesium fine particles in an environmentally friendly manner.
NOVELTY - Manufacturing fine particle of zinc using supercritical fluid process, comprises (a) dissolving the mixed solvent of supercritical fluid in an organic solvent of zinc, and contacting by spraying to produce zinc particle, and (b) removing the organic solvent from the mixed solution by introducing supercritical fluid, where the organic solvent is 0.0001-0.50 wt.% fraction of zinc, preferably 0.001-0.20 wt.%.    USE - The fine particle of zinc is useful for chelating of heavy metal in a detoxification system development.    ADVANTAGE - The method provides super fine particles of zinc compared to existing zinc particle, is environment-friendly.
NOVELTY - Preparing cystine comprises dissolving quasi drug in an organic solvent to obtain a mixed solution, and separating fine particles from the mixed solution, where the amount of the organic solvent is 0.001-0.50 wt.%, preferably 0.001-0.20 wt.%.    USE - The method is useful for preparing cystine (claimed).    ADVANTAGE - The method is capable of preparing the non-toxic cystine in an environmentally manner.
NOVELTY - The system has subcritical water-treatment unit (2) that carries out subcritical water treatment of mixture of cake and water. A methane fermentation unit (4) ferments the processed material in which subcritical water treatment is carried out to liquid squeezing separated in solid-liquid separation unit (1C). A purifier (6) purifies methane gas from biogas which is fermented and produced in methane fermentation unit. An electric power generating apparatus (7) generates electric power as fuel methane gas purified by purifier.    USE - Electric power generation system for producing methane gas from slurry-like crushed material such as organic waste. Can also be used in food waste, biomass feedstock, sludge, timber and plant waste, and livestock waste.    ADVANTAGE - The Maillard reaction is inhibited effectively at the time of subcritical water treatment. The methane-ferment is efficiently performed in short time. The electric power generation amount of electric power generating apparatus is reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the methane gas electric power generation system. (Drawing includes non-English language text)    Solid-liquid separation unit (1C)    Subcritical water-treatment unit (2)    Methane fermentation unit (4)    Purifier (6)    Electric power generating apparatus (7)
NOVELTY - The apparatus (C) has preprocessor (1) which pre-processes raw material supplied to receiving unit from exterior of container (15). A subcritical water-treatment unit (2) is provided to perform subcritical water treatment of processed material having solid content pre-processed on specific subcritical water-treatment conditions. The methane fermentation unit (4) which methane-ferments processed material, the purifier (6) which purifies methane gas, and electric power generating apparatus (7) which electric-power-generates methane gas as fuel are accommodated in single container.    USE - Container type electric power generating apparatus.    ADVANTAGE - The highly efficient methane gas electric power generation is performed, by electric power as fuel methane gas purified by purifier inside single container. The various apparatuses of container type electric power generating apparatus are compactly positioned inside the container.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for management system of container type electric power generating apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the container type electric power generation apparatus structure.    Preprocessor (1)    Subcritical water treatment unit (2)    Methane fermentation unit (4)    Purifier (6)    Electric power generation apparatus (7)    Container (15)    Container type electric power generation apparatus structure (C)
NOVELTY - The equipment has a pipe which comprises a circulation circuit that circulates a sludge containing liquid between a bioreaction tank (20) and a membrane separation module (1). A supply pipe (25) is provided to supply a sludge containing liquid to the membrane separation module from a bioreaction tank. A return pipe (26) is provided to return the sludge containing liquid discharged from the membrane separation module to the bioreaction tank.    USE - Membrane separation activated sludge process equipment for water treatment apparatus used for purification of water such as turbidity removal of river water and underground water, clarification of industrial water and waste water, disposal of sewage water and desalination of sea water.    ADVANTAGE - The energy consumption for the operation of the membrane separation activated sludge process equipment is reduced, and operation cost of the equipment is reduced. The solid substance adhering to the inner surface of the hollow fiber membrane of the membrane separation module is removed easily by the drive of back wash pump, so that the filtration operation is performed stably, and performance of activated sludge process equipment is enhanced. Thus the quantity of the treated water is increased, and the highly efficient water treatment is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the membrane separation activated sludge process equipment.    Membrane separation module (1)    Bioreaction tank (20)    Supply pipe (25)    Return pipe (26)    Flow volume adjustment unit (28)
NOVELTY - Oxidative coupling of hydrocarbons involves reacting methane with toluene, isobutylene, t-butyltoluene, or trimethylbenzene. The oxidative coupling reaction is exothermic and generates heat energy. At least a portion of the heat energy generated by the oxidative coupling reaction is recovered and utilized in a facility.    USE - For oxidative coupling of hydrocarbons which generates heat energy that is utilized in a facility i.e. an ethylene production facility (claimed).    ADVANTAGE - The heat recovery allows for greater control of the highly exothermic methane coupling reaction, while at the same time reducing energy costs by providing heat for the cracking reaction zone.
NOVELTY - The apparatus (100) has a modifier (1) that generates a hydrogen-containing-gas using raw material. A hydro-desulphurization device (3) is provided with hydro-desulphurization agent to oxidatively degrade and remove the sulfur compound in raw material. A controller (10) is not provided for performing material supply operation which supplies raw material to modifier after generation stop of hydrogen-containing-gas in modifier, when recycle flow path (4) for supplying hydrogen-containing-gas to hydro-desulphurization device and oxygen concentration in raw material are relatively high.    USE - Hydrogen generating apparatus for fuel cell system (claimed).    ADVANTAGE - The oxidative degradation of the hydro-desulphurization agent is suppressed, so that the operating life of hydrogen generating apparatus is prolonged.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a fuel cell system;    (2) an operating method of hydrogen generating apparatus; and    (3) an operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Modifier (1)    Hydro-desulphurization device (3)    Recycle flow path (4)    Controller (10)    Hydrogen generating apparatus (100)
NOVELTY - The device has an upper tank connected with an inner part of a reactor. Gravity biomass particles are placed on a drying and heating column. A mixing and rising agitator stirs the gravitational biomass particles. A heat exchanger recirculates exhaust gas. A biomass contracting layer is formed on a conical grate. A scraper agitator is connected with a cooling chamber.    USE - Biomass carbonizing device.
NOVELTY - A orthorhombic CdS quantum dots in germanium dioxide based glass nanocomposite is disclosed. The glass nanocomposite comprises 50 to 60% germanium dioxide (GeO2) 8 to 16% potassium oxide (K2O), 10 to 12% zinc oxide (ZnO), 3 to 6% sodium oxide (Na2O), 4to 8% aluminium oxide (A12O3), 4 to 6% boron trioxide (B203), 1 to 2% titanium dioxide (Ti02), and 0.7 to 2% cadmium sulfide (CdS), wherein homogenously distributed CdS quantum dots having an orthorhombic lattice phase and size in the range of 4 to 14 nm are obtained in a glass matrix by heating the glass composition for 12 to 30 hours at a temperature between 450 and 475 degree C. The glass nanocomposite is particularly suitable for use as a photocatalyst in the photo-production of H2 gas from H2S in the presence of visible light.
NOVELTY - A cathode-based carbon fiber in-situ regeneration method involves carrying out cathode regeneration periodically using ultrasound at a frequency range of 10-50 kHz.    USE - Method for in-situ regeneration of cathode-based carbon fiber in electrolytic production of hydrogen.
NOVELTY - A composite electrode comprises a matrix of metal or alloy and a solute embedded in the matrix, where the composite electrode is prepared by immersing the matrix in a plating bath at 15-60 degrees C, preferably 25-40 degrees C, under cathodic current density of 0.1-6 A/dm2, preferably 0.5-3 A/dm2 such that the matrix is embedded in the composite. The plating bath comprises cobalt (II) sulfate heptahydrate, nickel sulfate hepahydrate, cobalt (II) chloride, nickel chloride hexahydrate, sodium tungstate dihydrate, sodium molybdate dihydrate and vanadyl sulfate trihydrate.    USE - Composite electrode for separating and ionizing hydrogen.    DETAILED DESCRIPTION - A composite electrode comprises a matrix of metal or alloy and a solute embedded in the matrix, where the composite electrode is prepared by immersing the matrix in a plating bath at 15-60 degrees C, preferably 25-40 degrees C, under cathodic current density of 0.1-6 A/dm2, preferably 0.5-3 A/dm2 such that the matrix is embedded in the composite. The plating bath comprises cobalt (II) sulfate heptahydrate, nickel sulfate hepahydrate, cobalt (II) chloride, nickel chloride hexahydrate, sodium tungstate dihydrate, sodium molybdate dihydrate, vanadyl sulfate trihydrate, ammonium perrhenate, sodium hypophosphite dihydrate, potassium sodium tartrate tetrahydrate, trisodium citrate dihydrate, boric acid, ammonium chloride, sodium chloride, water and ammonia. The metal is chosen from iron, nickel and cobalt. The alloy is chosen from nickel alloy and di-, tri-and multi-component alloys of nickel, cobalt and iron with transition metals, preferably tungsten, molybdenum, vanadium or rhenium.
NOVELTY - A solid fuel comprises 95 wt.% lignite and 60 wt.% biodegradable waste, preferably mechanically separated rejects obtained from pulping of waste paper and cardboard wastes, where the solid fuel is prepared by taking brown coal from a reservoir and grinding brown coal to grain size of less than 3 mm. Biodegradable waste is subjected to grinding in a bead-percussion rotor, and the biodegradable waste and the brown coal are fed to a mixer and subjected to intensive mixing process. The resulting mix is guided to a pelletiser and subjected to pressure granulation to obtain the finished product.    USE - Solid fuel.    DETAILED DESCRIPTION - A solid fuel comprises 95 wt.% lignite and 60 wt.% biodegradable waste, preferably mechanically separated rejects obtained from pulping of waste paper and cardboard wastes, where the solid fuel is prepared by taking brown coal having moisture content of less than 35% from a reservoir and grinding brown coal to grain size of less than 3 mm. Biodegradable waste is subjected to grinding in a bead-percussion rotor that is provided with a screen having mesh aperture of less than 8 mm. The biodegradable waste and the brown coal are fed to a mixer and subjected to intensive mixing process. The resulting mix is guided to a pelletiser and subjected to pressure granulation to obtain the finished product.
NOVELTY - Seed-dressing fertilizer comprises 0.01-0.02 pts. wt. pyrrolidine methanol derivative, 20-30 pts. wt. 25% or 30% compound fertilizer, 40-50 pts. wt. plant straw, 3-6 pts. wt. potassium humate, and 1-2 pts. wt. zinc sulfate. The pyrrolidine methanol derivative is N-(4-methoxybenzyl)- alpha , alpha -bis(4-methoxyphenyl)-2-pyrrolidinemethanol or N-4-methylbenzyl- alpha , alpha -diphenyl-2-pyrrolidinemethanol. The compound fertilizer is potassium sulfate.    USE - Seed-dressing fertilizer used for promoting growth and cultivation of plant roots and killing soil insects.    ADVANTAGE - The fertilizer improves crop yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising taking 25% or 30% compound fertilizer for further use; taking plant straw, mixing, crushing, composting, fermenting for 7-15 days, ventilating, drying; taking yellow potassium humate and fertilizer grade zinc sulfate, for further use; mixing products; stirring; diluting 0.01 pt. wt. pyrrolidine methanol derivative with 50-100 pts. wt. water; uniformly spraying on the product obtained in fourth step; mixing stirring; drying; processing into seed size particles; and distributing 1 kg granules per bag.
NOVELTY - Preparation of trospium chloride intermediate comprises reacting alpha -tropine with ethyl chloroformate to obtain N-ethoxycarbonyl tropine (I); reacting with diphenyl glycolic acid ester activator and 4-N,N-dimethylaminopyridine to obtain N-ethoxycarbonyl diphenyl glycolic acid ester tropine (II); and reacting with ammonium formate/palladium on carbon catalyst to carry out catalytic hydrogen transfer reduction.    USE - Method for preparation of trospium chloride intermediate (claimed).    ADVANTAGE - The method has short reaction time, high yield, simple operation, low cost and no strong acid and strong alkali conditions, and does not adversely affect the environment.    DETAILED DESCRIPTION - Preparation of trospium chloride intermediate comprises reacting alpha -tropine with ethyl chloroformate to obtain N-ethoxycarbonyl tropine (I); reacting with diphenyl glycolic acid ester activator and 4-N,N-dimethylaminopyridine to obtain N-ethoxycarbonyl diphenyl glycolic acid ester tropine (II); and reacting with ammonium formate/palladium on carbon catalyst to carry out catalytic hydrogen transfer reduction. The synthetic ester activator is carbodiimide and/or organic phosphorus-based condensing agent. The carbodiimide is dicyclohexyl carbodiimide, diisopropyl carbodiimide, and/or 1-(3-dimethylaminopropyl)-3-ethylcarbodiimide hydrochloride.
NOVELTY - A dihydro erythromycin is prepared by Beckmann rearrangement comprising reacting erythrocin A9-oxime, water and rearrangement reagent, adding alkali solution to adjust pH at 3-7, adding reducing agent, and acid hydrolyzing.    USE - Method for preparing dihydro erythromycin (claimed).    ADVANTAGE - The method reduces waste and production cost, has high product yield and mild reaction condition, and is environment-friendly.
NOVELTY - Fermented complex fertilizer and its preparation method are claimed. The fermented complex fertilizer comprises 60-65 pts. wt. bamboo charcoal, 30-34 pts. wt. peanut, 40-45 pts. wt. rice hull, 40-45 pts. wt. edible fungi bran, 23-26 pts. wt. potassium chloride, 2-3 pts. wt. olive oil, 3-4 pts. wt. ligusticum, 1-2 pts. wt. nux vomica, 20-23 pts. wt. potassium dihydrogen phosphate, 2-3 pts. wt. zinc chloride, 30-34 pts. wt. urea, 10-12 pts. wt. potassium nitrate, 3-4 pts. wt. effective microorganism (EM), and 4-6 pts. wt. coating agent.    USE - The fermented complex fertilizer is useful for preventing and controlling disease and insect pest in seedless grape (claimed).    ADVANTAGE - The fermented complex fertilizer is cost-effective and environmentally-friendly, and has balanced nutrition, improved yield of grape root, and reduced soil damage as compared with traditional fertilizer.    DETAILED DESCRIPTION - Fermented complex fertilizer and its preparation method are claimed. The fermented complex fertilizer comprises 60-65 pts. wt. bamboo charcoal, 30-34 pts. wt. peanut, 40-45 pts. wt. rice hull, 40-45 pts. wt. edible fungi bran, 23-26 pts. wt. potassium chloride, 2-3 pts. wt. olive oil, 10-12 pts. wt. Brachypudum, 3-4 pts. wt. ligusticum, 1-2 pts. wt. nux vomica, 20-23 pts. wt. potassium dihydrogen phosphate, 2-3 pts. wt. zinc chloride, 30-34 pts. wt. urea, 10-12 pts. wt. potassium nitrate, 3-4 pts. wt. effective microorganism (EM), and 4-6 pts. wt. coating agent, where the coating agent comprises 20-22 pts. wt. paraffin, 2-3 pts. wt. silane coupling agent KH-570, 0.1-0.2 pts. wt. nano-carbon, 2-3 pts. wt. jade powder, and 2-3 pts. wt. polyoxyethylene sorbitan monooleate. The preparation method involves mixing the above-mentioned raw materials, grinding and uniformly dispersing the obtained product.
NOVELTY - A methanol preparing method involves circulating a reaction gas containing carbon monoxide and hydrogen in an autothermal catalyst bed reactor and reacting under steam and under pressure of 4-8 MPa to obtain condensed reaction products, where the reactor contains an adiabatic reactor and two tubular reactors, which are arranged in series.    USE - Method for preparing methanol.
NOVELTY - A methanol from the reaction gas preparing method involves taking mixture of synthesis gas such as carbon monoxide and hydrogen in a reactor under heat to produce steam. The products are allowed for condensation reactions. Synthesis process is carried out in reactors arranged in series, and in one or two water-cooled reactors at temperature of not lower than 150 degrees C, heated at temperature of not less than 270 degrees C followed by reacting mixture with catalyst bed, cooling autothermal gas, and obtaining methanol under pressure of 4-8 MPa.    USE - Method for preparing methanol from the reaction gas.
NOVELTY - The system (100) has a greenhouse (10) at which a solar cell module (12) is installed. Domestic animals field (21) is formed on underground. An outlet port (43) is formed in a bottom surface of a livestock shed (30), and an inlet port (42) is exposed on ground, so that the air of ground is induced to the inside of underground, and air is supplied to livestock shed. An excrement handling portion (60) is formed in lower region of domestic animals field, and is connected to power generation heat supply (80) which uses biogas stored in a gas-storage tank (81) as an energy source.    USE - Converged system for livestock production.    ADVANTAGE - The space of ground is utilized effectively. The power generation heat supply can produce electricity through solar cell module by using biogas stored in gas-storage tank as energy source, so that the energy is saved and livestock excretion is fermented. The constant temperature and humidity is maintained in livestock shed by flowing outside air to the cattle shed, without the need of separate heating and cooling facility, and ventilator. The generation of bad smell inside livestock shed is suppressed. The rainwater of ground is collected and used inside cattle shed, so that the need of separate water supply facilities inside the greenhouse is eliminated, and the facility management cost is reduced. The need of using separate daytime lamp is eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the converged system for livestock production.    Roof (11)    Solar cell module (12)    Domestic animals field (21)    Chain-installed livestock shed (30)    Exposed vent (40)    Inlet port (42)    Outlet port (43)    Excrement handling portion (60)    Power generation heat supply (80)    Gas-storage tank (81)    Superiority waterspout (90)    Converged system for livestock production (100)
NOVELTY - Making pazopanib (Ia) or its salt, involves treating 2,3-dimethyl-6-nitro-2H-indazole with Raney nickel to obtain 2,3-dimethyl-2H-indazol-6-amine (II); treating the compound (II) at less than or equal to 45 degrees C with 2,4-dichloropyrimidine to obtain N-(2-chloropyrimidin-4-yl)-2,3-dimethyl-2H-indazol-6-amine (III); converting the compound (III) to the compound (Ia) or its salt; and isolating the compound (Ia) or its salt.    USE - For the preparation of pazopanib or its salt (claimed).    ADVANTAGE - The process offers recycling of the Raney nickel catalyst used in the process, and an easy filtration work-up procedure; offers selective reduction under mild conditions that is economical to use at an industrial scale; avoids the use of at least two solvents, and additionally, also circumvents heating and cooling procedures during the reaction; produces the compound (III) with a lesser amount of N-(4-chloropyrimidin-2-yl)-2,3-dimethyl-2H-indazol-6-amine (CPDMI) impurity; and provides the compound (Ia) or its salts in comparable yield and suitable purity required for medicinal preparations.    DETAILED DESCRIPTION - Preparation of pazopanib of formula (Ia) or its salt, involves treating 2,3-dimethyl-6-nitro-2H-indazole with Raney nickel to obtain 2,3-dimethyl-2H-indazol-6-amine compound of formula (II); treating the compound (II) at less than or equal to 45 degrees C with 2,4-dichloropyrimidine to obtain N-(2-chloropyrimidin-4-yl)-2,3-dimethyl-2H-indazol-6-amine compound of formula (III); converting the compound (III) to the compound (Ia) or its salt; and isolating the compound (Ia) or its salt.
NOVELTY - The method involves providing a substrate (104). A source region (116) and drain region (120) are supported with the substrate. An insulator layer (108) is formed above the source region and the drain region. A porous metallic gate region (112) is formed above the insulator layer using plasma enhanced atomic layer deposition (PEALD). A desired porous metallic gate region thickness is determined. A desired number of PEALD cycles are determined based upon the determined desired porous metallic gate region thickness.    USE - Method of fabricating semiconductor sensor device used for detecting target gases such as carbon monoxide, nitrogen dioxide, ammonia, methane and volatile organic compounds in automobile exhaust system. Can also be used in home appliance, laptop, handheld or portable computer, mobile telephone, smart phone, wireless device, personal data assistant, portable music player, film camera, digital cameras, GPS receiver, satellite navigation system, electronic reading display, projector, cockpit control, game console, earpieces, headset, hearing aid, wearable display device, and security system.    ADVANTAGE - The semiconductor sensor device with desirable porous metallic gate region can be formed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a semiconductor sensor device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the semiconductor sensor device.    Substrate (104)    Insulator layer (108)    Porous metallic gate region (112)    Source region (116)    Drain region (120)
NOVELTY - Preparing bis(3-aminophenyl)disulfide compounds (I) and/or 3-aminothiol compounds (II), comprises (A) reducing 3-nitrophenyl-sulfonyl chloride compounds (III) with catalytic amount of iodide in presence of hypophosphorous acid to obtain bis(3-nitrophenyl)disulfide compounds (IV), and (B) reducing (IV) with hydrogen in presence of a metal catalyst to obtain (I) and/or (II).    USE - (I) and/or (II) are useful as intermediate products for preparing insecticidally, acaricidally and nematicidally active phenyl sulfoxides.    ADVANTAGE - The method is simple, economic and environmentally-friendly, and produces (I) and/or (II) in high yields and with high purity.    DETAILED DESCRIPTION - Preparing bis(3-aminophenyl)disulfide compounds of formula (I) and/or 3-aminothiol compounds of formula (II), comprises (A) reducing 3-nitrophenyl-sulfonyl chloride compounds of formula (III) with catalytic amount of iodide in presence of hypophosphorous acid or their salts to obtain bis(3-nitrophenyl)disulfide compounds of formula (IV), and (B) reducing (IV) with hydrogen in presence of a metal catalyst to obtain (I) and/or (II).X, Y1 = H, 1-4C alkyl, 1-4C alkoxy, halo or NH2.    INDEPENDENT CLAIMS are also included for:    (1) bis(3-nitrophenyl)disulfide compounds of formula (IVa);    (2) bis(3-aminophenyl)disulfide compounds of formula (Ib);    (3) 3-aminothiol compounds of formula (IIa); and    (4) 3-nitrophenyl-thiol compounds of formula (V).    X2, Y2 = H, CH3, ethyl, OCH3, ethoxy, F or Cl.
NOVELTY - A biological dimethoxy alkane diesel oil comprises 50-60 wt.% 1,1-dimethoxy-3-methylbutane, 15-20 wt.% 1,2-bis-(dimethylamino)-2-methylpropane, 5-10 wt.% 1,1,1-triethoxy-3-methylbutane, and 10-20 wt.% impurity component.    USE - Biological dimethoxy alkane diesel oil.    ADVANTAGE - The diesel oil has cheap and easy to obtain raw materials, low freezing point, high heating value, good lubricating property, low temperature resistance, and excellent hydrolytic stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological dimethoxy alkane diesel oil comprising mixing 2-methyltetrahydrofuran and dimethyl ether catalyst at mass ratio of 1:20-100 at 100-200 degrees C with reaction pressure of 1-4 MPa for 2-4 hours, and reacting with mixtures of 1,1-dimethoxy-3-methylbutane, 1,2-bis-(dimethylamino)-2-methylpropane, and 1,1,1-triethoxy-3-methylbutane.
NOVELTY - Pseudomonas strain is new, which preserved in China general microbiological culture collection center under preservation number CGMCC NO: M2013468.    USE - Pseudomonas strain used for degrading polyvinyl alcohol 1799 and wastewater contaminants in sewage (claimed).    ADVANTAGE - The Pseudomonas strain reduces environment pollution and cost of sewage treatment.
NOVELTY - A chlorophenol in wastewater is biodegraded by fermenting Armillaria tabescens laccase as biological catalyst at 50-60 degrees C and pH of 3.6-4.5 in which chlorophenol compound is 2,4-dichlorophenol, 2-chlorophenol, and/or 4-chlorophenol.    USE - Biodegradation of chlorophenol (claimed).    ADVANTAGE - Process is fast and has high degradation rate.
NOVELTY - Anaerobic reactor comprises a housing with chambers of hydrolysis and methane fermentation, the device of loading and mixing the substrate in the chambers, the hydraulic valve and the column for enrichment of biogas, divided by partitions into biogas collector and sections filled with immobiliser backfilling. The housing and the column are connected by two pipes, one of which is connected between the outlet of the substrate from the reactor housing and the upper part of the column. The other is connected between the outlet of the biogas from the reactor housing and the lower part of the column. In the reactor a diaphragm electrolyser is mounted. The outlet with the hydrogen gas is connected to the lower part of the column of enrichment. The outlet with the analyte is connected to the entry of the housing into the hydrolysis chamber. The outlet of the electrolyser with the catholyte is connected to the chambers of methane fermentation. The outlet the biogas collector in the column the hydraulic valve is connected. The backfilling in the sections of the column of gas enrichment the fibrous graphite material with a large extended surface is used between the hydraulic water seal at the outlet of biogas from the column of enrichment and the pipe in the lower part of the column the pump is mounted for reblow biogas through it.    USE - Energy industry.    ADVANTAGE - Increase in efficiency and quality of produced biogas and serviceability.2 cl, 1 dwg
NOVELTY - The present disclosure is in relation to the preparation of tricyclic antidepressants Doxepin/Dothiepin and salt thereof. The method helps in achieving the pharmaceutically acceptable ratio of the isomers of said compounds. The disclosed method involves cost effective reagents, mild conditions and few steps to beget said compounds economically.
NOVELTY - Use of at least one biotin molecule grafted with at least one molecule to determine the presence and/or dosing the amount in a solution of an element comprising mercury, lead, copper, cadmium, arsenic, cobalt, iron, aluminum, nickel, chromium, zinc and uranium, where the molecule is a molecule capable of binding the element, is claimed.    USE - The biotin molecule is useful for: analyzing polluting element in rivers, water body or drinking water; controlling decontamination of element of a solution after a cleansing treatment; controlling the saturation of uranium contained in treatment stations; monitoring radionuclides contained in rivers, water body or water consumption; and determining uranium present in urine samples (all claimed).    ADVANTAGE - The biotin molecule effectively analyzes the polluting element in a rapid manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the molecule having a biotinylated bisphosphonate compound of formula (I); and    (2) a kit for determining uranium in the solutions, comprising a microplate, whose bottom of wells are functionalized with a biphosphonate, a streptavidin or a avidin, (I) that is in powdered form or solution form, a solution of streptavidin-peroxidase or avidin-peroxidase, a solution of substrate of the avidin-peroxidase or streptavidin-peroxydase, and a solution to stop the reaction between avidin-peroxidase or streptavidin-peroxydase and its substrate.    X1 = O or NH;    R1 = H or OH;    X2 = C, H, O, N, P, S or divalent group of formula (-(CH2)n-) (a) or (-CH2-O-(CH2-CH2-O)n-CH2-CH2-) (b); and    n = greater than or equal to 1.
NOVELTY - Liquefaction of waste hair by non-thermal treatment and continuous microbial fermentation method, involves (a) inoculating soil microbial communities isolated from primary cultures into a culture medium, (b) placing the microbial culture in an incubator, sub-culturing the microbial culture, (c) opening the outlet valve of incubator and adjusting the flow rate of the filler, and (d) adding waste hair to the incubator through the opening.    USE - Liquefaction of waste hair.    DETAILED DESCRIPTION - Liquefaction of waste hair by non-thermal treatment and continuous microbial fermentation method, involves (a) inoculating soil microbial communities isolated from primary cultures into a culture medium and preparing a microbial culture, (b) placing the microbial culture in an incubator, sub-culturing the microbial culture, where microorganism is attached to the inner filler phase, (c) opening the outlet valve of incubator and adjusting the flow rate of the filler, where the microorganisms will not fall from the culture solution and microorganisms attached to the filler discharge slowly, and (d) adding waste hair to the incubator through the opening, where the waste hair is decomposed by the microbial fermentation.
NOVELTY - Polyhydric alcohol having 3 or more hydroxyl groups is dehydrated by heating using microwaves in presence of ionic liquid as reaction solvent, to obtain cyclic ether.    USE - Manufacture of cyclic ether e.g. isosorbide (claimed) is used as raw material for synthesis of resin used for electrical and electronic material.    ADVANTAGE - The environmentally-friendly cyclic ether is manufactured with high yield in a short period of time even without using supercritical fluid and high pressure reactor.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) recycling of ionic liquid, which involves recovering and recycling ionic liquid after manufacturing cyclic ether; and    (2) manufacture of isosorbide, which involves performing dehydration of sorbitol by heating using microwaves in presence of ionic liquid as reaction solvent.
NOVELTY - Method for producing bio-colony using plant biomass, involves (a) washing plant biomass raw materials, drying washed biomass raw material and crushing dried material, (b) adding 1-5% hydrogen peroxide solution to crushed product, and subjecting obtained mixture to hydrolysis process under acidic conditions at 60-80 degrees C, 90-100 Bar and 4-6 pH for 8-12 hours, (c) filtering obtained hydrolyzate and concentrating obtained filtrate, (d) subjecting obtained concentrate to high temperature sterilization, and (e) freeze-drying sterilized product.    USE - The method is useful for producing plant biomass derived bio-colony used for promoting growth of microorganisms that bio-ferments biomass for producing at least energy sources chosen from ethanol, methanol, hydrogen and bio-diesel (all claimed).    ADVANTAGE - The method enables effective utilization of the plant biomass wastes, and hence environmental pollution caused by disposal of wastes is prevented. The plant biomass serves itself as a source of energy for the microorganisms contained in the bio-colonies. The bio-colony has microporous structure and improves degradability and process efficiency of organic substances or matter contained in the food wastes.
NOVELTY - Benzophenone (II) and alpha -haloester (III) are reacted in presence of low chiral catalyst (V), to obtain (2S)-epoxy-3,3-diphenylpropionate (IV). The compound (IV) is subjected to ring-opening reaction in presence of acid catalyst and methanol under acidic condition, to obtain (2S)-2-hydroxy-3-methoxy-3,3-diphenylpropionate (VI). The compound (VI) is reacted with 4,6-dimethyl-2-methylsulfonyl pyridine in alkaline compound to obtain methoxy group-containing compound (VII). The compound (VII) is hydrolyzed in alkaline compound and acidified in protonic acid (b), to obtain vinorelbine (I).    USE - Preparation of vinorelbine (claimed).    ADVANTAGE - The method enables preparation of vinorelbine with high purity and yield by environmentally-friendly process.    DETAILED DESCRIPTION - Benzophenone of formula (II) and alpha -haloester of formula (III) are reacted in presence of low chiral catalyst of formula (V), to obtain (2S)-epoxy-3,3-diphenylpropionate of formula (IV). The compound (IV) is subjected to ring-opening reaction in presence of acid catalyst and methanol under acidic condition, to obtain (2S)-2-hydroxy-3-methoxy-3,3-diphenylpropionate of formula (VI). The compound (VI) is reacted with 4,6-dimethyl-2-methylsulfonyl pyridine in alkaline compound to obtain methoxy group-containing compound of formula (VII). The compound (VII) is hydrolyzed in alkaline compound and acidified in protonic acid (b), to obtain vinorelbine of formula (I).    R=CH3- or CH3CH2;    X=C1 or Br;    Ph=phenyl;and    R'=9-phenyl.
NOVELTY - Composition comprises fulvic acid produced by fermentation of kitchen waste material and diatomite    USE - Used as fertiliser for improving and loosening soil, promoting plant growth and combating drought.    ADVANTAGE - The composition has a high and prolonged fertilizer effect in the soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the composition which involves uniformly mixing diatomite and kitchen waste material, carrying out wet granulation with ethanol, drying, adding water, carrying out fermentation, granulating and boiling mixture.
NOVELTY - The reactor has a reactor main portion that includes lower multi-flow chamber (2) and a flow distribution chamber (3). The width of lower flow distribution chamber is less than width of upper flow distribution chamber. A reaction room is provided with upward flow anaerobic sludge layer (4) and filler layer (5). The filling material is made as bio-filler combination and photosynthetic bacteria growth form bio-membrane filler. The filler is set in upper portion of mounting light source (7), and external main portion of power supply is connected with anaerobic baffle plate reactor.    USE - Optical energy-saving anaerobic reactor for processing high chromatic wastewater.    ADVANTAGE - The wastewater device-coloring efficiency and energy utilization of anaerobic reactor are increased. The electric consumption and the wastewater processing cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view illustrating the energy-saving anaerobic reactor for processing high chromatic wastewater.    Multi-flow chamber (2)    Flow distribution chamber (3)    Sludge layer (4)    Filler layer (5)    Outlet wire (6)    Light source (7)
NOVELTY - Synthesis of 4-methyl-2-hydrazino benzothiazole involves adding aqueous solution of hydrazine hydrate and 4-methyl-2-amino-benzothiazole (I) as raw material into a pressure vessel containing hydrochloric acid, heating, and obtaining 4-methyl-2-hydrazino benzothiazole (II).    USE - Synthesis of 4-methyl-2-hydrazino benzothiazole (claimed).    ADVANTAGE - The method enables the synthesis of 4-methyl-2-hydrazino benzothiazole with high yield, and reduced dosage of hydrazine hydrate and energy loss, by simple, economical, and environmentally-friendly process.    DETAILED DESCRIPTION - Synthesis of 4-methyl-2-hydrazino benzothiazole involves adding aqueous solution of hydrazine hydrate and 4-methyl-2-amino-benzothiazole of formula (I) as raw material into a pressure vessel containing hydrochloric acid, heating, and obtaining 4-methyl-2-hydrazino benzothiazole of formula (II).
NOVELTY - This utility new type relates to a one fertilizer production device, specifically to a one peptidase synergistic compound fertilizer with steel structure and a high tower, include a tower body, the tower body set with upper end of melting chamber and melting chamber connected lower end of granulator, a tower body of lower end is a discharging end, wherein the tower body upper part set with dust-cloth, the spraying end of the pelletizer through dust-cloth extending to the lower part of dust-cloth, using said structure, this utility new type a rear one of a gold peptide enzyme synergistic compound fertilizer production with steel structure and high tower granulating through a dust-removing cloth downwards move dust, the dust-blocking up the dust-removing cloth to prevent the dust pollution to air, and not for low secondary granulation would produce, increase the whole quality of fertilizer, mixed to prevent material in chemical fertilizer.
NOVELTY - A walnut nutrition fertilizer composition comprises sprout fertilizer, and flower fertilizer, where the sprout fertilizer comprises following components: 500 pts. wt. of decomposed organic fertilizer, 20 pts. wt. of urea, 200 pts. wt. of mushroom fermentation fertilizer, and 10 pts. wt. of trace element fertilizer, and the flower fertilizer comprises following components: 400 pts. wt. of nitrogen phosphorus potassium compound fertilizer, 200 pts. wt. of fermentation fertilizer, and 10 pts. wt. of trace element fertilizer.    USE - As walnut nutrition fertilizer composition (claimed).    ADVANTAGE - The fertilizer improves size, taste and nutrition value of walnut, improves plant yield, greatly increases fruit size, saves cost of planting, and increases the income. The fertilizer overcomes the shortcoming of the existing technology and provides scientific proportion, and satisfies different nutrition requirements.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the walnut nutrition fertilizer comprising sprout fertilizer and flower fertilizer involving taking each component i.e. the decomposed organic fertilizer, urea, mushroom fermentation fertilizer and trace element fertilizer according to the proportions, mixing and adding to stirrer, starting blade, and stirring uniformly to form finished product i.e. sprout fertilizer; forming flower fertilizer by taking nitrogen-phosphorus-potassium compound fertilizer, fermentation fertilizer and trace element fertilizer according to specific amounts, mixing and adding in stirrer, starting blade, stirring uniformly to form the finished product i.e. flower fertilizer; and mixing the sprout fertilizer and flower fertilizer to form the walnut nutrition fertilizer.
NOVELTY - Ecological fertilizer comprises inorganic fertilizer component and organic fertilizer component. The inorganic fertilizer component contains nutrient component including 7-20 wt.% of nitrogen (N), 4-20 wt.% of phosphorus pentoxide (P2O5), 4-20 wt.% of potassium oxide (K2O), 0.05-30 wt.% of calcium (Ca) and 0.00001-0.1 wt.% of molybdenum (Mo).    USE - The ecological fertilizer is useful for the growth of Eucalyptus (claimed).    ADVANTAGE - The ecological fertilizer satisfies the growth of Eucalyptus by meeting the demand for nutrients with increased growth rate and improved Eucalyptus timber volume.
NOVELTY - Preparation of lamotrigine comprises reacting 2,3-dichlorobenzoyl chloride (I) with potassium ferrocyanide in the presence of catalyst to obtain 2,3-dichlorobenzoyl cyanide (II); condensing with aminoguanidine bicarbonate to obtain amine containing dichlorobenzene derivative (III); and carrying out cyclization reaction, where catalyst is phase transfer catalyst and metal iodide and phase transfer catalyst is quaternary ammonium salt.    USE - Method for preparing lamotrigine (claimed).    ADVANTAGE - The method is environment-friendly and high reaction efficiency.    DETAILED DESCRIPTION - Preparation of lamotrigine comprises reacting 2,3-dichlorobenzoyl chloride (I) with potassium ferrocyanide in the presence of catalyst to obtain 2,3-dichlorobenzoyl cyanide (III); condensing with aminoguanidine bicarbonate to obtain amine containing dichlorobenzene derivative of formula (IV); and carrying out cyclization reaction, where catalyst is phase transfer catalyst and metal iodide and phase transfer catalyst is quaternary ammonium salt.
NOVELTY - An anaerobic two-phase process for the treatment of organic waste involves: introducing a feed stream comprising organic waste into a first phase reactor; generating an effluent from the first phase reactor; and providing the effluent from the first phase reactor to a second phase reactor, where, during at least the start-up period of the process, the first phase reactor has a sludge retention time (SRT) of 10-25 days and the pH is maintained at a pH of 4.5-6.0.    USE - The anaerobic two-phase process is useful for the treatment of organic waste (claimed).    ADVANTAGE - The process reduces the sulfate and/or sulfide content of organic matter undergoing treatment, and enhances the degradation of organic waste and biogas generation in an anaerobic digestion system.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a waste treatment plant using the process above; and    (2) a two-phase reactor system for the treatment of biodegradeable waste, comprises a first phase reactor and a second phase reactor that is downstream of the first phase reactor and is in fluid connection therewith, where the first and second phase reactors are adapted to use the process.
NOVELTY - Preparation of municipal sludge flower matrix comprises air-drying municipal sludge, crushing, screening using mesh filter with 1-2 mm pore size, mixing municipal sludge and wheat straw at mass ratio of 4:1 to obtain matrix I, adding 68-72 wt.% water, mixing matrix I and microbial fermentation agent at feed ratio of 5 m3:1 kg at 30 degrees C to obtain matrix II, and fermenting matrix II at room temperature for 25 days to obtain municipal sludge vegetable matrix.    USE - Method for preparing municipal sludge flower matrix (claimed).    DETAILED DESCRIPTION - Preparation of municipal sludge flower matrix comprises air-drying municipal sludge, crushing, screening using mesh filter with 1-2 mm pore size, mixing municipal sludge and wheat straw at mass ratio of 4:1 to obtain matrix I, adding 68-72 wt.% water, mixing matrix I and microbial fermentation agent at feed ratio of 5 m3:1 kg at 30 degrees C to obtain matrix II, and fermenting matrix II at room temperature for 25 days to obtain municipal sludge vegetable matrix. The microbial fermentation agent comprises 20-25 pts. wt. soybean extract, 1-2 pts. wt. Bacillus subtilis, 3-4 pts. wt. silicate bacteria, 2-4 pts. wt. Trichoderma viride, 8-12 pts. wt. Lactococcus lactis, 2-4 pts. wt. Actinomyces, 1-2 pts. wt. Bacillus mucilaginosus, 2 pts. wt. rice Flavobacterium, 3-6 pts. wt. yeast, 10-13 pts. wt. Azotobacter chroococcum, 8-12 pts. wt. cellulase, 8-12 pts. wt. protease and 5-6 pts. wt. phosphorylase.
NOVELTY - Manufacture of glycopyrronium bromide involves dissolving ( alpha )-cyclopentylmandelic acid in dimethylformamide using excess carbonyldiimidazole as condensing agent, pretreating, adding 1-methyl-3-pyrrolidinol, performing ester exchange reaction, terminating reaction using purified water, obtaining intermediate, performing organic solvent extraction of obtained intermediate, purifying by washing with water, performing quaternary ammonium reaction of resultant product with bormomethane in polar solvent, filtering, obtaining crude product, adding to organic solution and recrystallizing.    USE - Manufacture of glycopyrronium bromide used for medical application.    ADVANTAGE - The method efficiently enables manufacture of glycopyrronium bromide by simple, environmentally-friendly and economical process.
NOVELTY - Preparing Grignard reagent methyl magnesium halide involves taking tetrahydrofuran as the solvent in reaction vessel under lower temperature of 20-80 degrees C, in an inert gas, adding magnesium particles and iodine as a catalyst to reaction activated magnesium grains, and a few times using the method of the first gas through the small amount of initiator haloalkoxy Grignard reaction, Grignard reaction. The remaining initiator haloalkoxy after a certain time the gas fed. The reaction was refluxed to magnesium particles after natural cooling to room temperature.    USE - For preparing a Grignard reagent methyl magnesium halide (claimed).    ADVANTAGE - The method improves the magnesium bromide and betamethasone intermediate (II) purity significantly reduced the consumption of methyl bromide gas, and improves the safety of the reaction and reduces environmental pollution.    DETAILED DESCRIPTION - Preparing a Grignard reagent methyl magnesium halide involves taking tetrahydrofuran as the solvent in the reaction vessel under lower temperature of 20-80 degrees C, in an inert gas, adding magnesium particles and iodine as a catalyst to the reaction activated magnesium grains, and a few times using the method of the first gas through the small amount of initiator haloalkoxy Grignard reaction, Grignard reaction. The remaining initiator haloalkoxy after a certain time the gas fed. The reaction was refluxed to the magnesium particles after the whole solution was concentrated after natural cooling to room temperature to obtain Grignard reagent which is methyl magnesium halide, or 2-4% alkyl halide gas.
NOVELTY - Preparation of 4-difluoro methoxyaniline involves reacting sodium acetaminophen produced by reacting 4-nitrophenol in sodium hydroxide, and reacting with difluoromonochloro methane under alkaline condition to obtain 4-difluoromethoxy nitrobenzene, subjecting 4-difluoromethoxy nitrobenzene, ferric oxide and activated carbon to co-catalysis reaction, reducing nitro group of obtained product using water and hydrazine hydrate into amine group.    USE - Preparation of 4-difluoro methoxyaniline (claimed).    ADVANTAGE - The 4-difluoro methoxyaniline is economically prepared with high yield by environmentally-friendly method.
NOVELTY - A biomass feedstock process vehicle (1) comprises pulverization unit (3) which pulverizes biomass feedstock, molding unit (4) which heats and compresses the pulverized biomass feedstock and biocoke molding apparatus (2) which is mounted in the vehicle stand and molds and extrudes a biocoke.    USE - A vehicle for processing biomass feedstock e.g. chaff.    ADVANTAGE - Cost is reduced and biocoke is molded without applying an effort.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of the biomass feedstock process vehicle.    Biomass feedstock process vehicle (1)    Biocoke molding apparatus (2)    Pulverization unit (3)    Molding unit (4)    Chaff feeder (5)    Cutting machine (6)    Drive unit (7)    Control apparatus (8)    Heating unit (9)
NOVELTY - Antiseptic-sprinkling apparatus has (a) bucket, (b) spray tank comprising liquid agent, (c) spraying nozzle unit attached to the bucket, (d) piping connecting the above-mentioned spraying nozzle unit with spray tank, and (e) transport control system for transporting liquids and solutions in the spray tank to the spraying nozzle unit through piping.    USE - The antiseptic-sprinkling apparatus is useful for equipping heavy machine for preparing compost.    ADVANTAGE - The antiseptic-sprinkling apparatus has improved work efficiency.
NOVELTY - Preparation of phosphite acid-g-chitosan oligosaccharide composite biological medical fertilizer comprises preparing chitosan oligosaccharide-biomass vinegar composite medicine liquid by slowly adding chitosan oligosaccharide powder to biomass vinegar liquid, stirring; preparing phosphite-biomass vinegar composite medicine liquid by mixing phosphorous acid crystals and anhydrous potassium carbonate, grinding, neutralizing, dissolving, neutralizing, stirring, adding biomass vinegar, stirring; mixing with chitosan oligosaccharide-biomass vinegar composite medicine, and adjusting pH.    USE - Method for preparing phosphite acid-g-chitosan oligosaccharide composite biological medical fertilizer (claimed) used as biological pesticide and repair agent for heavy metal contaminated soil.    ADVANTAGE - The method has no residue and is environment-friendly.    DETAILED DESCRIPTION - Preparation of phosphite acid-g-chitosan oligosaccharide composite biological medical fertilizer comprises preparing chitosan oligosaccharide-biomass vinegar composite medicine liquid by taking 5-15 g chitosan oligosaccharide powder, slowly adding to 150-300 g biomass vinegar liquid, electrically stirring for 5 hours, adjusting pH to 4.5-5.5 using potassium hydroxide solution; preparing phosphite-biomass vinegar composite medicine liquid by taking 40-60 g phosphorous acid crystals and 55-65 anhydrous potassium carbonate, mixing, grinding, neutralizing by mixing phosphorous acid and potassium carbonate, ammonium carbonate, slowly adding 80-150 g clean water, dissolving, further neutralizing, stirring for 30-60 minutes, adding 50-75 g biomass vinegar, regulating pH value to 6.5-8.5, stirring; mixing 250 g phosphate-biomass vinegar composite medicine liquid and 250 g chitosan oligosaccharide-biomass vinegar composite medicine, and adjusting pH to 6-7.
NOVELTY - One pot boiling method preparation of diosmetin involves dissolving hesperidin in solvent (A), adding additives (B and C), concentrating obtained diosmetin reaction solution under reduced pressure, adding predetermined amount of purified water, stirring, filtering, adding purified water into the filter cake, stirring, precipitating, filtering, adding solvent (S) and crude diosmetin in a reactor, stirring to dissolve crude diosmetin, adding activated carbon, filtering, drying the filtrate by double-cone rotary vacuum dryer, crushing, mixing, and packing.    USE - One pot boiling method preparation of diosmetin (claimed).    ADVANTAGE - The diosmetin is efficiently and economically prepared under mild reaction conditions with high yield and purity, by environmentally-friendly process.
NOVELTY - An Aspergillus flavus strain TG7 (CGMCC NO: 8570), is new.    USE - The A.flavus strain TG7 is useful for preparing rutin, aflatoxin and/or mono epipodophyllotoxin glucoside (claimed).    ADVANTAGE - The method is simple, cost-effective and environmentally-friendly, and avoids large amount of picropodophyllin excavation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing rutin, aflatoxin and/or mono epipodophyllotoxin glucoside, which involves fermenting the above-mentioned A.flavus strain TG7.
NOVELTY - The system has an aerobic tank (6) which purifies polluted waste water purified at anaerobic tank (5) which purifies water supplied from pre-processing unit, and supplies purified water to waste-water collection tub (7) installed with sewage pump. A post-process unit is equipped with aerator which purifies polluted waste water purified in pre-processing unit. One end of transfer pipe (21) is connected to pump while locating other end with aerator. One end of return pipe (24) is connected to transfer pipe having backflow prevention valve (23) while locating other end in anaerobic tank.    USE - Polluted waste water purifying system used during purification process of polluted waste water supplied from holding tank of toilet room in boat and ship, and car-washing holding tank of car washing system, washing machine, bathtub and sink cabinet. Can also be used for purifying polluted waste water supplied from flush toilet apparatus installed in beach, alpine area, stricken area and islet.    ADVANTAGE - The structure of the polluted waste water purifying system is compact. The versatility of the polluted waste water purifying system is improved. The compactization of the polluted waste water purifying system is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the return mechanism of the polluted waste water purifying system.    Anaerobic tank (5)    Aerobic tank (6)    Waste-water collection tub (7)    Transfer pipe (21)    Backflow prevention valve (23)    Return pipe (24)
NOVELTY - Reducing a viscosity of process streams during production of ethanol from biomass, comprises (a) adding cellulase enzymes into a mash or feedstock comprising a non-cellulosic sugar and a cellulosic sugar, (b) fermenting fermentation mash to produce ethanol and a post-fermentation biomass, (c) generating process streams comprising whole stillage, thin stillage, concentrated thin stillage and/or syrup streams from the post fermentation biomass, and (d) adding an additional enzyme or enzyme cocktail to one of the post fermentation process stream to reduce the viscosity of the syrup stream.    USE - The method is useful for reducing a viscosity of process streams during production of ethanol from biomass (claimed).    ADVANTAGE - The method can reduce the ultimate viscosity of the process streams in an ethanol production plant thus improving the efficiency and throughput or production capacity of the ethanol production process and enhancing the co-fermentation of starch and cellulose in the simultaneous saccharification and fermentation process.    DETAILED DESCRIPTION - Reducing a viscosity of process streams during production of ethanol from biomass, comprises (a) adding cellulase enzymes into a mash or feedstock comprising a mixture of a non-cellulosic sugar and a cellulosic sugar to produce a fermentation mash, (b) fermenting the mash to produce ethanol and a post-fermentation biomass, (c) generating process streams comprising whole stillage, thin stillage, concentrated thin stillage and/or syrup streams from the post fermentation biomass, and (d) adding an additional enzyme or enzyme cocktail to one of the post fermentation process stream to reduce the viscosity of the syrup stream.
NOVELTY - Organic wastewater is anaerobically treated by methane-fermenting organic wastewater containing compound of carbon number 1, adding metallic cation which has valence of more than bivalence in methane-fermentation-treated water discharged from methane fermentation process of desorbing emitted biogas, and returning a part or all parts of sludge to methane fermentation process in which sludge is separated and recovered by sludge separation process which separately processes methane-fermentation-treated water to which metallic cation is added and separate-and-recovers sludge and treated water.    USE - Anaerobic treatment of organic wastewater (claimed).    ADVANTAGE - Methane fermentation microbe can be separated and recovered as sludge, the amount of sludge in methane fermentation tank can be maintained by returning sludge to methane fermentation process, and outflow of sludge can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic treatment apparatus organic wastewater comprising sludge collection tank provided with a part for adding metallic cation, methane fermentation tank provided with gas-separation unit, and sludge return pipe which returns sludge recovered by sludge collection tank to methane fermentation process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the processing method of organic wastewater. (Drawing includes non-English language text).
NOVELTY - The hydrogen generation system (100) has fuel generator which generates the fuel gas containing hydrogen from reforming reaction with a raw material and water. A combustor (16) burns the fuel gas and heats the fuel generator. A flame detector (27) detects the combustion state in the combustor. A controller increases the raw material feed rate of the material supply device (13), before detecting the quenching process with the combustor, and performs combustion with the combustor, when the fuel gas is supplied to combustor and the quenching process with the combustor is detected.    USE - Hydrogen generation system used in fuel cell system (claimed) used for electric power generation.    ADVANTAGE - As the raw material feed rate of the material supply device is increased, before detecting the quenching process with the combustor, and combustion with the combustor is performed, when the fuel gas is supplied to combustor and the quenching process with the combustor is detected, the precision of the flame detection at the time of post-burning process is improved, so that the stable supply of fuel gas is performed continuously.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the hydrogen generation system. (Drawing includes non-English language text)    Material supply device (13)    Combustor (16)    Igniter (26)    Flame detector (27)    Hydrogen generation system (100)
NOVELTY - A Cel-KG35 endo-glucanase derived from ruminant stomach microorganism of black goat, comprising a 320 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The recombinant Cel-KG35 endo-glucanase protein is useful in detergent composition and feed additive for promoting decomposition of glucan, and for producing biofuel (all claimed).    ADVANTAGE - The recombinant Cel-KG35 endo-glucanase protein can be mass produced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the endo-glucanase protein;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector;    (4) antibody with respect to endo-glucanase protein;    (5) method for producing endo-glucanase in host cell, involves introducing the recombinant vector into host cell and overexpressing the endo-glucanase; and    (6) method of producing biofuel, involves hydrolyzing biomass using the recombinant endo-glucanase.
NOVELTY - A Cel-KG52 cellulase protein derived from ruminant stomach microorganism of black goat, comprising a 518 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The recombinant Cel-KG52 cellulase protein is useful in detergent composition and feed additive for promoting decomposition of cellulose, and for producing biofuel (all claimed).    ADVANTAGE - The recombinant Cel-KG52 cellulase protein can be mass produced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the Cel-KG52 cellulase protein;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector;    (4) antibody with respect to cellulase protein;    (5) method for producing cellulase in host cell, involves introducing the recombinant vector into host cell and overexpressing the cellulase; and    (6) method of producing biofuel, involves hydrolyzing biomass using the recombinant cellulase protein.
NOVELTY - A Cel10-KG42 endo-xylanase derived from ruminant stomach microorganism of black goat, comprising a 368 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The recombinant endo-xylanase protein is useful in detergent composition and feed additive for promoting decomposition of xylan, and for producing biofuel (all claimed).    ADVANTAGE - The recombinant endo-xylanase protein can be mass produced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the endo-xylanase protein;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector;    (4) antibody with respect to endo-xylanase protein;    (5) method for producing endo-xylanase in host cell, involves introducing the recombinant vector into host cell and overexpressing the endo-xylanase; and    (6) method of producing biofuel, involves hydrolyzing biomass using the recombinant endo-xylanase.
NOVELTY - The system (100) has a fuel cell (5) for generating electric power utilizing oxidizing agent gas i.e. air, and fuel gas. A circulation path (8) circulates cooling water, which absorbs heat of the fuel cell. A cooling water tank (11) is arranged on the circulation path, and supplies cooling water through a water supply part (23). A controller (101) performs purification process for purifying the cooling water by a water purification device after water supply of the cooling water tank is started. The controller carries out water supply to the cooling water tank.    USE - Fuel cell system.    ADVANTAGE - The controller performs purification process for purifying the cooling water by the water purification device after water supply of the cooling water tank is started, so that the cooling water can be purified before electric-power generating of the fuel cell even when city water is supplied, thus improving reliability of the fuel cell system and ensuring stable operating of the system.    DETAILED DESCRIPTION - The fuel cell is an internal reformation-type solid oxide fuel cell and an indirect internal reforming-type solid oxide fuel cell. The controller is a MPU.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell system.'(Drawing includes non-English language text)'    Fuel cell (5)    Circulation path (8)    Cooling water tank (11)    Water supply part (23)    Fuel cell system (100)    Controller (101)
NOVELTY - A Cel-KG24 endo-glucanase derived from ruminant stomach microorganism of black goat, comprising a 462 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The recombinant Cel-KG24 endo-glucanase protein is useful in detergent composition and feed additive for promoting decomposition of glucan, and for producing biofuel (all claimed).    ADVANTAGE - The recombinant Cel-KG24 endo-glucanase protein can be mass produced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the Cel-KG24 endo-glucanase protein;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector;    (4) antibody with respect to endo-glucanase protein;    (5) method for producing endo-glucanase in host cell, involves introducing the recombinant vector into host cell and overexpressing the endo-glucanase; and    (6) method of producing biofuel, involves hydrolyzing biomass using the recombinant endo-glucanase.
NOVELTY - A Cel-KG20 cellulase protein derived from ruminant stomach microorganism of black goat, comprising a 579 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The recombinant Cel-KG20 cellulase protein is useful in detergent composition and feed additive for promoting decomposition of cellulose, and for producing biofuel (all claimed).    ADVANTAGE - The recombinant Cel-KG20 cellulase protein can be mass produced.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene encoding the Cel-KG20 cellulase protein;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector;    (4) antibody with respect to cellulase protein;    (5) method for producing cellulase in host cell, involves introducing the recombinant vector into host cell and overexpressing the cellulase; and    (6) method of producing biofuel, involves hydrolyzing biomass using the recombinant cellulase protein.
NOVELTY - Producing beta -glucanase involves utilizing fungal biomass of Botryosphaeria that produces extracellular beta -glucans. The obtained beta -glucans are frozen, lyophilized and pulverized. The fungal biomass is provided as a source for converting beta -glucan to beta -glucanase.    USE - Method for producing beta -glucanase using mycelial biomass.    ADVANTAGE - The method enables to produce beta -glucanase efficiently.
NOVELTY - An endoxylanase protein derived from a ruminant stomach microorganism of a Capra aegagrus subsp. hircus comprising a 136 amino acid sequence (SEQ ID NO: 2) fully defined in the specification, is new.    USE - The endoxylanase protein is useful in feed additive and detergent composition and for producing biofuel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gene coding the endoxylanase protein;    (2) recombinant vector comprising the above-mentioned gene;    (3) host cell transformed with the vector;    (4) antibody against the endoxylanase protein;    (5) method for mass-producing the endoxylanase from the host cell, involves overexpressing the endoxylanase by transducing the recombinant vector to the host cells;    (6) recombinant endoxylanase protein produced by the above-mentioned method;    (7) method for producing the biofuel, involves adding the recombinant endoxylanase protein produced by the host cell in the biomass matter and hydrolyzing to obtain product;    (8) feed additive comprising the endoxylanase protein and recombinant endoxylanase protein; and    (9) detergent composition comprising the endoxylanase protein and recombinant endoxylanase protein.
NOVELTY - Measuring compost maturity comprises adding sodium hydroxide and potassium hydroxide aqueous solution in the compost for leaching, and measuring absorbance of leachate.    USE - The method is useful for measuring compost maturity (claimed).    ADVANTAGE - The method is capable of simply measuring compost maturity based on the color change.
NOVELTY - The system has a fuel cell unit compressing and saving evaporative gas, which is supplied from a storage tank for preparing liquefied natural gas (LNG) in a hull. An additional generation unit generates electricity with an electrochemical reaction by utilizing energy. A buffer unit supplies high pressure fuel in a high pressure state. The buffer unit is provided with an evaporative gas buffer tank for storing the evaporative gas. A compressor compresses the evaporative gas, which is supplied to the storage tank. A generator is fixed in a turbo expander.    USE - Marine fuel cell generation system.    ADVANTAGE - The system suspends a supply of the fuel to the fuel cell, operates the fuel cell without pause of the fuel cell, improves solubility of the fuel cell, and additionally produces electricity for the solubility improvement of the fuel cell by utilizing the fuel of the high pressure, so that efficiency of the whole system can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a marine fuel cell generation system.'(Drawing includes non-English language text)'
NOVELTY - The device (100) has a lower side of an upper die (20) installed at a frame (10). A pure water storage tank (60) is provided for supplying the ultra-pure water to a junction (40) in order to generate steam in the junction. A steam injection unit (50) is provided for spraying steam to a membrane-electrode assembly base material (7) and to a gas diffusion layer (3), which are equipped in the junction. The junction is installed at the upper die. The steam injection unit is equipped in a hot plate (41).    USE - Device for manufacturing fuel cell stack unit.    ADVANTAGE - The device has a lower side of an upper die installed at a frame, where a pure water storage tank is provided for supplying ultra-pure water to a junction in order to generate steam in the junction, and hence ensures cost effective and improved fuel cell stack unit manufacturing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell stack unit manufacturing device. (Drawing includes non-English language text).    Gas diffusion layer (3)    Membrane-electrode assembly base material (7)    Frame (10)    Upper die (20)    Junction (40)    Hot plate (41)    Steam injection unit (50)    Pure water storage tank (60)    Fuel cell stack unit manufacturing device (100)
NOVELTY - The fuel cell and gas engine hybrid poly-generation system has a compressor drive for generating oxygen and an exhaust gas treatment section for processing a fuel cell and combustible waste gas generated in the power generation. A heat supply driving unit is provided with a gas engine unit (100) and an oxygen storage tank (210) for storing the oxygen. A carbon dioxide storage tank (120) is provided for storing carbon dioxide at high density. The hydrogen electrolyzing water is supplied in an electrolysis portion (200).    USE - Fuel cell and gas engine hybrid poly-generation system.    ADVANTAGE - The fuel cell and gas engine hybrid poly-generation system has a compressor drive for generating oxygen and an exhaust gas treatment section for processing a fuel cell and combustible waste gas generated in the power generation, and hence ensures efficient and improved fuel cell and gas engine hybrid poly-generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell and gas engine hybrid poly-generation system. (Drawing includes non-English language text).    Fuel delivery system (10)    Control valve (11)    Gas engine unit (100)    Carbon dioxide storage tank (120)    Electrolysis portion (200)    Oxygen storage tank (210)
NOVELTY - A Chlorella sp. strain isolated from Arctic ocean and capable of producing lipid and starch at high concentration, is new.    USE - The Chlorella sp. strain is useful for producing lipid and starch, and in method for producing biodiesel and glycerol (all claimed).    ADVANTAGE - The strain produces 25-35% starch and 35-45% lipid per cell with respect to dry weight e.g. 50-60% linoleic acid and oleic acid and 10% unsaturated fatty acid with respect to total weight of lipid, grows in freshwater and seawater in any seasons, and does not need a special temperature condition during culturing since the strain grows well in at least freezing temperature.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) microbial agent comprising the strain or its culture medium as active ingredient;    (2) method for producing lipid involves cultivating the strain and separating the lipid; and    (3) method for producing biodiesel and glycerol involves culturing the strain, separating the lipid from the culture medium, performing transesterification of lipids to fatty acid esters, and obtaining glycerol.
NOVELTY - The system (1) has an electric power system (100) which produces electricity to a turbine rotated at the heat of combustion of the predetermined feed. A fuel cell generation system (200) produces electricity through the chemical energy generated by the oxidation of the predetermined reactant used as fuel. A recirculation system (300) is configured to supply egesta including carbon dioxide and water to the reactant of the fuel cell generation system.    USE - Hybrid electric power generating system used in power plant.    ADVANTAGE - Since the recirculation system is configured to supply egesta including carbon dioxide and water to the reactant of the fuel cell generation system, the power generation efficiency of the hybrid electric power generating system is improved and the exhaustion of the carbon dioxide to the environmental is minimized to prevent environmental contamination.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the hybrid electric power generating system.    Hybrid electric power generating system (1)    Electric power system (100)    Pure oxygen combustor (110)    Fuel cell generation system (200)    Recirculation system (300)
NOVELTY - Pre-treating a biomass slurry, comprises: obtaining a dry matter content of the biomass slurry of 15-60 wt.%; introducing a flow of steam to a reaction chamber containing the biomass slurry; while introducing the flow of steam to the reaction chamber, introducing a flow of oxygen to the reaction chamber and the biomass slurry to cause oxidation of a lignin component of the biomass slurry; venting carbon dioxide from the reaction chamber to maintain amount of available oxygen within the chamber at 0.01-15% of chemical oxygen demand (COD); and flashing the biomass to a secondary holding unit.    USE - The method is useful for pre-treating a biomass slurry (claimed) by targeted wet oxidation method for producing fuels and/or chemical products.    ADVANTAGE - The method is capable of economically pre-treating the biomass slurry with improved bioaccessibility.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method-1 for oxidizing lignin components in the biomass slurry, comprising removing water from the biomass slurry with the dry matter content of 15-60 wt.%; subjecting the biomass slurry to a stream of oxygen and a stream of steam, venting carbon dioxide from the biomass slurry, and flashing the biomass to a secondary holding unit by a pressure difference.
NOVELTY - Fermented marine material obtained by adding strain with marine by-product, is claimed.    USE - The fermented marine material is useful in a marine compost (claimed), which is useful in farmland.    ADVANTAGE - The marine fermented material increases the soil property of the farmland, thus improving the growth of the crops.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) marine compost comprising fermented marine material; and    (2) manufacturing marine compost comprising controlling the moisture content of collected marine by-product and then adding strain and fermenting.
NOVELTY - Method (M1) for introducing recombinant DNA constructs into at least one bacterium.    USE - For introducing recombinant DNA constructs into at least one bacterium (claimed) for producing industrial butanol and biofuel.    ADVANTAGE - The method enables high-efficiency transformation of Clostridium pasteurianum via a series of treatments and electroporation conditions which successfully negotiate the resistant cell wall of Clostridium pasteurianum. The transformation efficiency is sufficiently high to perform all of the normal genetic engineering manipulations needed to produce high-producing industrial strains.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a bacterial cell which contains at least one recombinant DNA construct.
NOVELTY - Cellulolytic enzyme composition comprises an unprocessed pellet of a cellulosome-producing microorganism, where cells of the cellulosome-producing microorganism contained within the pellet are inactivated, and the cellulolytic enzyme composition further comprises detectable extra-cellular beta -glucosidase.    USE - The cellulolytic enzyme composition is useful for degrading a cellulosic substrate (claimed) including cellulose, hemicelluloses and lignin.    ADVANTAGE - The enzyme composition can be simply and economically produced with high cellulolytic activity, and can be simply recycled by subjecting samples to brief centrifugation (or other means of separation such as filtration through a micro sieve membrane) and replacing the supernatant fluids with fresh cellulosic substrate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) method-I for producing the cellulolytic enzyme preparation, comprising (i) culturing the cellulosome-producing microorganism in a medium comprising a cellulosic material until late exponential phase or stationery phase, (ii) centrifuging or filtering the medium following the culturing to obtain a pellet, (iii) separating the obtained pellet from the supernatant and inactivating the cells of the microorganism, and (iv) using the obtained pellet without purification of enzymes or other components to enzymatically hydrolyze cellulosic substrates; and    (2) method-II for degrading a cellulosic substrate, comprising contacting the cellulosic substrate with the composition.
NOVELTY - Preparation of potassium dihydrogen phosphate involves forming intermediate by reacting carboxamide and wet-process phosphoric acid, and reacting intermediate with potassium hydroxide.    USE - Preparation of potassium dihydrogen phosphate (claimed).    ADVANTAGE - The potassium dihydrogen phosphate having purity of 98% or more is prepared with high productivity by simple, safe, environmentally-friendly and economical method.
NOVELTY - Microbial fertilizer comprises 5-50 wt.% Bacillus BC39 bacterial powder, 20-50 wt.% peat soil, 20-70 wt.% humic acid, 1-15 wt.% micro-fertilizer and 0.5-10 wt.% auxiliary agent.    USE - The microbial fertilizer is useful for preventing and controlling soil-borne disease, promoting plant growth and treating plant diseases. The plant is chosen from cucumber, pepper, watermelon, tomato and strawberry (all claimed).    ADVANTAGE - The microbial fertilizer avoids usage of chemical fertilizer and environmental pollution problems, protects soil environment, and improves plant product quality and yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the microbial fertilizer, which involves obtaining fermented Bacillus BC39 bacterial powder, adding peat soil, humic acid, auxiliary agent and mixing uniformly, pelleting the obtained mixture, and drying the obtained granules to obtain product.
NOVELTY - Preparation of caffeic acid phenethyl ester involves subjecting caffeic acid and ( beta )-phenyl ethyl bromide to inorganic weak alkali catalytic reaction in a polar aprotic solvent, washing using specified amount of dichloromethane and water washing, obtaining crude product, and recrystallizing the resultant product using polar organic solvent.    USE - Preparation of caffeic acid phenethyl ester (claimed).    ADVANTAGE - The method enables easy and environmentally-friendly preparation of caffeic acid phenethyl ester under mild reaction conditions by a simple process.
NOVELTY - Vildagliptin is obtained by reacting raw material and 3-hydroxy-amantadine in a mixed system of organic solvent and water, condensing in the presence of a catalyst, carrying out extraction-separation after reaction completion, and concentrating to obtain high-purity crystals with high vildagliptin content.    USE - Synthesis of vildagliptin (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly industrial synthesis of vildagliptin with high purity, crystal content, and yield.
NOVELTY - 2-Chloro-N-(2-chloro-4-methylpyridin-3-yl)pyridine-3-carboxamide (III) is subjected to catalyzed coupling reaction with mono-substituted amine: R-NH2 (IV) under metal catalyst, to obtain 2-amino-N-(2-chloro-4-methylpyridin-3-yl)pyridine-3-carboxamide derivative (V). The resulted product is subjected to intramolecular cyclization reaction, to obtain 5,11-dihydro-6H-pyrido-bis(3,2-b:2',3'-e)(1,4)benzodiazepine compound (I).    USE - Preparation of 5,11-dihydro-6H-pyrido-bis-benzodiazepine compound (claimed).    ADVANTAGE - The 5,11-dihydro-6H-pyrido-bis-benzodiazepine compound is prepared by simple, safe and economical method under mild reaction conditions.    DETAILED DESCRIPTION - 2-Chloro-N-(2-chloro-4-methylpyridin-3-yl)pyridine-3-carboxamide of formula (III) is subjected to catalyzed coupling reaction with mono-substituted amine of formula: R-NH2 (IV) under metal catalyst, to obtain 2-amino-N-(2-chloro-4-methylpyridin-3-yl)pyridine-3-carboxamide derivative of formula (V). The resulted product is subjected to intramolecular cyclization reaction, to obtain 5,11-dihydro-6H-pyrido-bis(3,2-b:2',3'-e)(1,4)benzodiazepine compound of formula (I).    R=H, 1-6C alkyl or 3-6C cycloalkyl.
NOVELTY - Preparing organic fertilizer comprises preparing microbial inoculum culture liquid by culturing a strain, Pseudomonas fluorescens, Bacillus subtilis and Bacillus megaterium to obtain composite microbial inoculum culture liquid, fermenting the culture liquid in an anaerobic bacterium broth comprising alcohol distillers at 55-65 degrees C for 15-30 days, and stacking for 15-20 days.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method is capable of preparing organic fertilizer with short production cycle and high process stability in an environmental-friendly manner.
NOVELTY - The system has artificial floating sewage processing system that includes one upper end opening container, water inlet system comprising T-type cloth water tube (1) and drainage system comprising three water outlets. The upper portion of wind-light complementation aeration device (2) is provided with floating head (15). A foam board (8) is provided in upper portion of oxygen-restoring plant sewage treatment area and is inserted with composite cutting oxygen plant (3). Fibrous filler is provided in bottom portion of sewage processing system (7).    USE - Wind-light complementary type aeration sewage treatment system.    ADVANTAGE - The system improves water quality, beautifies the environment, and has good application prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the wind-light complementary type aeration sewage treatment system.    T-type cloth water tube (1)    Wind-light complementation aeration device (2)    Composite cutting oxygen plant (3)    Sewage processing system (7)    Foam board (8)    Floating head (15)
NOVELTY - (2-Bromomethyl-phenyl)-methoxyimino-acetic acid methyl ester and initiator are added into a reactor, stirred, and heated at 60-65 degrees C. Mixture of liquid bromine and carbon tetrachloride are added into reaction solution, and stirred at 60-65 degrees C. An oxidizing agent is added when the reaction solution becomes pale yellow color, heated at 65-75 degrees C, and stirred at 65-75 degrees C. The reaction solution is washed using water, aged, organic phase is separated, and solvent is removed under reduced pressure, to obtain light yellow oily substance which is (E)-2-(2-methylphenyl)-2-methoxyimino acetate.    USE - Preparation of (2-Bromomethyl-phenyl)-methoxyimino-acetic acid methyl ester used as trifloxystrobin intermediate.    ADVANTAGE - The (2-Bromomethyl-phenyl)-methoxyimino-acetic acid methyl ester is economically prepared with high yield and reduced discharge of bromine-containing wastewater, by environmentally-friendly process, reduces corrosion resistance of the production equipment, and improves quality of trifloxystrobin.
NOVELTY - A febuxostat intermediate compound (I), is new.    USE - New febuxostat intermediate compound (claimed).    ADVANTAGE - The febuxostat intermediate compound having high purity is manufactured by economical and environmentally-friendly process.    DETAILED DESCRIPTION - A febuxostat intermediate compound of formula (I), is new. An INDEPENDENT CLAIM is included for preparation of febuxostat intermediate compound, which involves reacting 2-bromo-4-methyl-thiazole-carboxylic acid benzyl ester and Grignard reagent of formula (II).
NOVELTY - The bioreactor has a mobile fermentation pouch (2) for processing biomass and provided with gas-tight doors and a separated space technology (3). A septic tank is equipped with a coat at inside a metal separator heater (10). Nozzles (7) are provided in the septic tank for spraying slurry. A closed system is equipped with a tank (9) and installed in the space technology. A waste pipe (8) of a pump is connected to the septic tank for draining excess percolate. Sensors (11) are located inside the septic tank to monitor fermentation parameters, which are controlled by a control unit (4).    USE - Dry fermentation anaerobic bioreactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a dry fermentation anaerobic bioreactor.    Mobile fermentation pouch (2)    Separated space technology (3)    Control unit (4)    Nozzles (7)    Waste pipe (8)    Tank (9)    Metal separator heater (10)    Sensors (11)
NOVELTY - Use of cement-free alkali-activated binder comprising aluminosilicate source material, lead-silicate glass, calcinated metakaolin clay, and alkaline inorganic material comprising sodium material is claimed.    USE - Use of cement-free alkali-activated binder as pH stabilizer and material for cell immobilization and for producing biogas from cheese whey (all claimed).    ADVANTAGE - The biogas having is efficiently produced with high productivity using cement-free alkali-activated binder.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cement-free alkali-activated binder;    (2) method for producing biogas from cheese whey, which involves providing fermentation medium containing 50-80 wt.% inoculum, and 20-50 wt.% cheese whey, adding 10-20 wt.% cement-free alkali-activated binder, performing fermentation, and collecting obtained biogas; and    (3) biogas.
NOVELTY - An anti-cropping high-yield agent comprises castor seed cake, tobacco straw, shell powder, Bacillus subtilis, thick spore Verticillium, alanine, cysteine, threonine, arginine, glycine, magnesium amino acid chelate, amino acid chelated boron, zinc amino acid chelate, iron amino acid chelate, amino acid chelate copper, manganese amino acid chelate, molybdenum amino acid chelate, rare earth nitrate, vitamin B1, vitamin B6, vitamin B12, and choline chloride.    USE - Anti-cropping high-yield agent.    ADVANTAGE - The agent solves the problem of multiple plant disease and insect pest, quality and yield reduction, residual fruits and vegetables and high-poison pesticide polluted soil, and reduces human health and environmental harm.    DETAILED DESCRIPTION - An anti-cropping high-yield agent comprises 25-35 wt.% castor seed cake, 25-35 wt.% tobacco straw, 15-20 wt.% shell powder, 1-2 wt.% Bacillus subtilis, 1-2 wt.% thick spore Verticillium, 0.5-2 wt.% alanine, 0.5-2 wt.% cysteine, 0.5-2 wt.% threonine, 0.5-2 wt.% arginine, 0.5-2 wt.% glycine, 1-5 wt.% magnesium amino acid chelate, 1-3 wt.% amino acid chelated boron, 1-3 wt.% zinc amino acid chelate, 1-3 wt.% iron amino acid chelate, 1-3 wt.% amino acid chelate copper, 1-2 wt.% manganese amino acid chelate, 0.5-1.5 wt.% molybdenum amino acid chelate, 0.5-3 wt.% rare earth nitrate, 0.1-1 wt.% vitamin B1, 0.1-1 wt.% vitamin B6, 0.1-1.5 wt.% vitamin B12, and 0.1-1.5 wt.% choline chloride. An INDEPENDENT CLAIM is included for preparation of agent comprising fermenting castor seed cake, crushing into 20-60 meshes powder, fermenting tobacco straw, and crushing into 20-60 meshes powder; mixing remaining raw materials for 10-15 minutes, adding 3 times water, atomizing, and spraying; putting into extrusion molding machine, extruding, and molding.
NOVELTY - Preparation of simvastatin ammonium salt acyl donor comprises reacting 2-mercaptoethanol and 2,2-dimethylbutanoic acid at - 5-5 degrees C for 2-6 hours under protection of nitrogen, reacting at 30-60 degrees c for 8-12 hours to obtain 2,2-dimethylbutyric acid-2-mercaptoethanol, reacting with acetyl chloride at 0-10 degrees C for 2-3 hours, reacting at 20-30 degrees C for 6-12 hours, and generating 2,2-dimethyl-butyric-2-oxoethoxymercapto acetate.    USE - Method for preparing simvastatin ammonium salt acyl donor (claimed).    ADVANTAGE - The method has inexpensive raw materials, simple process, easy magnification, low boiling point and no pollution.
NOVELTY - A remnant removing unit (120) removes solidity or liquid remnant generated according to decay of waste. A disinfection unit (111) removes pathogenic material generated waste. A gas exhaust port (110) processes gas generated according to decay of waste. An inclination adjuster (140) is arranged in lower portion of reaction bath (100) to distribute waste in reaction bath. Encapsulated type reaction bath disassembles organic waste put into through input unit (200). A grinding unit (220) crushes organic waste and input unit injects organic waste by reaction bath from outside.    USE - System for treating organic waste.    ADVANTAGE - The organic waste is safely processed by organic waste processing closed system without the bad smell and environmental contamination.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic waste processing system.    Reaction bath (100)    Gas exhaust port (110)    Disinfection unit (111)    Remnant removing unit (120)    Inclination adjuster (140)    Input unit (200)    Grinding unit (220)
NOVELTY - A diesel fuel preparing method involves subjecting raw material i.e. municipal waste, to catalytic depolymerization in a separation unit and an evaporator that is connected to a turbine with stirring. The catalytic depolymerization is carried out by periodically examining the calorific value of individual types of waste and adjusting the proportion of waste to obtain a raw mixture. The raw mixture is fed to the separation unit and the evaporator followed by adding a colloidal solution containing silver nanoparticles and subjecting depolymerized material to distillation to obtain a fuel.    USE - Method for preparing diesel fuel.    DETAILED DESCRIPTION - A diesel fuel preparing method involves subjecting raw material i.e. municipal waste, to catalytic depolymerization in a separation unit and an evaporator that is connected to a turbine with stirring. The catalytic depolymerization is carried out by periodically examining the calorific value of individual types of waste and adjusting the proportion of waste to obtain a raw mixture having calorific value of 10-15 MJ/kg. The raw mixture is fed to the separation unit and the evaporator followed by adding a colloidal solution containing silver nanoparticles having size of 3-8 nm. The depolymerized material is subjected to distillation to obtain a fuel, where portion of the resulting fuel is consumed to power a diesel-electric generator, and the final concentration of silver nanoparticles in the fuel is 2-20 ppm.
NOVELTY - A refined diesel fuel preparing method involves drying shredded municipal waste and/or organic material and processing the dried material in a separation unit and an evaporator. Catalytic depolymerization is carried out on the processed materials in presence of sodium aluminum silicate, and the depolymerized material is distilled to obtain a fuel. The obtained fuel is added to colloidal solution containing cerium oxide nanoparticles and copper nanoparticles to obtain the finished product.    USE - Method for preparing refined diesel fuel that is utilized in engine.    DETAILED DESCRIPTION - A refined diesel fuel preparing method involves drying shredded municipal waste and/or organic material and processing the dried material in a separation unit and an evaporator that is connected to a turbine. Catalytic depolymerization is carried out on the processed materials, and the depolymerized material is distilled to obtain a fuel, where the catalytic depolymerization is carried out in presence of 5-35 kg sodium aluminum silicate per 1000 l of fuel as a catalyst, and a process control unit automatically monitors sensors associated with various blocks of catalytic depolymerization process. The obtained fuel is added to colloidal solution containing cerium oxide nanoparticles having a particle size of 10-50 nm and copper nanoparticles having particle size of 10-50 nm to obtain the finished product, where the final concentration of cerium oxide nanoparticles in the fuel reaches 20-100 ppm and the final concentration of copper nanoparticles in the fuel reaches 20-50 ppm.
NOVELTY - A refined diesel fuel producing method involves performing catalytic depolymerization by drying shredded municipal waste and/or organic waste as raw material, separating and evaporating with turbine stirring, in presence of sodium aluminum silicate as a catalyst to monitor process control block in the sensors related parties of various blocks of catalytic depolymerization process. Depolymerized material is distilled to produce fuel, where catalyst activates the dispenser catalyst, using metered dose of turbine and catalyst in an amount of 5-35 kg per 1000 l of fuel in circulation process.    USE - Method for producing refined diesel fuel for diesel engine.    DETAILED DESCRIPTION - A refined diesel fuel producing method involves performing catalytic depolymerization by drying shredded municipal waste and/or organic waste as raw material, separating and evaporating with turbine stirring, in the presence of sodium aluminum silicate as a catalyst to automatically monitor process control block in the sensors related parties of various blocks of catalytic depolymerization process. Depolymerized material is distilled to produce fuel, where the catalyst activates the automatic dispenser catalyst, using metered dose of a turbine and catalyst in an amount of 5-35 kg per 1000 l of fuel in the circulation process, returns to monitor the operation of individual blocks, and the Fuel is composed of colloidal cerium oxide nanoparticles having a particle size of 10-50 nm for light oil distillates, final concentration of cerium oxide nanoparticles in the fuel level is 20100 ppm, and a colloidal solution nanoparticles of silver has a particle size of 3-8 nm in diesel oil, and silver concentration of the nanoparticles in the fuel is 2-20 ppm.
NOVELTY - Cultivating varbuscular mycorrhizal fungi carrier comprises crushing biomass and then screening to remove impurities, drying purified biomass, heating the biomass, in an oxygen-free atmosphere, in a closed container to produce bio-charcoal, and pulverizing the bio-charcoal into particles having a first size of 2-3 mm, a second size of 0.5-2 mm, a third size of 0.05-0.5 mm and a fourth size of less than 0.05 mm. The amount of first particle is 50-60 vol.%, the amount of second particle is 20-30 vol.%, the amount of third particle is 10-20 vol.%, and the amount of fourth particle is 10 vol.%.    USE - The method is useful for cultivating varbuscular mycorrhizal fungi carrier (claimed).    ADVANTAGE - The vesicular arbuscular mycorrhizal fungi carrier improves yield of plant.
NOVELTY - A phenazine compound (I) and (II), are new.    USE - The phenazine compound is useful as fungicidal composition for controlling fungal plant disease (claimed).    ADVANTAGE - The phenazine compound is environmentally-friendly.    DETAILED DESCRIPTION - A phenazine compound of formulae (I) and (II), are new. INDEPENDENT CLAIMS are included for the following: (1) preparation of the above-mentioned compound, which involves (a) inoculating Burkholderia strain 411gr-6 in agar plate using substrates 5,10-dihydro-4,9-dihydroxyphencomycin methyl ester, and phencomycin, 4-hydroxyphencomycin, or 4-hydroxyphencomycin methyl ester derivative of formula (III), and incubating with solid phase, (b) extracting cells from the plate using methanol, and obtaining crude extract, (c) extracting the crude extract using chloroform, and (d) purifying the extract using HPLC; and (2)pH indicator comprising the above-mentioned phencomycin, and 4-hydroxyphencomycin methylester.    R1 and R2= Hydrogen (H), OH or CH3.    (i) When R1-R2 are Hydrogen (H), the compound is phencomycin; (ii) When R1 is Hydrogen (H), and R2 is OH, the compound is 4-hydroxyphencomycin; and (iii) When R1 is CH3 and R2 is OH, the compound is hydroxyphencomycin methylester.
NOVELTY - Pandoraea WL1 strain is new, where preservation number of strain is CGMCC NO.7897.    USE - Pandoraea WL1 strain used for degrading organic waste containing p-xylene (claimed).    ADVANTAGE - The Pandoraea WL1 strain has improved adaptive ability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for culturing bacterial strain, which involves:    (A) taking pharmaceutical factory sewage discharge activated sludge in a culture vessel;    (B) adding inorganic salt culture medium of p-xylene in the culture vessel;    (C) incubating in a shaker to obtain microbial colony; and    (D) purifying and separating strain in R2A solid culture medium using diluting and marking method to obtain the desired strain.
NOVELTY - Processing and fermenting chicken manure, involves diluting chicken manure using water, preparing traditional Chinese medicinal sterilization liquid, primarily fermenting mixture, stirring the chicken manure, corn powder, yeast, and brown sugar or white sugar in a bucket, adding the traditional Chinese medicinal sterilization liquid to regulate water content to 50-55%, mixing the materials, adding mixture to fermenting tank, sealing the tank using plastic cloth, and performing anaerobic fermentation for 15-25 days at 70 degrees C.    USE - The method is useful for processing and fermenting chicken manure (claimed).    ADVANTAGE - The method retains nutritional component in chicken manure.    DETAILED DESCRIPTION - Method for processing and fermenting chicken manure, involves diluting chicken manure using water, removing feather, impurity and soil, adjusting water content to 15-20%, preparing traditional Chinese medicinal sterilization liquid using 500 g Omphalia, 300 g Celastrus angulatus, and 200 g quisqualis, betelnut and elecampane, adding 100 kg water to the materials, primarily fermenting mixture, stirring the chicken manure, corn powder, yeast, and brown sugar or white sugar in a bucket, adding the traditional Chinese medicinal sterilization liquid to regulate water content to 50-55%, mixing the materials, adding mixture to fermenting tank, sealing the tank using plastic cloth, and performing anaerobic fermentation for 15-25 days at 70 degrees C.
NOVELTY - The flame generator comprises an electrolyzer (5) for producing oxygen and hydrogen by electrolysis of water containing an electrolyte agent, and a torch (22) for producing flame. The torch is connected to the electrolyzer by a first conduit for the hydrogen and a second conduit, which is different from the first conduit, for the oxygen. The generator further comprises: a drying unit (6) located on the oxygen and hydrogen conduits; and a pressure sensor, a temperature sensor and an electrolyte circulation sensor for delivering a signal for controlling the electrolyzer.    USE - The flame generator is useful as a torch, a burner or a welding equipment.    ADVANTAGE - The generator produces the flame without a risk of explosion using separate conduits for oxygen and hydrogen.    DETAILED DESCRIPTION - The flame generator comprises an electrolyzer (5) for producing oxygen and hydrogen by electrolysis of water containing an electrolyte agent, and a torch (22) for producing flame. The torch is connected to the electrolyzer by a first conduit for the hydrogen and a second conduit, which is different from the first conduit, for the oxygen. The generator further comprises: a drying unit (6) located on the oxygen and hydrogen conduits; and a pressure sensor, a temperature sensor and an electrolyte circulation sensor for delivering a signal for controlling the electrolyzer. The drying unit is connected to a feeding circuit of water by a return circuit. The hydrogen and oxygen conduits comprise a security valve opening into a vent located outside of the generator. The electrolysis reaction is carried out at a temperature of lower than 60 degrees C.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a flame generator.    Electrolyzer (5)    Drying unit (6)    Torch (22)    Pressure sensor (25)    Temperature sensor. (26)
NOVELTY - Food waste processing device comprises a pre-processing (100) unit provided with a dehydrating unit (130) for separating food wastewater and sludge by dehydrating debris removed food waste by a selection unit, which filters the debris from food waste chopped by a crushing unit (110); a feed portion (200) provided with a drying unit (210) for drying the sludge; and a composing portion provided with a sieve part for filtering materials from the food wastewater stirred with a reaction unit mixes food wastewater in a food wastewater tank for storing food wastewater.    USE - Used as a food waste processing device.    ADVANTAGE - The device reprocesses the food waste, is environmentally friendly, and minimizes the generation of waste.    DETAILED DESCRIPTION - Food waste processing device comprises a pre-processing (100) unit provided with a dehydrating unit (130) for separating food wastewater and sludge by dehydrating debris removed food waste by a selection unit, which filters the debris from food waste chopped by a crushing unit (110); a feed portion (200) provided with a drying unit (210) for drying the sludge; and a composing portion provided with a sieve part for filtering materials from the food wastewater stirred with a reaction unit mixes food wastewater in a food wastewater tank for storing food wastewater. The pre-processing unit comprises an adsorption unit provided with a filter made of coco peat for purifying by collecting bad smell generated during processing the food waste in the composting portion and the freed portion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the food waste processing device (Drawing includes non-English language text).    Pre-processing unit (100)    Crushing unit (110)    Dehydrating unit (130)    Feed portion (200)    Drying unit (210)
NOVELTY - A solid oxide fuel cell system has fuel cell stack (2) which produces electric power by reacting oxidizing agent gas and hydrogen-containing fuel gas, modifier (3) provided with modification catalyst which produces hydrogen-containing fuel gas from source gas, water supply machine which supplies water to modifier used during modification reaction, oxidizing agent gas supply device which supplies oxidizing agent gas to modifier used during modification reaction, and on-off valve (9) provided at the 1st path which connects the oxidizing agent gas supply device and the modifier.    USE - Solid oxide fuel cell system for electric power generation used at home or power station.    ADVANTAGE - Oxidant gas supply device deterioration is prevented, and performance decline is prevented.    DETAILED DESCRIPTION - A solid oxide fuel cell system has fuel cell stack (2) which produces electric power by reacting oxidizing agent gas and hydrogen-containing fuel gas, modifier (3) provided with modification catalyst which produces hydrogen-containing fuel gas from source gas, water supply machine which supplies water to modifier used during modification reaction, oxidizing agent gas supply device which supplies oxidizing agent gas to modifier used during modification reaction, and on-off valve (9) provided at the 1st path which connects the oxidizing agent gas supply device and the modifier. The on-off valve closes when a pressure more downstream than the on-off valve rises in the flow of oxidizing agent gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the fuel cell system. (Drawing includes non-English language text).    Housing (1)    Fuel cell stack (2)    Modifier (3)    Combustor (4)    Desulfurizer (5)    On-off valve (9)
NOVELTY - Glutarimide (I) is halogenated, to obtain 3-halo-2,6-piperidinedione (II). The compound (II) and 4-nitro-isoindole-1-one (III) are subjected to nucleophilic substitution reaction under alkaline conditions, to obtain nitro group-containing compound (IV). The compound (IV) is reduced using reducing agent, to obtain lenalidomide (V).    USE - Preparation of lenalidomide (claimed).    ADVANTAGE - The method enables economical preparation of lenalidomide with high yield, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Glutarimide of formula (I) is halogenated, to obtain 3-halo-2,6-piperidinedione of formula (II). The compound (II) and 4-nitro-isoindole-1-one of formula (III) are subjected to nucleophilic substitution reaction under alkaline conditions, to obtain nitro group-containing compound of formula (IV). The compound (IV) is reduced using reducing agent, to obtain lenalidomide of formula (V).    X=chloro, bromo or iodo.
NOVELTY - An organic fertilizer comprises 80-85 wt.% peat containing more than 30% humic acid, 12-17 wt.% natural mineral powder, 2-5 wt.% nutrient synergistic agent, and 1-2 wt.% water-retaining agent.    USE - Organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer is environmentally-friendly, and safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer which comprises adding 5 l effective microorganisms to peat containing more than 30% humic acid and phytase, processing in stacks for 5-7 days, mixing with natural mineral powder, nutrient synergistic agent and water retaining agent, granulating, polishing, drying, cooling and packaging.
NOVELTY - This utility new type claims a biogas purifying one cold water system, comprise through pipeline connecting in turn of absorption tower, desorption, one level combination of desorption, desorption tower set with two combination a water outlet, wherein one water outlet through a circulation water pump, and the other one a process water outlet pipe connecting, combination desorption tower cold water machine set and the combination of desorption tower through pipeline and the process water pump of entrance connecting, process water pump exit and entrance upper side connect absorption tower. The new-type simplifies the carrying out cold water process, desorption tower using combination vertical structure, liquid phase space height high enough, circulation liquid there is no overflow in the desorption tower and combination process water pump is pumping out of, a greatly increases system stability.
NOVELTY - Preparation of coal-based solid acid involves crushing different degree coal, drying, extracting at room temperature to 300 degrees C for 0.5-24 hours under pressure of atmospheric to 35.2 MPa using organic solvent, obtaining extraction product and residual coal, separating extraction product and organic solvent, recycling organic solvent for extraction process, removing solvent from residual coal, sulfonating with sulfonating agent at 20-200 degrees C for 0.01-20 hours, washing solid reaction product for removing impurities, and drying.    USE - Preparation of coal-based solid acid used as catalyst for hydrolysis of cellulose into glucose, and for producing fuel ethanol.    ADVANTAGE - The coal-based solid acid is prepared by simple and economical method. The catalyst has high stability and activity, and is environmentally-friendly.
NOVELTY - Producing combustible gas includes generating set and gas separating machine, where generator set in non-optimal load state and non-optimal load state of operation of thermal generator set load increase, the generating set exceeds the power grid and generating electrical energy corresponding to number of non-generating set assistant type of gas separation. Gas is separated by physical method. Power grid load balances gas separation process, where power grid is provided with gas separating machine.    USE - Method for producing combustible gas (claimed).    ADVANTAGE - The method improves power generation efficiency.
NOVELTY - Enzymatic hydrolysis of food waste involves utilizing kitchen waste, where kitchen waste is added with methane sludge, acetic acid, volatile fatty acid, propionic acid, butyric acid, valeric acid and ethanol. The obtained mixture is transferred in a sequencing batch reactor, where domestic sewage and carbon source is added is added in a reactor. Chemical oxygen demand of waste water is regulated for six times to adjust the pH of the product at 7-8.    USE - Method for enzymatic hydrolysis of food waste (claimed).    ADVANTAGE - The method enables to hydrolyze food waste in a cost-effective manner.
NOVELTY - Adsorbent preparation involves mixing biomass material, epoxy chloropropane, ethylene diamine and triethylamine. The mixture is stirred at 20-120 degrees C for 30-600 minutes to obtain biomass adsorbent. The obtained biomass adsorbent is filled in the adsorption column, where the adsorption column is added with perchlorate solution to obtain water enriched biomass adsorbent. The obtained product is cultured in culture reactor at 15-50 degrees C, where the pH of the mixture is 5-10. The mixture is added with anaerobic active sludge to obtain domesticated sludge.    USE - Method for preparing adsorbent for microbial reduction of perchlorate in water (claimed).    DETAILED DESCRIPTION - Adsorbent preparation involves mixing biomass material, epoxy chloropropane, ethylene diamine and triethylamine. The mixture is stirred at 20-120 degrees C for 30-600 minutes to obtain biomass adsorbent. The obtained biomass adsorbent is filled in the adsorption column, where the adsorption column is added with perchlorate solution to obtain water enriched biomass adsorbent. The obtained product is cultured in culture reactor at 15-50 degrees C, where the pH of the mixture is 5-10. The mixture is added with anaerobic active sludge to obtain domesticated sludge. The obtained product is added with carbon source and then stirred at 10-50 degrees C to obtain desired product.
NOVELTY - Biological treatment of oil sewage involves introducing oil station water into flotation unit, removing crude oil and suspended solids, introducing resultant dissolved air flotation water into microbial oil pool, further removing crude oil in water after decomposing biofilm in microbial oil pool, introducing resultant water into biological aerated filter pool, filtering residual oil and suspended solids in water, degrading microbial film, and filtering remaining residue of micro-suspension in water using polymer sintered filter.    USE - Biological treatment of oil sewage (claimed).    ADVANTAGE - The method enables economical treatment of oil sewage without using pharmaceutical and nutritional agents, by simple process. The treated oil sewage has high quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of microbial oil pool; and    (2) preparation of biological aerated filter pool.
NOVELTY - Bio-fertilizer is prepared by taking liquid culture medium comprising yeast extract (5g/L), peptone (10g/L), sodium chloride (3g/L) and water (1L), where pH of medium is 7.2-7.4. The mixture is sterilized at 121 degrees C for 30 minutes. Bacillus subtilis is inoculated in solid culture medium (5ml) at 35-37 degrees C and 300-400 revolutions per minute for 20-24 hours to obtain a seed culture liquid, where the solid culture medium comprises yeast extract (5g/L), peptone (10g/L), sodium chloride (3g/L), agar (20g/L) and water (1L) at pH of 7.2-7.4, and is sterilized at 121 degrees C for 30 minutes.    USE - Bio-fertilizer used for crops such as corn, wheat, soybean, sugar cane and fruit trees such as peach, pear, jujube, apple, and used for vegetables and fruits such as cucumber, tomato, cabbage, bean, eggplant, lettuce, wheat, Chrysanthemum, gourd, pepper, rapeseed, melon, strawberry and grape (claimed).    ADVANTAGE - The bio-fertilizer promotes plant growth and improves crop yields with economic and social benefit.
NOVELTY - Biological fertilizer preparation involves adding brown sugar in water, and dissolving the obtained material. EM (RTM: Effective micro-organisms) liquid is added the dissolved material. The obtained EM bacterial liquid is mixed with grain and sugarcane leaves. The obtained mixture is covered with plastic film or canvas seal. The obtained mixture is fermented under anaerobic condition for 10 days in summer or 15 days in winter to obtain sugarcane bio-fertilizer, where weight ratio of water, brown sugar, EM bacteria liquid, grain and sugarcane leaves is 30-50:0.5-2:0.5-2:50-200:400-800.    USE - Method for preparing biological fertilizer (claimed).    ADVANTAGE - The method is simple and easy to control, and enables to produce biological organic fertilizer that is eco-friendly without inorganic fertilizer components.
NOVELTY - Fertilizer comprises (in pts.wt.): animal manure (50-80), organic matter (10-30), humic acid (5-15) and biological ferment liquid (1-5).    USE - Fertilizer.    ADVANTAGE - The fertilizer is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing animal excrement, organic matter and humic acid;    (B) drying and crushing obtained mixture to obtain powder; and    (C) mixing biological ferment liquid and powder to obtain desired product.
NOVELTY - Producing biofertilizer involves fermenting fungi raw materials having water content (65-70%) at 55-65 degrees C for 6-8 hours. The fermented materials are dried to obtain product with water content of 18-22%. Trichoderma fungi and Bacillus licheniformis bacteria are inoculated in fermentation medium for 5-7 days at less than 30 degrees C to obtain product. The product is dried in shade to retain moisture content up to 15% in order to facilitate bacteria in dormant or semi-dormant stage. The obtained product is packed and then stored.    USE - Method for producing biofertilizer (claimed).    ADVANTAGE - The method enables to produce biofertilizer that improves soil quality and prevents soil-borne diseases.
NOVELTY - Producing biofertilizer involves utilizing (in kilograms): bagasse (600), animal manure (200), pond residue (200), strain (1) and brown sugar (3). The strain and sugar are mixed with water. Fungus is added in obtained solution that is stirred for 3-4 days to obtain culture medium. The culture medium is mixed with other materials and water to retain water content at 55-65%. The obtained mixture is covered tightly using plastic film cloth to facilitate anaerobic fermentation for 6-8 days. The fermented material is dried at 60 degrees C to retain water content of 8-10% to obtain product that is packed.    USE - Method for producing biofertilizer (claimed).    ADVANTAGE - The method enables to produce biofertilizer that improves soil quality, increases product quality and yield, and reduces application of chemical fertilizer.
NOVELTY - Preparing fertilizer involves drying crop straw or livestock and poultry excrement in a carbonization furnace at high temperature, and then cooled to obtain a biochar. Biochar (10-20 pts.wt.) is mixed with livestock and poultry manure (65-85 pts.wt.) and phosphate powder (3-5 pts.wt) to obtain a mixture. Efficient microbe bacterial liquid (100-200l) and water (40-50%) are added into the mixture, and then stirred uniformly to obtain a product. The product is poured into a sealed fermenting tank for fermentation, where fermentation product is decomposed and dried until water content is 20-30%.    USE - Method for preparing fertilizer used in agriculture (claimed).    DETAILED DESCRIPTION - Preparing fertilizer involves drying crop straw or livestock and poultry excrement in a carbonization furnace at high temperature, and then cooled to obtain a biochar. Biochar (10-20 pts.wt.) is mixed with livestock and poultry manure (65-85 pts.wt.) and phosphate powder (3-5 pts.wt) to obtain a mixture. Efficient microbe bacterial liquid (100-200l) and water (40-50%) are added into the mixture, and then stirred uniformly to obtain a product. The product is poured into a sealed fermenting tank for fermentation, where fermentation product is decomposed and dried until water content is 20-30%. The fermentation product is dried and mixed uniformly with potassium (0-5 pts.wt.) and clay (2-5 pts.wt.), and then crushed to obtain a powder. The powder is granulated and dried to obtain the desired product.
NOVELTY - Bio-fertilizer pellets comprise enzyme probiotics, wheat bran, soybean powder, potassium dihydrogen phosphate, crop straw (fermentation), mushroom rods, Chlorella minutissima, plant straw ash, bentonite, humic acid, starch plant sludge, biological modifiers, urea phosphate, phytase, and bentonite and water mixture. Bio-fertilizer pellets are prepared in pellet mill.    USE - Bio-fertilizer pellets for improving soil, keeping nutrients and water in soil, promoting crop growth metabolism, resisting bacteria, preventing and treating crop diseases and increasing crop yield.
NOVELTY - A complex enzyme bacteria organic fertilizer comprises urea phosphate, biological microbial inoculum, trace element, amino acid, humic acid, xanthan gum, EDTA, active ingredients and plant growth regulator.    USE - Complex enzyme bacteria organic fertilizer used for promoting plant growth and increasing soil utilization rate.    ADVANTAGE - The complex enzyme bacteria organic fertilizer is inexpensive, increases yield, and improves quality of crops.
NOVELTY - Tea seed oil organic fertilizer comprises 40-50 pts. wt. tea seed cake, 15-20 pts. wt. peat soil, 20-30 pts. wt. cow manure, 5-10 pts. wt. urea, 10-15 pts. wt. alum powder, 4-8 pts. wt. chlorinated paraffin, 10-15 pts. wt. bentonite, 0.02-0.03 pt. wt. microbial fermentation inoculum, 3-5 pts. wt. quicklime, 6-12 pts. wt. ammonium bicarbonate and 2-4 pts. wt. composting accelerator.    USE - Tea seed oil organic fertilizer.    ADVANTAGE - The fertilizer is safe and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of tea seed oil organic fertilizer comprising mixing cow dung and peat soil, drying, fermenting tea seed oil for 10-15 days, adding quicklime, ammonium bicarbonate and accelerator, fermenting at 50-60 degrees C for 20-25 days, drying, sieving, adding remaining raw materials, mixing, extruding at 30-45 degrees C, granulating, drying and packaging.
NOVELTY - Method for cultivating pepper by potted plants technique involves adding 2 kg ash, 1 kg rock phosphate, 3 kg cow dung, 100 kg soil and 20 kg sand on ground, spreading uniformly using shovel, adding suitable amount of water and culture medium, covering using plastic film, fermenting for 30 days, loading fermented product in two-third of pots, choosing healthy young pepper seedlings, planting 2 seedlings in each flower pots, pressing and adding suitable amount of water to root, arranging the pots neatly, and performing management measures during growth period.    USE - The method is useful for cultivating pepper by potted plants technique (claimed).    ADVANTAGE - The pot can be moved and placed in inner room.
NOVELTY - Manufacture of chromium picolinate involves adding 0.05-0.1 mol 2-cyanopyridine to 25-75 ml methanol, stirring, heating to 65-78 degrees C, adding 7-10 ml 20-30% aqueous sodium hydroxide or potassium hydroxide, reacting with 15-20 ml water at 50-70 degrees C for 1 hour, adjusting pH to 8-9 using hydrochloric acid, stirring at 50-70 degrees C, hydrolyzing, adding 41.5-59.2 ml aqueous potassium chromium solution, cooling to 25 degrees C, filtering, washing filtrate with 20-30 ml water, washing with 20-30 ml ethanol and drying at 60-80 degrees C.    USE - Manufacture of chromium picolinate (claimed).    ADVANTAGE - The method efficiently enables manufacture of chromium picolinate having high purity of 99.8% with high yield by simple process with reduced consumption of energy.
NOVELTY - Synthesizing vinpocetine involves performing alkaline hydrolysis of vincamine in presence of reaction catalyst, and then obtained product is purified and crystallized to obtain desired product.    USE - Method for synthesizing vinpocetine (claimed).    ADVANTAGE - The method enables to synthesize vinpocetine in simple, cost-effective and eco-friendly manner.
NOVELTY - This new type utility claims an integrated membrane biological reactor biogas slurry processing device, comprise biogas liquid tank, the biogas liquid tank connecting of aeration and membrane reaction area, the reaction area connected with the film of the water device and fan, the membrane reaction area is set with the water device of the mobile cleaning device, a fan through aeration tube a and the aeration, membrane reaction area connected, the water device through a clean water tube and the membrane reaction area connected, the structure occupies small space, sewage treatment efficiency is high, the structure is compact.
NOVELTY - A liquid fuel oxidative desulfurization method involves mixing ionic liquid comprising catalyst with fuel at a volume ratio of 3:6-10 in an high pressure kettle, followed by passing oxygen gas to reach oxygen pressure of 0.1-0.5 Mpa, closing oxygen valve, opening oil bath, performing magnetic stirring and heating by controlling extraction agent and fuel volume ratio to be 0.1-5:1, catalyst and total sulfur content of the fuel molar ratio to be 0.1-5:1 and stirring to obtain mixture. The mixture is heated to 30-130? to react for 1-5 hours.    USE - Method for oxidative desulfurization of liquid fuel.    ADVANTAGE - The method enables oxidative desulfurization of liquid fuel in a simple and inexpensive manner.
NOVELTY - A biological diesel comprises 2.5-30 vol.% direct-coal-liquefied hydrogenation-modified full distillate oil and 70-97.5 vol.% waste oil biological diesel.    USE - A biological diesel (claimed).    ADVANTAGE - Biological diesel has reduced cloud point and pour point and improved low-temperature fluidity, and preparation is simple and effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological diesel which involves mixing direct-coal-liquefied hydrogenation-modified full distillate oil and waste oil biological diesel and standing for 8-12 hours.
NOVELTY - Biogas is liquefied by sending biogas from digester to 1st filter using pipe, filtering out liquid and impurities, sending to 2nd filter, desulfurizing, dehydrating, removing carbon dioxide, adding cosolvent, sending to air compressor, compressing, cryogenically liquefying biogas into liquid, and packaging in biogas tank using high-pressure pipeline.    USE - Liquefaction of biogas (claimed).    ADVANTAGE - Liquefaction of biogas reduces methane volume, and biogas has trace volatilization during transportation.
NOVELTY - Device comprises a crushing machine (1), a separator (3), a dehydrator (5), a sewage purification standard treatment machine (8), a burning furnace (9), a smoke waste heat steam boiler (2), and a smoke gas purification device (4). Pyrolysis system comprises a pyrolysis reactor (17), a condenser (18), a gas-liquid separation tank (15) and a tank (16), which in turn is connected to a gas storage cabinet (12). The waste materials fed into the sorter is discharged into the dehydrator through an inlet to obtain incinerated solid waste.    USE - Device used for preparing fuel from domestic waste.    ADVANTAGE - The device effectively processes carbohydrate into a dehydrated solid waste and also improves the calorific value of dehydrated solid waste. The device also enables to perform pyrolysis of dehydrated solid waste to obtain oil and gas as fuels in a simple, economical and an eco-friendly manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a device. (Drawing includes non-English language text).    Crushing machine (1)    Smoke waste heat steam boiler (2)    Separator (3)    Smoke gas purification device (4)    Dehydrator (5)    Sewage purification standard treatment machine (8)    Burning furnace (9)    Gas storage cabinet (12)    Gas-liquid separation tank (15)    Tank (16)    Pyrolysis reactor (17)    Condenser (18)
NOVELTY - Comprehensive processing involves removing impurities from Coptis wood seed, and then drying, and storing it in air. The stored Coptis wood seed is performed for winnowing, screening and magnetic separation for removing impurity. The cleaned Coptis wood seed is fried and crushed. Oil is squeezed from the obtained crushed product by settling preparation, and then cooled and filtered to obtain clear standard oil for preparing raw flavored oil. Filter residue is collected in pre-pressing cake.    USE - Method for comprehensive processing of Coptis wood seed for preparing edible oil and biological diesel (claimed).    ADVANTAGE - The method enables to process Coptis wood seed, ensures development of biological energy.    DETAILED DESCRIPTION - Comprehensive processing involves removing impurities from Coptis wood seed, and then drying, and storing it in air. The stored Coptis wood seed is performed for winnowing, screening and magnetic separation for removing impurity. The cleaned Coptis wood seed is fried and crushed. Oil is squeezed from the obtained crushed product by settling preparation, and then cooled and filtered to obtain clear standard oil for preparing raw flavored oil. Filter residue is collected in pre-pressing cake. The obtained oil is degummed, deacidified, decolored and refined to obtain refined edible oil. The residue of sewage is refined by soapstock acidification process to produce byproduct. The obtained pre-pressing cake and product obtained form acidification process is used for preparing non-refined biological diesel. The obtained product is processed to obtain standard biodiesel, crude glycerine and little biological residual oil.
NOVELTY - The method involves using waste oil as raw material, where the raw material is preprocessed by adding glycerin. Low carbon alcohol ester is added for exchanging process to receive glycerin, where the glycerin is a side product of ester exchange reaction.    USE - Method for producing fuel glycerol (claimed).    ADVANTAGE - The method produces the fuel glycerol having reduced solidifying point of glycerol, and improved cetane number.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the fuel glycerol production method. (Drawing includes non-English language text).
NOVELTY - Producing marsh gas involves using sugarcane leaves and then adding nitrogenous substance and water to obtain mixture, where weight ratio of nitrogenous substance and water is 1:20-30. Fermenting agent is added into obtained mixture and then covered with plastic film at 50 degrees C for 5 days to obtain another mixture. Human and animal excreta are added into obtained mixture and then water is added to obtain a third mixture. The obtained third mixture is sealed for 1-2 days to obtain the marsh gas.    USE - Method for producing marsh gas (claimed).
NOVELTY - The design and arc floor independent of domestic sewage treatment device is one strip-shaped marsh gas tank, the sewage input end, namely the end set with marsh gas tank ((/xuanlu:)) composite sewage separator, marsh gas tank top set with gas discharge tube, a methane tank tail end set with biogas residue discharging tube and marsh gas pool liquid level regulator and oxygen wall. ((/xuanlu:)) composite separator is conical tube, the cylinder wall ((/kelu:)) water liquid, with a rotational flow separation and the effect of filtering water liquid, the rear separating lennon dirt discharged to the biogas pneuma pool, sewage filter liquid water pump by the flushing with soda. Lennon sewage through biogas pool a pneuma, pneuma as cooking with, slag discharge as agricultural fertilizer, the marsh gas pool liquid level controller of filter water wall upon the fixed high discharge tube into the river. The facility is economic, practical and good.
NOVELTY - This utility new type claims a one integrated A2/O bio-membrane reactor, category sewage treatment device field. The reactor include: water inlet area set with the reactor tank body and inner of non-oxidation, an adjustable area, an aerobic area, contact oxidation, reflux area and non-oxidation area, area, an aerobic area, oxide area and contact area are orderly set with the reactor tank body, and connected in turn, set with water outlet, inner contact oxide area set with biological filler area, inlet area set with raw water inlet and water inlet channel, water inlet area in a non-oxidizing area set with one side, through water inlet channel of multi-set with the water outlet point and non-oxidation zone connected, reflux area on the other side set with non-oxidation area, set with return channel, the return channel of multi-set with the reflux point and non-oxidation connected. The reactor used for municipal sewage of doped Industrial Park, has high efficiency for removing nitrogen and phosphorus in effect, which greatly shortens the biochemical residence time, stable, good water quality and load resistant impact property of good.
NOVELTY - This utility new type claims a garbage percolate processing field, which provide a one waste leachate biological denitrification reaction device, include denitrification tank, tank and nitrification tank, water first entering into a denitrification tank and denitrification tank water to carbide tank, lower part of the water tank to the water outlet of a nitrification tank, a nitrification tank to subsequent processing unit, the bottom a mix liquid through reflux pump reflux to the denitrification tank. A carbide tank through a dissolve oxygen in a carbonization action of inner nitrifying a dissolve oxygen a nitrification tank, mix of inner nitrifying liquid refluxing to denitrification tank inner tank, a denitrification inner the denitrifying tank. This utility new type has the carbonized and nitrification, a dominant form of each strain, more high of efficiency.
NOVELTY - This utility new type claims a new-type one pig slurry treatment device, comprise coagulating and flow tank, the device further comprise a primary settling tank, pH value regulating pool and the shallow blowing tank, the pH adjusting pool, A/O biochemical pool, final sedimentation and light catalytic device, a coagulating, a pH value regulating pool and the shallow blowing tank, the pH adjusting pool, A/O biochemical pool, pond, light catalytic device and the flow tank through pipeline connecting in turn. Compared with the traditional technique, this utility new type for removal of each contaminant in pig farm biogas liquid of high efficiency, a water quality of water stable, operation is convenient and the cost is low.
NOVELTY - A one in a ethane from liquefied natural gas device, belonging to the LNG (liquefied natural gas) ethane recovery process technology field. LNG pump connecting first distributor, first distributor connecting plate-fin heat exchanger, a demethanizer, demethanizer reflux pump connect, durene, fin heat exchanger connecting a return tank, a first circulator, demethanizer, deethanizer, first circulator connecting the demethanizer, a return tank connecting reflux pump, reflux pump connect second; second distributor connecting second circulation device, second circulator connecting deethanization tower, ethane tower connecting balancer. This utility new type has simple structure, through heat exchange between the plate-fin heat exchanger of each stream to provide mass balance and energy balance of the device. Through a demethanizer of separating methane in LNG; through a deethanizer realize separation of ethane in LNG. A final recovery of ethane purity reaches 94% out of a liquefied pneuma and satisfy liquefied pneuma of our country standard.
NOVELTY - This utility new type relates to a one 4-amino-antipyrine production device, comprise first storage bin, a pyrazolone first pyrazolone hopper and first dimethyl sulphate measuring tank connect with the first methylation tank, a first tank and the first methylation hydrolysis tank connecting the first hydrolysis with alkali treatment tank connecting tank, alkali tank and is a oil storage tank connecting antipyrine; second pyrazolone hopper and second dimethyl sulphate measuring tank connecting with a second methylation tank, second tank and the second methylation hydrolysis tank connect, second hydrolysis tank, antipyrine oil storage tank, a third water metering pour a connecting with the sulphuric acid antipyrine quaternary ammonium salt tank, a sulphuric acid antipyrine quaternary ammonium salt tank and a nitrite measuring pour a connect with the nitrosation reaction tank, reaction tank and the nitrosification reduction reaction tank connect, reducing reaction tank and the neutralizing tank connecting hydrolysis, first hydrolysis tank is connected with the liquid alkali metering pour connecting. This utility new type environment-friendly, technique is simple, the operation is convenient, the product yield is high.
NOVELTY - This utility new type provide a one is simple and easy to control, good heat preservation effect, rational process of broad spectrum combination type biomass gasification device. Broad spectrum combination type biomass gasification device include shell, inner shell set with a first gasification room, second gasification room and third room and fourth gasification chamber, inner chamber is set with a fourth separator, separator with fuel gas exit, separator lower part connected material said one end and said other end connected material returning device, returning the first gasification room is connected, lower part connected with a return material returning air room, the returning air room is connected with the third gasification room connected, a shell side wall is provided with a feeding port and a secondary air entrance.
NOVELTY - This utility new type belongs to marsh gas purifying device technology field, and claims a one for marsh gas purifying lampblack filter. Comprise hollow tube, one tube end is an air inlet end, an air inlet connecting interface, and the other end is air outlet end, connecting with an air outlet interface, a tube inner tube air outlet end of connecting with the filter core, the improved, the inner tube is a tube between the air inlet end of the filter core connecting with, the top set with tube with valve of the air inlet bypass pipe connecting the air inlet end of the non-return device, an air outlet connecting the filter core with the air outlet end, the tube side wall of position between the non-return device and the filter core set with sight glass, a cylinder body at the bottom of the position of the check device and the filter core set with drainage tube, a drainage tube set with drain valve. This utility new type filter filter efficiency is high, the structure is simple, the operation is convenient, cleaning filter core does not need, and can observe the internal condition filter and rational exhaust of impurity and water.
NOVELTY - The system has a bio-mass semi-gasification furnace (11) provided with a heat exchanger (28), a chimney and an air pre-heating tube (15). An energy-saving water tank (16) is connected with the bio-mass semi-gasification furnace through a high-temperature water inlet pipe (25). The water inlet pipe is fixed at a first heat exchanger interface (27). The bio-mass semi-gasification furnace is fixed with a second heat exchanger interface (29) through a low-temperature return water pipeline (30), where an inner part of the bio-mass semi-gasification furnace is provided with a burner (13).    USE - Bio-mass semi-gasification heating system for use in a rural area.    ADVANTAGE - The system has low maintenance cost, high energy-saving effect and high production efficiency, and is convenient to popularize, and increases utilization rate of bio-mass energy.    DETAILED DESCRIPTION - The burner is formed as a bucket-shaped structure. The bio-mass semi-gasification furnace is provided with a hearth i.e. round table-shaped furnace chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a bio-mass semi-gasification heating system.    Bio-mass semi-gasification furnace (11)    Burner (13)    Air pre-heating tube (15)    Energy-saving water tank (16)    High-temperature water inlet pipe (25)    Heat exchanger interfaces (27, 29)    Heat exchanger (28)    Low-temperature return water pipeline (30)
NOVELTY - The device has a device body connected with an air pre-heating tube (15). A biomass semi-gasification furnace (11) is provided with an energy saving water tank (16). The energy saving water tank and the biomass semi-gasification furnace are connected with a heat exchanger (28). An air pre-heating tube (20) is fixed on a chimney. The energy saving water saving tank is connected with a water cooling pipe (18). An electromagnetic valve (26) is connected with a first heat exchanger interface (27). An inner part of the chimney is connected with the water cooling tube.    USE - Heating device for house.    ADVANTAGE - The device has low cost and simple structure. The device is convenient to use, and is convenient to rural areas.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a heating device.    Biomass semi-gasification furnace (11)    Air pre-heating tube (15)    Energy saving water tank (16)    Water cooling pipe (18)    Air pre-heating tube (20)    Electromagnetic valve (26)    First heat exchanger interface (27)    Heat exchanger (28)
NOVELTY - One to a mixture of coal, organic garbage and coal, wood as fuel, can be used for provide water, hot air, charcoal processing, waste incineration of multifunctional furnace. The furnace body by lengthways distribute of storage chamber, a gasification room, burning room and heat exchange area, pipe, a flue. The disposable chamber, adding needed in the combustion room furnace grate is cone design, and it greatly increases the combining surface of the air and the carbon, the material storage chamber is a closed space, the fuel oxygen gasification room and high temperature in the environment of gasifying a fuel gas and clean carbon, a clean combustion (especially mixture of straw, thin film, clothes, garbage and coal) and improves heat efficiency of at the same time reduces the waste discharge pneuma and energy-saving environment-friendly effect, designing cone of furnace grate body realize the automatic falling and ash discharging function of the fuel storage chamber, the furnace heat exchange area inner medium is inner water can realize heating function, heat exchange area medium is air can be a hot air furnace function, fuel wood is used of charcoal production and processing.
NOVELTY - The device has a cylindrical or flat anode room (1) that is provided with a pair of injection hole (101,103) and an electrode hole (102). A liquid outlet (105) of anode room is provided at a side plate (104). A silicon rubber pad (4) is fixed on the anode room. A cathode room (2) is provided with a pair of injection hole (201,203) and an electrode hole (202). A silicon rubber pad (11) is fixed on upper portion of the cathode room. A proton exchange film (3) is embedded on the silicon rubber pads. The anode room and cathode room are connected to form a single unit.    USE - Microbial fuel cell generating device.    ADVANTAGE - The reaction space of microbial fuel cell is increased, so that the zero angle of microbial fuel cell is washed conveniently. The liquid leakage phenomenon of microbial fuel cell generating device is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the microbial fuel cell generating device.    Anode room (1)    Cathode room (2)    Proton exchange film (3)    Silicon rubber pads (4,11)    Injection holes (101,103,201,203)    Electrode hole (102,202)    Side plate (104)    Liquid outlet (105)
NOVELTY - Improving platinum catalyst oxidation performance by removing carbon monoxide, comprises oxidizing platinum catalyst, using hydrogen gas feed, where the amount is 0.5-2.5%, adding carbon monoxide as a cocatalyst.    USE - The method is useful for improving platinum catalyst oxidation performance by removing carbon monoxide (claimed).    ADVANTAGE - The method: reduces carbon monoxide impurities to 20 ppm and concentration.
NOVELTY - Corn organic fertilizer comprises 10-20 wt.% of plant ash, 30-50 wt.% of bran, 20-25 wt.% of sawdust, and 40-60 wt.% of livestock manure.    USE - The organic fertilizer is useful for improving growth of corn and protecting the corn against disease.
NOVELTY - Liquid pesticide-containing fertilizer comprises 9-11 pts. wt. nitrogenous fertilizer, 8-8.5 pts. wt. phosphate fertilizer, and 6-7 pts. wt. potash fertilizer. The fertilizer further comprises 10-12 pts. wt. microbial flora, 5-6 pts. wt. humic acid, 0.7-0.9 pts. wt. insecticide, 6-7 pts. wt. water soluble release agent, 0.3-0.5 pts. wt. plant growth regulator, 3-4 pts. wt. iron fertilizer, 0.2-0.4 pts. wt. salicylic acid, and 120 pts. wt. water.    USE - The fertilizer is useful for controlling lawn pests (claimed); and killing insect pests.    ADVANTAGE - The fertilizer: provides nutrition substance to the crop; can be absorbed by plant leaf; has quick absorption, which does not easily loose nutrition substances; utilizes microbial flora, which increases light photosynthesis of crop; promotes absorption and utilization of nutrition substances; promotes lawn growth; and can degrade pesticide residue.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the liquid pesticide-containing fertilizer, comprising (i) dissolving nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and iron fertilizer in water, adding humic acid, and shaking for 60-65 minutes, and allowing to stand for 35 minutes; (ii) adding the plant growth regulator and microbial flora to resulting solution, shaking for 70 minutes, and allowing to stand for 48 minutes; (iii) adding water-soluble release agent to the resulting fertilizer, shaking for 2-2.5 hours, and allowing to stand for 30 minutes; and (iv) adding insecticide and salicylic acid to the resulting fertilizer, and packaging to obtain the finished product.
NOVELTY - Liquid fertilizer comprises 7-7.8 pts. wt. microflora, 11.2-11.8 pts. wt. humic acid, 7-8 pts. wt. nitrogen, 0.5-0.8 pts. wt. phosphate, 0.6-0.9 pts. wt. potash, 0.2-0.4 pts. wt. borax, 0.6-0.7 pts. wt. insecticide, 0.5-0.8 pts. wt. water-soluble isolating agent, 0.04-0.05 pts. wt. plant growth regulators, and 110 pts. wt. of water.    USE - The liquid fertilizer is useful for increasing yield of strawberry (claimed) and killing insect in the strawberry.    ADVANTAGE - The liquid fertilizer can promote absorption of nutrition substance in the crop, and has good degrading property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the liquid fertilizer comprising adding the nitrogen, phosphate and borate, adding water to the mixture to dissolve, adding humic and borax and mixing for 36-39 minutes, then standing for 32 minutes, then adding the plant growth regulator and the microflora and mixing for 30-35 minutes, standing for 10-15 minutes, then soluble isolating agent and stirring for 0.5-1.5 hours, then standing for 45 minutes, and packaging.
NOVELTY - Recycling dairy manure to produce straw coal composite fuel material comprises adding 40-50 wt.% of dairy manure, 20-30 wt.% of coal powder, 10-15 wt.% of coal gangue powder, 1.2-1.5 wt.% of catalyst, 0.5-0.9 wt.% of combustion improver, 1.5-5 wt.% of forming agent, 0.2-0.6 wt.% of active substance, and 10-18 wt.% of water into a forming machine.    USE - The method is useful for recycling dairy manure to produce straw coal composite fuel material (claimed).    ADVANTAGE - The method is capable of recycling dairy manure to produce straw coal composite fuel material in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a circulation dairy manure powder forming device.
NOVELTY - The cutting device has a knife rest that is provided with a cutter. A tool rest is mounted with a telescopic connecting device comprising an electric connecting box which is arranged with a connecting bracket. The electric connecting box is formed with an upper regulating switch. The cutting knife is connected with a conveyor belt to transfer the straw to a feeding tube.    USE - Cutting device for straw gasification furnace used in paper making industry and animal feeding industry.    ADVANTAGE - The combustion of straw in the gasification furnace is enabled efficiently and straw cutting efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the cutting device. (Drawing includes non-English language text)
NOVELTY - Tomato soil-less culture composite matrix comprises shiitake mushroom compost fermentation substrate and vermiculite compost.    USE - Tomato soil-less culture composite matrix.    ADVANTAGE - The inexpensive culture composite matrix promotes growth of tomato and increases yield of tomato.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of tomato soil-less culture composite matrix comprising fermenting shiitake mushroom compost fermentation substrate for not less than 15 days, adding vermiculite compost, and mixing.
NOVELTY - A fuel pellet producing method involves mixing sawdust and wood chips to obtain mixture. The mixture is dried and mixed with additives. The resultant mixture is pre-dried to obtain mixture. The mixture is mixed with spent oil and subjected to averaging process. The resultant mixture is activated in steam and mixed with a natural binder in the form of precipitate and lignin obtained from the organic material vegetable to obtain mixed product. The mixed product is subjected to breaking process and granulation by molding to obtain granulated product, which is cooled.    USE - Method for producing fuel pellet from sawdust.    ADVANTAGE - The method enables producing fuel pellet with increased calorific value.    DETAILED DESCRIPTION - A fuel pellet producing method involves mixing sawdust with a moisture content of 50-70% and wood chips to obtain mixture. The mixture is dried and mixed with additives that attract and stabilize quality and caloric content of final product. The resultant mixture is pre-dried at 400 degrees C for 1 hour to obtain mixture with moisture content of 14-16%. The 85-98% mixture is mixed with spent oil and subjected to averaging process. The resultant mixture is activated in steam at 120-150 degrees C and mixed with a natural binder in the form of precipitate and lignin obtained from the organic material vegetable to obtain mixed product. The mixed product is subjected to breaking process, and granulation by molding at high temperature of 100-120 degrees C to obtain granulated product with diameter of 8-12 mm. The granulated product is cooled to 20 degrees C for 5-10 minutes, and treated to separate particles that not granulated.
NOVELTY - Manufacturing biologically-derived paraffinic jet and diesel fuels, solvents and base oils from a biological hydrocarbonaceous oxygenated oil, involves: (a) hydrotreating the biological hydrocarbonaceous oxygenated oil to form a first effluent mixture comprising propane, carbon monoxide, carbon dioxide, water and a n-paraffinic product; (b) recovering the n-paraffinic product from the first effluent mixture; and (c) converting the n-paraffinic product of step (b) over a paraffin disproportionation catalyst.    USE - The process is useful for manufacturing biologically-derived paraffinic jet and diesel fuels, solvents and base oils from a biological hydrocarbonaceous oxygenated oil including rapeseed oil, colza oil, canola oil, tall oil, sunflower oil, soybean oil, hempseed oil, olive oil, linseed oil, mustard oil, palm oil, peanut oil, castor oil, coconut oil, lard, tallow or train oil (all claimed).    ADVANTAGE - The process does not employ hydrogen gas thus avoiding usage of expensive recycle gas compressors, and does not require expensive reactor quench systems or inter-stage reheaters to control the temperature during hydrogenation/dehydrogenation and olefin metathesis processes.    DETAILED DESCRIPTION - Manufacturing biologically-derived paraffinic jet and diesel fuels, solvents and base oils from a biological hydrocarbonaceous oxygenated oil, comprising triglycerides, involves: (a) hydrotreating the biological hydrocarbonaceous oxygenated oil to form a first effluent mixture comprising propane, carbon monoxide, carbon dioxide, water and a n-paraffinic product; (b) recovering the n-paraffinic product from the first effluent mixture; and (c) converting the n-paraffinic product of step (b) over a paraffin disproportionation catalyst to form a second effluent mixture comprising a light n-paraffinic biologically derived product and a heavy n-paraffinic biologically derived product.
NOVELTY - Producing coke oven gas and tar, comprises (a) introducing coal blend into a carbonizing chamber of a coke oven; (b) supplying biomass on top of coal blend; and (c) heating biomass and coal blend using waste heat in the carbonizing chamber of the coke oven.    USE - The method is useful for producing coke oven gas and tar (claimed).    ADVANTAGE - The method provides quantitative yield of coke oven gas; and is convenient and economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart for producing coke oven gas and tar (Drawing includes non-English language text).
NOVELTY - Composite fresh water system comprises reverse osmosis unit which desalinates raw water by supplying electric energy generated by fuel cell unit, and membrane distillation unit which desalinates brine discharged from the reverse osmosis unit by membrane distillation process.    USE - Composite fresh water system (claimed).
NOVELTY - The method comprises: applying glass microparticles and/or glass nanoparticles to hydrocarbons in a contaminated area; removing the glass microparticles and/or the glass nanoparticles soaked with the hydrocarbons from the contaminated area; and regenerating the glass microparticles and/or the glass nanoparticles by removing the hydrocarbons. The glass microparticles and/or the glass nanoparticles are produced from recycled glass.    USE - The method is useful for removing environmental hydrocarbon contamination in a contaminated area such as roadway, driveway, raceway or parking area, where the hydrocarbon includes oil, gas, diesel, motor oil, ethanol, methanol, brake and transmission fluids and/or acetone (all claimed).    ADVANTAGE - The method is capable of easily removing the environmental hydrocarbon contamination in the contaminated area in a simple and economical manner.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic projection view of a hydrocarbon sensor.    Housing (110)    Elongated rod (132)    Spring (136)    Sensor (138)    Signaling system. (140)
NOVELTY - The method involves spraying water on the product gas generated by gasifying organic raw material such as biomass with respect to the product gas passed through the flow path of cavity. The bubble is generated in the water with product gas stored in the storage tank. The product gas is cooled by contact with cooling heating surface. The temperature of product gas is set to predetermined range. The tar contained in the water sprayed in the separation tank is separated.    USE - Manufacturing method of product gas used as source gas for chemo-synthesizing gas fuel, methanol and gas to liquid fuel /petroleum equivalent fuel for electric power generation.    ADVANTAGE - The economical efficiency is improved effectively. The cooling load is minimized in large sized plant.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) Tar removal apparatus; and    (2) manufacturing apparatus of product gas.    DESCRIPTION OF DRAWING(S) - The drawing shows block diagram of the manufacturing apparatus of product gas. (Drawing includes non-English language text)    Organic raw material (101)    Modifier (102)    Organic raw material supply apparatus (103)    Modifier supply apparatus (104)    Gasification reaction apparatus (105)
NOVELTY - Organic fertilizer comprises monocalcium phosphate, urea, monoammonium phosphate, potassium chloride, potassium sulfate, chitin, pentachloronitrobenzene, glycerol monostearate, humic sesame, Oxalis triangularis, microbial inoculum, film-forming agent and balance water. The film-forming agent comprises paraffin, dipentaerythritol hexaacrylate, silane coupling agent, aluminum trichloride, aluminum oxide, crosslinking agent, nanocarbon, mineral powder and gluconate.    USE - Organic fertilizer used for improving crop yield and nutrient absorption.    ADVANTAGE - The organic fertilizer is inexpensive, environmental-friendly, safe and nutrient-rich.    DETAILED DESCRIPTION - Organic fertilizer comprises 40-45 pts. wt. monocalcium phosphate, 30-34 pts. wt. urea, 20-23 pts. wt. monoammonium phosphate, 12-15 pts. wt. potassium chloride, 5-7 pts. wt. potassium sulfate, 3-4 pts. wt. chitin, 1-2 pts. wt. pentachloronitrobenzene, 1-2 pts. wt. glycerol monostearate, 30-34 pts. wt. sesame, 10-12 pts. wt. Oxalis triangularis, 3-4 pts. wt. microbial inoculum, 4-6 pts. wt. film-forming agent and balance water. The film-forming agent comprises 20-22 pts. wt. paraffin, 10-12 pts. wt. dipentaerythritol hexaacrylate, 2-3 pts. wt. silane coupling agent, 2-3 pts. wt. aluminum trichloride, 1-2 pts. wt. aluminum oxide, 1-2 pts. wt. crosslinking agent, 0.1-0.2 pt. wt. nanocarbon, 2-3 pts. wt. mineral powder and 1-2 pts. wt. gluconate. An INDEPENDENT CLAIM is included for the preparation of organic fertilizer comprising drying Oxalis triangularis, crushing, soaking in water for 5-6 hours, adding humic sesame, potassium sulfate, chitin, pentachloronitrobenzene, glycerin monostearate, mixing, heating, adding urea, monoammonium phosphate and potassium chloride, mixing, adding water and microbial inoculum, fermenting for 15-20 days, drying and granulating.
NOVELTY - A diaphragm comprises a sheet-like porous support material (3) and a microporous film (2,2',21) laminated on surface(s) of the porous support material and containing mono layer containing organic polymer resin. The average hole diameter (Pc) in the cross section (C) which is parallel to the membrane surface (B) of the microporous film which contacts the porous support material and the membrane surface (A) of the microporous film on the opposite side to surface (B) is less than the average hole diameter (Pa) in the surface (A) and average hole diameter (Pb) in the surface (B).    USE - Diaphragm is used for alkaline water electrolysis apparatus (claimed) for manufacturing hydrogen. Uses include but are not limited to petroleum refining, chemosynthesis material, metal refinement, domestic cogeneration system and fuel cell electric vehicle.    ADVANTAGE - The diaphragm has excellent gas barrier property and ionic permeability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) alkaline water electrolysis apparatus; and    (2) manufacture of diaphragm.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of microporous film.    Microporous film (2,2',21)    Porous support material (3)    Surfaces (A,B,C)    Average hole diameters (Pa,Pb,Pc)
NOVELTY - A biofuel from straw producing method involves introducing stream of biomass particulate with 1 wt.% lime, to form recycled material, and subjecting to the pre-aeration in the air stream. The mixture is pre-saturated with calcium oxide, pulverized biomass is reduced at size to the final fraction of 2-8 mm and mixed and allowed to stand for aging in the tank. Process is carried out on the uniform dispersion of dust fraction by conditioning and subjected to molding, thermal pressing, and subjecting resulting product for cooling at ambient temperature to obtain finished product.    USE - Method for producing biofuel from straw.    ADVANTAGE - The method enables eliminating the chlorine and sulfur.    DETAILED DESCRIPTION - A biofuel from straw producing method involves introducing stream of biomass particulate with 1 wt.% lime, to form recycled material, and subjecting to the pre-aeration in the air stream of the biomass in an amount of 6000-8000 m3/ho, and air speed of 120 m/second. The mixture is pre-saturated with calcium oxide, pulverized biomass is reduced at size to the final fraction of 2-8 mm and mixed by swirling and allowed to stand for aging for 10-15 minutes in the tank. Process is carried out on the uniform dispersion of dust fraction by conditioning and subjected to molding, thermal pressing at 95 degrees C, and subjecting resulting product for cooling at ambient temperature to obtain finished product.
NOVELTY - An agricultural long term potato granular fertilizer comprises 75-85 wt.% fertilizer core, 8-15 wt.% coating layer and 5-10 wt.% coating agent.    USE - Agricultural long term potato granular fertilizer.    ADVANTAGE - The method is simple, and has low energy consumption and material cost. The fertilizer reduces cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of agricultural long term potato granular fertilizer comprising mixing nitrogen fertilizer, phosphate fertilizer, potassium fertilizer and additive, spray or disk granulating, drying at 80-120 degrees C, spraying coating agent, atomizing, spraying coating layer, curing at less than or equal to 70-100 degrees C, and rolling.
NOVELTY - A 0.9 mol dichloroethane, 1.85 mol m-cresol, o-cresol or p-cresol and 35 ml water are added into reactor, 49 wt.% aqueous solution sodium hydroxide is added dropwise for 20 minutes, heated, refluxed for 3 hours, and solution is transferred to a separator. The aqueous layer is discharged, and the reactor is reversed for condensation reaction at 70-80 degrees C for 3 hours. The temperature is raised to 100 degrees C, allowed to stand, purified by distillation to obtain 195.1 g 1,2-dimethylphenoxy ethane.    USE - Preparation of thermosensitive sensitizing agent (claimed).    ADVANTAGE - The method produces highly pure thermosensitive sensitizing agent with high yield, using simple and environmentally-friendly process, economically, under mild reaction conditions. The reaction product can be used as starting material, after extraction of impurities, for the continuation of reaction.    DETAILED DESCRIPTION - A 0.9 mol dichloroethane, 1.85 mol m-cresol, o-cresol or p-cresol and 35 ml water are added into a reactor, under nitrogen protection and stirred. 49 Wt.% aqueous solution of 100 g sodium hydroxide is added dropwise for 20 minutes, heated, refluxed for 3 hours. The solution is transferred to a separator, aqueous layer is discharged, the reactor is reversed for condensation reaction at 70-80 degrees C for 3 hours. 95 ml Water is shunted, 175 ml water is added with stirring, and reactor temperature is raised to 100 degrees C. The reaction mixture is allowed to stand to form 204.7 g 1,2-dimethylphenoxy ethane crude organic layer, having purity of 96.5% and yield of 93.98%, based on HPLC, and purified by distillation to obtain 195.1 g 1,2-dimethylphenoxy ethane.
NOVELTY - A waste substance and biomass pyrolysis and gasification method involves drying waste materials and biomass and heating dried materials at 70 degrees C. The hot materials are subjected to pyrolysis at 200-800 degrees C and gasification at 800-950 degrees C. The resulting gas is subjected to combustion in a combustion chamber and the exhaust gas is transferred to a heat exchanger. The hot gas is circulated through thin tubes at 450-500 degrees C and fed into an injector under pressure of 60-70 bar followed by carrying out vitrification process and cooling resulting product to obtain solidified mass.    USE - Method for pyrolysis and gasification of waste substance and biomass.    DETAILED DESCRIPTION - A waste substance and biomass pyrolysis and gasification method involves drying waste materials and biomass and heating dried materials at 70 degrees C. The hot materials are subjected to pyrolysis at 200-800 degrees C and gasification at 800-950 degrees C. The resulting gas is subjected to combustion in a combustion chamber and the exhaust gas is transferred to a heat exchanger. The hot gas is circulated through thin tubes at 450-500 degrees C and fed into an injector under pressure of 60-70 bar followed by carrying out vitrification process at 1600 degrees C and cooling resulting product in a water bath at 100 degrees C to obtain solidified mass in form of granules and beads.
NOVELTY - The system has a hopper (230) that receives the waste synthetic resin ejected from a conveyor (220) in a vibration board. A primary crusher (210) crushes the waste synthetic resin filtered in a filter section. A cooling water pipe is mounted in a rotary shaft, for cooling the crushed waste synthetic resin in form of the gel. The cooled waste synthetic resin is crushed by a secondary crusher combined with the rotary shaft, for completely removing the foreign substance in the waste synthetic resin.    USE - Solid fuel product pelletization system for processing agricultural waste and industrial waste.    ADVANTAGE - The configuration of the solid fuel product pelletization system is simplified so that the manufacturing and maintenance costs of the solid fuel product pelletization system are reduced significantly. The durability and impurity removal effect of the solid fuel product pelletization system are improved efficiently while suppressing the environmental contamination.    DESCRIPTION OF DRAWING(S) - The drawing shows a configuration diagram of the solid fuel product pelletization system.    Primary crusher (210)    Conveyor (220)    Hopper (230)    Case (300)    Opening and closing portion (310)
NOVELTY - A herbicidal composition comprises microcapsules having a polymer shell and containing in it clomazone and a liquid carrier having a lipid extracted from an alga.    USE - For controlling plant growth at a locus (claimed).    ADVANTAGE - The composition has reduced environmental impact, an increase in agricultural production with high efficiency, increased user friendliness, and a reduced toxicity. The process for preparing the composition is readily applied on a commercial scale.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a herbicide composition, involving providing a water immiscible phase comprising clomazone, an algae-originating lipid, an isocyanate and optionally an ACD cross-linker; providing an aqueous phase comprising at least one surfactants; combining the water immiscible phase and the aqueous phase to form a dispersion of the water immiscible phase in the aqueous phase, to form microcapsules of polyurea containing droplets of the water immiscible phase; and curing the microcapsules.
NOVELTY - A fuel comprises 40-90 wt.% sterilized and dried biomass and/or municipal waste containing chlorinated organic compounds and reagent in the form of alkali metal compounds, preferably calcium hydrate, and 3-15 wt.% additives in the form of organic material, preferably protein, where the fuel is prepared by mixing biomass and/or municipal waste material with reagent and ground lime to obtain a homogeneous moist mass. The obtained mass is sterilized, dried, heated and subjected to carbonization, sterilization and multi-stage separation screening to obtain finished product.    USE - Fuel for reducing dioxin emission.    DETAILED DESCRIPTION - A fuel comprises 40-90 wt.% sterilized and dried biomass having moisture content of 5-25% and/or municipal waste having moisture content of 5-50 wt.% and containing 5-25 wt.% chlorinated organic compounds and reagent in the form of alkali metal compounds, preferably calcium hydrate, and 3-15 wt.% additives in the form of organic material, preferably protein, where the fuel is prepared by removing metal and mineral impurities from biomass and/or municipal waste and refining the materials to less than 5 cm. The refined material is hydrated and mixed with reagent and ground lime to obtain a homogeneous moist mass. The homogeneous moist mass is sterilized and dried in an environment free of oxygen to obtain a homogeneous material having a porous structure. The protein in the homogeneous material is hydrolyzed, and the homogeneous material is heated at 60-80 degrees C followed by drying, carbonizing and sterilizing by passing a gas stream rich in carbon dioxide at 60-150 degrees C for 5 - 60 minutes, preferably 40 minutes. The resulting material is dried and subjected to multi-stage separation screening to separate fuel, mineral and organic fractions as products.
NOVELTY - Flower fertilizer comprises 40-45 pts. wt. bamboo, 23-26 pts. wt. chaff, 12-14 pts. wt. cotton seed hull, 10-12 pts. wt. corn starch, 12-14 pts. wt. urea, 12-14 pts. wt. potassium chloride, 2-3 pts. wt. ethylenediamine tetraacetic acid, 4-5 pts. wt. polyvinyl alcohol, 1-2 pts. wt. copper powder, 2-3 pts. wt. zinc sulfate, 2-3 pts. wt. borax, 3-4 pts. wt. EM microbial inoculum, 4-6 pts. wt. coating agent and balance water.    USE - Flower fertilizer.    DETAILED DESCRIPTION - Flower fertilizer comprises 40-45 pts. wt. bamboo, 23-26 pts. wt. chaff, 12-14 pts. wt. cotton seed hull, 10-12 pts. wt. corn starch, 12-14 pts. wt. urea, 12-14 pts. wt. potassium chloride, 2-3 pts. wt. ethylenediamine tetraacetic acid, 4-5 pts. wt. polyvinyl alcohol, 1-2 pts. wt. copper powder, 2-3 pts. wt. zinc sulfate, 2-3 pts. wt. borax, 3-4 pts. wt. EM microbial inoculum, 4-6 pts. wt. coating agent and balance water. Coating agent contains 12-15 pts. wt. dimethyl silicone oil, 13-16 pts. wt. crosslinking agent TAC, 1-2 pts. wt. nano carbon, 0.1-0.2 pts. wt. medical stone powder and 1-2 pts. wt. orthoboric acid, and prepared by mixing raw materials, grinding and dispersing to obtain the product. An INDEPENDENT CLAIM is included for preparation of flower fertilizer comprising heating urea and potassium chloride, stirring, and spray drying to obtain mixed fertilizer; adding EDTA, polyvinyl alcohol, sulfuric acid, copper powder, zinc powder, borax powder and iron in warm water, adding corn starch, and fully stirring to obtain liquid mixture; and mixing chaff, cotton, liquid mixture, EM, coating agent and other remaining component mix, stirring, sealing, supplying oxygen, fermenting for 20-30 days at room temperature, drying to prepare granule, mixing with mixed fertilizer to obtain product.
NOVELTY - A laboratory wastewater processing device comprises sewage storage tank (1), sewage treatment groove (2), snake-shaped clapboard, and bacteria silk bag filled with wastewater organic poison and mycelial pellets dye, where mycelium pellets are Trametes gallica, Coriolus versicolor, and Pleurotus ostreatus.    USE - Laboratory wastewater processing device.    ADVANTAGE - The method has low processing cost. The device is simple, easy to operate, can process little sewage and colored and concentrated organic substance, preferably phenol aniline substances, and has more than 90% degradation rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing of laboratory wastewater comprising introducing sewage into multi-sewage treatment groove through Trametes gallica, Coriolus versicolor, and Pleurotus ostreatus; and rinsing mycelium bag, placing mycelium pellet in nutrient regeneration tank, adding sterile nutrient solution, shaking for 1-2 days, releasing nutrient solution, rinsing surface to remove nutrient solution, and preserving at 4-10 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of laboratory wastewater processing device.    Sewage storage tank (1)    Sewage treatment groove (2)    Tube (8)    Sealing clamp (9)    Mycelium bag rinse tank (10)
NOVELTY - Use of Pycnarrhena poilanei is claimed in preparation of composition for preventing tobacco black shank disease.    USE - The P.poilanei is useful in preparation of composition for preventing tobacco black shank disease (claimed).    ADVANTAGE - The P.poilanei causes low toxicity and no environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the above-cited P.poilanei composition, which involves smashing P.poilanei, sieving using 200 mesh sieve, mixing the sieved material with methanol in a weight ratio of 1:3, extracting for 3 times (each time for 7-10 days), filtering the extracts, combining the filtrates, concentrating the combined filtrate until the filtrate dries, dissolving 100 g dried concentrate in 1000 ml 95% ethanol, and refrigerating the obtained mixture at 20 degrees C.
NOVELTY - A struvite precipitation is performed by measuring aquaculture wastewater anaerobic fermentation slurry in terms of ammonium, magnesium and phosphate ion concentrations; adding struvite to the slurry for precipitation; separating solids and liquids; inoculating; and solid-liquid separating.    USE - Struvite precipitation for coupling microalgae culture biogas slurry and biogas purification (claimed).    ADVANTAGE - The method improves transparency of biogas slurry which is more beneficial to growth of microalgae.
NOVELTY - An organic cultivation substrate comprises 20-40 pts. wt. bamboo cuttings, 20-40 pts. wt. bagasse, and 5-15 pts. wt. dairy manure.    USE - Organic cultivation substrate.    ADVANTAGE - The substrate high organic cultivation which achieves seedlings high survival rate. The method is environment-friendly and easy to operate, utilizes organic solid waste material, reduces production cost, and has simple preparation process matrix.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of substrate by fermenting bamboo cuttings at 50-60 degrees C for 20-45 days through aerobic bacteria fermentation, adding with bagasse and dairy manure, mixing, and aging for 20-45 days until water content is 15-30%.
NOVELTY - A kitchen waste biological treatment device comprises first conveyor (1), high-speed centrifuge (2), second conveyor (3), mixer (4), third conveyor (5), and screw conveyor (6).    USE - Kitchen waste biological treatment device.    ADVANTAGE - The method is simple and environment-friendly, utilizes high-efficiency equipment with low energy consumption, and has short processing, and high economic efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included biologically treating kitchen waste by manually sorting waste material, conveying to high-speed centrifuge using first conveyor, separating, conveying to mixer using second conveyor, adding fermentation agent, high-speed stirring, and adding auxiliary material, preferably sawdust, black carbon and aerobic bacteria using screw conveyor; aerobically fermenting at 0-15 degrees C for 10-20 days, increasing temperature to 15 degrees C or more for 10-15 days, and naturally drying until no more foul odor; and stacking fruits, vegetables, water without overflowing, covering with fermented material at 10-15 cm high, fermenting, and screening to obtain 60-80 wt.% fermentation reusable materials and 20-40 wt.% organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of kitchen waste biological treatment device.    First conveyor (1)    High-speed centrifuge (2)    Second conveyor (3)    Mixer (4)    Third conveyor (5)    Screw conveyor (6)
NOVELTY - Urea production with carbon dioxide stripping is carried out by connecting medium-pressure pre-separator (5), medium-pressure rectifying tower (6) and medium-pressure carbon dioxide gas stripping tower (7) in series, sending ammonia solution to the carbon dioxide gas stripping tower at 1.65-1.85 MPa and decomposing ammonia at 110-115 degrees C; concentrating ammonia vapor in evaporative concentrator (9) at 0.3-0.4 MPa; sending concentrate to urea synthesis tower (1) and low pressure rectifying tower (8), and performing flash separation and carbon dioxide gas stripping.    USE - Method for urea production with carbon dioxide stripping (claimed).    ADVANTAGE - The method is energy-saving and convenient to operate, has simple process flow and high yield, and can increase urea production by 30-60%.    DETAILED DESCRIPTION - Urea production with carbon dioxide stripping comprises:    (A) connecting medium-pressure pre-separator (5), medium-pressure rectifying tower (6) and medium-pressure carbon dioxide gas stripping tower (7) in series, sending ammonia solution to the carbon dioxide gas stripping tower at 1.65-1.85 MPa and decomposing ammonia at 110-115 degrees C, and separating vapor in the pre-separator and rectifying;    (B) concentrating ammonia vapor in evaporative concentrator (9) at 0.3-0.4 MPa;    (C) sending concentrate to urea synthesis tower (1) and low pressure rectifying tower (8) connected in parallel, performing flash separation, liquid distillation and carbon dioxide gas stripping; and    (D) conveying obtained urea solution to urea tank (16).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for urea production with carbon dioxide stripping.    Urea synthesis tower (1)    Medium pressure pre-separator (5)    Medium-pressure rectifying tower (6)    Medium-pressure carbon dioxide gas stripping tower (7)    Low pressure rectifying tower (8)    Evaporative concentrator (9)    Urea tank (16)
NOVELTY - A (2R,3R)-dihydromyricetin product is prepared by providing 3,4,5-trihydroxy-phenyl acrylic acid, acyl chloride and phloroglucinol as raw materials, performing acylation, attaching double bond peroxide into epoxy bond, performing open-loop reaction with phenol hydroxyl ether, separating, purifying, and crystallizing.    USE - Method for preparation of (2R,3R)-dihydromyricetin (claimed).    ADVANTAGE - The product has high content and high purity. The method is green and environment-friendly.
NOVELTY - A 3-N-dimethylamino-1-(2-thienyl)-1-propanone hydrochloride is prepared by providing 2-O-acetyl thiophene as initial raw material, low carbon alcohol as solvent, low catalytic Lewis acid, methylamine hydrochloride and formaldehyde, and performing Mannich reaction to obtain desired product.    USE - Method for preparation of 3-N-dimethylamino-1-(2-thienyl)-1-propanone hydrochloride (claimed).    ADVANTAGE - The method has high yield of 80-85 wt.%, has simple operation, prepares good purity product, and has environment-friendly production process.
NOVELTY - Preparing tea saponin palmitate surfactants involves adding catalysts, tea saponin, and palmitic acid chloride to the organic solvent into esterification reaction until the completion of reaction to give tea saponin palmitate surfactant.    USE - For preparing tea saponin palmitate surfactants (claimed), used in food, medicine, pesticide, daily, mineral, oil.    ADVANTAGE - The method has simple process, is friendly environment, has higher surface activity, and the reaction condition is easy to control.
NOVELTY - Extracting and purifying betulin involves grinding the dried birch bark to a certain size, then adding methanol, ethanol, petroleum ether, chloroform, and heating reflux extraction for 4 times, each time for 2 hours, combining the extracting liquid concentrate to saturated, adding proper active carbon to decolor, then cooling/crystallizing to obtain birch wood alcohol crude product, using methanol, ethanol, isopropanol to obtain birch wood alcohol.    USE - For extracting and purifying botulin, as intermediate for preparing betulinic acid.    ADVANTAGE - The method is simple and easy to operate, the extraction of pieces of mild, and has little environmental pollution
NOVELTY - Fluorescent nano-cluster preparation involves preparing glutathione solution with a certain concentration, gold reagent and cerium reagent water solution. 1.5-10 mmol/l of glutathione aqueous solution is mixed in 0.5-5 mmol/l metal reagent uniformly with shaking to obtain a colorless solution. The obtained solution is heated in water bath after adding 0.025-5 mmol/l of cerium reagent, where the obtained reaction mixture is cooled to form a fluorescent fine gold cerium oxide nanometer composite material.    USE - Method for preparing fluorescent nano-cluster for treating tumor cell selected from liver cancer, lung cancer, cervical cancer, leukemia or bone tumor (claimed).    ADVANTAGE - The method prepares fluorescent nano-cluster having good biocompatibility.
NOVELTY - The furnace has furnace body (1) formed with a guide layer (3), a water cooling layer (4) and a water regulating layer (5). A top part of the furnace body is provided with a hopper (2). A stirring device comprises a motor, a sieve plate (7) and a transmission gear. The furnace body is connected with the sieve plate. A ring gear is engaged with the furnace body. The guide layer is surrounded with the water cooling layer that is provided with a water channel and surrounded with the water regulating layer. The water regulating layer is connected with the water channel.    USE - Biomass straw gasification combustion furnace.    ADVANTAGE - The furnace can save energy, realize combustion gas generating process and automatic straw feeding process by using a raw material feeding device, improve production efficiency, ensure production safety, stir a straw by using the stirring device, contact the straw with combustion and gasification air, so that the straw combustion ash can be generated from a mesh of the sieve plate, thus avoiding straw ash burning phenomenon and improving burning-gasifying effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass straw gasification combustion furnace.    Furnace body (1)    Hopper (2)    Guide layer (3)    Water cooling layer (4)    Water regulating layer (5)    Sieve plate (7)
NOVELTY - The system has a water-washed tar unit whose input end is connected with a charcoal baking room and a straw gasifier. The gasifier is provided with an inner circulation water cooling fire grate that is installed between two adjacent table devices. A foundation comprises a left wall, a right wall, a rear wall and a roof. A house is covered with a steel plate. A lower end of the arched roof is connected with the left wall and the right wall. The roof is formed with an air inlet hole. An upper part of the rear wall is provided with an air outlet.    USE - Straw gasifying comprehensive processing system.    ADVANTAGE - The system avoids wastage of charcoal and ensures straw gasification furnace normal temperature, and is simple in structure and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a straw gasifying comprehensive processing system.
NOVELTY - The device has an annular seal water channel (1) and a nozzle that are connected with a connecting tube (2). The connecting tube is connected with a gasification furnace (3). An end opening of the connected tube is formed on the annular seal water channel. A bottom part of the annular seal water channel is located on a furnace side wall of the gasification furnace. The annular seal water channel is made of stainless steel/aluminum alloy material and formed by welding process. The connecting tube and the gasification furnace are coated with glass glue.    USE - Energy-saving biomass straw combustion gasification furnace water sealing device.    ADVANTAGE - The device can prevent gas leakage, ensure smooth gas collecting process and reduce and regulate gasification furnace pressure in reasonable range so as to avoid excessive damage of the gasification furnace caused by pressure change, thus prolonging service life of the gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an energy-saving biomass straw combustion gasification furnace water sealing device.    Annular seal water channel (1)    Connecting tube (2)    Gasification furnace (3)
NOVELTY - The structure has a furnace body (1) connected with a guide pneumatic layer (2) that is surrounded with a water cooling layer (3). The water cooling layer is arranged with a water channel and surrounded with a water regulating layer (4). The water regulating layer is arranged with the water channel. The water cooling layer is connected with the water regulating layer.    USE - Combustion energy-saving bio-mass straw burning gasification furnace structure.    ADVANTAGE - The structure realizes gasification furnace temperature regulating process and water amount regulating process so as to adjust inner cooling effect temperature with the gasification furnace, reduce production cost and improve production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a combustion energy-saving bio-mass straw burning gasification furnace structure.    Furnace body (1)    Guide pneumatic layer (2)    Water cooling layer (3)    Water regulating layer (4)
NOVELTY - Engine fuel composition comprises (in wt.%): methanol (50-60), ethanol (25 -35), dimethyl ether (8-12) and methyl tert-butyl ether (2-8).    USE - Engine fuel composition.    ADVANTAGE - The engine fuel composition is eco-friendly, cost-effective and economical.
NOVELTY - Producing natural gas involves mixing ethanol and methanol. Methanol and ethanol mixture is vaporized by heating. Acid catalyst is added to reactor. Mix gas vaporization is introduced to reactor, where the temperature is not less than 180 degrees C and pressure is not less than 0.15 megapascal. Space velocity is set to obtain methane gas.    USE - Method for producing natural gas (claimed).    ADVANTAGE - The method enables production of natural gas in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a methanol conversion device, which comprises metering pump, vaporizer, cooler and gas-liquid separator.
NOVELTY - Biomass granule fuel comprises bamboo material and non-bamboo material by biomass resources. Bamboo material is bamboo wood and non-bamboo material is obtained from organic waste.    USE - Biomass granule fuel.    ADVANTAGE - The biomass granule fuel is eco-friendly and economic and has high heat productivity and low ash content.
NOVELTY - Biofertilizer comprises 5-50 pts. wt. tea powder, 5-30 pts. wt. amino acid, 5-10 pts. wt. Cyrtomium fortunei, 5-20 pts. wt. konjak, 5-20 pts. wt. rhizoma kaempferiae, 5-10 pts. wt. nitrogen-phosphorus potassium fertilizer, and 50-100 pts. wt. water.    USE - As biofertilizer.    ADVANTAGE - The fertilizer is rich in selenium.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the biofertilizer, which involves (a) adding water to tea powder, fermenting at low temperature for 5-10 days, until the organic matter reaches low, (b) adding amino acid, mixing and fermenting at room temperature for 5-8 days, and (c) crushing C.fortunei konjak, rhizoma kaempferiae, and nitrogen-phosphorus potassium fertilizer into 500-1500 nm, and fermented mixture obtained in step (b), and stirring at high speed to obtain slurry, and storing the slurry in storage tank and fermenting for 2-15 days, until free of odor, and filtering using pressing filter, until the concentration reaches 50-65%.
NOVELTY - A Saccharomyces cerevisiae SC-X234 (CCTCC 2014005), is new.    USE - The S.cerevisiae SC-X234 is useful in production of fermentation ethanol (claimed) which is used as fuel.    ADVANTAGE - The S.cerevisiae SC-X234 gradually increase yeast tolerance in alcohol, produces ethanol to the yield of 15.75%, greatly increases fermentation yield and sugar alcohol conversion rate, and increases the ethanol yield to 126 g/l in 5 l fermentation tank, and has high economic value.
NOVELTY - A Bacillus licheniformis (CGMCC 6677), is new.    USE - The B.licheniformis is useful for controlling plant disease and promoting growth of plant, in method for preparing microbial inoculum (all claimed) which is used in production of tea and vegetable, and as pesticide and fertilizer.    ADVANTAGE - The B.licheniformis is obtained simply and cost-effectively and suitably used in large-scale industrial production, causes reduced pollution. The method prepares with increased yield, and improved quality of tea and vegetable, and is performed cost-effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing microbial inoculum of A B.licheniformis, which involves preprocessing sweet potato starch waste water, regulating pH using aqueous sodium hydroxide or lime water to 6.5-7.7 at 110-126 degrees C for 10-35 minutes, placing the liquid seed preparation in a triangular bottle, inoculating the B.licheniformis, culturing at 25-37 degrees C under the oscillation of 120-200 revolutions/minute (rpm) for 24-36 hours, performing liquid fermentation by inoculating the seed liquid in a volume ratio of seed liquid 2-15% in fermentation tank inoculation, culturing at 25-37 degrees C under sterile condition for 15-36 hours, where the cultured fermentation liquid contains viable count of more than 1x 109 colony forming unit (CFU)/g, and the obtained fermentation liquid is used as liquid microbial inoculum, sieving the biological carbon through 30 meshes sieve, and adding in fermentation liquid in a weight ratio of 1:1-1:5, mixing uniformly, drying until the water content reaches 30%, packing, and storing in shady and dry place to obtain solid inoculum.
NOVELTY - A Bacillus amyloliquefaciens with preservation number CGMCC NO. 6676 is new.    USE - A Bacillus amyloliquefaciens with preservation number CGMCC NO. 6676 for preparing microbial fertilizer (claimed).    ADVANTAGE - Microbial fertilizer promotes plant growth and prevents and treats plant disease, and production of microbial fertilizer is simple and low-cost and reduces pollution discharge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of microbial fertilizer which involves pretreating food waste by pulping kitchen waste in homogenizer, diluting with water to solid content of 10-60 g/L, adjusting pH to 6.8-7.7 using aqueous sodium hydroxide or lime water, and boiling for 10-35 minutes in microwave to sterilize, inoculating inclined-surface-preserved B. amyloliquefaciens in pretreated food waste, shaking culturing at 25-37 degrees C with shaking speed of 120-200 rpm for 24-36 hours to obtain liquid seed, inoculating in fermenter containing pretreated food waste with inoculation amount of 2-15 vol.%, culturing in sterile air at 25-37 degrees C for 15-36 hours to obtain fermentation culture liquid with viable count measured by flat plate bacterial count of greater than or equal to 2x 109 CFU/ml, mixing fermentation culture liquid:30 mesh bio-carbon with weight ratio of 1:1-1:3, ventilating and drying to moisture content of less than or equal to 25% to obtain solid microbial inoculum, preparing microbial fertilizer by mixing solid microbial inoculum:organic fertilizer with weight ratio of 1:1-1:5 and ventilating and drying to moisture content of less than or equal to 25% or by directly mixing fermentation culture medium:organic fertilizer with weight ratio of 1:2-1:10 and ventilating and drying to moisture content of less than or equal to 25%, packaging, and storing in cool and dry place in which bio-carbon is prepared by pyrolyzing biomass.
NOVELTY - Producing marsh gas involves mixing dry matter and kitchen garbage in mass ratio 3:1 in hydrolysis acidification device. Fermentation liquid is sprayed on mixed material to convert fermentation liquid into organic acid. Organic acid is dissolved into fermenting gas generating device to produce marsh gas. Remaining organic acid is circulated for hydrolysis acidification as liquid return in the device.    USE - Method for producing marsh gas.    ADVANTAGE - The method for producing marsh gas is suitable for rural areas.
NOVELTY - Preparing bisphenol comprises adding phenol, 9-fluorenone and cysteamine in a container, where the mol ratio of phenol and 9-fluorenone is 4-10:1, dropping concentrated sulfuric acid at less than 30 degrees C under stirring condition, finishing dropping at 50-60 degrees C, reacting and stirring for 3-12 hours, after completing the reaction, adding water (specific amount) neutralizing with liquid alkali, separating oil layer, recovering phenol under reduced pressure, and recrystallizing using mixed solvent of ethanol and water.    USE - The method is useful for preparing bisphenol (claimed).    ADVANTAGE - The method: has mild reaction, simple process; utilizes cysteamine, which is safe, odorless and tasteless; will not cause poisoning and air pollution; produces the product with good quality; has high yield and high economical efficiency; and is suitable for large-scale industrial production.
NOVELTY - This utility new type belongs to a one burning organic waste sewage of a coal gasification device, include organic waste sewage storage tank, oxygen storage tank, a dry coal powder storage tank and water storage tank, a dry coal powder storage tank and water storage tank is connected with the inlet of a water-coal-slurry storage tank, said organic waste sewage storage tank, oxygen storage tank, exit of dry coal powder storage tank and water-coal-slurry storage tank is connected with a burner part of burner is set on the top part of nozzle part and the membrane type water cooling wall is connected with oxygen storage tank through pipeline is set on the middle part of burner oxygen increasing pneuma nozzle is connected with a water storage tank and the membrane type water cooling wall is connected with the inlet of the bottom of burner is set with connecting cylinder, connecting cylinder passes through the top of water cooler, and is set on the inner upper part of water cooler, the water cooler of one side upper part set with synthetic pneuma exit, lower part of cooler set with a slag outlet, a connecting external barrel set with multi-layer baffle of gas ascending tube, a coal adaptability, coal gasification efficiency, large amount, pneuma clean and good mass and can treat sewage of organic waste.
NOVELTY - This utility new type relates to one to a main straw of multi-element material anaerobic dry fermentation system, comprise straw preprocessing integrated device, the fermentation library, regulating tank, a desulfurizing tank, a dehydration tank and gas storage film, straw preprocessing integrated device by the grinding part and part of connecting is composed of a straw preprocessing device integrated with the fermentation library between reseau conveyer belt through connecting, regulating pool through set with first pipeline and fermentation library of connected pump, the top part of the fermentation library set with elastic film, the bottom set with percolate storage tank, inlet of device for library set with inner spraying device, the spraying is set on inner percolate storage pool, fermenting library set with an air outlet, the air outlet through second pipeline in turn in series desulphurization tank, tank and gas storage film.
NOVELTY - Egg yolk lecithin powder production involves forming essence by processing Schizochytrium and algae at 25-30 degrees C, and adding culture agent to the essence. Fatty acid, carotene and fish oil are added to the essence. Deep-sea fish spine bone is crushed, and then sieved through 40 meshes sieve to obtain fish bone powder. The fish bone powder, essence, motherwort, herba epimedii and linseed oil are mixed to obtain a mixture.    USE - Method for producing egg yolk lecithin powder (claimed).    ADVANTAGE - The method enables producing egg yolk lecithin powder in a safe and eco-friendly manner, where the egg yolk lecithin powder has good mouth feel, is easy to digest and good for people, especially old people and pregnant women, and prevents pregnant women and infants from cardiovascular and cerebrovascular diseases.    DETAILED DESCRIPTION - Egg yolk lecithin powder production involves forming essence by processing Schizochytrium and algae at 25-30 degrees C, and adding culture agent to the essence. Fatty acid, carotene and fish oil are added to the essence. Deep-sea fish spine bone is crushed, and then sieved through 40 meshes sieve to obtain fish bone powder. The fish bone powder, essence, motherwort, herba epimedii and linseed oil are mixed to obtain a mixture. Soybean, lecithin and obtained mixture are homogenized in a high pressure homogenizer. Monoglyceride, protein, emulsifying agent and dextrin are added to the mixture. The mixture is dried to product. The obtained product is processed with docosahexaenoic acid to obtain the desired product.
NOVELTY - Preparation of anisaldehyde involves adding natural anethole, ethanol and water into a reactor, oxidizing, obtaining reaction product containing anisaldehyde, separating the obtained reaction product containing anisaldehyde, distilling the resultant upper layer liquid to obtain crude product of anisaldehyde (A), extracting the resultant lower layer liquid with ethyl acetate, obtaining extract, distilling the obtained extract, obtaining crude product of anisaldehyde (B), mixing the obtained crude product of anisaldehyde (A) and crude product of anisaldehyde (B) and rectifying.    USE - Preparation of anisaldehyde (claimed).    ADVANTAGE - The method environmentally-friendly provides anisaldehyde.    DETAILED DESCRIPTION - Preparation of anisaldehyde involves adding natural anethole, ethanol and water into a reactor, continuously introducing oxygen in rate of 0.1-0.3 m3/hour, oxidizing at 40-55 degrees C for 40-80 minutes, obtaining reaction product containing anisaldehyde, separating the obtained reaction product containing anisaldehyde, distilling the resultant upper layer liquid to obtain crude product of anisaldehyde (A), extracting the resultant lower layer liquid with ethyl acetate, obtaining extract, distilling the obtained extract, obtaining crude product of anisaldehyde (B), mixing the obtained crude product of anisaldehyde (A) and crude product of anisaldehyde (B), rectifying and obtaining anisaldehyde. The mass ratio of natural anethole, ethanol and water is 3:16-18:4-9.
NOVELTY - Preparation of Apigenin involves dissolving naringin in solvent (A), adding dehydrogenation reagent and additive, reacting, concentrating resultant reaction mixture under reduced pressure, adding purified water, stirring, filter-pressing, washing filter cake with purified water, obtaining crude product, drying, adding to purified reactor, adding solvent, dissolving by stirring, adding activated carbon, filtering, washing precipitate, dissolving in alkaline, filtering, adjusting pH, precipitating, filtering, washing, drying using dryer, crushing, packaging and storing.    USE - Preparation of Apigenin (claimed).    ADVANTAGE - The method efficiently enables preparation of Apigenin having high purity with high yield by economical and environmentally-friendly process in short period of time.
NOVELTY - The device has a circular sieve plate (2) whose periphery is provided with a toothed ring (4) and uniformly distributed with a mesh. A motor (1) is connected with a transmission gear (3) that is connected with a wheel tooth and the tooth ring. The tooth ring comprises a gear whistle.    USE - Combustion energy-saving furnace integrated biomass straw gasification stir device.    ADVANTAGE - The device is simple in structure, reasonable in design and convenient to use, solves combustion energy-saving furnace biomass straw gasification problems.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a combustion energy-saving furnace integrated biomass straw gasification stir device.    Motor (1)    Circular sieve plate (2)    Transmission gear (3)    Toothed ring (4)
NOVELTY - The furnace has a rocker handle (1) connected with a fixed block (2). The fixed block is connected with a stir paddle (3), where diameter of the fixed block is greater than that of the rocker handle and length of the stir paddle is 2.4m to 7.8m. The rocker handle is covered with heat insulating cotton (4).    USE - Straw gasification combustion furnace.    ADVANTAGE - The furnace has a coated grinding sand skid-proof jacket that is convenient to process stir operation, and increases safety of humanization production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a straw gasification combustion furnace.    Rocker handle (1)    Fixed block (2)    Stir paddle (3)    Heat insulating cotton (4)
NOVELTY - A Pseudomonas aeruginosa strain DSP-05 (CGMCC NO: 8390), is new.    USE - The P.aeruginosa strain DSP-05 is useful in preparation of immobilized beads for degradation of chlorpyrifos (all claimed) and treatment of wastewater.    ADVANTAGE - The strain is cost-effective, environmentally-friendly, convenient to use, easy to store, and suitable for industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing pellets, which involves (a) inoculating P.aeruginosa strain into lysogeny broth (LB) medium and culturing at 30 degrees C and 160 revolutions per minute (rpm) under shaking conditions, (b) centrifuging the culture broth in good condition at 8000 rpm for 2 minutes, discarding supernatant, adding sterile water, centrifuging at 8000 rpm for 2 minutes, and repeating steps to prepare bacteria liquid, (c) mixing 1 ml bacteria liquid and 20 ml 4% sodium alginate solution at room temperature, adding 3% calcium chloride into mixture, performing calcification for 6 hours, immobilizing mixture at 4 degrees C, washing immobilized beads using sterile water, and storing product at 4 degrees C.
NOVELTY - A Pseudomonas MC-05 (CGMCC NO: 8486) capable of degrading quinclorac, is new.    USE - The Pseudomonas MC-05 is useful for degrading quinclorac and treatment of quinclorac polluted soil (all claimed).    ADVANTAGE - The Pseudomonas MC-05 is environmentally-friendly and has good colonization ability of soil.
NOVELTY - A hydrogen-generating device has chemical tank and electrochemical pool which are set in anode chamber of electrochemical cell, ion exchange membrane in cathode chamber, and anode and cathode which are connected to resistor wire and are installed in anode and cathode chambers, respectively. Anode is prepared by performing energy efficient electro-oxidization, preparing cathode by using low hydrogen peroxide potential material, filling anode chamber with neutral or alkaline electrolyte solution and cathode chamber with neutral or acidic electrolyte solution, and catalyzing substrate.    USE - A hydrogen-generating device (claimed).    ADVANTAGE - The device can be operated even in the absence of direct current.    DETAILED DESCRIPTION - A hydrogen-generating device has chemical tank and electrochemical pool which are set in anode chamber of electrochemical cell, ion exchange membrane in cathode chamber, and anode and cathode which are connected to resistor wire and are installed in anode and cathode chambers, respectively. Anode is prepared by performing energy efficient electro-oxidization of catalyst and anode substrate, preparing cathode by using low hydrogen peroxide potential material, filling anode chamber with neutral or alkaline electrolyte solution and cathode chamber with neutral or acidic electrolyte solution, and catalyzing substrate using low temperature catalytic oxidation to produce hydrogen in cathode chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the hydrogen-generating device. (Drawing includes non-English language text).
NOVELTY - A one integrated sewage processing device, include anaerobic reaction pool, a membrane biotic reactor and disinfecting pool, anaerobic reaction tank one side set with water inlet, and the other side set with a membrane bio-reactor and water inlet of connecting water outlet, a membrane bio-reactor is sludge pump, connecting pipeline conveying through membrane bio-reactor inner residual sludge to the anaerobic reaction pool, a film biological reactor by water inlet connecting self-sucking pump, a self-priming pump exit connect disinfecting tank inlet, a disinfecting pool bottom part set with water outlet. This utility new type set with anaerobic reaction tank, the anaerobic biogas producing pneuma technology, of organic pollutant in the sewage into a use of marsh gas, makes full use of the available resource, increase resource utilization rate, using the membrane bio-reactor in of flat membrane component of high efficiency separation, the rear of the water treatment water quality stable, residual sludge yield, small floor area, is not limited by occasion. limit, a removing ammonia nitrogen and difficultly decomposed organic matter, operation management is convenient, it is easy to realize automatic control.
NOVELTY - Sealed discharging process is carried out by placing hollow horizontal channel between feed inlet and discharge port (201) in which horizontal channel is material block with reciprocating movement, sealing horizontal channel inner wall connected to discharge pulley with feed inlet (202) used when not discharging in which pulley faces away from discharge hole to direction of horizontal channel (203) which opens port and allows material to flow through horizontal channel during discharge, and pushing materials to discharge port or feed inlet using discharge pulley (204).    USE - Sealed discharging process for continuous feeding device (claimed) used for biomass carbonization furnace.    ADVANTAGE - The sealed discharging process has static and dynamic tight-sealing manner, excellent sealing effect, and improved efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of sealed discharging process for continuous feeding device.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart for sealed discharging process. (Drawing includes non-English language text).    Placing hollow horizontal channel between feed inlet and discharge port (201)    Sealing horizontal channel inner wall connected to discharge pulley with feed inlet (202)    Facing pulley away from discharge hole to direction of horizontal channel (203)    Pushing materials to discharge port or feed inlet using discharge pulley (204)
NOVELTY - Preparation of biodiesel involves adding sulfuric acid in grease soapstock, reacting by sedimentation trap, filtering, dehydrating to obtain acidification oil, adding acid oil, methanol and sulfuric acid, reacting, then adding methanol and alkaline substance to obtain crude fatty acid methyl ester, dealcoholizing, performing primary distillation to obtain 8C, 10C, 12C, 14C-based light component, carrying out secondary distillation to obtain 16C-based component, and subjecting tertiary distillation to obtain 18C fatty acid methyl ester and biological asphalt.    USE - Preparation of biodiesel used for paint, plastic and paving road surface.    DETAILED DESCRIPTION - Preparation of biodiesel involves adding 3-6 pts. wt. sulfuric acid in 100 pts. wt. grease soapstock, reacting by sedimentation trap, filtering, dehydrating to obtain acidification oil, adding 100 pts. wt. acid oil, 20-40 pts. wt. methanol and 1-3 pts. wt. sulfuric acid, reacting, removing unreacted acid of alcohol, then adding 5-25 pts. wt. methanol and 0.2-2 pts. wt. alkaline substance to obtain crude fatty acid methyl ester, dealcoholizing, removing methyl alcohol and fat deposition to obtain dimethyl ester, performing primary distillation to obtain 8C, 10C, 12C, 14C-based light component, carrying out secondary distillation to obtain 16C-based component, and subjecting tertiary distillation to obtain 18C fatty acid methyl ester and biological asphalt. The biodiesel is 18C fatty acid methyl ester-containing component. An INDEPENDENT CLAIM is included for biodiesel.
NOVELTY - The production device has a mixer (1) whose lower end is tapered and arranged with a heating coil (16) in cone-shaped bottom surface. An acid alcohol exit (14) is located in the bottom of mixer and connected with a conductivity meter (2). A conductivity meter (3) is located in the mixer and a valve is provided in one end of the acid alcohol exit and other end of the acid alcohol exit is connected with an alcohol esterification tank. An esterification liquid outlet (13) and an esterification liquid inlet (11) are provided in upper and lower portions of the mixer.    USE - Biodiesel production device.    ADVANTAGE - The speed of esterification process can be increased significantly and efficiency of acidification reaction can be improved so that layering effect of the production device can be ensured. Hence, continuous production of biodiesel can be realized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the biodiesel production device.    Mixer (1)    Conductivity meters (2,3)    Esterification liquid inlet (11)    Esterification liquid outlet (13)    Acid alcohol exit (14)    Heating coil (16)
NOVELTY - A combustion catalyst contains 18-30 wt.% solvent containing sodium hydroxide and/or potassium hydroxide, 8-18 wt.% hydrogen peroxide, 12-22 wt.% clinker inhibitor chosen from borax, boracalcite, colemanite and sodium borate, 9-19 wt.% stabilizer chosen from silicon oxide, sodium oxide and sodium silicate, and 22-40 wt.% water. The solvent contains 61-71 wt.% sodium hydroxide and 29-39 wt.% potassium hydroxide. The content of borax and sodium borate is 59-69 wt.% and 31-41 wt.%, respectively. The stabilizer contains 57-67 wt.% silica and sodium oxide.    USE - Combustion catalyst (claimed).    ADVANTAGE - The combustion catalyst has improved combustion efficiency with respect to fossil fuel. The growth of clinker is suppressed.
NOVELTY - The method involves increasing load amount generated in a fuel cell stack of a molten carbonate fuel cell system (MCFC) with certain amount. Enhanced load amount is maintained within preset time of 1-10 minutes. Air volume of the fuel cell stack is maintained at regular period. Predetermined amount of a load is 1-10 mili ampere/square-centimeter.    USE - MCFC driving method.    ADVANTAGE - The method enables reducing temperature deflection of the MCFC within a fuel cell. The method enables improving durability of the fuel cell stack. The method enables reducing long time driving case rate of failure occurrence so as to enhance endurance enhancement of the fuel cell stack, thus improving performance of the MCFC.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a MCFC driving method.'(Drawing includes non-English language text)'
NOVELTY - This utility new type relates to a one pig dung dirt anaerobic processing environment-friendly system, include pig, marsh gas pool, anaerobic oxidation tank, a sedimentation tank, a drain tank, said anaerobic oxidation tank is made of glass fibre reinforced plastic cylindrical seal box body, a box body part is equipped with pig manure and acid-forming bacteria and methane producing bacteria. This utility new type building is convenient, the cost is low, the anaerobic treatment of effect is better, the generated marsh gas.
NOVELTY - The device has a synthetic gas capture tank (10) fixed with a pyrolysis gas generator (2). An oxygen tank (40) and a hydrogen tank (42) are connected to an exit of a reformer (6). The reformer allows synthetic gas to pass through the hydrogen tank. The pyrolysis gas generator is connected with the oxygen tank and the hydrogen tank. Gas emitted from a reforming furnace torch (14) is moved along horizontal direction. A reforming furnace cask (12) is horizontally installed in the reformer. A heat insulator is installed in an outer side of the reforming furnace cask.    USE - Horizontal form reformer device for biomass waste matter of synthesis gas.    ADVANTAGE - The device improves synthetic gas production efficiency of the reformer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a horizontal form reformer device.'(Drawing includes non-English language text)'    Pyrolysis gas generator (2)    Reformer (6)    Synthetic gas capture tank (10)    Reforming furnace cask (12)    Reforming furnace torch (14)    Oxygen tank (40)    Hydrogen tank (42)
NOVELTY - Device for compacting waste put into an extrusion cylinder of an apparatus for manufacturing a combustible waste fuel rod, comprises connecting rod, crankshaft, first supporting bar, third roller, cam groove and compacting bars, where a connecting rod (19) moves vertically according to the rotation of a crankshaft (20), a first supporting bar (15) accordingly moves vertically, and third roller (10) inserted in a cam groove (6) moves accordingly counterclockwise along the cam groove (6).    USE - The device is useful for compacting waste put into extrusion cylinder of apparatus for manufacturing combustible waste fuel rod.    DETAILED DESCRIPTION - Device for compacting waste put into an extrusion cylinder of an apparatus for manufacturing a combustible waste fuel rod, comprises connecting rod, crankshaft, first supporting bar, third roller, cam groove and compacting bars, where a connecting rod (19) moves vertically according to the rotation of a crankshaft (20), a first supporting bar (15) accordingly moves vertically, a third roller (10) inserted in a cam groove (6) moves accordingly counterclockwise along the cam groove (6), and thus waste compacting bars (11) are repeatedly inserted downwards into and withdrawn upwards from a vertical groove formed at the erected extrusion cylinder so as to compact the waste, which is put into the erected extrusion cylinder, at high speed.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of device.    Cam groove (6)    Third roller (10)    Waste compacting bars (11)    First supporting bar (15)    Connecting rod (19)    Crankshaft (20)
NOVELTY - The device (1) has a reactor cavity (2) that surrounds a reactor vessel (3). A filler sheath (4) is arranged for feeding biomass i.e. wood such as hogged wood, to the reactor cavity. A gas outlet (5) is arranged for discharging gas produced from the combustible biomass from the reactor cavity. A feed device (8) comprises a set of outlet openings (9) for outputting a gasifying agent into the reactor cavity. The set of outlet openings of the feed device is movable in a transverse direction i.e. preferably orthogonal, to a transport direction (7).    USE - Gasifier device i.e. wood gasifier, for recovery of combustible gas, from biomass i.e. wood such as hogged wood, timber chips and pellets, utilized as a fuel for a combustion engine.    ADVANTAGE - The set of outlet openings of the feed device is movable in the transverse direction i.e. preferably orthogonal, to the transport direction, thus allowing suction of the gas from the cavity during recovery of the gas to be performed in a continuous or intermittent and/or gradual manner, while avoiding hotspots and slagging in the oxidation zone and/or in the reactor cavity during the gasification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of a gasifier device.    Gasifier device (1)    Reactor cavity (2)    Reactor vessel (3)    Filler sheath (4)    Gas outlet (5)    Transport direction (7)    Feed device (8)    Outlet openings (9)
NOVELTY - Method of hydrolyzing cellulose containing biomass involves adding enzyme (a) or enzyme (a) composition to liquefy at least portion of solids present in the biomass and to maintain viscosity of the cellulose containing biomass to less than 1000 cP, preferably less than 800 cP, more preferably less than 600 component, and then adding enzyme composition (b) to form oligomeric and/or monomeric sugars. The enzyme (a) or enzyme composition (a) is different from enzyme composition (b). The enzyme (a) or enzyme (a) composition comprises endoglucanase.    USE - Method of hydrolyzing cellulose containing biomass used for forming biofuel e.g. bio-ethanol.    ADVANTAGE - The method is carried out economically using simple process.    DETAILED DESCRIPTION - Method of hydrolyzing cellulose containing biomass involves adding enzyme (a) or enzyme (a) composition to liquefy at least portion of solids present in the biomass and to maintain viscosity of the cellulose containing biomass to less than 1000 cP, preferably less than 800 cP, more preferably less than 600 component, and then adding enzyme composition (b) to form oligomeric and/or monomeric sugars. The enzyme (a) or enzyme composition (a) is different from enzyme composition (b). The enzyme (a) or enzyme (a) composition comprises endoglucanase. The enzyme (b) composition comprises cellulose. The enzyme (a) or enzyme (a) composition comprises more endogluconase than the enzyme (b) composition (in protein wt%).
NOVELTY - A novel lactic acid bacteria high temperature tolerance which does not become extinct in at least 60 degrees C, is new.    USE - The novel lactic acid bacteria is useful for composting organic substance which is useful in food processing (all claimed).    ADVANTAGE - The novel lactic acid bacteria has high temperature tolerance which does not become extinct in at least 60 degrees C, increased immunity with respect to the existing pathogenic microbe, reduces risk of food contamination, and rapidly decomposes waste materials as compared to existing lactic acid bacteria.
NOVELTY - Converting a lignin biomass feedstream to a converted lignin stream, comprises: combining the lignin biomass feedstream comprising lignin and at least a first solvent with a first catalyst (625) in a reaction vessel, where a mole ratio of the first catalyst to the lignin is 4:1-15:1; and deoxygenating the lignin biomass feedstream to a converted lignin stream at a deoxygenation temperature and a deoxygenation pressure for a deoxygenation time.    USE - The process is useful for converting a lignin biomass feedstream to a converted lignin stream (claimed), which is useful for producing phenolic compounds, jet fuel, or oils for making a polyester bottle, container, soft drink bottles, beer bottles, films, trays, preforms or jars.    ADVANTAGE - The process: provides high yield conversion of lignin; is cost effective and environmentally friendly; does not require surfactants or emulsifying agents; reduces the amount and cost of water treatment; saves the time and energy; provides slurry tank volume reduction; avoids the formation of char; and facilitates the recycling of the catalyst.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a continuous stir tank reactor for the lignin conversion process.    Ebullating bed reactor (500)    Dip tube (610)    Dip tube major length (612)    First catalyst (625)    Back pressure regulator (700)
NOVELTY - A wheat dietary beta -glucanase containing enzyme contains 100-140 pts. wt. xylanase, 8-12 pts. wt. cellulase, 15-20 pts. wt. beta-glucanase, 6-10 pts. wt. medium temperature alpha-amylase, and 0.5-2 pts. wt. traditional Chinese medicine obtained from fermentation of Bacillus licheniformis strain beta -10-25 with preservation number CCTCC No. M2013538.    USE - Wheat dietary beta -glucanase containing enzyme for animal feed (claimed).    ADVANTAGE - The wheat dietary beta -glucanase containing enzyme is suitable for high temperature, liquefaction, and saccharification processes, improves feed conversion rate, reduces feed cost, improves livestock immunity and disease prevention, improves feeding efficiency, promotes digestion and nutrient absorption, and has high activity, broad optical pH range, and high heat stability and storage stability.
NOVELTY - A fuel composition comprises residue obtained by separating process liquid into residue and liquid by solid-liquid separation after saccharifying and fermenting lignocellulosic raw material.    USE - A fuel composition (claimed).    ADVANTAGE - The fuel composition has high heating value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing method of fuel composition which involves recovering residue obtained by separating process liquid into residue and liquid by solid-liquid separation after saccharifying and fermenting lignocellulosic raw material.
NOVELTY - The generator has a combustion furnace (10) which generates hot combustion gas. A gasifier (20) separates organic substance into pyrolysis gas and carbonized material by indirect heating. A curing chamber (30) removes the coal tar fractions from the pyrolysis gas. The pyrolysis gas of the curing chamber interior is indirectly heated with the combustion gas. The organic substance is heated with the combustion gas after thermally radiating with respect to the pyrolysis gas, and is guided to the gasifier.    USE - Generator for generating fuel gas from organic substance such as wood chips, agricultural residue and foodstuff residue.    ADVANTAGE - Size reduction of the fuel gas generator can be achieved. The efficiency of the fuel gas generator can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel gas generator.    Combustion furnace (10)    Gasifier (20)    Branch pipe (23)    Curing chamber (30)    Scrambler (50)
NOVELTY - The method involve heating and gasifying organic raw material such as biomass on fire grate (12) with combustion gas generated by burning an organic substance fuel. The size of the gap is changed by required frequency, while burning the organic substance fuel on fire grate.    USE - Manufacturing method of product gas used as source gas for chemo-synthesizing gas fuel, methanol, gas to liquid fuel / petroleum equivalent fuel for electric power generation.    ADVANTAGE - The smooth supply of combustion gas is achieved, so that thermal efficiency in manufacture of product gas is improved. The generation of obstruction in the fire grate by clinker is eliminated, when burning organic substance fuel on fire grate. The stable operation of long time of high temperature combustion gas generator is enabled.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) high temperature combustion gas generator; and    (2) manufacturing apparatus of product gas.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the high temperature combustion gas generator. (Drawing includes non-English language text)    Organic substance fuel supply apparatus (10)    Fire grate (12)    Air intake (14)    High temperature combustion gas generator (101)    High temperature combustion gas exhaust pipe (109)
NOVELTY - Synthesizing vitamin E acetate comprises reacting 2,3,5-trimethylhydroquinone with isophytol in presence of a catalyst composed of straight-chain organic amine, zinc halide and hydrogen halide, to obtain tocopherol, and esterifying the resultant tocopherol with acetic anhydride.    USE - The method is useful for synthesizing vitamin E acetate.    ADVANTAGE - The method: is simple and adopts mild reaction conditions; reutilizes the catalyst; and produces less by-products and higher purity product yield.
NOVELTY - A biochar-based soil modifier contains biomass carbon which is obtained by performing thermal cracking carbonization to biomass carbon raw material under oxygen-limited condition.    USE - A biochar-based soil modifier used for improving albic soil (claimed).    ADVANTAGE - Biochar-based soil modifier is environment-friendly and low in cost, has wide raw material source and good light absorption heating resistance, reduces emission and occurrence of haze and other greenhouse gas, reduces carbon dioxide concentration in atmosphere, improves soil ventilation and water holding capacity, reduces leaching loss, prolongs effect, and improves utilization ratio of fertilizer, increases water and air permeability of soil, reduces soil bulk density, increases soil microorganism living environment and quantity, relieves acidification, and improves albic layer chemical properties.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of a biochar-based soil modifier albic soil physical and chemical properties change pattern. (Drawing includes non-English language text).
NOVELTY - Introducing recombinant DNA constructs into at least one bacterium, is claimed.    USE - The method is useful for introducing recombinant DNA constructs into bacterium where the bacterium is a gram-positive bacteria belonging to the genus Clostridium including Clostridium pasteurianum (claimed) which is useful for producing biofuel and biochemical n-butanol.    ADVANTAGE - The method provides high-efficiency genetic transformation of anaerobic bacterium including Clostridium pasteurianum.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a bacterial cell which contains at least one recombinant DNA construct
NOVELTY - A dust collector is connected with pellet discharge amount control outlet to collect foreign substance burying in pellet. The dust exhaust pipe is installed between lower portion of chill tank (10) and upper side of exhaust hopper (30) for discharging dust, so that pellet detection sensors senses load of pellet put into inside. A fixed frame (40) is installed in lower portion of chill tank and pellet dropped in lower end portion is ejected to exhaust hopper. Bottom plate (20) is installed at inner side at constant interval so that pellet loaded in inside is evenly ejected.    USE - Cooling apparatus of pellet such as timber pellet.    ADVANTAGE - The dusts burying in the pellet is removed efficiently and the cooling efficiency of the pellet is enhanced. The extrusion collar is formed in the dust exhaust pipe inner periphery of the chill tank and the flow of the air ejected in the chill tank is rapidly performed, so the exhaustion of the foreign substance and dust is enhanced. The power required in the operation of the blocking plate is minimized and the modulation of the discharging oil standing according to the size of the pellet is facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the pellet cooling apparatus.    Chill tank (10)    Bottom plate (20)    Exhaust hopper (30)    Fixed frame (40)    Pellet discharge control unit (50)
NOVELTY - A waste gas containing ammonia, hydrogen and nitrogen is discharged from manufacturing process of gallium-nitride-based compound semiconductor by heat pump using pressurizing process and cooling process. The ammonia in the waste gas is liquefied and recovered from waste gas. The hydrogen is recovered from waste gas containing hydrogen and nitrogen by pressure-swing-adsoprtion process.    USE - Collection method of ammonia and hydrogen used for manufacture of gallium-nitride-based compound semiconductor for light-emitting diode and laser diode.    ADVANTAGE - The method enables efficient collection and recovery of ammonia and hydrogen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for recycling method of ammonia and hydrogen, which involves supplying ammonia and hydrogen recovered to the manufacturing process of the gallium-nitride-based compound semiconductor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of apparatus for collection and recovery of ammonia and hydrogen.    Supply source of organometallic compound (1)    Supply source of nitrogen (2)    Supply source of hydrogen (3)    Supply source of ammonia (4)    Hydrogen purification apparatus (7)
NOVELTY - The recovery device comprises a first membrane (6) horizontally covering entire surface of a charged liquid effluent (3), a second membrane (7) vertically disposed around the first membrane, and a unit for discharging biogas and rainwater. The second membrane includes a lower part and an upper part disposed on one side of the first membrane. The device further comprises a guide unit provided with rings vertically arranged in pairs on the second membrane cooperating with wire ropes arranged on a vertical wall of a storage facility, and floatation elements.    USE - The recovery device is useful for separating biogas and rainwater in a storage facility for a charged liquid effluent such as manure (claimed).    ADVANTAGE - The recovery device economically and rapidly separates the biogas and the rainwater with reduced emissions of greenhouse gases and odor, and provides highly qualified water.    DETAILED DESCRIPTION - The recovery device comprises a first membrane (6) horizontally covering entire surface of a charged liquid effluent (3), a second membrane (7) vertically disposed around the first membrane, and a unit for discharging biogas and rainwater. The second membrane includes a lower part and an upper part disposed on one side of the first membrane. The device further comprises a guide unit provided with rings vertically arranged in pairs on the second membrane cooperating with wire ropes arranged on a vertical wall of a storage facility, floatation elements, which are fixed to the lower part of the second membrane, and sinkers located at a variable distance from the floatation elements. The sinkers are fixed with the floatation elements. The pair of rings is secured to the flotation element.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic vertical sectional view of a recovery device.    Charged liquid effluent (3)    First membrane (6)    Second membrane (7)    Floatation elements (8)    Rings. (10)
NOVELTY - Activating charcoal resulting from gasification, involves gasifying dried biomass material in a gasification reactor of an integrated biomass gasification system to produce charcoal, and activating the charcoal using heat generated from an integral heat source of the integrated biomass gasification system.    USE - For activating charcoal resulting from gasification (claimed) which is used in many industries, such as, for decolorization purposes, purification of air and gases, adsorption of vapors, and/or purification of water.    ADVANTAGE - The method provides activation of charcoal resulting from biomass gasification in a more efficient, economical manner, to increase the value of biomass gasification with minimal investment in the process; and provides activation of charcoal without using an external heat source.    DETAILED DESCRIPTION - Activating charcoal resulting from gasification, either involves method (M1): gasifying dried biomass material in a gasification reactor of an integrated biomass gasification system to produce charcoal, and activating the charcoal using heat generated from an integral heat source of the integrated biomass gasification system; or method (M2): gasifying dried biomass material in a gasification reactor of an integrated biomass gasification system to produce a stream of charcoal and producer gas; separating the charcoal from the producer gas of the stream using a hot screw conveyor; and activating the charcoal using heat generated from an integral heat source of the integrated biomass gasification system.
NOVELTY - The bioreactor has a mobile fermentation pouch for processing biomass and provided with gas-tight doors. An inner side of a septic tank is equipped with a metal coat. Separate radiators and upper parts of the septic tank are provided with nozzles for spraying slurry, which are part of an integral closed system. The closed system is equipped with a tank and installed in an area of a space technology. A waste pipe from a pump is connected with the septic tank to drain excess percolate. Sensors are located inside the septic tank. A control unit controls monitoring parameters of fermentation.    USE - Dry fermentation anaerobic bioreactor.
NOVELTY - The method involves arranging a floor unit with a tube that is placed in a compost pile. A control pump is connected with another tube and a solar collector. A solenoid valve is arranged between the tubes. The control pump and a temperature sensor are arranged on the compost pile.    USE - Method for installing heating pile during composting process.
NOVELTY - A biological active organic fertilizer comprises 40-60 pts. wt. livestock and poultry solid waste, 5-15 pts. wt. urea, 5-20 pts. wt. monoammonium phosphate, 4-15 pts. wt. potassium chloride, 2-5 pts. wt. trace element, 1-3 pts. wt. oxidizing agent, 2-5 pts. wt. bioactive agent, and 5-15 pts. wt. adhesive.    USE - Biological active organic fertilizer.    ADVANTAGE - The fertilizer contains variety of bioactive substances, soluble organic acids, nitrogen, phosphorus, potassium, iron, zinc, magnesium, molybdenum, and boron trace elements needed for crops growth, and has high efficiency and low cost.    DETAILED DESCRIPTION - A biological active organic fertilizer comprises 40-60 pts. wt. livestock and poultry solid waste, 5-15 pts. wt. urea, 5-20 pts. wt. monoammonium phosphate, 4-15 pts. wt. potassium chloride, 2-5 pts. wt. trace element, 1-3 pts. wt. oxidizing agent, 2-5 pts. wt. bioactive agent, and 5-15 pts. wt. adhesive. The livestock and poultry solid waste has 55-98 wt.% organic matter content and 50-60 wt.% water content. The oxidizing agent comprises sodium perborate and tetraacetylethylenediamine at weight ratio of 1:0.1-0.3. The bioactive agent is phytase or cellulase; Trichoderma harzianum or Trichoderma koningii; and Bacillus subtilis, Bacillus or Bacillus licheniformis at mass ratio of 1:(0.4-0.6):(0.2-0.4). The adhesive is calcium sulfate, precipitated calcium carbonate, and/or magnesium oxide. The fertilizer is prepared by mixing livestock and poultry solid waste and oxidizing agent, expanding through saturated steam at 1.42-1.73 MPa, adding bioactive agent, mixing, fermenting, adding urea, monoammonium phosphate, potassium chloride, trace element and adhesive, and uniformly mixing.
NOVELTY - Preparation of amino acid oil surfactant comprises heating acid and amino acid salt, adding catalyst, reacting at 130-190 degrees C for 2-8 hours, cooling at 60-90 degrees C, and adding neutralizer to pH of 7-8.    USE - Method for preparing amino acid oil surfactant (claimed).    ADVANTAGE - The simple and eco-friendly method ensures high product yield and high product purity.
NOVELTY - A Nannochloropsis strain ENN11-2 with preservation number CGMCC No. 6009 is new.    USE - New Nannochloropsis strain for food, animal feed, biofuel, nitrogen-phosphorus sewage, carbon dioxide emission reduction, and preparing medicine or health products for preventing and treating cardiovascular and cerebrovascular diseases (all claimed).    ADVANTAGE - The strain has improved growth rate and EPA content, stable performance, good environmental adaptability, and high resistance to pests and diseases.    DESCRIPTION OF DRAWING(S) - The drawing shows a variation curve of indoor plate reactor evaluation of dry strain. (Drawing includes non-English language text).
NOVELTY - Fermented composite fertilizer comprises 40-44 pts. wt. urea, 34-38 pts. wt. diammonium phosphate, 20-23 pts. wt. potassium sulfate, 2-3 pts. wt. calcium chloride, 10-12 pts. wt. peat, 2-3 pts. wt. citric acid, 30-34 pts. wt. thunder god vine, 3-4 pts. wt. carboxymethyl cellulose, 3-4 pts. wt. effective microorganisms (EM) microbial inoculum, and 4-6 pts. wt. coating agent. The coating agent comprises paraffin, KH-570 (RTM: gamma -methacryloyloxypropyltrimethoxysilane), nanocarbon, jade powder, and polyoxyethylene sorbitan monooleate.    USE - Fermented composite fertilizer used for grapes (claimed).    ADVANTAGE - The composite fertilizer has balanced nutrition and good soil protection effect, and improves yield and quality of grapes.    DETAILED DESCRIPTION - Fermented composite fertilizer comprises 40-44 pts. wt. urea, 34-38 pts. wt. diammonium phosphate, 20-23 pts. wt. potassium sulfate, 2-3 pts. wt. calcium chloride, 10-12 pts. wt. peat, 2-3 pts. wt. citric acid, 30-34 pts. wt. thunder god vine, 3-4 pts. wt. carboxymethyl cellulose, 3-4 pts. wt. EM microbial inoculum, and 4-6 pts. wt. coating agent. The coating agent comprises 20-22 pts. wt. paraffin, 2-3 pts. wt. KH-570 (RTM: gamma -methacryloyloxypropyltrimethoxysilane), 0.1-0.2 pt. wt. nanocarbon, 2-3 pts. wt. jade powder, and 2-3 pts. wt. polyoxyethylene sorbitan monooleate. The composite fertilizer is prepared by mixing raw materials, grinding, and uniformly dispersing. An INDEPENDENT CLAIM is included for composite fertilizer preparation by crushing thunder god vine; mixing peat and thunder god vine powder, adding EM microbial inoculum and water, uniformly stirring, stacking, and fermenting for 6-8 days, while turning once every 2-3 days until material is completely decomposed; uniformly mixing other raw materials excluding coating agent with fermented material; and heating obtained mixture to 80-90 degrees C, adding coating agent, uniformly stirring, and granulating.
NOVELTY - Producing a high-carbon number saturated hydrocarbon using a biomass involves introducing a mixed biomass solution containing benzyl phenyl ether to a reactor and further introducing an acid catalyst or difunctional catalyst to the reactor to carry out isomerization of the mixed biomass solution; and carrying out hydrodeoxygenation by introducing an acid catalyst or difunctional catalyst to the reactor together with hydrogen, after the isomerization, to induce hydrodeoxygenation of intermediate products obtained from the isomerization.    USE - For producing a high-carbon number saturated hydrocarbon (claimed), used as fuel e.g. diesel for vehicles.    ADVANTAGE - The method allows production of a high-carbon number saturated hydrocarbon with high efficiency.
NOVELTY - Water-soluble liquid fertilizer comprises Bacillus subtilis, Paenibacillus polymyxa, Bacillus thuringiensis, Bacillus licheniformis, Bacillus azotoformans, Paenibacillus durum, Bacillus megaterium, Bacillus coagulans, Bacillus pumilus or Trichoderma harzianum strain including 12-27 wt.% humic natural complex, 4-5 wt.% additive and 68-85 wt.% water.    USE - The fertilizer is useful for promoting seed crop germination.    ADVANTAGE - The fertilizer increases yield and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the water-soluble liquid fertilizer, comprising (a) dissolving humic natural complex and strong base at 20-50 degrees C for 20-40 minutes, (b) removing humus from the obtained humic complex solution by filtering, (c) adding the filtered humic complex solution into water, and (d) adding the filtered humic complex solution into the additive including thickener, molasses and antifreeze.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flow chart of the method for producing water-soluble liquid fertilizer (Drawing includes non-English language text).
NOVELTY - Hexanethiol, benzaldehyde, and a polar organic solvent are mixed and heat-reacted in the presence of an alkali catalyst under protection of dry air or inert gas, at 70-120 degrees C for 10-24 hours, with stirring. The molar ratio of hexanethiol and benzaldehyde is (1.2-1.4):1. After reaction completion, water is added to quench the reaction, organic solvent and residual oil are removed, and recrystallization is carried out at room temperature using a solvent. The solid is separated at -10 degrees C to -30 degrees C, filtered, and dried to obtain hexylthio-benzaldehyde.    USE - Preparation of hexylthio-benzaldehyde (claimed).    ADVANTAGE - The method enables easy, environmentally-friendly and economical preparation of hexylthio-benzaldehyde with low device requirement, and high product purity and yield.
NOVELTY - Recovering L-cis-diltiazem involves utilizing L-cis-lactam as raw material, 2-iodoxybenzoic acid as oxidizing agent and dimethyl sulfoxide as solvent, where water content is of dimethyl sulfoxide is 5-15%, and then thin layer chromatography is performed to detect raw material. Raw materials are mixed with continuous stirring for 1 hour, and then filtered to collect filter cake, which is washed using ethyl acetate, and then dried to obtain product. The obtained product is concentrated to obtain 1,5-benzothiazepine-3,4(2H,5H)-dione and recovered product.    USE - Method for recovering L-cis-diltiazem (claimed).    ADVANTAGE - The method enables to recover L-cis-diltiazem in simple and eco-friendly manner with high yield (more than 90%).
NOVELTY - An environment-friendly fermented compound fertilizer comprises 30-34 pts. wt. urea, 30-34 pts. wt. calcium superphosphate, 10-12 pts. wt. potassium chloride, 2-3 pts. wt. sodium selenite, 10-12 pts. wt. humic acid, 1-2 pts. wt. silica sol, 2-3 pts. wt. magnesium sulfate, 100-120 pts. wt. livestock and poultry manure, 40-45 pts. wt. sawdust, 3-4 pts. wt. Effective Microorganism agent, and 4-6 pts. wt. coating agent.    USE - Environment-friendly fermented compound fertilizer.    ADVANTAGE - The fertilizer stimulates growth of crops, improves product mass, high yield and high efficiency, and reduces damage degree of soil.    DETAILED DESCRIPTION - An environment-friendly fermented compound fertilizer comprises 30-34 pts. wt. urea, 30-34 pts. wt. calcium superphosphate, 10-12 pts. wt. potassium chloride, 2-3 pts. wt. sodium selenite, 10-12 pts. wt. humic acid, 1-2 pts. wt. silica sol, 2-3 pts. wt. magnesium sulfate, 100-120 pts. wt. livestock and poultry manure, 40-45 pts. wt. sawdust, 3-4 pts. wt. Effective Microorganism agent, and 4-6 pts. wt. coating agent. Coating agent includes 30-35 pts. wt. hydroxyethyl methacrylate, 10-15 pts. wt. trimethylol propane triacrylate, 2-3 pts. wt. silane coupling agent KH-570, 1-2 pts. wt. nanocarbon, and 2-3 pts. wt. jade powder. An INDEPENDENT CLAIM is included for preparation of environment-friendly fermented compound fertilizer comprising mixing livestock and poultry manure, sawdust, Effective Microorganism microbial inoculum and water, stirring uniformly, stacking, fermenting for 6-8 days, turning over for each 2-3 days, completely decomposing, heating at 80-90 degrees C, adding coating agent, stirring uniformly, and granulating.
NOVELTY - A supported metal catalyst is prepared by using carbon material as carrier, ruthenium, palladium, platinum, iron, cobalt, rhodium, rhenium, iridium, and/or nickel as active metal component in which loading amount of active metal component in carbon material carrier is 0.5-20 wt.%, mechanically mixing active metal component precursor and carbon material powder to obtain catalyst precursor powder in which mechanical mixing includes ball milling, grinding, manual mixing, or pneumatic mixing, tabletting by tablet press, crushing to obtain catalyst precursor particles, and reducing.    USE - Preparation of supported metal catalyst for ammonia synthesis, ammonia decomposition, and catalytic hydrogenation.    ADVANTAGE - Process is simple, solvent-free, and environment-friendly, and has short production period, high production efficiency, and low energy consumption. Catalyst has high dispersion degree and improved usage rate.
NOVELTY - Compost comprises sawdust, chicken manure, and Agaricus bisporus.    USE - The compost is useful in cultivation of crop such as Chinese cabbage (all claimed).    ADVANTAGE - The produced compost: has high organic, inorganic and nitrogen contents, so that the cultivation of crops can be promoted; and can be inexpensively prepared with high quality and yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparing compost comprising mixing sawdust, chicken manure and Agaricus bisporus in a volume ratio of 2.5-3.5:8-10:0.8-1.2 and then placing in a culture medium, and controlling the moisture content of the mixture for 1-3 times for 2-3 weeks; and (2) cultivating Chinese cabbage comprising adding 1800-2200 kg of the compost and then rearing the Chinese cabbage.
NOVELTY - Organic liquid fertilizer comprises 45-55 wt.% chicken manure, 22.5-27.5 wt.% rice bran and 22.5-27.5 wt.% soybean meal, which are mixed, diluted with water (four times), and fermented anaerobically for 40-60 days by avoiding direct sunlight.    USE - The liquid fertilizer is useful for cultivating red pepper using agricultural by-products (claimed).    ADVANTAGE - The liquid fertilizer is safe and environmentally friendly, improves chemical resistance, cation exchange capacity of soil and yield of red peppers, and lowers electrical conductivity of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing organic liquid fertilizer, comprising mixing chicken manure, rice bran and soybean meal, diluting with water (four times), anaerobically fermenting for 40-60 days by avoiding direct sunlight to prepare liquid fertilizer, and applying on red peppers in greenhouses by diluting with water (7-15 times).
NOVELTY - A cellulase gene cel-KG11 isolated from rumen microorganism of Capra aegagrus hircus, is new. The gene has a 3186 base pair sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The cellulase cel-KG11 gene is useful for producing cellulase used in feed additive and detergent composition, and for producing biofuel (all claimed). The cellulase is also useful in fabric softener.    ADVANTAGE - The cellulase encoded by the gene enables to produce inexpensive feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cellulase protein encoded by the above gene and having a 1061 amino acid sequence (SEQ ID NO: 2) fully defined in the specification and comprising carbohydrate-binding module 11 (CBM11) domain;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector; and    (4) method of producing biofuel involves contacting biomass with the cellulase protein and hydrolyzing the biomass.
NOVELTY - A cellulase gene cel-KG26 isolated from rumen microorganism of Capra aegagrus hircus, is new. The gene has a 1365 base pair sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The cellulase cel-KG26 gene is useful for producing cellulase used in feed additive and detergent composition, and for producing biofuel (all claimed). The cellulase is also useful in fabric softener.    ADVANTAGE - The cellulase encoded by the gene enables to produce inexpensive feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cellulase protein encoded by the above gene and having a 454 amino acid sequence (SEQ ID NO: 2) fully defined in the specification and comprising glycoside hydrolase 2C (GH2C) domain;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector; and    (4) method of producing biofuel involves contacting biomass with the cellulase protein and hydrolyzing the biomass.
NOVELTY - A cellulase gene cel-KG27 isolated from rumen microorganism of Capra aegagrus hircus, is new. The gene has a 384 base pair sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The cellulase cel-KG27 gene is useful for producing cellulase used in feed additive and detergent composition, and for producing biofuel (all claimed). The cellulase is also useful in fabric softener.    ADVANTAGE - The cellulase encoded by the gene enables to produce inexpensive feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cellulase protein encoded by the above gene and having a 127 amino acid sequence (SEQ ID NO: 2) fully defined in the specification and comprising glycoside hydrolase 4C (GH4C) domain;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector; and    (4) method of producing biofuel involves contacting biomass with the cellulase protein and hydrolyzing the biomass.
NOVELTY - A cellulase gene cel-KG33 isolated from rumen microorganism of Capra aegagrus hircus, is new. The gene has a 1566 base pair sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The cellulase cel-KG33 gene is useful for producing cellulase used in feed additive and detergent composition, and for producing biofuel (all claimed). The cellulase is also useful in fabric softener.    ADVANTAGE - The cellulase encoded by the gene enables to produce inexpensive feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cellulase protein encoded by the above gene and having a 521 amino acid sequence (SEQ ID NO: 2) fully defined in the specification and comprising glycoside hydrolase 2C (GH2C) domain;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector; and    (4) method of producing biofuel involves contacting biomass with the cellulase protein and hydrolyzing the biomass.
NOVELTY - A cellulase gene cel-KG43 isolated from rumen microorganism of Capra aegagrus hircus, is new. The gene has a 2694 base pair sequence (SEQ ID NO: 1) fully defined in the specification.    USE - The cellulase cel-KG43 gene is useful for producing cellulase used in feed additive and detergent composition, and for producing biofuel (all claimed). The cellulase is also useful in fabric softener.    ADVANTAGE - The cellulase encoded by the gene enables to produce inexpensive feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cellulase protein encoded by the above gene and having a 897 amino acid sequence (SEQ ID NO: 2) fully defined in the specification and comprising glycoside hydrolase 2C (GH2C) domain;    (2) recombinant vector comprising the gene;    (3) host cell transformed with the recombinant vector; and    (4) method of producing biofuel involves contacting biomass with the cellulase protein and hydrolyzing the biomass.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG55 gene derived from rumen microorganism of Capra aegagrus hircus comprising a 1161 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG55 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enable cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) GH2C domain cellulase protein derived from rumen microorganism of C.aegagrus hircus comprising a 386 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity comprising the above-mentioned cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing to obtain product.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG21 gene derived from rumen microorganism of Capra aegagrus hircus comprising a 1206 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG21 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enable cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) GH2C domain cellulase protein derived from rumen microorganism of C.aegagrus hircus comprising a 401 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity comprising the above-mentioned cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing to obtain product.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG25 gene derived from rumen microorganism of Capra aegagrus hircus comprising a 642 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG25 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enable cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) GH3 domain cellulase protein derived from rumen microorganism of C.aegagrus hircus comprising a 213 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity comprising the above-mentioned cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing to obtain product.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG36 gene derived from rumen microorganism of Capra aegagrus hircus comprising a 909 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG36 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enable cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) GH45 domain cellulase protein derived from rumen microorganism of C.aegagrus hircus comprising a 302 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity comprising the above-mentioned cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing to obtain product.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG38 gene derived from rumen microorganism of Capra aegagrus hircus, comprising a 2400 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG38 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enables cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) GH2 domain cellulase protein derived from the rumen microorganism of C.aegagrus hircus comprising a 799 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity, comprising the cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing the mixture to obtain product.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG45 gene derived from rumen microorganism of Capra aegagrus hircus, comprising a 2229 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG45 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enables cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) CBM6 domain cellulase protein derived from the rumen microorganism of C.aegagrus hircus comprising a 742 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity, comprising the cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing the mixture to obtain product.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG49 gene derived from rumen microorganism of Capra aegagrus hircus, comprising a 2217 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG49 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enables cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) alpha -amylase domain cellulase protein derived from rumen microorganism of the C.aegagrus hircus comprising a 738 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity, comprising the cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing the mixture to obtain product.
NOVELTY - A cellulase carboxyl ester lipase (cel)-KG51 gene derived from rumen microorganism of Capra aegagrus hircus, comprising a 1227 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The cellulase cel-KG51 gene is useful for producing cellulase protein which is used in feed additive and detergent composition, and for preparing biofuel (all claimed). The cellulase is used in fabric softener.    ADVANTAGE - The gene enables cost-effective production of feed additive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) GH2C domain cellulase protein derived from the rumen microorganism of C.aegagrus hircus comprising a 408 amino acid sequence (SEQ ID NO: 2) fully defined in the specification encoded by the above-mentioned gene; (2) recombinant vector comprising the gene; (3) host cell transformed with the above-mentioned recombinant vector; (4) feed additive with improved cellulase activity, comprising the cellulase protein; (5) detergent composition comprising the cellulase protein; and (6) method for preparing the biofuel, involves adding the cellulase protein in biomass material and hydrolyzing the mixture to obtain product.
NOVELTY - The present invention relates to an improved process for the preparation of Dexmethylphenidate hydrochloride of formula (A). More particularly, the present invention relates to an improved process for the preparation of Dexmethylphenidate hydrochloride of formula (A) and its intermediate d-threo ritalinic acid hydrochloride of formula (III).
NOVELTY - An invertebrate pest control composition comprises greater than or equal to 30% (v/v) compost and greater than or equal to 1% (v/v) soil amendment agent.    USE - Composition used for controlling soil-borne invertebrate pest, particularly nematode and increasing wetted soil volume. The nematode is selected from Aphelenehoides spp, Belonolaimus spp, Belonolaimus longicaudatus, Bursaphelenchus xylophilus, Criconemoides spp, Ditylenchus destructor, Ditylenchus dipsaci, Globodera pallida, Globodera rostochiensis, Helicotylenchu, Heterodera glycines, Heterodera schachtii, Heterodera zeae, Hoplolaimus galeatus, Longidorus, Macroposthonia xenoplax, Meloidogyne chitwoodi, Meloidogyne hapla, Nacobbus aberrans, Paratrichodorus, Pratylenchus spp, Radopholus similis, Rotylenchulus spp., Tylenchorhynchus spp., Tylenchulus semipenetrans, or Xiphinema americanum. (all claimed)    ADVANTAGE - The composition increases wetted soil volume so that there is an increased amount of water available for uptake by plant roots growing in the soil.
NOVELTY - Biological compound fertilizer comprises 50-60 pts. wt. tea waste residue, 15-35 pts. wt. tobacco waste, 0.1-1 pts. wt. wood vinegar, 20-30 pts. wt. quick-acting nutrient, and 0.1-1 pts. wt. microbial inoculum.    USE - As biological compound fertilizer.    ADVANTAGE - The fertilizer solves problem of farmers including chemical inorganic fertilizer, soil compaction and soil fertility, can be prepared conveniently, consumes less time, utilizes waste, provides economic benefit, and does not cause pollution of soil, water quality and air.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the biological compound fertilizer, which involves (a) crushing tea waste residue and tobacco waste using crusher, drying the crushed components until the moisture content is 20% or less, and performing sterilization, and (b) mixing the sterilized components of the step (a) with the wood vinegar, quick-acting nutrient and microbial inoculum, uniformly stirring the mixture, and controlling the temperature at 50-55 degrees C to obtain product.
NOVELTY - Total alkaloid extract is obtained by (a) crushing Corydalis ochotensis isocorydine, extracting the crushed material using alkaline ethanol or alkaline methanol, (b) concentrating the extract and drying the concentrate, (c) adding acid solution to the dried extract, filtering the solution, adding alkali solution to the filtrate and adjusting pH of the solution to 9-10, (d) adding organic solvent to the obtained solution, and recycling organic solvent, and (e) adsorbing the obtained product in silica column, eluting using 1-3 times ethyl acetate, and drying the eluent.    USE - The total alkaloid extract is useful for preventing and/or treating breast cancer, ovarian cancer, stomach cancer and lung cancer.    ADVANTAGE - The total alkaloid extract contains less than 50 wt.% alkaloid, and 10-12 wt.% protopine.    DETAILED DESCRIPTION - Total alkaloid extract is obtained by (a) crushing Corydalis ochotensis isocorydine, extracting the crushed material using 50-95%, 7-10 times alkaline ethanol or alkaline methanol at 40-80 degrees C, (b) concentrating the extract and drying the concentrate, (c) adding 0.5-4% acid solution to the dried extract in a mass ratio of 1-6:1, filtering the solution, adding 4-15% alkali solution to the filtrate and adjusting pH of the solution to 9-10, (d) adding 2-4 times organic solvent to the obtained solution, and recycling organic solvent, and (e) adsorbing the obtained product in silica column, eluting using 1-3 times ethyl acetate (5-10 times for eluting 50-100 times product), and drying the eluent. An INDEPENDENT CLAIM is included for method for extracting total alkaloid, which involves performing the above-mentioned steps (a)-(e).
NOVELTY - Preparing grass extract, comprises: adding grass with ethanol, soaking and extracting, filtering, recovering the ethanol, and concentrating and drying to obtain an extract A; adding water into the extract A, filtering to obtain medicine liquid A and precipitate A, adding hexane-ethyl acetate-methanol-water into the precipitate A, and concentrating and drying to obtain an extract B; passing the medicine liquid A through a resin, eluting by water and ethanol solution, and concentrating and drying to obtain an extract C; and adding and mixing the extract A, the extract B and the extract C.    USE - The method is useful for preparing grass extract that is useful for preventing and treating diabetes mellitus (all claimed).    DETAILED DESCRIPTION - Preparing grass extract, comprises: adding 6-15 times of grass with 0-90 % ethanol as solvent, soaking and extracting at 20-80 degrees C for 1-3 times and 1-4 hours, filtering, recovering the ethanol, and concentrating and drying to obtain an extract A; adding 5-20 times of water into the extract A, filtering to obtain medicine liquid A and precipitate A, adding hexane-ethyl acetate-methanol-water (2: 2: 3: 2) as solvent into the precipitate A, separating and purifying, recycling the solvent, and concentrating and drying to obtain an extract B; passing the medicine liquid A through a macroporous adsorption resin, eluting by water and then by 10-70% of ethanol solution, collecting different concentration of ethanol eluent, recycling the ethanol, and concentrating and drying to obtain an extract C; and uniformly adding and mixing the extract A, the extract B and the extract C.
NOVELTY - Multifunctional fertilizer comprises raw materials comprising 1000000 pts. wt. multifunctional active bacteria, 4000 pts. wt. naphthalene, 1000 pts. wt. milk powder, 800 pts. wt. gibberellin, 200 pts. wt. iron powder, 1000 pts. wt. zinc powder, 1000 pts. wt. copper powder, 1000 pts. wt. boron powder, 20 pts. wt. N-(2-benzimidazole)carbamate, 15 pts. wt. 3-hydroxy-5-methylisoxazole, 10 pts. wt. tolclofos methyl and 20 pts. wt. alkyl thio sulfonic acid ethyl ester.    USE - The multifunctional fertilizer is useful for preventing and treating dead vegetable (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves crushing 500000 pts. wt. sodium humate, 100000 pts. wt. urea, 200000 pts. wt. abamectin and 100000 pts. wt. lemon into 80 meshes, stirring, adjusting pH of the mixture into 7.6, and adding the above-mentioned raw materials.
NOVELTY - A one IC anaerobic reactor heating device, include IC anaerobic reactor, an IC anaerobic reactor produce marsh gas by marsh gas collecting tube upper part of a collecting marsh gas by backfire, then process, dehydrating process, and then pressurized through pressure transducer pressure adjusting through fire arrestor conveying marsh gas hot water boiler to produce hot water, to IC anaerobic reactor heating coil to a lower part of the waste water process. With simple and reliable structure, convenient operation, new energy, of energy-saving and environment-friendly.
NOVELTY - This utility new type claims a one anaerobic film biological reactor, referring to waste water processing technology field, comprise film separator, anaerobic reactor biogas pneuma and fan, the device can make the sludge completely dispersing, which is good for improving the mass transfer rate of, so as to speed up a process, marsh gas stirring time, can form the high of the cross-flow speed, sludge in the hollow fiber film forming to upper layer, it can reduce pollution of hollow fiber membrane, which is good for prolonging the use period of hollow fiber film inner the membrane reactor, in addition the marsh gas aeration form of a turbulent anaerobic to produce a gas with each other and poly, improves separation efficiency of a slurry and the pneuma in anaerobic reactor, and the film separator and a mud-water for a good separating, which cause separation of system of obtain.
NOVELTY - A double-head one manure turning target machine, the two head bottom plate middle position welded roller fixing board, the roller is movably sleeved on the upper roller shaft, roller shaft through the roller form an angle of 45 degrees is set rolling inner hexangular groove of the I-shaped steel guide rail, a walking wheel and a universal wheel on the ground, orderly fixing multiple turning upper turnover harrow rake teeth shaft, rake teeth from the ground is 20-50 mm, the motor of the power supply battery inner electric appliance box, driving gear of upper motor drives a speed reducer, a speed reducer output shaft to drive the transmission gear on the rotating shaft of upper, the connecting rotating turning rake rotating shaft two end axial direction of forward direction, when one strip channel turning target time after cutting off power supply, by the operator pushing the transfer to another one channel embodiment of , one function table is multi-house of a work, in particular to excavating manure fermenting tank, which greatly saves the investment, through single-row frame double-head poultry manure turning target machine is process of excrement, which solves the problem of finding the poultry excrement fermentation process of new.
NOVELTY - A one organic polluted soil of aerobic compost device, relating to a composting device comprise one; feeding hole cover, compost reactor, collecting port, sampling port, THE PLC control plate;;; door hinge, valve air inlet tube, gas flow meter, liquid collecting box, an air compressor, liquid collecting tube, the waste liquid collecting tank, gas collecting tube, the waste pneuma collecting box, a nut, bracket, stirrer, ventilating plate, sensor, short, compost reactor is one cuboid, the top end set with feeding port and collecting port, collecting port through collecting tube pneuma pneuma and waste collecting tank, side of reactor set with PLC control plate with temperature probe and machinery stirrer of reactor inside is connected set with front side are of uniform sampling port, reactor with the liquid tank using air plate of belt hole; the reaction condition can be a device, reduces the compost time and improves the compost efficiency, accumulate discharging of waste liquid, high degree of automation, easy operation.
NOVELTY - This utility new type relates to a stirring one biomass, belonging to the biomass carbonizing technology field. Comprise a furnace body and a set of combustion chamber, a preheating chamber, a carbonization chamber, gas-guide tube, a chimney and an upper cover inner furnace body, a pre-heating chamber is set above the coking chamber, a combustion chamber in coke, with a packing auger. inner the pre-heating chamber, a material leading-in channel., carbonizing room and burning room between the preheating cabin and carbonizing room. between a multi-guide tube, said inner carbonizing room. further with a stirrer. This utility new type through stirring, change the hot transferring way, the material of the heating speed is fast. Through stirring high-temperature material and low temperature heating of the material is blended with each other to make the transfer of hot surface material is greatly increased, the material movement, produce a convection heat exchange, the heating uniformity, carbonization uniform, mass. Hot cracking carbonization produce a fuel of directly burning inner gas in the furnace, in the carbonization period is provide enough thermal cracking of heat without additional fuel, to save energy.
NOVELTY - This utility new type relates to one a move of a nearby field carbonizing straw carbonizing furnace, wherein the furnace shell (5) is covered insulating material, inner furnace are uniformly distributed a plurality of exhaust angle box (6), the air inlet (7), a carbonization product discharge hole (12) through the discharging machine (21), the upper furnace shell (5). a poking opening (3), furnace in material array. umbrella (8), a stirring motor on the furnace top. through (2) drives the material array umbrella (8), a material stirring shaft is a hollow shaft, with inner water tube through the flexible water joint and the spray water pump (17-2) through the spraying head (9) to the cooling carbonization product furnace shell (2) upper part. combustion thermometer (18), and the lower part with a carbonization. thermometer (19), inner furnace waste pneuma the chiller (22), scrubbing tower (14), (15) a rear standard. Obtain a carbon sequestration and emission reduction, improves soil fertility improves yield and income of farmers in the effect.
NOVELTY - This new type utility claims a biomass pneuma one furnace slag discharging device for using biomass gasification furnace and the bottom of the slag discharging device, a hearth (1) set with one discharging device, said discharging device composed of an annular sieve plate (14) and annular air channel (18), the annular sieve plate (14) of lower vibration, slag through an annular sieve plate (14) entering into the annular air channel (18) in the annular air channel (18) of one of the upper tangential direction access one discharging air inlet (8) for an annular air channel (18) inner blast, the annular air channel (18) of the other one of the upper tangential direction access (4) used for discharging the slag, furnace slag entering into the annular air channel (18) rear to the slag inlet (8) is blast furnace slag lower the effect of wind power of blower (4) is slag. This utility new type through vibration of vibration sieve to make a fine ash and slag through the large holes and small holes entering into annular air channel, it is easy to slag is discharged, which saves complex slag machinery device.
NOVELTY - A machine-transplanted rice seedling substrate comprises chicken manure, cow dung, fermentation residue, and edible fungi cultivation waste residue at volume ratio of 1-1.5:2-3:3-4:2.5-3.    USE - Machine-transplanted rice seedling substrate used in promoting rice seedling root growth and improving stress resistance in rice seedling.    ADVANTAGE - The substrate does not cause harm to agriculture and forestry, is simple to use, and has good compatibility with mechanical sowing production line and good adaptability with wet irrigation method and high success rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the machine-transplanted rice seedling substrate, comprising mixing raw materials and uniformly stirring, adjusting final water content to 50-60%, stacking, adjusting stack center temperature to 58-62 degrees C and fermenting for 25-35 days, and drying completely fermented material, crushing, and sieving.
NOVELTY - The bioreactor has an aerobic reaction area (3) that is connected with anaerobic reaction area (7) through first clapboard (5). The aerobic reaction area is provided with sludge outlet (110) through first sludge valve (401) that is connected with sludge tube (6). Fourth back-flushing valve (902) is connected with water area (12) through third water tube (901). An alkali medicine adding area (812) is connected with first water tube (907) through alkaline agent valve (802). The air blower (20) is connected with the anaerobic reaction area through third air valve (101).    USE - Sewage treatment anaerobic membrane bioreactor.    ADVANTAGE - The amount of excess sludge can be reduced significantly. The energy consumption of bioreactor can be reduced, and the sludge concentration can be reduced. The speed of fall of pollutants can be accelerated.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a membrane module composite cleaning method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage treatment anaerobic membrane bioreactor.    Aerobic reaction area (3)    Clapboard (5)    Sludge tube (6)    Anaerobic reaction area (7)    Water area (12)    Air blower (20)    Air valve (101)    Sludge outlet (110)    Sludge valve (401)    Alkaline agent valve (802)    Alkali medicine adding area (812)    Water tubes (901,907)    Back-flushing valve (902)
NOVELTY - This utility new type relates to a one multi-element organic waste by using rural biogas production of device, comprise series of preprocessing pool, waste water anaerobic fermenting tank, straw bed reactor, deep tank and biogas storing tank, wherein the waste water anaerobic fermenting tank, straw bed reactor and liquid depth fermentation tank top part. with an air outlet, the waste water anaerobic fermenting tank and biogas pool using deep AF process, in preprocessing tank. collecting net straw using straw case. Presence of rural labour force requirement and shortage of this utility new type of advantages for fermentation raw material has wide adaptability, low investment, operation is simple and convenient, the operation cost is low, protection gas generating effect is good and stable and so on, output volume compared with the traditional method is greatly improved, fermentation raw material without additional preprocessing a directly fed and meets the diversified waste treatment of rural area, it has good popularization and use value of.
NOVELTY - A one integrated biogas production device, belonging to the field of environmental protection. This utility new type of purpose is through one whole set device through connecting pipe, a marsh gas generating system of the whole seal in, collecting of integrated biogas production device. This utility new type marsh gas tank through. of the hydrolysis acidification treatment tank with a pipeline of a feeding conveying pump connected, hydrolysis acidification tank through a. with a feeding pump of anaerobic digestion tank connected with the pipeline, the outer hydrolysis acidification treatment tank and the anaerobic digestion tank is covered with a water jacket, the outer jacket is coated with heat preservation material, the inner water tube of solar water heater is inserted into the marsh gas tank, solar water heater through a water inlet tube, a water return pipe and a hydrolysis acidification tank and the anaerobic digestion tank of water set connected, upper end of anaerobic digestion tank through the air outlet tube connected desulphurization device, a water collecting device, the pneuma; lower end of anaerobic digestion tank through hydraulic automatic control discharging switch with the solid liquid separating device. This utility new type collecting feeding, stirring, discharging, constant temperature and limited full automation control program, suitable for rural for production of marsh gas, collecting integrated.
NOVELTY - This utility new type refers to a mobile low-concentration coal bed gas one concentrate device, it comprise the mine. using THE PLC concentrated control system of upper flat mine car, one level explosion-proof inner shell of air compressor through high pressure glue tube sequence connecting gas preprocessing system, first-stage pressure swing adsorption concentrate system, wherein the first-stage pressure swing adsorption concentrate system through high pressure glue tube connecting order of secondary explosion-proof air compressor inner shell, second level pressure swing adsorption system concentrate. The device using modularized conformity in the ore using flat mine car up to realize the fast connect and move, it is suitable for extraction with, along with the move of extraction, two level explosion-proof air compressor, second level pressure swing adsorption system use concentrate, concentrate method using two level pressure swing adsorption technology concentrate low-concentration coal bed gas, daily processing ability is not less than 2.4 m3, in product pneuma methane content is not less than 80%, a is not less than 60%, the rear device unit product pneuma concentrate energy consumption is less than or equal to 1.2kWh/Nm3.
NOVELTY - This utility new type provide the one a structure is simple, the cost is low, a good effect of simple compost tank, include a fermenting tank, a fermenting tank set with above raw material preprocessing tank, raw material preprocessing tank and the fermenting tank set with feeding port, a fermenting tank set with a observation window of the top cover, a fermenting tank the lower part one side set with a discharging port, the discharging port set with a material outlet tank, a fermenting tank of upper side wall set with an exhaust pipeline, the free end of said exhaust pipeline connecting with a biological filler and tank, bottom plate of said fermenting tank set with the pneuma hole, the lower bottom plate set with a ventilation system, a ventilation system connecting with a fan, the lower part ventilation system set with a water cavity, a water cavity set with the lower part. This utility new type of simple compost tank, fermenting tank is heat loss of inner sealed container, the fermentation tank is low, and it is convenient for tail pneuma collecting and deodorizing process to realize the workshop does not generate fly, has no odour.
NOVELTY - Catalytic pyrolysis of microalgae, involves mixing algae powder granule, organic solvent and catalyst in a reactor at 3-8 MPa, increasing the temperature to 70-100 degrees C and maintaining for 20-60 minutes, continuously increasing the temperature to 230-500 degrees C and maintaining for 1-3 hours, and separating pyrolysis liquid product.    USE - Catalytic pyrolysis of microalgae (claimed).    ADVANTAGE - The method improves liquid content of catalytic pyrolysis product, compared with the existing liquid yield which is 29.2-35.3%.
NOVELTY - This utility new type provide the one with intelligent control function of a hydrogen producing device, comprise control circuit and anode electrode and cathode electrode, said control circuit comprise electric source module, display module, electric current detecting circuit, driving module, output circuit, switch unit and a controller, a motor and a cathode electrode and an anode output connecting circuit, which has a function of a hydrogen manufacturing device through microcomputer control external power supply of output for the anode electrode and cathode electrode, simple and intelligent circuit with over-current protection function, hydrogen process safety and reliable; a set starting and closing time, operation is simple, according to use requirement, flexibly adjust the time of hydrogen, and the working time to count down way up the LED digital tube display, a clear, avoid the hydrogen producing time the grows of the dangerous situation, which ensures the safety and reliability of using a hydrogen water.
NOVELTY - A high-energy environmentally-friendly regenerated clean fuel comprises 65.43% methanol, 30.5% additive, 3.3% denaturant, 0.57% solubilization-increasing additive and 0.2% dispersant. The additive comprises plant oil, methanol and catalyst in weight ratio of 81.4:15.2:1.1. The denaturant comprises cerium nitrate and phosphoryl methyl bromide in weight ratio of 1:3. The solubilization-increasing additive comprises isobutanol and octyl benzene in weight ratio of 1:4. The dispersant comprises carbon-based iron, carbonyl salt and sodium dihydrogen phosphate in weight ratio of 1:2.3:3.    USE - High-energy environmentally-friendly regenerated clean fuel (claimed).    ADVANTAGE - The environmentally-friendly regenerated clean fuel is economically prepared without producing waste by safe process and with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high-energy environmentally-friendly regenerated clean fuel, which involves adding plant oil, methanol and catalyst into reactor, stirring at 69-87 degrees C for 3 hours, adjusting pH value of resultant mixture to 6-8, adding methanol and denaturant into the reactor, stirring for 10 minutes, aging for 10 minutes, adding solubilization-increasing additive into the reaction kettle, stirring for 15 minutes, adding dispersant into the reactor, stirring for 30 minutes, and aging for 35 minutes.
NOVELTY - Preparation of biodiesel involves uniformly mixing Jatropha curcas crude oil and seaweed crude oil, decoloring, centrifuging the resultant material, adding solid alkali catalyst, heating, performing transesterification reaction, obtaining reaction mixture containing gum ester, free fatty acid and glycerol material, recycling methanol from the obtained reaction mixture, filtering and purifying.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The method efficiency and economically provides biodiesel with high yield, by a simple process.
NOVELTY - Production of low-temperature pyrolysis gas hydrogen and liquefied natural gas (LNG) comprises pressurizing coal, compressing and dividing gas into 2 part; desulfurizing first part of gas, converting, performing pressure swing adsorption, and extracting hydrogen to obtain pure hydrogen product; and converting second part of gas, converting carbon monoxide into hydrogen gas and carbon dioxide, washing with low-temperature methanol, decarbonizing, cooling, separating gas, purifying, and separating.    USE - Method for producing low-temperature pyrolysis gas hydrogen and LNG (claimed).    ADVANTAGE - The method has low investment, operation cost and energy consumption, and high energy utilization rate.
NOVELTY - Sewage treatment system using Vetiveria zizanioides has (a) pad layer accommodated with Vetiveria leaves and roots, (b) base layer accommodated with Vetiveria roots and stems, and (c) protruded portions of Vetiveria.    USE - As sewage treatment system.    ADVANTAGE - The sewage treatment system is cost-effective and environmentally-friendly, and has excellent sustainability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating sewage, involves adopting steps of land formation, plantation of Vetiveria, degradation, purification, Vetiveria leaf and root purification, and managing Vetiveria.
NOVELTY - The reactor has a reactor main portion whose bottom portion is provided with air inlet. A lower tower portion is provided with a glass separation hole plate (4). The suction inlet of air pump (6) is connected with gas flow meter (5), and the tower bottom aeration sand head (3) is connected with the pellet. The upper portion of reactor main portion is provided with feeding box (1), and the outermost layer is provided with reactor water bath jacket. The ratio of the diameter of tower portion is set to specific value.    USE - Waste water bubble column reactor for white rot fungi degradation, for use in paper making field.    ADVANTAGE - The operating efficiency of the reactor can be improved effectively. The paper can be manufactured efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the waste water bubble column reactor for white rot fungi degradation.    Feeding box (1)    Aeration sand head (3)    Glass separation hole plate (4)    Gas flow meter (5)    Air pump (6)
NOVELTY - A microorganism fermentation edible fungi residues and poultry feather organic fertilizer is produced by crushing edible fungi mushroom to obtain mushroom residue, inoculating fiber degrading bacteria in culture medium, shaking to obtain fiber degrading bacteria microbial inoculum, inoculating feather degrading bacteria in culture medium, shaking to obtain feather degradation bacteria microbial inoculum, mixing fiber degrading bacteria microbial inoculum, mushroom residue, poultry feather and feather degradation bacteria microbial inoculum, stacking, adding water, and fermenting.    USE - Method for producing microorganism fermentation edible fungi residues and poultry feather organic fertilizer (claimed).    ADVANTAGE - The method is simple, has small energy consumption and low cost, and utilizes waste resource. Fertilizer is highly efficient and environment-friendly.    DETAILED DESCRIPTION - A microorganism fermentation edible fungi residues and poultry feather organic fertilizer is produced by crushing edible fungi mushroom to obtain mushroom residue, inoculating fiber degrading bacteria in culture medium at 37 degrees C, shaking for 2 days at 160 revolutions/minute (rpm) to obtain fiber degrading bacteria microbial inoculum, inoculating fiber degrading fungus in culture medium at 28 degrees C, shaking for 5 days at 160 (rpm) to obtain fiber degrading fungus microbial inoculum, inoculating feather degrading bacteria in culture medium at 37 degrees C, shaking for 2 days at 160 rpm to obtain feather degradation bacteria microbial inoculum, mixing fiber degrading bacteria microbial inoculum and fiber degrading fungus microbial inoculum at volume ratio of 1:3, adding mushroom residue at mass ratio of 10:1, adding poultry feather and feather degradation bacteria microbial inoculum at mass ratio of 10:1, stacking for 28 days, adding water, and fermenting at not less than 8 degrees C.
NOVELTY - A silkworm composite vertical continuous solid organic fertilizer production device comprises solid material mixer A (1), vertical continuous solid fermentation device (3), packing machine (4), pump (5) and solid mixer B (6).    USE - Silkworm composite vertical continuous solid organic fertilizer production device.    ADVANTAGE - The device is smooth, utilizes energy, improves solid fermentation efficiency, and has simple structure, easy operation, stable mass, little investment, good economic benefit and ecological benefit.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of silkworm composite vertical continuous solid organic fertilizer production device.    Solid material mixer A (1)    Vertical continuous solid fermentation device (3)    Packing machine (4)    Pump (5)    Solid mixer B (6)
NOVELTY - Green fertilizer comprises 80-90 pts. wt. rapeseed cake, 50-55 pts. wt. biogas residue, 20-23 pts. wt. zeolite powder, 40-45 pts. wt. ammonium chloride, 24-47 pts. wt. potassium phosphate, 35-38 pts. wt. urea, 12-14 pts. wt. potassium sulfate, 2-3 pts. wt. magnesium sulfate, 2-3 pts. wt. polyethylene glycol, 1-2 pts. wt. polyvinyl alcohol, 1-2 pts. wt. Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate), 3-4 pts. wt. effective microorganisms agent, 4-6 pts. wt. film agent and water.    USE - Green fertilizer used for improving soil and strengthening drought resistance (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of green fertilizer comprising mixing rapeseed cake, biogas residue, zeolite powder and water to obtain mixture A; mixing ammonium chloride, potassium phosphate, urea and potassium sulfate to obtain mixture B; mixing magnesium sulfate, polyethylene glycol, polyvinyl alcohol, Tween 80 (RTM: polyoxyethylene (20) sorbitan monooleate) and water and heating to obtain mixture C; and mixing mixtures A, B and C, adding other remaining ingredients, stirring, performing aerobic fermentation for 20-25 days, drying and granulating.
NOVELTY - Peach fertilizer comprises 18-22 pts. wt. dry chicken manure, 10-14 pts. wt. dry duck manure, 11-15 pts. wt. dry pig manure, 28-32 pts. wt. plant ash, 8-12 pts. wt. bone powder, 4-8 pts. wt. soybean meal, 8-12 pts. wt. potassium dihydrogen phosphate, 8-12 pts. wt. urea, 1-5 pts. wt. growth hormone, 8-12 pts. wt. trichlorfon, 18-22 pts. wt. phenolic resin and 4-8 pts. wt. fennel powder.    USE - Peach fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of peach fertilizer comprising weighing raw materials, crushing to 50-60 mesh, adding human excrement and water, stirring, mixing, covering, fermenting for 24-36 hours, adding excrement and fermenting for 48-84 hours.
NOVELTY - Hexafluoroisopropanol, formaldehyde and aluminum trichlorides are mixed, to obtain chloromethyl hexafluoroisopropyl ether. The mixture is washed, crude product is purified by distillation, chloromethyl hexafluoroisopropyl ether is reacted with fluorinating agent using phase transfer catalyst and hindered amine, and crude product is purified by distillation, to obtain sevoflurane.    USE - Preparation of sevoflurane (claimed).    ADVANTAGE - The method economically and easily provides sevoflurane having high yield and purity without polluting the environment.
NOVELTY - Preparation of 4,4'-difluoro benzophenone involves adding aluminum trichloride in a solution of 4-fluoro benzoyl chloride and/or benzoyl peroxide at 150-250 degrees C, heating at 80-120 degrees C for 1-2 hours, adding solution of fluorophenyl, vacuum distilling under -0.85 MPa, adding activated carbon and ethanol, crystallizing, and filtering.    USE - Preparation of difluoro benzophenone (claimed).    ADVANTAGE - The environmentally-friendly method provides difluoro benzophenone with high yield.
NOVELTY - 11-Chloro-dibenzo (b,f) (l,4) thiazepine (I) synthesis involves heating 2-thia-9-azatricyclo (9.4.0.0(3,8))pentadeca-1(11),3,5,7,12,14-hexaen-10-one (II) with (chloromethylidene)dimethylazanium chloride (III) in presence of organic solvent to obtain desired product, where (chloromethylidene)dimethylazanium chloride (III) is obtained by reacting ditrichloromethyl carbonate (IV) with N,N-dimethylformamide (V).    USE - Method for synthesizing 11-chloro-dibenzo (b,f) (l,4) thiazepine (claimed).    ADVANTAGE - The method enables to prepare 11-chloro-dibenzo (b,f) (l,4) thiazepine in a convenient, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - 11-Chloro-dibenzo (b,f) (l,4) thiazepine of formula (I) synthesis involves heating 2-thia-9-azatricyclo (9.4.0.0(3,8))pentadeca-1(11),3,5,7,12,14-hexaen-10-one of formula (II) with (chloromethylidene)dimethylazanium chloride of formula (III) in presence of organic solvent to obtain desired product, where (chloromethylidene)dimethylazanium chloride (III) is obtained by reacting ditrichloromethyl carbonate (IV) with N,N-dimethylformamide (V)..
NOVELTY - Polyglutamic acid hydrogel preparation involves adding polyglutamic acid powder (5-15%) in purified water. The obtained mixture is stirred to dissolve completely. Epoxy succinic acid (0.01-0.1%) is added to the obtained mixture and then sodium chloride is added to adjust the pH value to 4.0-7.0. The obtained mixture is stirred and then heated at 30-60 degrees C for 2-8 hours. Poly(ethylene glycol) diglycidyl ether (0.1-1.5) is added to the obtained mixture, and then stirred at 40-65 degrees C, preferably temperature is 50-60 degrees C, where pH value is regulated at 5.0-6.5. The obtained mixture is stirred slowly.    USE - Method for preparing polyglutamic acid hydrogel used in agricultural fertilizer (claimed).    ADVANTAGE - The polyglutamic acid hydrogel preparation method enables to produce water absorbing resin that regulates soil in combination with fertilizer and has improved absorption capacity.    DETAILED DESCRIPTION - Polyglutamic acid hydrogel preparation involves adding polyglutamic acid powder (5-15%) in purified water. The obtained mixture is stirred to dissolve completely. Epoxy succinic acid (0.01-0.1%) is added to the obtained mixture and then sodium chloride is added to adjust the pH value to 4.0-7.0. The obtained mixture is stirred and then heated at 30-60 degrees C for 2-8 hours. Poly(ethylene glycol) diglycidyl ether (0.1-1.5) is added to the obtained mixture, and then stirred at 40-65 degrees C, preferably temperature is 50-60 degrees C, where pH value is regulated at 5.0-6.5. The obtained mixture is stirred slowly for 5 minutes, and then the reaction is continued for 8-20 hours at constant temperature to obtain gel-shaped product. The obtained product is dried at 40-80 degrees C for 12-24 hours to remove organic solvent. The obtained product is crushed to obtain the desired product.
NOVELTY - An aviation kerosene preparing method involves taking lignocellulosic furfural compounds and branched ketone condensate from the reaction between carbon chain length of 9-16 in an oxygen-containing organic compound. Metal catalyst is utilized for direct hydrogenation of the aldol condensation product of deoxygenation and obtaining a carbon chain length of 9-16 having high energy density, high stability, low freezing point branched alkane.    USE - Method for preparing aviation kerosene.    ADVANTAGE - The method enables preparing kerosene with higher energy density, stability and biomass kerosene branched hydrocarbon-lower freezing point 16.
NOVELTY - The line has a gasification furnace connected with a cooling dust-removing device, a filter, a vacuum pump, a fine filter device and a pneuma storage cabinet through a gas pipeline. The gasification furnace is provided with a furnace body. Upper and lower ends of the furnace body are sealed with a furnace cover that is provided with a feeding port. A first air outlet is connected with the cooling dust-removing device through a first gas pipeline. A second air outlet is connected with the cooling dust-removing device through a second gas pipeline.    USE - Biomass fuel gasification production line.    ADVANTAGE - The line is convenient for a user to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass fuel gasification production line.
NOVELTY - The system has a reaction furnace body (1) arranged with a feeding device (2), a stirring and ash falling device (3), a combustion-supporting device (4) and a main control chip. A reaction furnace temperature sensor (51) is connected with an input end of the main control chip. A feeding motor (21) and a stirring motor (31) are connected with an output end of the main control chip. A combustion-supporting tube (42) is extended into the reaction furnace body. A combustion-supporting blower (41) is connected with the output end of the main control chip.    USE - Biomass reaction furnace control system.    ADVANTAGE - The system enables controlling reaction furnace inner temperature in an accurate manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass reaction furnace control system.    Reaction furnace body (1)    Feeding device (2)    Stirring and ash falling device (3)    Combustion-supporting device (4)    Feeding motor (21)    Stirring motor (31)    Combustion-supporting blower (41)    Combustion-supporting tube (42)    Reaction furnace temperature sensor (51)
NOVELTY - A bioalcohol oil is prepared by mixing methanol, ethanol and acetone, adding stabilizer, ferrocene and water, and stirring.    USE - Method for preparing bioalcohol oil (claimed).    ADVANTAGE - The method reduces costs. The oil is stable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for composition of bioalcohol oil comprising 65-80 wt.% methanol, 10-15 wt.% ethanol, 5-10 wt.% stabilizer, 5-10 wt.% acetone, 0.1-1 wt.% ferrocene and 1-10 wt.% water.
NOVELTY - A methanol/gasoline solution comprises 25-30 pts. wt. methanol, 11-16 pts. wt. naphtha, 3-8 pts. wt. ethyl acetate, 5-11 pts. wt. acetone, 7-14 pts. wt. glycerides, and balance gasoline.    USE - Methanol/gasoline solution.    ADVANTAGE - The solution is waterproof.
NOVELTY - High proportion methanol gasoline compound additive comprises 50-70 wt.% fatty acid ester, 10-30 wt.% nitrate, 5-10 wt.% glycerol, 5-10 wt.% benzotriazole and 5-10 wt.% alcohol.    USE - High proportion methanol gasoline compound additive used for improving corrosion resistance, accelerating ignition and improving combustion.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of high proportion methanol gasoline compound additive comprising mixing raw materials at 60 degrees C and dissolving.
NOVELTY - Biofuel briquette comprises 40-45 wt.% pulverized coal ash, 2-5 wt.% sand, 20-25 wt.% straw and 25-30 wt.% plastic waste.    USE - Biofuel briquette.    ADVANTAGE - The briquette is inexpensive, environment-friendly, energy-saving and easy to produce.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of biofuel briquette comprising crushing raw materials, melting, drying, mixing at 200 degrees C, stirring, cooling to 70 degrees C, adding pulverized coal ash, straw and wood waste, stirring, mixing, molding and extruding.
NOVELTY - Preparation of dense sludge biomass briquette comprises selecting wastewater sludge raw material, measuring moisture content raw material, mixing raw material wastewater sludge to obtain moisture content of 60%, adding lignocellulosic biomass materials; deodorizing, fermenting; composting, decomposing lignin and complex organic compounds; drying, mixing, granulating and extruding.    USE - Method for preparing dense sludge biomass briquette.    ADVANTAGE - The environmentally-friendly method has low energy consumption.
NOVELTY - Producing biodiesel involves mixing animal fats and vegetable oils or waste grease raw material with methanol or ethanol in mass ratio of 2:1-10:1 to obtain a mixture. The mixture is injected simultaneously with solid catalyst into former fixed bed reactor, and then heated at 120-220 degrees C and 0.1-4.0megapascal pressure with space velocity 0.1-5.0 per hour. Esterification reaction is occured into the former fixed bed reactor where animal and vegetable grease or waste grease (40-80 wt.%) is converted into fatty acid ester biological diesel with glycerol separation.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method produces highly pure by-product glycerol and improves production efficiency.    DETAILED DESCRIPTION - Producing biodiesel involves mixing animal fats and vegetable oils or waste grease raw material with methanol or ethanol in mass ratio of 2:1-10:1 to obtain a mixture. The mixture is injected simultaneously with solid catalyst into former fixed bed reactor, and then heated at 120-220 degrees C and 0.1-4.0megapascal pressure with space velocity 0.1-5.0 per hour. Esterification reaction is occured into the former fixed bed reactor where animal and vegetable grease or waste grease (40-80 wt.%) is converted into fatty acid ester biological diesel with glycerol separation. Mixture of animal fats, vegetable oils or waste grease raw material with methanol or ethanol is mixed with separated glycerol layer (0.1-10 wt.%), and then injected with solid catalyst into a latter fixed bed reactor. The latter fixed bed reactor is heated at 120-220 degrees C and 0.1-4.0megapascal pressure with space velocity 0.1-5.0 per hour, where glycerol layer is separated to obtain biodiesel.
NOVELTY - Removing sand from biogas engineering fermentation raw material involves utilizing a sand tank, where processing material is fed into a sand body (2) through a material inlet (11). Water is poured into the sand body, where motor is started and processing material is stirred by using a stirring mill (10). Water is warmed by introducing a warming coil through an inlet tube (6) into a heating disk tube (5) of a tank wall and heating disk tube at tank bottom.    USE - Method for removing sand from biogas engineering fermentation raw material (claimed).    ADVANTAGE - The method enables to remove sand from biogas engineering fermentation raw material in a simple manner.    DETAILED DESCRIPTION - Removing sand from biogas engineering fermentation raw material involves utilizing a sand tank, where processing material is fed into a sand body through a material inlet. Water is poured into the sand body, where motor is started and processing material is stirred by using a stirring mill. Water is warmed by introducing a warming coil through an inlet tube into a heating disk tube of a tank wall and heating disk tube at tank bottom. The material liquid is heated at 30-35 degrees C for 1-2 days after completion of reaction, and then stirring mill and introduction of hot water are stopped. The material is hydrolyzed through a material exit of the tank body. Above steps are repeated and then sand is cleaned by opening the tank body and seal door.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a sand tank.    Sand body (2)    Heating disk tube (5)    Inlet tube (6)    Stirring mill (10)    Material inlet (11)
NOVELTY - An enhanced organic sludge acid fermentation device comprises main reaction vessel and self-generated dynamic membrane structure.    USE - Enhanced organic sludge acid fermentation device.    ADVANTAGE - The method increases conversion and acid fermentation rates of sludge, reduces operating costs and investment costs, and greatly optimizes existing anaerobic digestion of organic sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for acid fermentation of sludge by feeding raw sludge into main reaction vessel, stirring to carry out anaerobic acid fermentation reaction to obtain soluble organic acid, adding fermentation liquid to self-generated dynamic membrane structure, and discharging water and residual sludge.
NOVELTY - A Paenibacillus (G4) with preservation number CCTCC No. M2013548 is new.    USE - A Paenibacillus (G4) with preservation number CCTCC No. M2013548 for promoting growth of plant and chemical substance-producing plant, improving soil fertility, increasing soil microbial biomass and enzyme activities, and enhancing crop stress resistance (all claimed).    ADVANTAGE - Paenibacillus has strong activity.    DESCRIPTION OF DRAWING(S) - The drawing shows an optical micrograph of Paenibacillus (G4) single colony in silicate bacterial culture with 100 times magnification.
NOVELTY - Acinetobacter johnsonii strain AJ-3 has a preservation number CCTCCM2014023, and is new.    USE - Acinetobacter johnsonii strain AJ-3 used for removal of biological phosphorus from sewage water (claimed).
NOVELTY - A corn straw aerobic and anaerobic microorganism preprocessing is performed by cleaning fresh corn straw i.e. corn straw during harvesting season, cutting, adjusting moisture content, filling in sealed special device, compacting, covering using plastic film for 30 days, and performing combined aerobic and anaerobic microorganism preprocessing by relying on air and microflora of straw.    USE - Corn straw aerobic and anaerobic microorganism preprocessing for biogas fermentation.    ADVANTAGE - Preprocessing method is low in cost, has simple operation, increases untreated straw anaerobic digestion gas production rate, solves problem of high security risks due to raw material biogas storage, and effectively utilizes waste resource.
NOVELTY - A bacterial cellulose fabric is processed by using wheat straw/rice straw culture medium hydrolyzate as carbon source, adding 0.1-0.2% nitrogen source, sterilizing at 115-125 degrees C for 15-20 minutes to obtain culture medium, accessing acetic acid bacteria or glucose oxidase bacteria with inoculating amount of 5-10 vol.%, immersing in fermentation medium sealed pool equipped with vertical fabric, closing at 25-30 degrees C, passing oxygen air by injecting into fabric every 10-30 minutes, and performing continuous culture of bacterial cellulose at 25-30 degrees C for 6-25 days.    USE - Process of bacterial cellulose fabric (claimed).    ADVANTAGE - Product has good permeability, high tensile strength, and excellent sustainability.    DETAILED DESCRIPTION - A bacterial cellulose fabric is processed by using wheat straw/rice straw culture medium hydrolyzate as carbon source, adding 0.1-0.2% nitrogen source, sterilizing at 115-125 degrees C for 15-20 minutes to obtain culture medium, accessing acetic acid bacteria or glucose oxidase bacteria with inoculating amount of 5-10 vol.%, immersing in fermentation medium sealed pool equipped with vertical fabric, closing at 25-30 degrees C, passing oxygen air by injecting into fabric every 10-30 minutes, performing continuous culture of bacterial cellulose at 25-30 degrees C for 6-25 days to obtain acetic acid bacteria or glucose oxidase bacteria in outer surface of fabric, stripping out, washing with water to remove impurities, adding with 0.1 mol/L sodium hydroxide solution, boiling at 80 degrees C for 20 minutes to remove bacteria and residual medium, rinsing with water, and drying.
NOVELTY - Usage of transgenic yeast hybrid in ethanol fermentation from rice straw is performed by degrading rice straw cellulose and xylanase into glucose and xylose and performing in situ ethanol fermentation.    USE - Usage of transgenic yeast hybrid in ethanol fermentation from rice straw (claimed).    ADVANTAGE - Usage process reduces production cost.
NOVELTY - Preparing valsartan (I), comprises carrying out coupling reaction of L-(N-4-halobenzyl)-N-pentanoyl-valine compounds (VII) with 5-phenyltetrazole-borane derivatives (VIII) in presence of a palladium catalyst and a base in an organic solvent and/or an aqueous solution.    USE - The method is useful for preparing valsartan (claimed).    ADVANTAGE - The method: is simple and economical (claimed); utilizes cheap and easily available raw materials; has mild reaction conditions with fewer side effects, and high product yield; and is environment-friendly and suitable for industrial production.    DETAILED DESCRIPTION - Preparing valsartan of formula (I), comprises carrying out coupling reaction of L-(N-4-halobenzyl)-N-pentanoyl-valine compounds of formula (VII) with 5-phenyltetrazole-borane derivatives of formula (VIII) in presence of a palladium catalyst and a base in an organic solvent and/or an aqueous solution.    Either R2, R3 = 1-8C alkyl, 2-8C alkenyl, 2-8C alkynyl, 3-8C cycloalkyl or 2-8C saturated heterocyclyl, 6-12C aryl, 3-12C heteroaryl (all are optionally substituted); or    R2R3 = 3-12 membered ring with at least one O, N or S atom and at least one unsaturated bond; and    R1 = chloro, bromo or iodo.
NOVELTY - Crystalline cabazitaxel-ethyl acetate solvate (I) is new. (I) includes 8-10% ethyl acetate.    USE - The composition is useful as active component in preparing anti-tumor medicine (claimed).    ADVANTAGE - (I) has good stability with low moisture absorption, is economical and simple to prepare with high yield, environmentally friendly, energy-saving and meets industrial production requirements.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing (I); and    (2) composition, comprising (I) and a carrier or excipient.
NOVELTY - An o-aminophenol is prepared by choosing nitrobenzene as raw material, adding with sodium hydroxide solution, entering into hydrolysis kettle for hydrolysis reaction at 160-175 degrees C for 4.5 hours and at 0.68-0.72 MPa to obtain base sodium; adding obtained product in reduction kettle, adding hydrogen sulfide to obtain amidogen sodium, and reducing temperature to 60-80 degrees C within 4 hours; adding sulfuric acid solution, and separating out elemental sulfur; and adding alkali to neutralize, and filtering the solution to obtain o-aminophenol.    USE - Method for preparing ortho-aminophenol (claimed).    ADVANTAGE - The method saves energy and device, and produces wastewater with almost no impurity and that can be recycled.
NOVELTY - Method for preparing pesticide involves (a) weighing toosendanin, matrine, Cedrela sinensis juice, flos daturae, potassium chloride, radix stemonae, fulvic acid and modified starch, (b) adding modified starch into 10% fulvic acid solution, and stirring, (c) extracting flos daturae and radix stemonae using water, and mixing the extract with toosendanin, matrine, and A.altissima juice, and (d) mixing the products obtained in steps (b) and (c), adding potassium chloride, and mixing uniformly.    USE - The method is useful for preparing pesticide (claimed).    ADVANTAGE - The method enables simple and environmentally-friendly preparation of pesticide using plant source materials as main raw materials which is convenient to use.
NOVELTY - Time walking shaft upper end outer bottom plate of rectangular frame, motor and driving this utility new type claims a manure turning one target machine, comprise of two side plate and two welded cross beam is welded on the frame of upper, side plate and transmission support with the lower target turning shaft and orderly fixing multiple turning upper turnover harrow rake teeth shaft, upper of motor drives a speed reducer, a speed reducer output shaft is provided with a driven turning rake shaft of first chain driving and walking shaft of second chain, two two ends of walking shaft are extended out of side plate and outer side plate of extending are provided with walking wheel, a transmission box elastic overturning rake teeth of two side using a thickness of 1-2.5 mm of an elastic plate, elastic turning rake teeth of elbow to middle of transmission box thickness, the thickness of upper gear box. triangular anti-skid toothed block, a shaft elastic turnover harrow rake teeth with the triangular anti-skid toothed block inclined plane, the elastic effect delayed transmission case sliding the rebound, the transmission case also can obtain target turning and stirring, turning two end target shaft extends out of side plate, upper side outer plate of turning out target shaft of shaft end installation pool side turning rake teeth, so it can obtain inner stirring fermentation tank width range, curing is high, good fermentation effect, which greatly improves the poultry excrement of organic fertilizer value, deep by fruit, welcome of vegetable grower.
NOVELTY - Preparation of medicine includes providing 225 g longhairy antenoron herb, 225 g oriental wormwood, 90 g radix Curcumae, 150 g dried orange peel, 45 g radix Scutellariae, 35 g frankincense, 80 g mirabilite, 35 g white alum, 45 g rhubarb, 45 g rhizoma Sparganii, 45 g Gardenia, 25 g licorice and 35 g myrrh.    USE - Preparation of medicine used for inhibiting mice myeloma cell line FO proliferation (claimed).    ADVANTAGE - The method greatly improves hesperidin content.    DETAILED DESCRIPTION - Preparation of medicine comprises providing 225 g longhairy antenoron herb, 225 g oriental wormwood, 90 g radix Curcumae, 150 g dried orange peel, 45 g radix Scutellariae, 35 g frankincense, 80 g mirabilite, 35 g white alum, 45 g rhubarb, 45 g rhizoma Sparganii, 45 g Gardenia, 25 g licorice and 35 g myrrh, taking Glauber's salt and alum, ultra-micro-crushing into fine powder having a particle size of 5-45 mu m, taking frankincense and myrrh, crushing into fine powder, adding supercritical carbon dioxide (CO2), conducting supercritical CO2 extraction using ethanol as entrainer at 4-6 vol.% based on the total amount of raw materials, at 15-30 MPa, 30-50 degrees C and flow rate of 1-3 ml/g raw medicine-minute, for 180-220 minutes, obtaining supercritical extract, crushing the frankincense and myrrh residue and other nine medicinal raw materials, adding 3.6 L of 70% ethanol, microwave extracting at 600-800 W for 2 times, each for 5-10 minutes, combining the extracting liquids, concentrating, adding into Diaion HP-10 (RTM: macroporous adsorption resin column), eluting with 70% ethanol, collecting 5 times by column volume, vacuum recovering ethanol, concentrating and drying to obtain microwave extract, uniformly mixing fine powder of Glauber's salt and alum, supercritical extract and microwave extract, adding 70% ethanol, granulating, drying, tableting and preparing 500 pieces, each weighing 0.3 g.
NOVELTY - A composite biomass filter material comprises 70-80 wt.% biomass granular particles and 20-30 wt.% diatomaceous earth. The biomass granular particles is obtained by drying biomass feedstock to moisture content of 15-20 wt.%, pulverizing to product having particle size of 3-5 mm, soaking in petroleum ether for 2 hours, removing, drying to product having moisture content of less than 10% and grinding to product having particle size of 1.5 mm. The diatomaceous earth is pretreated by soaking in petroleum ether for 1 hour, removing, soaking in ethanol, sonicating for 10 minutes, removing and drying.    USE - Composite biomass filter material (claimed).    ADVANTAGE - The composite biomass filter material is environmentally-friendly and economical and has excellent absorption ability.
NOVELTY - A solid alkali catalyst comprises lanthanum-doped zinc-aluminum spinel containing 1.7-17 wt.% lanthanum, and zinc-aluminum spinel (I).    USE - Solid alkali catalyst is used for producing bio-diesel by performing transesterification of fatty acid glycerides and lower alcohols.    ADVANTAGE - The solid catalyst has high activity and stability.    DETAILED DESCRIPTION - A solid alkali catalyst has lanthanum-doped zinc-aluminum spinel comprising 1.7-17 wt.% lanthanum, and zinc-aluminum spinel of formula: ZnAlxO1+1.5 (I).    x=1.5-2.5.    An INDEPENDENT CLAIM is included for preparation of solid alkali catalyst, which involves preparing aluminum and lanthanum salt solution (A), such that the total concentration of metal ions is 0.5-2.5 mol/L with respect to zinc, preparing solution (B) using 1-4.5 mol/L alkaline precipitating agent, adding aluminum and lanthanum salt solution (A) and solution (B) into deionized water, stirring, precipitating, stopping stirring, maintaining mother liquor, aging precipitate at 20-100 degrees C for 2-48 hours, filtering mother liquor, washing resulted filter cake using deionized water until pH of filtrate is 7, drying at 120 degrees C, and calcining at 600-900 degrees C for 2-8 hours. The dropping rate of aluminum and lanthanum salt solution (A) is 5-10 ml/minute.
NOVELTY - A high-loaded slurry bed methanation catalyst comprises 50-90 wt.% nickel, 9.8-49 wt% carrier and 0.1-10 wt% auxiliary agent oxide.    USE - High-loaded catalyst used for slurry bed methanation process.    ADVANTAGE - The catalyst has favorable stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) preparation of high-loaded slurry bed methanation catalyst, which involves adding nickel nitrate, soluble salt auxiliary agent oxide and soluble salt carrier and soluble organic fuel in water to prepare aqueous solution containing 0.1-1 g solute with respect to 1 ml water, heating at 300-700 degrees C, or microwave radiation heating with microwave wavelength of 10-20 cm, power of 30-100 W/mL, collecting, grinding and granulating to obtain nickel-based catalyst; and    (2) usage method of high-loaded slurry bed methanation catalyst, which involves adding high-loaded slurry bed methanation catalyst to paraffin hydrocarbon, heat-conducting oil or hydrogenated terphenyl, and inert liquid phase component, reacting at 250-350 degrees C under pressure of 1-4 MPa with space velocity of 1000-4000 mL/g.hour and slurry bed catalyst concentration of 0.013-0.05 mu g/mL, carbon monoxide/hydrogen volume ratio of 2.5-3.7, and stirring rate of 100-2000 rmp.
NOVELTY - A refrigerating oil comprises monoester compound (I) having kinematic viscosity of less than 7 mm2/second at 40 degrees C, hydrocarbon refrigerant mixture comprising propane R290, R600 and/or isobutane and acid-absorbing agent comprising epoxy ring-containing compound or carbodiimide compound.    USE - Refrigerating oil is used for refrigerator (claimed).    ADVANTAGE - The refrigerating oil has low viscosity, excellent stability and suppressed greenhouse effect.    DETAILED DESCRIPTION - A refrigerating oil comprises monoester compound of formula (I) having kinematic viscosity of less than 7 mm2/second at 40 degrees C, hydrocarbon refrigerant mixture comprising propane R290, R600 and/or isobutane and acid-absorbing agent comprising epoxy ring-containing compound or carbodiimide compound.    R1=linear or branched 5-9C hydrocarbyl;and    R2=linear or branched 8-10C hydrocarbyl.    An INDEPENDENT CLAIM is included for refrigerator.
NOVELTY - The method involves filling of hydrocarbon-containing input material into a reactor that comprises a heat-carrier on which the hydrocarbon-containing input material is provided. A centering flow is generated in the heat carrier and the products of oil contamination are recovered from the reactor. The geometric shaped particles are offset to produce the centering flow in rotation. The geometric shaped particles are wholly or partially of paramagnetic or ferromagnetic material. The heat transfer medium comprises silver and tin.    USE - Method for oiling of hydrocarbon-containing input material such as biomass, sewage sludge, plastics, tires, vegetable or mineral fats, waste oil, wax, lipids, protein and kitchen fats in crude oil fraction, for producing fuels or raw materials for chemical industry or for purification of substances with carbon-contaminated material input.    ADVANTAGE - The efficiency of oiling of hydrocarbon-containing input material is improved. The coking is excluded. The heat transfer liquid metals have high density and are easily separated from the products of oiling. The sufficient oiling is ensured and unwanted side reactions in the oiling of hydrocarbon-containing input material are avoided. The optimal mixing is achieved. The cost is saved. The need for external heat supply is eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process for oiling of hydrocarbon-containing input material. (Drawing includes non-English language text)
NOVELTY - Fuel cell system (100) comprises coolant circulation channel (41) through which coolant circulates to cool fuel cell (1); circulation pump (46) provided in coolant circulation channel to circulate coolant; pump inlet port pressure sensing mechanism (48) for detecting inlet port pressure of circulation pump; pressure control mechanism for controlling pressure of reactive gas supplied to fuel cell based on running state of fuel cell system; and pressure-correction mechanism that carries out correction of reactive gas pressure when pump inlet port pressure becomes negative pressure.    USE - Fuel cell system used for supplying reactive gas to fuel cell to generate electric power.    ADVANTAGE - The fuel cell system can suppressed contraction change of cooling-water-flow channel, while preventing durability deterioration of cooling-water-flow channel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of fuel cell system (Drawing includes non-English language text).    Fuel cell (1)    Coolant circulation channel (41)    Circulation pump (46)    Pump inlet port pressure sensing mechanism (48)    Fuel cell system (100)
NOVELTY - The reactor (100) has a reactor vessel (110) including a light-transmissible surface proximate to a reaction zone (111). A movable reactant delivery system is positioned within the reactor vessel. A product removal system is positioned within the reactor vessel. A solar concentrator (101) is positioned to direct solar radiation/energy (103) i.e. heat, through the light transmissible surface to the reaction zone. The reactant delivery system includes a rotatable screw including an outwardly-extending helical thread positioned to convey reactants to the reaction zone.    USE - Chemical reactor for producing clean-burning hydrogen-based fuels from feedstocks, and for producing structural building blocks from carbon.    ADVANTAGE - The reactor increases commercial viability of the renewable reactants and energy sources to produce the products by improving the efficiency with which hydrogen and carbon are produced in the reactor vessel. The reactor effectively reduces volume between neighboring screw threads along a direction toward the reaction zone, thus compacting the reactant. The reaction zone can have an annular shape, and includes insulation to prevent heat from escaping from the vessel.    DETAILED DESCRIPTION - The reactants are methane, municipal solid waste streams and biomass reactants. An INDEPENDENT CLAIM is also included for a method for performing a chemical reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a reactor system including a solar concentrator that directs heat to a reactor vessel.    Chemical reactor (100)    Solar concentrator (101)    Solar radiation/energy (103)    Reactor vessel (110)    Reaction zone (111)
NOVELTY - Reforming liquid fuel cell fuel comprises: mixing liquid fuel with supplied vapor in a reforming reactor, forming hydrogen-rich reformed gas by reformed liquid fuel, desulfurizing the reformed gas, and supplying the desulfurized reformed gas into the fuel cell; or conversion of hydrocarbon in the liquid fuel to methane by methanation, mixing the methanation processed liquid fuel with supplied vapor in a reforming reactor, forming hydrogen-rich reformed gas by reformed liquid fuel, desulfurizing the reformed gas, and supplying the desulfurized reformed gas into the fuel cell.    USE - The method is useful for reforming liquid fuel cell fuel (claimed).    ADVANTAGE - The method: does not require separate supply of hydrogen for the desulfurization process; is economical; and reduces the size of the whole system.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the process flow for reforming liquid fuel cell fuel.
NOVELTY - Production of renewable materials involve hydrolyzing a polysaccharide material while purifying the renewable material from a mixture comprising the polysaccharide material and the renewable material.    USE - For the production of renewable materials (claimed) such as biofuels.    ADVANTAGE - Compared to traditional processing of lignocellulosic biomass, the present methods result in minimized capital while maintaining or improving yields. The distillative hydrolysis, e.g. achieves capital minimization by enabling the recovery of ethanol vapors in the same equipment where fiber pretreatment occurs, thus reducing the overall number of unit operations (and eliminating roller mills, hydrolysis, and/or detox sections), distillative hydrolysis and the other process intensification arrangements also provide a number of secondary benefits including better alignment with 5C de-polymerization/degradation kinetics, enablement of two-stage pretreatment, reduced inhibitor/aldehyde formation, improved operability by maintaining solid:liquid ratio 3-3.5 throughout the plant, bio-burden control by lowering incoming feed and fermenting at pH of 4-4.5, and by conducting separate hydrolysis and fermentation (SHF) at 70-80 degrees C, alignment with 5C/6C enzyme temperature optimum for improved SHF kinetics, reduction in pH and temperature oscillations across the plant, lower acid/base use, lower osmotic/salt stress, elimination of acetate inhibition by acid-catalyzed esterification to ethyl acetate co-product, and recovery in distillative hydrolysis section.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for producing renewable materials from lignocellulosic feedstock, comprising: a distillative hydrolysis unit; and a fermenting unit.
NOVELTY - The equipment has a solid fuel storage unit that stores the solid fuel from the dryer. A heater accommodating chamber (611) is formed in a lower portion of a main unit (610). A heater (630) heats up the heating bath (620) which supplies the sludge to a fermenting device through a sludge outlet of main unit. A liquefying device (700) for liquefying steam filtered in a filter tool of the liquid livestock excretion disposal device (600) through the steam outlet of the main unit. A liquefied fertilizer storage unit (800) stores the liquefied fertilizer from the liquefying device.    USE - Apparatus for manufacturing solid fuel using livestock excretions of pig and hen.    ADVANTAGE - The solid fuel can be manufactured efficiently. The utilization of livestock manure is excellent. The sludge within the liquid livestock excretions in which the complete solid-liquid separation does not become once more the liquid livestock excretions is completely filtered out. The livestock manure used in the manufacture of solid fuels is utilized more efficiently. The impurities in the polluted gas are removed. The bad smell generated in the heater can be prevented. The fuel cost can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the liquid livestock excretion disposal device. (Drawing includes non-English language text)    Liquid livestock excretion disposal device (600)    Main unit (610)    Heater accommodating chamber (611)    Heating bath (620)    Heater (630)    Liquefying device (700)    Liquefied fertilizer storage unit (800)
NOVELTY - Preparing 1-benzyl-N,4-dimethyl-piperidin-3-amine (IV) comprises: either (a) reducing a 1-benzyl-N,4-dimethyl-pyridin-1-ium-3-amine compound (III) to obtain (IV); or (b) treating a 4-methylpyridine compound (V) with a benzyl halide to obtain a 1-benzyl-4-methyl-pyridin-1-ium compound (VI), (c) treating (VI) with methylamine to obtain (III) and (d) reducing (III) to obtain (IV); or the steps (c) and (d) as above per se.    USE - The process is useful for preparing (IV), (VI), (III) and tofacitinib (all claimed) having Janus kinase activity.    ADVANTAGE - The process economically prepares (IV) in an environmentally friendly manner.    DETAILED DESCRIPTION - Preparing 1-benzyl-N,4-dimethyl-piperidin-3-amine of formula (IV) comprises: either (a) reducing a 1-benzyl-N,4-dimethyl-pyridin-1-ium-3-amine compound of formula (III) to obtain (IV); or (b) treating a 4-methylpyridine compound of formula (V) with a benzyl halide to obtain a 1-benzyl-4-methyl-pyridin-1-ium compound of formula (VI), (c) treating (VI) with methylamine to obtain (III) and (d) reducing (III) to obtain (IV); or the steps (c) and (d) as above per se.    X- = Cl-, Br- or I-; and    X = Cl Br or I.    INDEPENDENT CLAIMS are included for:    (1) a process-A for preparing (VI) comprising the step (b) as above per se;    (2) a process-B for preparing (III) comprising either the steps (b) and (c) as above per se, or the step (c) as above per se;    (3) a process-C for preparing tofacitinib or its isomer and/or salt comprising either the step (d) as above per se, and converting (IV) into tofacitinib, or the steps (b)-(d) as above per se, and converting (IV) into tofacitinib, or the steps (c) and (d) as above per se, and converting (IV) into tofacitinib;    (4) the 1-benzyl-N,4-dimethyl-pyridin-1-ium-3-amine (III); and    (5) the 1-benzyl-4-methyl-pyridin-1-ium (VI).
NOVELTY - A biogas plant with stackable components is provided. The biogas plant with stackable components includes a digester tank, a gasholder tank, a partition insert and pivot pipe assembly. A pivot pipe assembly is installed inside a digester tank aligned with its axis and a partition insert is installed concentric to the digester tank. This partition insert creates two concentric compartments, inside one for biodigestible slurry and outside one as water jacket. A gasholder tank is placed in a manner that the guide pipe of the gasholder tank is concentric with the pivot pipe. This gasholder tank moves up and down in the water jacket in sliding manner because of concentric alignment of pivot pipe and guide pipe. All major components like digester tank, gasholder tank and partition insert have tapered walls for permitting stackability and hence easy transportability.
NOVELTY - The apparatus has a hydrolysis tub which ejects produced anaerobic digestion liquid to first anaerobic bioreactor (200). The anaerobic digestion liquid is pre-entered to exhaust duct (50) placed in center of bioreactors when bioreactors (200,300) successively increases wastewater through up-flow mode. The biogas generated in bioreactors is collected in gas collecting pipe (400) provided above bioreactors. The digestion liquid ejected from second bioreactor (300) with final exhaustion is re-circulated to tub for performing hydrolysis of raw water.    USE - Organic wastewater amixis anaerobic digestion apparatus.    ADVANTAGE - The in-flow capacity of each aerobic bioreactor can be made enlarged, so that the production rate of the anaerobic fermentation efficiency can be ensured. The installation expense of the anaerobic digestion apparatus can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the anaerobic bioreactors. (Drawing includes non-English language text)    Guiding layer (20)    Biogas seizing layer (40)    Exhaust duct (50)    Anaerobic bioreactors (200,300)    Gas collecting pipe (400)
NOVELTY - Preparation of vitamin B6 involves mixing 3-cyano-propionaldehyde solution with formaldehyde in an acidic catalyst at 30-100 degrees C, obtaining 5-formyl-6-cyano-1,3-dioxo-cycloheptane, recovering reaction product by solvent, cooling, extracting, obtaining 5-formyl-cyano-1,3-6-dioxo cycloheptyl, mixing 1-4C alcohol in a solvent or ether solvent in the presence of a base, reacting 5-formyl-6-cyano-1,3-dioxo-cycloheptane with 2-amino-propionate hydrochloride for cyclization, reacting at 20-50 degrees C and carrying out ring-forming reaction in the hydrochloric acid.    USE - Preparation of vitamin B6 (claimed).    ADVANTAGE - The method economically provides vitamin B6 having high purity and selectivity without polluting the environment, by a simple process.    DETAILED DESCRIPTION - Preparation of vitamin B6 involves mixing 3-cyano-propionaldehyde solution with formaldehyde in an acidic catalyst at 30-100 degrees C, obtaining 5-formyl-6-cyano-1,3-dioxo-cycloheptane, recovering reaction product by solvent, cooling, extracting, obtaining 5-formyl-cyano-1,3-6-dioxo cycloheptyl, mixing 1-4C alcohol in a solvent or ether solvent in the presence of a base, reacting 5-formyl-6-cyano-1,3-dioxo-cycloheptane with 2-amino-propionate hydrochloride for cyclization, reacting at 20-50 degrees C and carrying out ring-forming reaction in the hydrochloric acid. The alkali is sodium carbonate, potassium carbonate, sodium hydroxide, potassium hydroxide, sodium methoxide, sodium alcoholate or Lewis base.
NOVELTY - A bavachin ether C ring carbonyl reduction product is new.    USE - A bavachin ether C ring carbonyl reduction product for antitumor medicine preparation (claimed).    ADVANTAGE - The bavachin ether C ring carbonyl reduction product is low cost, environment-friendly, promotes normal cell growth, and has high yield, simple separation and purification, and antitumor activity.    DETAILED DESCRIPTION - A bavachin ether C ring carbonyl reduction product of formula (I) is new. An INDEPENDENT CLAIM is included for preparation of bavachin ether C ring carbonyl reduction product which involves subjecting bavachin ether substrate to biocatalyst reaction using Penicillium raistrickki with preservation number ATCC No. 10490.    DESCRIPTION OF DRAWING(S) - The drawing shows a X-ray diffraction spectrum of bavachin ether C ring carbonyl reduction product i.e. (2S,4R)-2-(4-hydroxyphenyl)-1-methoxy-6-(3-methylbutyl-2-enyl)-chroman-4-ol.
NOVELTY - A Bacillus subtilis HR-1019 strain (KACC91711P) capable of solubilizing phosphate, is new.    USE - The B.subtilis HR-1019 strain is used in fertilizer for cultivating leafy vegetables (all claimed).    ADVANTAGE - The B.subtilis is environmentally-friendly and promotes growth of plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizer, which comprises 0.1 pts. wt. B.subtilis HR-1019 strain, 20 pts. wt. N-acetyl-L-thioproline, 80 pts. wt. amino acid powder as an excipient, and dilution agent.
NOVELTY - The system has a wave power generator (20) which is installed between the culture apparatuses (30) through a first connecting rod (5) and a second connecting rod (6). A power supply apparatus (2) and an air compressor (3) are installed on an administration support stand (1). The air compressor is provided for injecting the carbon dioxide into the culture apparatuses. The administration support stand is connected to the wave power generator. The administration support stand controls the administration of carbon dioxide into the culture apparatuses.    USE - System for culturing aquatic biomass e.g. marine microalgae for producing biofuel such as bioethanol and biodiesel using independent power plant.    ADVANTAGE - The aquatic biomass can be cultured effectively using the wave energy continuously generated in underwater of the oceanic environment by the tidal force generator connected to the pond. The bio energy can be produced by increasing the contact of the carbon dioxide with the wave energy. The obtained wave energy is converted into the electric power, so as to increase the productivity of the aquatic biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the system for culturing aquatic biomass using independent power plant.    Administration support stand (1)    Power supply apparatus (2)    Air compressor (3)    First connecting rod (5)    Second connecting rod (6)    Wave power generator (20)    Culture apparatus (30)
NOVELTY - The utility model claims one waste slurry production device's sulfur ammonium phosphate product. The device comprises ammoniation reaction part, mixing part of the slurry circulating part, drying part, crushing and sieving part, a cooling wrap portion and tail gas washing part; the slurry the slurry slag, the granulation/drying granulation, a semi-finished product by crushing and sieving, washing to obtain the qualified's product particles, according to need to add colorant, to obtain sulphur ammonium phosphate product. The utility model adopts production sulphur ammonium phosphate product is nutrient is stable, and uniform and high compressive strength, and greatly reduces the environmental protection caused by the enterprise's pressure.
NOVELTY - This utility new type claims a one environment-friendly garbage bucket, comprise shell, the technology point is: a shell set with upper end is integrally formed with the shell of the top cover, the top cover is above the lamp shell, the lamp shell is set with inner through lead is connected with battery and lighting lamp, of inner shell set with garbage collecting room, top cover set with inner upper garbage entrance, a garbage collecting room and garbage collecting room of set with connected with cavity of support beam, a support beam of inner cavity is filled with thermoelectric conversion material, upper end of support beam through the top cover and the lamp shell, thermoelectric conversion material of inner cavity of the inner lamp shell connecting battery, a top cover of lower upper surface set with microorganism storing box, the storing box surface microorganism is uniformly distributed with through-hole, the upper bottom plate garbage collecting room of the lower part set with fertilizer collecting bucket, a garbage collecting room of uniformly distributed with leaking. This utility new type a the garbage into fertilizer taking two times and the produce of heat into electric energy waste decomposing is illuminating lamp power supply, the garbage bucket with night lighting function.
NOVELTY - Multi-point water inlet work alternately multi layer composite filler denitrification sewage treatment device, include a filler layer of reactor main body, pump is connected with the water inlet of sewage water inlet tube, pump pneuma and controller, a reactor main body through intervals of first vertical clapboard and vertical clapboard is divided into multi-second of reaction room, the first vertical partition board bottom end of the reactor main body, the bottom of the second vertical baffle plate of upper end reactor and the upper part body; reaction room is divided into aerobic area and anaerobic area, an aerobic area and anaerobic area are arranged at intervals; each aerobic area and the bottom of the anoxic area are equipped with aerator, reactor main body two end set with the water outlet, each of reaction room upper end are set with the sewage inlet, a sewage water inlet tube through a branch pipeline and the reaction room connected, forming multi-point water inlet structure, pneuma pump connected with the air inlet of a all of aerator, a controller with a water inlet pump, an aerator. This utility new type of beneficial effects as follows: improving effect of the maximum degree of the sludge.
NOVELTY - This utility new type claims a new-type glass fibre reinforced plastic septic tank one marsh gas tank, septic tank comprise pneuma biogas tank body, a feeding tube, a hydraulic liquid, marsh gas pipe, tank body glass steel section separating plate, upper partition plate lower material liquid flow , the liquid does not need stirring, a swirling mix, pneuma in seal of marsh gas tank body, the waste is changed into treasure, energy-saving and environment-friendly. The tank body is wound once machinery manufacturing method for rotary rotational moulding of glass steel marsh gas tank, high strength, good air tightness, long service life, one tank, the cost is low;
NOVELTY - A one hot vector from the circulation heating type agriculture and forestry waste pyrolysis liquefaction system, belonging to a renewable sources utilization technology field, wherein, comprise in turn connecting circulation of lifting tube burner, a gas-solid separator, hot carrier and carbon powder, V type descending tube reactor, hot carrier separator and hot carrier feeder, wherein, a gas-solid separator and lifting tube burner upper part using connecting pipeline, hot carrier separator through hot carrier and lifting tube burner lower part connecting lifting tube burner lower part connecting with a first biomass feeder, a hot carrier and carbon powder storage hopper connect with a second biomass feeder, V type descending tube reactor upper part connecting third biomass feeder, a lifting tube burner bottom connecting air inlet pipeline, a lifting tube burner in solid as a hot carrier. This utility new type can make full use of the lifting tube burner of heat, high efficiency, low cost and stable operation.
NOVELTY - A silicon carbide base material is prepared by preparing 0.006-0.05 mol.% sodium polyacrylate and alkali solution of hexadecyl trimethyl ammonium bromide, and reacting with ethyl orthosilicate at 30-50 degrees C for 3-5 hours to obtain solution A; and adding vinylidene chloride monomer, azo di-iso butyric acid diester as initiator to solution A and reacting at 40-45 degrees C, uniformly stirring, adding bentonite dispersing agent and reacting for 10-15 hours to obtain particulate polymer precursor; and filtering particulate polymer precursor, washing, drying to obtain desired material.    USE - Method for preparing silicon carbide base material (claimed).
NOVELTY - A highly active oxygen carrier comprises 1-30 wt.% silicon oxide (SiO2) as carrier body, 5-20 wt.% nickel oxide (NiO) as active component, calcium oxide (CaO) as auxiliary agent. The mass content of CaO is 1-20%, preferably 1-10%.    USE - Highly active oxygen carrier used for hydrogen combustion reaction process.    ADVANTAGE - The carrier has small active component particle diameter. It also has high temperature and/or long period operation active high stability. The preparation method is simple.
NOVELTY - Method for recycling and disposing sludge, involves taking sludge as raw material, subjecting the sludge to aerobic fermentation, crushing, screening and hot air drying the fermented sludge, and processing and pressing the dried sludge.    USE - The method is useful for recycling and disposing sludge (claimed).    ADVANTAGE - The method recycles the waste sludge, consumes energy, and reduces emission.
NOVELTY - Fertilizer comprises 3-6 pts. wt. of ferrous sulfate, 1-2 pts. wt. of borax, 42-55 pts. wt. of sheep manure, 5-6 pts. wt. of Bacillus subtilis, 20-30 pts. wt. of lees, 22-28 pts. wt. of potato skins, 25-33 pts. wt. of sugar cane waste, 12-18 pts. wt. of walnut skin, 2-3 pts. wt. of Bacillus pumilus, 6-9 pts. wt. of yeast, 5-7 pts. wt. of Trichoderma, and 26-35 pts. wt. of cow dung.    USE - Vegetable fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing fertilizer comprising weighing the potato skins, sugar cane waste, lees and walnut peel and then heating at 120 degrees C for 30 minutes and naturally cooling to 40 degrees C to obtain mixture and then adding to Bacillus subtilis, Bacillus pumilus and Trichoderma and sealing for 8-11 days, adding cow dung in the sealed mixture and then stirring for 4-6 days, adding the ferrous sulfate and borax to the sealed mixture and then stirring, naturally drying and grinding into powder.
NOVELTY - Organic fertilizer comprises 30-75 pts. wt. livestock and poultry excrement, 2-3 pts. wt. calcium superphosphate, 2-7 pts. wt. fly ash, 10-25 pts. wt. edible fungus waste and 0.08-0.3 pts. wt. fermentative bacteria.    USE - As organic fertilizer (claimed).    ADVANTAGE - The fertilizer has convenient raw material source, has improved phosphorus content and nitrogen content. The fermentation process is simple and cost-effective, and produces malodorous gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves crushing livestock and poultry excrement, adding edible fungi waste, calcium superphosphate, and fly ash, uniformly mixing components, stacking mixture in a fermentation groove, performing primary fermentation, until fermented material is brown and odorless, drying, granulating, sieving, checking and packaging product.
NOVELTY - Biological fertilizer comprises microorganism strain and biological organic fertilizer. The microorganism strain is Bacillus subtilis or B.brevis. The biological organic fertilizer comprises 10-20 %mass microbial strain agent, 20-30 %mass humic acid, 30-60 %mass calcium nitrate or nitric acid phosphate, 5-10 %mass boric acid, 5-12 %mass magnesium sulfate, 5-8 %mass ferrous sulfate, 1.5-5 %mass organic matter, 2-6 %mass sulfur powder, 0.5-1 %mass bentonite and 1-5 %mass inducing agent.    USE - As biological fertilizer.    ADVANTAGE - The fertilizer improves nutritive value of fertilizer raw material, soil physicochemical property, and soil structure, and adjusts pH of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) inoculating B.subtilis or B.brevis into inclined plane culture medium, and culturing medium at 28 degrees C for 48 hours, (b) sterilizing 100 ml liquid seed culture medium, adding activated strain to obtain seed culture medium, and culturing medium at 32 degrees C for 16-20 hours to obtain seed liquid, (c) inoculating the 50-100 ml seed liquid into culture medium, culturing medium at 32 degrees C for 10 hours to obtain fermentation liquid, and adding oxalic acid, and calcium carbonate as absorbent in a ratio of 1:8, where the inclined plane culture medium comprises 10-20 g/l sugarcane, 0.5-5 g/l dipotassium hydrogen phosphate, 0.2-5 g/l platinum chloride, 1-10 g/l silicon dioxide, 0.2-5 g/l magnesium sulfate, 1-10 g/l calcium carbonate, 0.4-5 g/l yeast extract and 10-20 g/l agar (pH 7.2-7.4) and seed culture medium comprises 1-5 g/l sugar, 1-5 g/l dipotassium hydrogen phosphate, 0.7-5 g/l yeast extract, 0.2-5 g/l sulfuric acid, 1-5 g/l peptone and 0.2-5 g/l calcium sulfate (pH 7.2-7.4).
NOVELTY - Method for preparing seedlings matrix material plate of fresh crop, involves uniformly mixing livestock manure, straw chips, and starch to obtain solid mixture, adding effective microorganisms (EM) raw liquid, sugar and water, uniformly mixing materials, fermenting mixture for 10-15 days, adding chemical fertilizer, uniformly mixing, adding 3.5-4.5 pts. wt. biological insecticidal substance, uniformly mixing, pressing the mixture into blanks, and drying obtained substrate material plate until the water content is less than 10%.    USE - The method is useful for preparing seedlings matrix material plate (all claimed) which is used for cultivating vegetable shoots.    ADVANTAGE - The method reduces agricultural waste, is environmentally-friendly and cost-effective and improves quality of life.    DETAILED DESCRIPTION - Method for preparing seedlings matrix material plate of fresh crop, involves uniformly mixing 90-110 pts. wt. livestock manure, 90-110 pts. wt. straw chips, and 18-22 pts. wt. starch to obtain solid mixture, adding 2-3 pts. wt. effective microorganisms (EM) raw liquid, 2-3 pts. wt. sugar and 20-30 pts. wt. water, uniformly mixing materials, fermenting mixture for 10-15 days, adding 4-6 pts. wt. chemical fertilizer, uniformly mixing, adding 3.5-4.5 pts. wt. biological insecticidal substance, uniformly mixing, pressing the mixture into blanks, and drying obtained substrate material plate until the water content is less than 10%.
NOVELTY - A hydrogenated butadiene exhaust system comprises butadiene exhaust (1), absorbent (2), phase mixture (3), hydrogen (4), reaction product (5), non-condensing gas, absorption tower, booster pump, hydrogenation reactor and desorption tower.    USE - Hydrogenated butadiene exhaust system.    ADVANTAGE - The exhaust system is simple and energy efficient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for process of hydrogenation method of comprising absorbing, adding hydrogen, entering into hydrogenation device, carrying out hydrogenation reaction, and desorbing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of hydrogenated butadiene exhaust system.    Butadiene exhaust (1)    Absorbent (2)    Phase mixture (3)    Hydrogen (4)    Reaction product (5)
NOVELTY - M15 Methanol gasoline vapor pressure stabilizer comprises 18-31 %mass tert-butyl-N-(3-aminopropyl)-N-methyl-carbamate, 15-29.5 %mass 2-dimethylamino-2-methyl-1-propanol, 15-24.5 %mass 6-methyl-3,5-heptadien-2-one, 13-24 %mass diethylphosphonoacetic acid tert-butyl ester and 10-20.5 %mass 2,2,5,5-tetramethyltetrahydrofuran, as raw materials.    USE - Vapor pressure stabilizer is used for M15 Methanol gasoline.    ADVANTAGE - The stabilizer reduces vapor pressure of M15 Methanol gasoline.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of M15 Methanol gasoline vapor pressure stabilizer, which involves mixing raw materials at room temperature.
NOVELTY - An oil sludge granule fuel comprises oil-containing sludge and coal powder in the weight ratio of 5-15:95-85. The oil sludge granule fuel has grain diameter of less than 10 mm and water content of less than 10 wt.%.    USE - Oil sludge granule fuel is used for fluidized bed boiler.    ADVANTAGE - The oil sludge granule fuel is economical and environmentally-friendly. The occurrence of agglomeration of granules in the oil sludge granule fuel is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of oil sludge granule fuel, which involves dissolving a mixture containing oil sludge and coal powder in water, stirring, granulating, drying, sieving, and obtaining the oil sludge granule fuel.
NOVELTY - Blue algae raw material is dried, crushed into powder, and fed into a reaction furnace at 400-600 degrees C. The reaction furnace is filled with quartz sand having a particle diameter of 0.45-0.63 mm. The lower portion of furnace is connected with a nitrogen blower. Nitrogen is blown and the quartz sand is fluidized. The residence time of material in the reaction furnace is 15-25 minutes. The obtained gas-solid mixture is separated in a cyclone dust collector. The gas is condensed to obtain bio-oil.    USE - Preparation of bio-oil from blue algae (claimed).    ADVANTAGE - The method enables preparation of bio-oil with a yield of more than 50%, which is improved by 20% or more.    DETAILED DESCRIPTION - Blue algae raw material is dried and crushed into powder with a grain diameter of 0.2-0.45 mm. The powder is fed from a feed port at 3.5-4.5 kg/hour into a reaction furnace at 400-600 degrees C. The reaction furnace is filled with quartz sand having a particle diameter of 0.45-0.63 mm. The mass ratio of quartz sand and raw material is 15-25:75-85. The lower portion of furnace is connected with a nitrogen blower. Nitrogen is blown and the quartz sand is fluidized. The residence time of material in the reaction furnace is 15-25 minutes. The obtained gas-solid mixture is separated in a cyclone dust collector. The gas is condensed to obtain bio-oil.
NOVELTY - Preparing bio-diesel involves: constructing recombinant plasmid lipase gene and ligating it to a target recombinant plasmid and transforming in competent cells of Pichia pastoris to obtain high copy target gene transformant; subjecting recombinant engineered yeast cell to induction to form yeast cells expressing the intracellular lipase, in the form of wet whole cells; subjecting cells to permeability treatment using short-chain alcohols to give transparent whole yeast cells (C1); and synthesizing oils and short chain alcohols in a substrate using (C1) as catalyst.    USE - For preparing bio-diesel using Pichia pastoris and lipase (claimed).    ADVANTAGE - The present process is simple; doesn't provide pollution; provides bio-diesel with high yield; has low cost; and also provides good economic and social benefit.    DETAILED DESCRIPTION - Preparing bio-diesel using Pichia pastoris and lipase involves: (1) constructing recombinant plasmid lipase gene and ligating it to a target recombinant plasmid and then transforming in competent cells of Pichia pastoris to obtain high copy target gene transformant; (2) induction step: involving subjecting recombinant engineered yeast cell to accumulation stage and lipase induced phase culture methods, to form yeast cells expressing the intracellular lipase, in the form of wet whole cells; (3) subjecting cells to permeability treatment using short-chain alcohols and/or freeze-dried whole cells to give transparent whole yeast cells; and (4) synthesizing oils and short chain alcohols in a substrate using the transparent whole yeast cell as catalyst, optionally in presence of a solvent system to form biodiesel.
NOVELTY - An industrial bio-diesel preparing method involves selecting soybean oil, cotton seed oil, palm oil or coptis wood seed oil as raw material and dissolving the raw material in 0.1% methanol. The resulting solution is reacted in presence of 0.5-1.5% sodium hydroxide or potassium hydroxide as catalyst.    USE - Method for preparing industrial bio-diesel.    ADVANTAGE - The method enables preparing industrial bio-diesel in a safe and time saving manner, ensuring high safety, preventing oil from deterioration and achieving national standard requirements.
NOVELTY - A synthetic biological alcohol oil is obtained by mixing potassium hydroxide and water in weight ratio of 0.8-0.95:2, cooling, adding sodium hydroxide and water in weight ratio of 0.8-0.95:2, cooling, mixing potassium hydroxide aqueous solution and sodium hydroxide aqueous solution, cooling, adding ethyl acetate, anhydrous ethanol and combustion-supporting agent.    USE - Synthetic biological alcohol oil (claimed).    ADVANTAGE - The synthetic biological alcohol oil is environmentally-friendly, and has excellent storage stability.
NOVELTY - This new type utility claims one a multifunctional integrated marsh gas tank, comprise one level and second level marsh gas tank, marsh gas tank upper first-stage marsh gas tank and the bottom of second level marsh gas tank set with filter plate, the filter plate is equipped with two group, one level marsh gas tank and inner gas storage room of second level marsh gas tank set with methane sensor and carbon dioxide sensor, one level marsh gas tank and the top part of second level marsh gas tank set with air outlet, air outlet and two marsh gas collecting room connect. Material rear one level of marsh gas tank fermenting, through filter plate feeding to second level inner marsh gas tank fermenting process, the material classification, not only increases the fermentation rate, but also improves the fermentation efficiency, two biogas pool production of marsh gas pipeline conveying to the gas collection chamber to prevent the inner the marsh gas tank, marsh gas is good for reasonable use of the inner tank is equipped with marsh gas methane sensor and carbon dioxide sensor can be of gas inner storage room for a valid.
NOVELTY - A sewage treatment system comprises biochemical tank divided into anaerobic area (7) and aerobic area (8) by wall. The anaerobic area has at least one stirrer (1) on entrance. The aerobic area has aerator (3), water decanter, activating strain entrance and residual sludge exit. The biochemical tank is set with return sludge pipeline (13).    USE - Sewage treatment system.    ADVANTAGE - The method uses cyclic activated sludge system tank as biochemical tank to improve sludge retention. It reduces impacts of temperature and water quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sewage processing comprising adding ammonia-nitrogen strain into container, opening jet aeration device for 22-26 hours to obtain sludge-water mixture, controlling dissolved oxygen content, precipitating and activating.    DESCRIPTION OF DRAWING(S) - The drawing shows a plan view of sewage treatment system.    Stirrer (1)    Aerator (3)    Anaerobic area (7)    Aerobic area (8)    Return sludge pipeline (13)
NOVELTY - Use of composite microbial inoculum is claimed for processing petrochemical sewage sludge.    USE - The composite microbial inoculum is useful for processing petrochemical sewage sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing biological carrier, which involves adding glutaraldehyde into polyphenylene oxide, washing, adding phosphate buffered saline and calcium chloride, allowing to stand, performing microbial inoculum expanded culture, preparing biological carrier, placing the biological carrier in petrochemical sewage, continuously added to stationary phase, forming biomembrane surface biological carrier which allows metabolism, adsorption, absorption, digestion and decomposition of organic pollutant in petrochemical sewage, and thus converting harmful substance into harmless substance.
NOVELTY - Short range nitration and denitrification process comprises inoculating 30-50 vol.% of 2000-4000 mg/L activated sludge using sequencing batch reactor, adjusting pH value to 7.5-8.0 and chemical oxygen demand concentration to 500-800 mg/L, ammonium influent concentration to 200-400 mg/L and total phosphorus concentration to 20-40 mg/L, controlling dissolved oxygen to 0.5-2 mg/L at 22-28 degrees C for 16-24 hours, carrying out single-cycle aeration for 300-400 minutes, settling for 15-25 minutes and standing for 60-l20 days to allow nitrite accumulation and obtain ammonia-oxidizing microorganism.    USE - Method for carrying out short range nitration and denitrification process.    ADVANTAGE - The method is simple.
NOVELTY - The inner automatic building pit tank has a toilet drain sewer pipeline which is connected an inner underground pit tank at middle portion. The pipeline valves are provided to cover the surface of the pool in the shade well. The overcast underground wells are provided near the kitchen. The inner pit tank is connected to the coal gas stove valve by pipeline.    USE - Inner automatic building pit tank for extracting marsh gas.    ADVANTAGE - The inner automatic building pit tank for extracting marsh gas ensures environment-friendly and high utilization in efficient manner.
NOVELTY - Wastewater treatment system comprises digesters (1), pipeline, pressure valve, exhaust pipe (3), biogas tank (5), gas pipe, biogas digester discharge pipe (2), excrement feed pipe (6) and excrement drainage.    USE - Wastewater treatment system.    ADVANTAGE - The system has continuous marsh gas production.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of wastewater treatment system.    Digesters (1)    Biogas digester discharge pipe (2)    Exhaust pipe (3)    Biogas tank (5)    Excrement feed pipe (6)
NOVELTY - Method for processing kitchen waste, involves collecting kitchen waste, culturing microorganisms, mixing collected kitchen waste and cultured microorganism, standing and fermenting, where the microorganisms is Saccharomyces cerevisiae.    USE - The method is useful for processing kitchen waste, which is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The organic fertilizer increases root nodule in soybean and chlorophyll content in soybean leaves during summer and improves yield and promotes income of farmers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of products preferably organic fertilizer, which involves using kitchen waste.
NOVELTY - An excrement composting microbial inoculum agent comprises beneficial microorganism, organic matter biodegradation speed factor, and heavy metal binding material at mass ratio of 1-2:3-5:4-6. The beneficial microorganism comprises photosynthetic bacteria, lactic acid bacteria, Bacillus, microzyme, fungus, actinomycetes, nitrogen-fixing bacteria, Trichoderma and nitrifying bacteria. The organic matter biodegradation speed factor comprises 5-15 wt.% inorganic salt, 0.1-0.6 wt.% synergistic cellulase protein, 1-6 wt.% organic acid, and balance water-soluble saccharide.    USE - Excrement composting microbial inoculum agent.    ADVANTAGE - The microbial inoculum agent can reduce manure composting odor pollution, heavy metal pollution and material shortage.    DETAILED DESCRIPTION - An excrement composting microbial inoculum agent comprises beneficial microorganism, organic matter biodegradation speed factor, and heavy metal binding material at mass ratio of 1-2:3-5:4-6. The beneficial microorganism comprises photosynthetic bacteria, lactic acid bacteria, Bacillus, microzyme, fungus, actinomycetes, nitrogen-fixing bacteria, Trichoderma and nitrifying bacteria. The organic matter biodegradation speed factor comprises 5-15 wt.% inorganic salt, 0.1-0.6 wt.% synergistic cellulase protein, 1-6 wt.% organic acid, and balance water-soluble saccharide. The heavy metal binding material is bentonite molecular sieve or fly ash molecular sieve. An INDEPENDENT CLAIM is included for excrement compost treatment, comprising diluting excrement composting microbial inoculum agent with water for 8-10 times, and then adding into 50-60 wt.% excrement and uniformly stirring.
NOVELTY - Phosphate fertilizer is prepared by mixing animal manure and fertilizer in a ratio of 3:1, crushing the obtained mixture, piling the obtained mixture, covering the pile with a layer of loam, maintaining for 4 weeks and then covering with a layer of normal soil, making a concave hole on the top of the pile, adding human and animal manure into the hole, preventing from leaking, closing the hole with mud, maintaining for 10 days, turning for 1 time, and drying the finished product.    USE - As phosphate fertilizer.    DETAILED DESCRIPTION - Phosphate fertilizer is prepared by mixing animal manure and fertilizer in a ratio of 3:1, crushing the obtained mixture, piling the obtained mixture, covering the pile with a layer of loam, maintaining for 4 weeks and then covering with a layer of normal soil, making a concave hole on the top of the pile, adding human and animal manure into the hole, preventing from leaking, closing the hole with mud, maintaining for 10 days, turning for 1 time, and drying the finished product, where during summer the drying process is performed for 20 days and during winter the drying process is performed for 25-30 days.
NOVELTY - Production of cassava residue decomposition agent comprises mixing filter mud, manioc waste and bagasse ash at weight ratio of 3-4:3-4:2, adding microbial cells, fermenting for 25-40 days, crushing and drying at low temperature to obtain straw rotten agent.    USE - Method of production of cassava residue decomposition agent (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the production of cassava residue decomposition agent (Drawing includes non-English language text).
NOVELTY - Use of filter mud, cassava residue and alcohol waste mash, is claimed for producing straw decomposition agent. The straw decomposition agent is prepared by mixing filter mud, cassava residue and alcohol waste mash in a weight ratio of 3-4:3-4:2, adding microbial cells to the obtained mixture, mixing uniformly and fermenting for 15-30 days, crushing and drying at low temperature to obtain finished product, where the microbial cells are Aspergillus niger and Aspergillus oryzae (1-4:1-4), and the total weight of the raw materials is 2-8%.    USE - The filter mud, cassava residue and alcohol waste mash are useful for producing straw decomposition agent (claimed). The straw includes banana straw, corn straw, wheat straw, rice straw and rape straw.    ADVANTAGE - The filter mud, cassava residue and alcohol waste mash enable to produce straw decomposition agent cost-effectively, and improves fiber content of domestic garbage.
NOVELTY - Production of cassava residue decomposition agent comprises mixing filter mud, manioc waste and bagasse ash at weight ratio of 3-4:3-4:2, adding microbial cells, fermenting for 5-10 days, crushing and drying at low temperature.    USE - Method of production of cassava residue decomposition agent (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the production of cassava residue decomposition agent (Drawing includes non-English language text).
NOVELTY - Method for fermenting solid organic matter, involves (a) crushing straw into 25-35 meshes of fine powder until the water content is 10-20%, uniformly mixing fine powder having water content of 75-85% and municipal sludge in a ratio of 25-30:1, (b) drying mixture until the water content is 60-65%, uniformly mixing urea, powdered rock phosphate, potassium chloride and biological humic acid, and preparing to water content of 50-55%, and (c) filtering the mixture, fermenting mixture, and maintaining fermentation temperature.    USE - The method is useful for fermenting solid organic matter (claimed).    ADVANTAGE - The method provides high quality, and is simple, environmentally-friendly and easy to carry out.    DETAILED DESCRIPTION - Method for fermenting solid organic matter, involves (a) crushing straw into 25-35 meshes of fine powder until the water content is 10-20%, uniformly mixing fine powder having water content of 75-85% and municipal sludge in a ratio of 25-30:1, where the weight ratio of the straw powder and sludge is 1:8-12, (b) drying mixture until the water content is 60-65%, uniformly mixing urea, powdered rock phosphate, potassium chloride and biological humic acid, and preparing to water content of 50-55%, where weight ratio of the mixed material, urea, powdered rock phosphate, potassium chloride, and biological humic acid is 100:1-2:8-10:1-2:0.3-0.6, and (c) filtering the mixture, fermenting mixture for 24-48 hours, and maintaining fermentation temperature at 60-70 degrees C.
NOVELTY - Biological fertilizer comprises animals fed with mud feed fermentation bed material as main raw material, and crop straw as auxiliary material to indigenous bacteria.    USE - Biological fertilizer.    ADVANTAGE - The fertilizer has low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological fertilizer comprising mixing crop straw material, crushing to 20-50 meshes, adding on fermenting bed, mixing with indigenous bacteria, and stirring to obtain mixed material; adjusting water content of material to 55-60%; mixing raw material, piling at high length of 1-1.2 mm, width of 2-3 strip-shaped stack, fermenting for 12-20 days to obtain raw material; and drying at low temperature, adjusting water content to less than 8%, and packing in bag.
NOVELTY - Method for processing dead pig and pig manure compost, involves mixing pig manure and auxiliary material, uniformly mixing materials, lifting dead pig of more than 100, feeding young pig after birth, covering material with dead pig stack, stacking mixture using ventilation quantity of 60-100 l/minutes and fermenting compost for 42 days.    USE - The method is useful for processing dead pig and pig manure compost (claimed).    ADVANTAGE - The method does not use special device, and is simple, cost-effective and environmentally-friendly.
NOVELTY - An organic fertilizer is prepared by taking 25-60 pts. wt. ground bentonite ore, 20-70 pts. wt. livestock manure, 20-80 pts. wt. traditional Chinese medicine slag, 1-2.5 pts. wt. effective microorganism biological agents, and 10-20 pts. wt. straw ash, fermenting at room temperature for 7-45 days, turning over, aging for 5-10 days, drying, and granulating.    USE - Method for preparing organic fertilizer.    ADVANTAGE - The fertilizer improves soil structure, and crop quality.
NOVELTY - Watermelon seedling matrix comprises raw materials comprising 15-30 pts. coconut shell powder base material, 15-30 pts. alcohol fermented biogas residue, 15-25 pts. carbonized rice hull, 1-2 pts. stillage, 5-10 pts. perlite, and 15-25 pts. vermiculite. The coconut shell powder base material is obtained from domestic or imported coconut shell. The carbonized rice hull is obtained by burning of rice hull.    USE - As watermelon seedling matrix.    ADVANTAGE - The watermelon seedling matrix is cost-effective and highly nutritious, and has light texture.    DETAILED DESCRIPTION - Watermelon seedling matrix comprises raw materials comprising 15-30 pts. coconut shell powder base material, 15-30 pts. alcohol fermented biogas residue, 15-25 pts. carbonized rice hull, 1-2 pts. stillage, 5-10 pts. perlite, and 15-25 pts. vermiculite. The coconut shell powder base material is obtained from domestic or imported coconut shell. The alcohol fermented biogas residue is obtained by extracting leftover of cassava using alcohol, fermenting the obtained extract (anaerobic fermentation), digesting the obtained extract in biogas, drying the obtained product, and crushing the obtained product to particle size of 1-3 mm. The carbonized rice hull is obtained by burning of rice hull. An INDEPENDENT CLAIM is included for method for preparing the above-mentioned watermelon seedling matrix, which involves drying the alcohol fermented biogas residue till water content of 25-35%, and crushing to a particle size of 3 mm, drying the coconut shell powder base material till water content of 40-50%, and crushing to a particle size of 1-6 mm, drying the stillage till water content of 20% and crushing to 50 mesh size, and crushing the carbonized rice hull to 50 mesh size, (b) mixing the products obtained in step (a), (c) adding the above-mentioned perlite and vermiculite to the obtained mixture, and (d) packing the obtained product in bag (each nag contains 0.01-0.1 m3 product).
NOVELTY - A biochar-based conditioning agent (I) comprises 75-85 mass % biomass-derived granular char and 15-25 mass % wood vinegar. The biomass-derived granular char consists of corncob, rice husk, peanut shell, rice straw and/or mushroom biomass-derived granular char prepared via biomass carbonization. The wood vinegar is obtained by condensing the biomass carbonization furnace gas generated during preparation of biomass-derived granular char, standing the condensed liquid for 48 hours to obtain suspension, and mixing with water based on 1:1 ratio to obtain acidic liquid, namely wood vinegar.    USE - Biochar-based conditioning agent (I) used for livestock and poultry manure compost fertilizer (claimed).    ADVANTAGE - The biochar-based conditioning agent (I) can quickly raise the temperature in the manure composting process, prolong the duration of composting under high temperature condition, improve the dehydration effect in the compost product, reduce the composting process nitrogen loss and odor pollution, increase the organic phosphorus content and reduce the heavy metal concentration in the compost product, thus it has wide application prospect in agricultural industry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for application of biochar-based conditioning agent (I) in livestock and poultry manure compost fertilizer, comprising mixing 2-6 mass % (based on total weight of resulting mixed material) biochar-based conditioning agent (I), fresh livestock and poultry manure, sawdust, and rotten livestock and poultry manure; and then composting to obtain livestock and poultry manure compost fertilizer.
NOVELTY - A fermented fruit tree fertilizer comprises 34-38 pts. wt. calcium phosphate; 24-27 pts. wt. urea; 16-18 pts. wt. potassium chloride; 20-23 pts. wt. ammonium persulfate; 10-12 pts. wt. active carbon; 10-12 pts. wt. bean dregs powder; 4-6 pts. wt. pepper powder; 3-4 pts. wt. chitin; 3-4 pts. wt. effective microorganism; 4-6 pts. wt. water; and coating agent.    USE - A fermented fruit tree fertilizer.    ADVANTAGE - The fertilizer has improved utilization ratio, is quick and can supplement all nutrition element for plants, enhances disease resistance and drought resistance of plant, increases yield of plant, and improves plant quality.    DETAILED DESCRIPTION - A fermented fertilizer comprises 34-38 pts. wt. calcium phosphate; 24-27 pts. wt. urea; 16-18 pts. wt. potassium chloride; 20-23 pts. wt. ammonium persulfate; 10-12 pts. wt. active carbon; 10-12 pts. wt. bean dregs powder; 4-6 pts. wt. pepper powder; 3-4 pts. wt. chitin; 3-4 pts. wt. effective microorganism; 4-6 pts. wt. water; and coating agent containing 20-22 pts. wt. chlorinated paraffin, 10-12 pts. wt. dipentaerythritol hexaacrylate, 2-3 pts. wt. silane coupling agent KH-570, 1-2 pts. wt. aluminum trichloride, 2-3 pts. wt. aluminum oxide, 1-2 pts. wt. crosslinking agent triallyl cyanurate, nanocarbon 0.1-0.2 pts. wt. nano carbon, 2-3 pts. wt. gluconate, and 1-2 pts. wt. zinc gluconate, and is prepared by mixing raw material, grinding and dispersing to obtain product.
NOVELTY - Continuous peanut cropping high-yield agent is prepared by taking humic acid, peat, calcium sulfate, magnesium sulfate, zinc sulfate, manganese sulfate, ferrous sulfate, borax, rare earth nitrate, ammonium citrate, rhododendron molle, marigold, ningnanmycin, Verticillium fungus and Bacillus subtilis as raw materials; crushing humic acid and peat powder, adding other raw materials except ningnanmycin, mixing, adding water, spraying ningnanmycin, introducing into forming machine, extruding and molding.    USE - Method for preparing continuous peanut cropping high-yield agent (claimed).    ADVANTAGE - The agent improves soil environment, nutrient balance and fertilizer effect, establishes soil bacteria growth and propagation environment, and ensures healthy and strong peanut.    DETAILED DESCRIPTION - Continuous peanut cropping high-yield agent is prepared by taking 30-40 wt.% humic acid, 25-35 wt.% peat, 10-20 wt.% calcium sulfate, 5-8 wt.% magnesium sulfate, 3-5 wt.% zinc sulfate, 3-5 wt.% manganese sulfate, 5-8 wt.% ferrous sulfate, 3-5 wt.% borax, 1-2 wt.% rare earth nitrate, 0.1-1.5 wt.% ammonium citrate, 0.5-3 wt.% rhododendron molle, 0.5-3 wt.% marigold, 0.3-1.5 wt.% 8% ningnanmycin and 1-2 wt.% Verticillium fungus and 1-2 wt.% Bacillus subtilis as raw materials; crushing humic acid and peat into 20-60 mesh powder, adding other raw materials except ningnanmycin, mixing uniformly for 10-15 minutes, adding 2 times water to dilute, spraying ningnanmycin, stirring, introducing into forming machine, extruding and molding.
NOVELTY - Sheep manure fertilizer comprises sheep manure, straw powder, urea, phosphonium acid, potassium chloride, kaolin, montmorillonite, silicon dioxide, microbial inoculum, film-forming agent and water. The film-forming agent comprises paraffin, dipentaerythritol hexaacrylate, silane coupling agent, aluminum trichloride, aluminum oxide, crosslinking agent, nanocarbon, mineral powder and gluconate.    USE - Sheep manure fertilizer used for improving soil organic matter content and soil buffering ability.    ADVANTAGE - The sheep manure fertilizer improves crop yield and plant quality.    DETAILED DESCRIPTION - Sheep manure fertilizer comprises 100-120 pts. wt. sheep manure, 20-23 pts. wt. straw powder, 23-25 pts. wt. urea, 34-36 pts. wt. phosphonium acid, 16-18 pts. wt. potassium chloride, 12-14 pts. wt. kaolin, 4-5 pts. wt. montmorillonite, 2-3 pts. wt. silicon dioxide, 3-4 pts. wt. microbial inoculum, 4-6 pts. wt. film-forming agent and balance water. The film-forming agent comprises 20-22 pts. wt. paraffin, 10-12 pts. wt. dipentaerythritol hexaacrylate, 2-3 pts. wt. silane coupling agent, 2-3 pts. wt. aluminum trichloride, 1-2 pts. wt. aluminum oxide, 1-2 pts. wt. crosslinking agent, 0.1-0.2 pt. wt. nanocarbon, 2-3 pts. wt. mineral powder and 1-2 pts. wt. gluconate. An INDEPENDENT CLAIM is included for the preparation of sheep manure fertilizer comprising crushing dried sheep manure, mixing, adding straw powder, kaolin, montmorillonite, silicon dioxide and water, mixing slurry, adding microbial inoculum, stirring, fermenting for 20-30 days, adding urea, phosphonium acid, potassium chloride and balance raw materials, mixing, drying and granulating.
NOVELTY - Rice cropping agent is prepared by sieving peat, and biogas residue, mixing peat powder, residue powder, ammonium humate, sodium silicate, magnesium amino acid chelate, zinc amino acid chelate, manganese amino acid chelate, boron amino acid chelate, rare earth nitrate, dicyanamide, polyaspartic acid, Bacillus subtilis, and Verticillium, mixing for 10-15 minutes, diluting 3% emulsifiable concentrate into 2 times water, atomizing aqueous solution, and spraying material into mixture, mixing and stirring into extrusion molding machine, extruding and molding.    USE - Rice cropping agent used for increasing yield and disease resistance (claimed).    ADVANTAGE - The agent improves environment soil nutrient.    DETAILED DESCRIPTION - Rice cropping agent is prepared by taking 30-35 pts. wt. peat, 30-35 pts. wt. biogas residue, 15-20 pts. wt. ammonium humate, 5-8 pts. wt. sodium silicate, 1-3 pts. wt. magnesium amino acid chelate, 1-3 pts. wt. zinc amino acid chelate, 1-3 pts. wt. manganese amino acid chelate, 1-3 pts. wt. boron amino acid chelate, 1-3 pts. wt. rare earth nitrate, 0.5-3 pts. wt. dicyandiamide, 1-3 pts. wt. polyaspartic acid, 1- pts. wt. Bacillus subtilis, 1-2 pts. wt. Verticillium, 0.5-2 pts. wt. azadirachtin ( 3% emulsifiable concentrate); sieving peat, and biogas residue through 20-60 mesh sieve, mixing peat powder, residue powder, ammonium humate, sodium silicate, magnesium amino acid chelate, zinc amino acid chelate, manganese amino acid chelate, boron amino acid chelate, rare earth nitrate, dicyanamide, polyaspartic acid, Bacillus subtilis, and Verticillium, mixing for 10-15 minutes, diluting 3% emulsifiable concentrate into 2 times water, atomizing aqueous solution, and spraying material into mixture, mixing and stirring into extrusion molding machine, extruding and molding.
NOVELTY - Rice seedlings seeds soil cover composition comprises 3-5 pts. wt. Agaricus bisporus decomposed soil mix material, 2-3 pts. wt. edible fungi leftovers, 1-2 pts. wt. river low pond mud, permafrost or humus, 2-3 pts. wt. chaff rice husk ash, and 0.1-0.3 wt.% soil conditioner.    USE - Rice seedlings seeds soil cover composition.    ADVANTAGE - The composition ensures good effect and promotes healthy and strong seedling growth.    DETAILED DESCRIPTION - Rice seedlings seeds soil cover composition comprises 3-5 pts. wt. Agaricus bisporus decomposed soil mix material, 2-3 pts. wt. edible fungi leftovers, 1-2 pts. wt. river low pond mud, permafrost or humus, 2-3 pts. wt. chaff rice husk ash, and 0.1-0.3 wt.% soil conditioner. Edible fungi leftover is leftovers of needle mushroom, oyster mushroom, Hypsizygus marmoreus, Pleurotus eryngii and wood rot fungi. Rice seedlings seeds soil cover composition is prepared by mixing Agaricus bisporus decomposed soil mix material and high temperature fast rotting agent and fermenting for 15-20 days, preprocessing chaff rice husk ash, river pond mud, permafrost or humus, fermenting for 15- 30 days, natural composting mushroom grass soil for 1 year, fermenting for 15-30 days, crushing, drying, sieving, adding soil conditioner and disinfectant, metering and packaging. The high temperature fast rotting agent is Actinomycetes, Saccharomycetes, lactic acid bacteria or Bacillus with valid active bacteria of 0.5-1 million units/g. The soil cover has less than 50% water content, more than 30% organic matter, 60-75% total porosity, 0.35-0.6 g/ml bulk density, 1.5-2% total nutrient content, 5.5-7 pH, 3 mS/cm effective concentration value and not greater than 4.5 mm granularity. Soil conditioner contains pure natural soil conditioner, sulfuric acid and organic material.
NOVELTY - Producing terpineol comprises adding 35-45 mass% of phosphoric acid and then mixing with 100 pts. wt. of turpentine, 10-150 pts. wt. of acid catalyst, and 0.01-5 pts. wt. of emulsifier and then string in an autoclave at 60 plus minus 10 degrees C, heating and reacting for 4-8 hours to obtain reaction solution and then separating, washing the materials with water into a reactor and standing, washing the organic phase with hydrochloric acid, adding alkaline to adjust pH using alkaline and then mixing with water and standing, separating solids and then mixing with remaining materials for fractionation.    USE - The method is useful for producing terpineol (claimed).    ADVANTAGE - The method is capable of simply producing terpineol in an economical manner with less energy consumption and high purity and yield.
NOVELTY - Carbon dioxide supercritical extraction of paeonol comprises washing raw moutan bark, drying and ventilating, milling, crushing, adding ethanol, ultrasonically stirring, filtering, drying, adding beta -cyclodextrin, granulating, sieving, and drying; mixing with emu oil, adding to supercritical extraction kettle, injecting carbon dioxide fluid, and extracting; and taking out extract, refrigerating, automatically layering to obtain pale yellow liquid upper layer and reddish brown solid lower layer, and collecting high-purity liquid.    USE - Method for carbon dioxide supercritical extraction of paeonol (claimed).    ADVANTAGE - The method in nontoxic, has simple extraction process with high extraction rate, low extraction temperature, short extraction time and no residue, achieves extraction yield of up to more than 1.4%, and saves energy consumption.    DETAILED DESCRIPTION - Carbon dioxide supercritical extraction of paeonol comprises:    (A) washing raw moutan bark, drying and ventilating until moisture is less than 10%, milling, crushing into 40-60 mesh powder, adding 3-4 times ethanol, ultrasonically stirring at ultrasonic power of 500-600 W and frequency of 20-25 Hz at intervals of 10-15 seconds for 20-30 minutes, filtering, drying, adding beta -cyclodextrin at mass ratio of 2-3:1, granulating, sieving through 20-40 mesh, and drying;    (B) mixing 0.2-20 wt.% powder with emu oil, adding to supercritical extraction kettle, injecting 2-3 L/hour carbon dioxide fluid, and extracting to 40-55 degrees C at 15-35 MPa for 2-3 hours; and    (C) taking out extract, refrigerating to - 5-5 degrees C for 1-2 hours, automatically layering to obtain pale yellow liquid upper layer and reddish brown solid lower layer, and collecting high-purity liquid.
NOVELTY - Separation and purification of eicosapentaenoic acid (EPA) comprises dissolving crude EPA in methanol, and filtering to obtain sample solution; mixing 80-95 wt.% methanol and water to obtain mobile phase, pumping sample solution into dynamic axial compression column with filler, eluting with mobile phase, collecting target component, and purifying through high-performance liquid chromatography; and collecting fractions, and concentrating.    USE - Method for separation and purification of eicosapentaenoic acid (claimed).    ADVANTAGE - The method is simple and pollution-free and has high extraction rate and purity which is suitable for large-scale industrial production.
NOVELTY - Preparing febuxostat (I), comprises carrying out hydrolysis of benzyl 2-(3-cyano-4-isobutoxyphenyl)-4-methylthiazole-5-carboxylate (V) in presence of a hydrolysis catalyst.    USE - The method is useful for preparing febuxostat (claimed).    ADVANTAGE - The method: produces febuxostat with an yield of more than 90% and purity of more than 99%; avoids usage of toxic cyanide; utilizes economic and environment-friendly dehydrating agent; and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing febuxostat of formula (I), comprises carrying out hydrolysis of benzyl 2-(3-cyano-4-isobutoxyphenyl)-4-methylthiazole-5-carboxylate of formula (V) in presence of a hydrolysis catalyst.
NOVELTY - Extracting high purity eta -viniferin from grape vine, comprises dissolving resveratrol and eta -viniferin solid mixture in chloromethane, separating using column chromatography to obtain eluate comprising eta -viniferin crude product, cooling the eluate to lower than 60 degrees C, concentrating, drying to obtain eta -viniferin crude product, dissolving the eta -viniferin crude product in methanol, performing chromatography using Sephadex (RTM: Cross-linked dextran gel) column to obtain eta -viniferin-containing eluate, allowing to stand, crystallizing, and centrifuging to obtain eta -viniferin monomer.    USE - The method is useful for extracting high purity eta -viniferin from grape vine (claimed).    ADVANTAGE - The method: utilizes grape vine waste as raw material and hence saves resources and achieves waste utilization; protects environment; produces resveratrol as by-product, which is a useful medicine and chemical raw material and hence improves the utilization value of grape vine; has simple operating process; and is suitable for industrial production.    DETAILED DESCRIPTION - Extracting high purity eta -viniferin from grape vine, comprises: (i) dissolving resveratrol and eta -viniferin solid mixture in chloromethane, separating using column chromatography, gradient eluting using chloromethane and methanol mixed solution to obtain eluate comprising eta -viniferin crude product; and (ii) cooling the eluate to lower than 60 degrees C, concentrating and drying to obtain eta -viniferin crude product, dissolving the eta -viniferin crude product in methanol, performing chromatography using Sephadex (RTM: Cross-linked dextran gel) column, isocratic eluting using methanol as eluent to obtain eta -viniferin-containing eluate, allowing to stand, crystallizing, and centrifuging to obtain eta -viniferin monomer.
NOVELTY - Method for preparing aloin, involves obtaining Aloe powder, extracting the obtained powder for 1-2 times using 40-60% ethanol at 70 degrees C, combining the extract, and concentrating the extract, dissolving obtained extract (crude product) in 40-60% methanol and water, eluting the obtained product, and sampling using HPLC, and concentrating the obtained product.    USE - The method is useful for preparing aloin (claimed).    ADVANTAGE - The method prepares aloin with high purity, and is environmentally-friendly.
NOVELTY - A high performance liquid chromatographic acarbose is prepared by performing isocratic elution using high performance liquid chromatographic separation system at 0-50 degrees C, using acetonitrile and water as flow phase, and filling with stationary phase 18 carbon (C18) filler having particle size of 10-30 mu m.    USE - Preparation of high performance liquid chromatographic acarbose (claimed).    ADVANTAGE - Preparation process is simple and environment-friendly and has high automation degree and high production efficiency, and product has high purity and stable quality.
NOVELTY - Integrated wood drying and charring device comprises inner kiln body (1), fan (5), heater (2), water spray, water tube (3), saturated steam tank, kiln top, humidity-discharging window (7), fan motor (6), frequency conversion device and variable frequency device.    USE - Integrated wood drying and charring device.    ADVANTAGE - The device reduces energy consumption and emissions.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the drying and charring method comprising entering wood into kiln body, starting fan and heater, gradually heating kiln to 50-75 degrees C, drying wood until water content of 10-12%, drying at 65-75 degrees C, gradually heating kiln to 120-130 degrees C, drying wood until water content is 2-4%, raising temperature to 180-220 degrees C, maintaining temperature, carbonizing, controlling frequency conversion device, spraying saturated water steam, keeping wet bulb temperature at 99.5-100 degrees C, keeping oxygen content at less than 2%, keeping water content at less than 0.5%, cooling, regulating humidity, controlling heater, stop heating, cooling tube to 116-112 degrees C, reducing content to 4-5%, and cooling to 25-30 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of integrated wood drying and charring device.    Inner kiln body (1)    Heater (2)    Water tube (3)    Fan (5)    Fan motor (6)    Humidity-discharging window (7)
NOVELTY - Rolling type biomass pyrolysis multi-joint device comprises hot pressing roller (1), feeding system (2), drying system (3), roller type pyrolysis reactor (4), gas-solid separation system (5), condensing system (6), gas combustion system (7), solid coke collecting box (8), liquid collecting box (9) and gas storage tank (10). The roller type pyrolysis reactor comprises supporting belt, transmission roller, driving system, seal reaction room, high temperature smoke heat exchange coil and transfer hot pressing roller.    USE - Rolling type biomass pyrolysis multi-joint device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of rolling type biomass pyrolysis multi-joint device (Drawing include non-English language texts).    Hot pressing roller (1)    Feeding system (2)    Drying system (3)    Roller type pyrolysis reactor (4)    Gas-solid separation system (5)    Condensing system (6)    Gas combustion system (7)    Solid coke collecting box (8)    Liquid collecting box (9)    Gas storage tank (10)
NOVELTY - An internal combustion heated rotary vane type biomass gasification furnace comprises furnace body (1), gasification layer (8), gasification layer wall (7), hot exhaust gas layer (6), hot exhaust gas layer wall (5), fuel gas layer (4), fuel gas layer wall (3), heat preservation layer (2), rail, internal combustion rotary pipeline, multileaf joint plate, blade, rotary support pipeline, air inlet pipeline, combustion air pipeline, feeding hopper, conical furnace bottom and draft fan.    USE - Internal combustion heated rotary vane type biomass gasification furnace.    ADVANTAGE - The convenient furnace greatly improves biomass gasification and thermal value, avoids secondary pollution, reduces cost, and simplifies operation management and maintenance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of internal combustion heated rotary vane type biomass gasification furnace.    Furnace body (1)    Heat preservation layer (2)    Fuel gas layer wall (3)    Fuel gas layer (4)    Hot exhaust gas layer wall (5)    Hot exhaust gas layer (6)    Gasification layer wall (7)    Gasification layer (8)
NOVELTY - A continuous biochar production device cracking tank comprises cracking tank body (1), feeding port, discharging port and oil gas hole.    USE - Continuous biochar production device cracking tank.    ADVANTAGE - The cracking tank has increased volume, prolonged carbonization time, slow and uniform heating, and maximized biomass utilization.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of continuous biochar production device cracking tank.    Cracking tank body (1)    Incubator (2)    Support frame (3)    Combustion furnace (7)    Blower (9)
NOVELTY - A continuous biochar production device comprises metal shell (13), support frame (17), feeding and discharging system, feeding conveyor, discharge conveyor (3), cooling conveyor, cracking tank (12), collecting-and-conveying system, furnace (11), air supply system, cooling system, temperature measuring system, feeding hopper (10), oil gas hole and inner air outlet.    USE - Continuous biochar production device.    ADVANTAGE - The non-polluting biochar production device has low energy consumption, high efficiency, and low heating condition, avoiding oil and gas pipeline blockage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of continuous biochar production device.    Discharge conveyor (3)    Feeding hopper (10)    Furnace (11)    Cracking tank (12)    Metal shell (13)    Support frame (17)
NOVELTY - Inner combustion heating rotary vane type biomass pyrolysis liquefying device comprises reactor with jacket structure, hot solution layer, thermal layer wall, hot exhaust gas layer, hot exhaust gas layer wall, heat preservation layer and rail. Reactor is set with two horizontal internal combustion rotary pipeline, leaf stitch plate, blade, hopper and tapered bottom. Internal combustion rotary pipeline is connected to rotation support concentric pipe set with combustion gas inlet and outlet ducts. Draft fan is connected to reactor.    USE - Inner combustion heating rotary vane type biomass pyrolysis liquefying device.    ADVANTAGE - The device improves biomass liquefaction, bio-oil heating value and property and reduces cost. It has simple and convenient maintenance.
NOVELTY - The method involves adding dimethyl ether composite catalyst and modified ZSM-5 catalyst in a section reactor at normal pressure, and mixing hydrogen and nitrogen for a section catalyst reduction process. A catalyst reduction is finished, and pneuma compressed voltage is synthesized for circulation pneuma mix. A decarburization tower is used to remove the carbon dioxide, and gas of carbon dioxide entering into the section reactor is removed. The dimethyl ether reaction is synthesized, and section of tail pneuma is generated to obtain liquid phase product crude gasoline product.    USE - Method for synthesizing pneuma.    ADVANTAGE - The method enables realizing simple technique, low synthetic pneuma hydrogen carbon ratio and high CO conversion, low section pressure and low water consumption and low investment and operation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a pneuma synthesizing method. '(Drawing includes non-English language text)'
NOVELTY - A clean fuel contains 60-80% methanol, 10-30% solvent oil, 5-15% ethanol, and 1-3% acetone.    USE - Clean fuel for liquefied petroleum gas alternative.    ADVANTAGE - The clean fuel is environment-friendly, simple, low cost, highly efficient, highly volatile, does not have smoke and coke, and has low resistance.
NOVELTY - A biodiesel comprises 60-90% rapeseed oil, 10-30% turpentine oil, 5-10% alkane and 0.2-0.5% ferrocene.    USE - Biodiesel (claimed).    ADVANTAGE - The biodiesel contains light alkane, which cleaves on ignition at ambient temperature, and can be reconciled with petrochemical diesel during use, in specified proportion.
NOVELTY - An additive comprises 40-60 wt.% methanol, 3-5 wt.% dimethyl carbonate, 1-3 wt.% alkyl naphthalene, 1-3 wt.% corrosion inhibitor, 2-5 wt.% methyl tert-butyl ether, 1-3 wt.% acetone and 3-6 wt.% tert-butanol.    USE - Additive is used for methanol-diesel blended fuel.
NOVELTY - A methanol gasoline additive contains 40-60 wt.% methanol, 3-5 wt.% dimethyl carbonate, 1-3 wt.% T-80 (RTM: Polyoxyethylene (20) sorbitan monooleate), 1-3 wt.% S-80 (RTM: Sorbitan monooleate), 2-5 wt.% methyl tert.-butyl ether (MTBE), 1-3 wt.% acetone, and 3-6 wt.% tert.-butanol.    USE - Methanol gasoline additive for automobile fuel pump.    ADVANTAGE - The methanol gasoline additive is environment-friendly, energy-saving, simple, easy to store, suitable for production under normal temperature and pressure, suitable for cold start, does not require oil refining equipment, saves cost, reduces oil and gasoline consumption, and has prolonged service life, high gasoline octane number, antiknock agent, and corrosion resistance.
NOVELTY - The system has a pre-processing device (2) provided with a refrigeration device, an absorber and a reactor. The reactor is filled with alkaline solution and metal oxide. A liquefying device (3) is connected with the refrigeration device. The liquefying device is utilized for providing low temperature fluid to a heat exchanger. An air inlet of the liquefying device is connected with a liquefied natural gas storage tank (4). A liquefied natural gas carburetor (5) is connected with a pneumatic engine (6). A marsh gas generator (1) is connected with the pre-processing device.    USE - Rural biomass energy comprehensive utilization system.    ADVANTAGE - The system performs low temperature liquefaction process. The system purifies 50-70 % of methane biogas into liquefied natural gas. The system improves biogas application value so as to improve utilization rate of biogas. The system performs thermoelectric cooling process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rural biomass energy comprehensive utilization method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a rural biomass energy comprehensive utilization system.    Marsh gas generator (1)    Preprocessing device (2)    Liquefying device (3)    Liquefied natural gas storage tank (4)    Liquefied natural gas carburetor (5)    Pneumatic engine (6)
NOVELTY - Silicon-based biodiesel lubricating base oil is biologically prepared by mixing hydrogen silicone oil and solid catalyst, heating to perform hydrosilylation reaction, adding fatty acid methyl ester, reacting until iodine value is less than or equal to 5 g/100 g, separating hot solid catalyst, and vacuum distilling.    USE - Biological preparation of silicon-based biodiesel lubricating base oil (claimed).    ADVANTAGE - The biological preparation of silicon-based biodiesel lubricating base oil is environment-friendly, simple, easy to separate, suitable for recycling, does not corrode equipment, does not produce acidic waste water, and has low process equipment demand which produces product with high catalytic activity, high flash point, good viscosity-temperature property, oxidation stability, and excellent friction and lubricating property.
NOVELTY - Use of molasses is claimed as a substrate for producing biogas, which involves (a) regulating pH of molasses to be 5.5-5.0, and filtering to obtain pretreated raw material, (b) diluting the pretreated raw material using water, where the pretreated raw material has chemical oxygen demand (COD) of 2000-25000 mg/l, carbon/phosphorus mass ratio of 100-300:1 and carbon/nitrogen mass ratio of 10-80:1, and (c) fermenting 10-80% anaerobic fermentation strain to fermentation medium at 15-50 degrees C for 2-20 hours, and collecting biogas discharged from fermentation reactor.    USE - The molasses are useful as substrate for production of biogas (claimed).    ADVANTAGE - The molasses are not easy to acidify and produces of biogas in large amount by direct and simple process, and avoid the hydrolysis of lignocellulosic materials.
NOVELTY - A banana tree and pig manure biogas is prepared by crushing banana branch and banana fragments to pieces, mixing banana powder mixture and sodium hydroxide solution, sealing, mixing banana powder mixture and hydrochloric acid solution, sealing, mixing 2 mixtures, adding manure while controlling nitrogen content, inoculating sludge, adjusting pH, and performing anaerobic fermentation.    USE - Preparation of banana tree and pig manure biogas (claimed).    ADVANTAGE - The device has high degradation efficiency, and method has high yield, and requires short processing time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermenting device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of fermenting device.    Fermenter (1)    Water pipes (2)    Lower outlet pipe (3)    Upper water pipe (4)    Pump (5)    Valve (6)
NOVELTY - A silkworm mulberry biomass microbial fermentation method is performed by taking mulberry-silkworm biomass, drying, crushing, sieving, selecting Ganoderma lucidum microbial strain, activating potato dextrose agar (PDA) culture medium covered with mycelium ball to obtain G. lucidum bacterial liquid, adding silkworm mulberry, glucose and potassium nitrate (KNO3), dissolving in water, uniformly mixing, adjusting pH to neutral, sterilizing, inoculating activated G. lucidium bacteria liquid, collecting strain fermentation product, drying, and crushing.    USE - A silkworm mulberry biomass microbial fermentation method for improving 1-deoxynojirimycin content (claimed).    ADVANTAGE - The method reduces amount of macromolecules, and is simple.    DETAILED DESCRIPTION - A silkworm mulberry biomass microbial fermentation method is performed by taking mulberry-silkworm biomass, naturally drying or performing hot-air drying, crushing, sieving through 40 mesh-sieve, selecting G. lucidum microbial strain, activating PDA culture medium covered with mycelium ball to obtain G. lucidum bacterial liquid, adding silkworm mulberry, glucose and potassium nitrate at weight ratio silkworm mulberry:glucose:potassium nitrate of (4-5):(1-1.2):(0.8-1), dissolving in water at 18-20 times volume of mixture, uniformly mixing, adjusting pH to neutral, sterilizing at 120 degrees C for 20-30 minutes, inoculating 2-3 vol.% activated G. lucidium bacteria liquid at 25-28 degrees C for 2-3 days, collecting strain fermentation product, drying, and crushing.
NOVELTY - Engine comprises main body, upper electrolytic groove, electrode, electrode plate, bottle, filter, pressure regulator, water inlet and outlet connected to a water tank, upper shell with anode and cathode connected to a power source, oxygen outlet and hydrogen inlet tube.    USE - Engine for hydrogen-oxygen vehicle.    ADVANTAGE - Fuel is hydrogen and oxygen, thus making it clean and environment friendly.
NOVELTY - A biomass is preprocessed by crushing biomass by machinery while subjecting cellulose biomass to heat and chemical degradation in which crushing by machine produce biomass and improves mixture of chemical medicine.    USE - Preprocessing of biomass for conversion of monosaccharide (claimed).    ADVANTAGE - Process is simple and easy, has high energy utilization, low energy consumption, and improved enzymolysis efficiency, and saves water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for conversion of biomass to monosaccharide which involves preprocessing biomass, pretreating cellulose biomass by enzymolysis, crushing, and washing in which enzyme is cellulase, beta -glucosidase, and/or xylanase.
NOVELTY - System (10), comprises: a gasifier (12) configured to gasify a mixture of a biomass feedstock (14) and an oxidant (20) to generate a producer gas; a producer gas purification system configured to purify the producer gas from the gasifier; and a gas supply system configured to supply a recycle gas to at least one of the gasifier and/or the producer gas purification system. The recycle gas comprises an exhaust gas and/or at least one gas separated from the exhaust gas, generated from a combustion system.    USE - The system is useful in biomass gasification (claimed).    ADVANTAGE - The system: reduces the amount of exhaust gases and flames that are normally expelled into the atmosphere; and reduces the need to pressurize the gases, and thus reduces the auxiliary power consumption by the gas supply system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for biomass gasification, comprising: gasifying a mixture of a biomass feedstock and an oxidant in a gasifier to generate a producer gas; purifying the producer gas from the gasifier using a producer gas purification system; combusting the producer gas to generate an exhaust gas using a combustion system; separating the exhaust gas into a first gas and a second gas using a pressure swing adsorption system; and supplying the first gas to at least one of the gasifier and/or the producer gas purification system.    DESCRIPTION OF DRAWING(S) - The figure illustrates a schematic block diagram of a biomass gasification system with an exhaust manager and a gas supply system.    Biomass gasification system (10)    Gasifier (12)    Biomass feedstock (14)    Dry feedstock (18)    Oxidant (20)
NOVELTY - The system has a control unit determining whether malfunction is generated in a fuel cell stack based on amount of water ejected from the stack and output current amount of the stack. The output current amount of the stack is measured by an output measurement part. The output measurement part is connected to the stack. Amount of the water ejected from the stack is measured by a flux measurement part, which is connected to the stack. The stack generates electricity through electro chemical reaction, arbitrary hydrogen and oxygen. An alarm part is connected to the control unit.    USE - Fuel cell system.    ADVANTAGE - The system specifically and accurately determines whether malfunction is generated in the fuel cell stack so as to quickly diagnosis fault of the fuel cell stack.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for controlling a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system. '(Drawing includes non-English language text)'
NOVELTY - Producing hydrogen from hydrogen-containing compounds, comprises using an oxidizing agent, which comprises at least two oxidizing agents, as an input parameter for the hydrogen generating reactors.    USE - The method is useful for producing hydrogen from hydrogen-containing compounds (claimed).    ADVANTAGE - The method is carried out in simple and cost efficient manner.
NOVELTY - Recovering an oil composition from fermentation process, comprises: fermenting a starch composition to form a fermented product; separating an oil fraction from the fermented product, where the oil fraction contains the oil composition; adjusting the pH of the oil fraction; and recovering the oil composition from the pH adjusted oil fraction.    USE - The method is useful for recovering an oil composition from a fermentation process (claimed), where the oil composition is useful in bio-diesel production and other edible applications.    ADVANTAGE - The safe and efficient method ensures effective recovery of oil composition from a fermentation product with high yield and quality, and low levels of free fatty acids, thus reducing the need for front-end or pretreatment processing in the context of bio-diesel production.    DESCRIPTION OF DRAWING(S) - The figure shows schematic flow diagram of a method for recovering an oil composition.
NOVELTY - Hay-based log (42) comprises a mixture of hay and a binder pressed together.    USE - The hay-based log is useful as fuel log (claimed) in a woodstove, as a fire log or a ore component in a fireplaces.    ADVANTAGE - The hay-based log: is fabricated easily and economically; can be transported and used safely and more easily than wood logs; is environmentally friendly and is formed of materials that are readily available; and can be used in pre-existing burning devices and in fireplaces and as well as delivers heat when burned of satisfactory intensity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for making a hay-based fuel log, comprising: processing hay into hay pieces; mixing the hay pieces with a binder to make a hay and binder mixture; and pressing the mixture into the form of a log.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of equipment used to make the hay-based log.    System for making the hay-based log (30)    Containment tube (32)    First hydraulic cylinder (34)    Re-circulation tubing (40)    Hay-based log (42)
NOVELTY - A sludge compost experiment device comprises a fermentation groove (3) of peripheral sidewall using foam heat preservation plate (2) as side plate. The fermenting groove of upper floor is uniformly distributed with cloth channels (1). The fermenting groove is divided into gas distribution areas (4). A gas supplying branch tube comprises cloth cross tube (8) and distributing pipe (9). A supply pipe is connected with the fermentation groove of centrifugal air blowers (12).    USE - A sludge compost experiment device.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the sludge compost experiment device.    Cloth channels (1)    Foam heat preservation plate (2)    Fermentation groove (3)    Gas distribution areas (4)    Cloth cross tube (8)    Distributing pipe (9)    Centrifugal air blowers (12)
NOVELTY - A 4-(4-aminophenyl)-3-morpholinone is prepared by mixing benzamide-substituted 4-methylmorpholin-3-one derivative (6) with ammonia, reacting, adding inorganic alkali solution, and sodium hypochlorite solution or sodium bromate, and performing Hofmann degradation; or dissolving 4-morpholin-4-ylbenzoyl chloride derivative (5) in ketone solvent, dropping sodium azide, reacting, dissolving in t-butanol, immersing in chlorinated alkane solvent or ether solvent in the presence of inorganic or organic acid, and reacting.    USE - Method for preparing 4-(4-aminophenyl)-3-morpholinone (claimed).    ADVANTAGE - The method is suitable for industrial production and reduces cost. It uses cheap and environment-friendly raw materials.    DETAILED DESCRIPTION - A 4-(4-aminophenyl)-3-morpholinone is prepared by mixing benzamide-substituted 4-methylmorpholin-3-one derivative (6) with ammonia to obtain 4-morpholin-4-ylbenzoyl chloride derivative (5), reacting at 0-50 degrees C, adding inorganic alkali solution, and sodium hypochlorite solution or sodium bromate, and performing Hofmann degradation; or dissolving 4-morpholin-4-ylbenzoyl chloride derivative (5) in ketone solvent, dropping sodium azide, reacting at 0-50 degrees C to obtain benzaldehyde derivative (7), dissolving in t-butanol to obtain di-tert-butyl dicarbonate-substituted aniline derivative (8), immersing in chlorinated alkane solvent or ether solvent in the presence of inorganic or organic acid with pH value of less than or equal to 2, and reacting at 0-50 degrees C.
NOVELTY - Toothpaste comprises 35-45 pts. wt. of calcium hydrophosphate, 0.06-0.15 pts. wt. of sodium carboxymethyl cellulose, 10-14 pts. wt. of bamboo salt, 10-12 pts. wt. of glycerol, 13-15 pts. wt. of xylitol, 0.5-1 pts. wt. of sodium pyrophosphate, 2-2.8 pts. wt. of lauryl sodium sulfate, 1.5-2.5 pts. wt. of tea polyphenol, 0.9-1.1 pts. wt. of essence, and 10-40 pts. wt. of deionized water.    USE - The toothpaste is useful for preventing oral cavity ulcer, dental plaque and dental hypersensitivity, diminishing inflammation.    ADVANTAGE - The toothpaste can be rapidly prepared with good antiinflammatory effect and less energy consumption.
NOVELTY - Preparing 4,6-dichloro-2-propylsulfanyl-pyrimidin-5-ylamine intermediate (I) comprises cyclizing protected 2-amino-1,3-malonate and thiourea, sulfur alkylation of obtained protected 5-amino-2-thioxo-sodium pentobarbital with halogenated propane to obtain protected 4,6-dihydroxy-5-amino-2-(mercapto-propyl) pyrimidine, chlorination reaction of obtained protected 4,6-dihydroxy-5-amino-2-(mercapto-propyl) pyrimidine to obtain protected 4,6-dichloro-5-amino-(mercapto-propyl) pyrimidine, and deprotecting obtained protected 4,6-dichloro-5-amino-(mercapto-propyl) pyrimidine.    USE - The method is useful for preparing (I) (claimed).    ADVANTAGE - The simple method is capable preparing (I) with economic and eco-friendly manner.    DETAILED DESCRIPTION - Preparing 4,6-dichloro-2-propylsulfanyl-pyrimidin-5-ylamine intermediate of formula (I) comprises cyclizing protected 2-amino-1,3-malonate and thiourea to obtain protected 5-amino-2-thioxo-sodium pentobarbital and halogenated propane, sulfur alkylation of obtained protected 5-amino-2-thioxo-sodium pentobarbital with halogenated propane to obtain protected 4,6-dihydroxy-5-amino-2-(mercapto-propyl) pyrimidine, chlorination reaction of obtained protected 4,6-dihydroxy-5-amino-2-(mercapto-propyl) pyrimidine to obtain protected 4,6-dichloro-5-amino-(mercapto-propyl) pyrimidine, and deprotecting obtained protected 4,6-dichloro-5-amino-(mercapto-propyl) pyrimidine.
NOVELTY - The method involves preparing a prepreg at temperature condition of 50-110 degree Celsius by using mixture of polymer resin and conductive filler. The prepared prepreg is molded. The membranous polymer resin is selected from a group such as thermosetting resin, thermoplastic resin and engineering plastics. The conductive filler is selected from a group such as carbon-powder, graphite, carbon black, acetylene black, Ketjen black, denka black, activated carbon, carbon nanotube, carbon nanofiber, carbon nanowire, carbon nano-horn and carbon nano ring.    USE - Method for manufacturing a separator of a fuel cell (claimed).    ADVANTAGE - The method enables providing high conductivity and high-strength property and manufacturing a separator of a fuel cell by utilizing the prepreg of a semi-harden sheet form with better confinement of gas. The method enables facilitating storage of the prepreg and improving manufacturing environment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a separator    (2) a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a photographic view of a separator.
NOVELTY - Enzyme saccharification reaction accelerator comprises compound (A) having at least 3 hydroxy groups in the molecule and having a average molecular weight of 1500-30000.    USE - The enzyme saccharification reaction accelerator is useful in enzyme saccharification reaction accelerator composition which is used for manufacturing sugar for bioethanol (all claimed) from cellulose biomass, including scrap wood.    ADVANTAGE - The enzyme saccharification reaction accelerator enables improved rate of conversion from cellulose to a sugar during enzymatic saccharification reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for enzyme saccharification reaction accelerator composition comprising the enzyme saccharification reaction accelerator, saccharogenic amylase, and water.
NOVELTY - Preparing ethanol by hydrogenation of a low-carbon ester, involves passing a raw material gas containing a low-carbon ester and hydrogen gas through a gas distributor in the middle of a reactor to uniformly distribute the same into a catalyst bed of a copper-based catalyst, and performing hydrogenation at a reaction temperature of 200-320 degrees C under 0.5-20 MPa a reaction pressure, and a volume space velocity of 1000-40000 per hour to prepare ethanol.    USE - The method is useful for preparing ethanol by hydrogenation of a low-carbon ester (claimed).    ADVANTAGE - The method increase conversion of the low-carbon ester, effectively controls the temperature distribution of the catalyst bed, improves the conversion and selectivity of the target product, and extends the lifetime of the catalyst.    DETAILED DESCRIPTION - Preparing ethanol by hydrogenation of a low-carbon ester, involves passing a raw material gas containing a low-carbon ester and hydrogen gas through a gas distributor in the middle of a reactor to uniformly distribute the same into a catalyst bed of a copper-based catalyst, and performing hydrogenation at a reaction temperature of 200-320 degrees C under 0.5-20 MPa a reaction pressure, and a volume space velocity of 1000-40000 per hour to prepare ethanol. The reaction zone comprises one reactor or multiple reactors connected in serial and/or parallel, each reactor contains at least one catalyst bed, the raw gas is evenly distributed into each catalyst bed through the gas distributor arranged between the reactors.
NOVELTY - Producing fermentable sugars from whole biomass, involves: (a) providing a whole biomass feedstock comprising cellulose, hemicellulose, lignin, and non-lignocellulosic sugars; (b) in a digestor, fractionating the feedstock under effective fractionation conditions in the presence of an acid catalyst, a solvent for lignin, and water; (c) substantially removing the cellulose-rich solids from the liquor; (d) hydrolyzing the dissolved hemicellulose contained in the liquor; (e) optionally hydrolyzing the cellulose-rich solids to produce glucose; and (f) recovering the hydrolyzed liquor.    USE - The process is useful for producing fermentable sugars from whole biomass (claimed).    ADVANTAGE - The process is highly economical and has high yield.    DETAILED DESCRIPTION - Producing fermentable sugars from whole biomass, involves: (a) providing a whole biomass feedstock comprising cellulose, hemicellulose, lignin, and non-lignocellulosic sugars; (b) in a digestor, fractionating the feedstock under effective fractionation conditions in the presence of an acid catalyst, a solvent for lignin, and water, to produce a liquor containing cellulose-rich solids, dissolved lignin, dissolved hemicellulose, and at least a portion of the non-lignocellulosic sugars contained in the feedstock; (c) substantially removing the cellulose-rich solids from the liquor; (d) hydrolyzing the dissolved hemicellulose contained in the liquor, under effective hydrolysis conditions, to produce a hydrolyzed liquor comprising hemicellulosic monomers and the non-lignocellulosic sugars; (e) optionally hydrolyzing the cellulose-rich solids to produce glucose; and (f) recovering the hydrolyzed liquor, and optionally the glucose if step (e) is conducted, as fermentable sugars.
NOVELTY - An alkene-producing yeast cell comprises a bacterial fatty acid decarboxylase enzyme, is new.    USE - As alkene-producing yeast cell (claimed), useful in the production of biofuels and/or biochemicals.    ADVANTAGE - The yeast cell produces alkenes in good yields; produces alkenes without making use of a heterologous expression vector.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing an alkene comprising culturing the cell.
NOVELTY - Gasification combined equipment for carbon fuel, has gasifier capable of producing synthetic gas which reacts with carbon fuel and gasification agent, flash dryer provided with heat exchanger for reducing moisture content of carbon fuel using pressure steam generated during a carbon fuel gasification process, and water gas shift reactor for generating hydrogen and carbon dioxide from synthetic gas.    USE - The gasification combined equipment is useful for carbon fuel including biomass or petroleum coke (claimed).
NOVELTY - Method for preparing high concentration of fermentable sugar from wood-based biomass, involves pre-treating the wood to remove impurities and extractible substances such as mineral salts and extracting biomass using hot water, performing enzymatic saccharification of biomass to obtain sugar solution, concentrating the sugar solution using separator membrane and performing solid-liquid separation without washing the solid content with water.    USE - The method is useful for preparing high concentration of fermentable sugar which is useful for culturing various industrial fermentation bacteria.    ADVANTAGE - The method is cost-effective and maximizes xylan yield rate and hence achieves maximum inhibition of over-decomposed products of sugar.
NOVELTY - Processing system for transesterification/esterification of fatty acid source with alcohol, to form fatty acid alkyl esters, comprises reaction vessel configured for reacting reaction medium including fatty acid source and at least one of alcohol and alcohol donor in presence of immobilized lipase preparation, where immobilized lipase preparation comprises at least one lipase immobilized on hydrophobic porous support and processing system is configured for passing reaction medium through immobilized lipase preparation in direction at least partially opposed to gravity.    USE - The processing system is useful for transesterification/esterification of fatty acid source with alcohol, to form fatty acid alkyl esters (claimed), which is used in the bio fuels, food, cosmetics, pharmaceuticals and detergents industries.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for transesterification/esterification of a fatty acid source with alcohol, to form fatty acid alkyl esters, comprising reacting a reaction medium including a fatty acid source and alcohol or alcohol donor in the presence of an immobilized lipase preparation, where the immobilized lipase preparation comprises at least one lipase immobilized on a hydrophobic porous support and the reaction medium optionally stirred and contains the aqueous alkaline buffer solution and water, free or mixed with a polyol/polyols, and the reaction medium is passed through the immobilized lipase preparation in a direction at least partially opposed to gravity.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of processing system.    Reactor vessel (102)    Preparation vessel (104)    Product separation vessel (106)    Jacket (149)    Vessel inlets (172)
NOVELTY - Obtaining microorganisms with cellulolytic activity, comprises feeding folivore monkey with a diet comprising a cellulose compound for at least 12 hours, preferably at least 96 hours, recovering a sample previously taken from microbial flora of the digestive tract of the monkey, and culturing the sample in a medium containing the cellulose compound for 12 hours, preferably at least 7 days.    USE - The method is useful for obtaining host bacterium type microorganisms e.g. yeast or fungus and enzymes (all claimed) to degrade cellulose and hemicellulose and for producing biofuels and other chemicals.    ADVANTAGE - The method is capable of economically producing the microorganisms with good cellulolytic activity.
NOVELTY - A hydrogen generating device (100) has a reformer (3) for generating a hydrogen-containing gas using a starting material (AA), a hydro-desulfurizer (2) for removing a sulfur compound from the starting material, a recycling channel (8) for supplying the hydrogen-containing gas to the starting material before introducing the starting material to the hydro-desulfurizer, a booster (1) for supplying the starting material to the reformer, and a starting-material supply channel (5) through which the starting material flows, and an ejector (9).    USE - Hydrogen generating device is used for fuel cell system (claimed).    ADVANTAGE - The fuel cell system having the hydrogen generating device has suppressed supplying of condensed water to the booster.    DETAILED DESCRIPTION - A hydrogen generating device has a reformer for generating a hydrogen-containing gas using a starting material, a hydro-desulfurizer for removing a sulfur compound from the starting material, a recycling channel for supplying the hydrogen-containing gas to the starting material before introducing the starting material to the hydro-desulfurizer, a booster for supplying the starting material to the reformer, and a starting-material supply channel through which the starting material flows, and an ejector into which the hydrogen-containing gas from the recycling channel is passed, and positioned in the starting-material supply channel at a location downstream of the booster and upstream of the hydro-desulfurizer. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of hydrogen generating device. (Drawing includes non-English language text)    Booster (1)    Hydro-desulfurizer (2)    Reformer (3)    Starting-material supply channel (5)    Recycling channel (8)    Ejector (9)    Hydrogen generating device (100)    Starting material (AA)
NOVELTY - The apparatus (100) has a modifier (1) that generates a hydrogen-containing-gas using source gas. A hydrodesulfurization device (2) removes the sulfur compound in the source gas. A recycle flow path (3) supplies a hydrogen-containing-gas to source gas before flowing in into the hydrodesulfurization device. The hydrodesulfurization device is provided in an upstream source gas flow path. An ejector (5) flow the hydrogen-containing-gas from the recycle flow path.    USE - Hydrogen generating apparatus used in fuel cell system (claimed).    ADVANTAGE - The hydrogen generating apparatus can reduce the increase in the flow path resistance by the condensed water in the ejector with which the hydrogen-containing-gas from a recycle flow path flows in hydrodesulfurization device. The flow-path obstruction by the condensed water of a recycle flow path can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the hydrogen generating apparatus.(Drawing includes non-English language text)    Modifier (1)    Hydrodesulfurization device (2)    Recycle flow path (3)    Ejector (5)    Hydrogen generating apparatus (100)
NOVELTY - A hydrogen generation system (100) has hydrogen generator (11) which produces fuel gas by modifying source gas which contains hydrocarbon and hydrogen, source gas path (12) for connecting to the hydrogen generator and supplying the source gas to the hydrogen generator, fuel gas path which leads-out the fuel gas produced by the hydrogen generator, pressure detector (13) which detects the pressure of the source gas within the source gas path, gas supply device (14) provided on the source gas path and supplies the source gas to the hydrogen generator, and controller (17).    USE - Hydrogen generation system for fuel cell system (claimed).    ADVANTAGE - The structure is simple and cheap.    DETAILED DESCRIPTION - A hydrogen generation system (100) has hydrogen generator (11) which produces fuel gas by modifying source gas which contains hydrocarbon and hydrogen, source gas path (12) for connecting to the hydrogen generator and supplying the source gas to the hydrogen generator, fuel gas path which leads-out the fuel gas produced by the hydrogen generator, pressure detector (13) which detects the pressure of the source gas within the source gas path, gas supply device (14) provided on the source gas path and supplies the source gas to the hydrogen generator, and controller (17). Operation is stopped when abnormality is reported in the difference between the detected 2nd pressure from 2nd operating quantity and detected 1st pressure from 1st operating quantity during the operation of gas supply device. INDEPENDENT CLAIMS are included for:    (1) fuel cell system; and    (2) operating method of the hydrogen generation system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generation system. (Drawing includes non-English language text).    Hydrogen generator (11)    Source gas path (12)    Pressure detector (13)    Gas supply device (14)    Controller (17)    Hydrogen generation system (100)
NOVELTY - Biodiesel production system consists of raw material tank for storing and supplying oil raw materials, transesterification reaction apparatus for producing crude biodiesel by transesterifying oil raw materials with alcohol using catalyst, aeration apparatus for aerating gas to crude biodiesel for removing alcohol, and first impurity removal apparatus to remove impurity precipitated or floated in crude biodiesel.    USE - The system and method are useful for producing biodiesel (claimed).    ADVANTAGE - The system is simple, efficient, cost-effective, and smaller in size as wastewater treatment apparatus is unnecessary, and eliminates washing using water and reducing pressure steps. The produced biodiesel has high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing biodiesel, which involves transesterifying oil raw materials with alcohol to obtain crude bio-diesel, aerating gas to the crude bio-diesel, removing alcohol, and removing impurity which precipitates or floats from the crude biodiesel.
NOVELTY - Soil conditioner comprises chopped and shredded green waste and green waste charcoal and other additives, and artificial peat comprising ingredients of green waste, green waste chaff, green waste fibers and green waste charcoal.    USE - Used as a soil conditioner.    ADVANTAGE - The soil conditioner: has artificial peat which is a ready to use (claimed); and allows relaxation of soils.
NOVELTY - The apparatus has a boiler (3) that is provided for combustion of biogas (2) produced by digestion system. Actuated process gas input valve (8) controls input of heated process gases based on temperature feed-back protocol. Actuated hot water intake valve (24) controls input of heated water to hot water pipes within walls and floor of sanitization vessel (9). A computerized control system (23) receives information from flow meter, pressure sensor, gas sensor, oxygen sensor and temperature sensor, and utilizes data to control pump, blower, valves and compressor to operate vessel.    USE - Apparatus for achieving controlled logarithmic pathogen reduction in solid state anaerobic digestate using anaerobic digestion heat process.    ADVANTAGE - Logarithmic pathogen in solid state anaerobic digestate can be effectively reduced. Mechanisms can be used to reduce or remove the pathogens from the material to allow for safe subsequent use. Anaerobic digestion system can be use biogas derived heat to achieve targeted and measured reduction in the pathogen concentrations.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for reducing the pathogen content of solid state anaerobic digestate utilizing heat process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of the general arrangement and assembly of main components.    Biogas (2)    Boiler (3)    Actuated process gas input valve (8)    Sanitization vessel (9)    Computer control system (23)    Actuated hot water intake valve (24)
NOVELTY - The system (1) has a water electrolysis apparatus (11) which electrolyzes water using the received electric power, and generates high pressure hydrogen gas and high pressure oxygen gas. An oxygen liquefier (12a) carries out expansion pressure reduction, cools the oxygen gas, and generates liquid oxygen. A hydrogen liquefier (12b) cools and carries out expansion pressure reduction of the hydrogen gas using the liquid oxygen, and generates liquid hydrogen. A liquefied gas storage apparatus (13) stores the liquid oxygen and the liquid hydrogen.    USE - System for storing energy using hydrogen and oxygen generated by super-high pressure water electrolysis.    ADVANTAGE - The hydrogen and oxygen can be liquefied by the water electrolysis apparatus. The energy storage can be performed using hydrogen and oxygen by the water electrolysis apparatus. The stored energy can be recyclable as the electric power. The occurrence of danger due to the mixing of the hydrogen and the oxygen can be prevented effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for storing energy using hydrogen and oxygen generated by super-high pressure water electrolysis.    DESCRIPTION OF DRAWING(S) - The drawing shows a functional block diagram of the system for storing energy using hydrogen and oxygen generated by water electrolysis. (Drawing includes non-English language text)    System for storing energy using hydrogen and oxygen generated by water electrolysis (1)    Water electrolysis apparatus (11)    Oxygen liquefier (12a)    Hydrogen liquefier (12b)    Liquefied gas storage apparatus (13)
NOVELTY - The apparatus comprises a cylindrical shaped pipe for transferring carbon gas to a carbonization furnace, a hopper for generating carbon gas and including a metering feeder, a unit for supplying carbonized ash to the carbonization furnace, a rotary shaft configured to rotate both end parts of the carbonization furnace, an insulation unit for covering an external side of the carbonization furnace, a pipe for circulating hot air through the rotary shaft and the carbonization furnace, and a unit for preventing leakage of carbon gas in the carbonization furnace.    USE - The apparatus is useful for carbonizing combustible waste (claimed).    ADVANTAGE - The apparatus is capable of carbonizing the combustible waste in an eco-friendly manner with excellent heat resistance, durability and thermal conduction rate.    DETAILED DESCRIPTION - The apparatus comprises a cylindrical shaped pipe for transferring carbon gas to a carbonization furnace, a hopper for generating carbon gas and including a metering feeder, a unit for supplying carbonized ash to the carbonization furnace, a rotary shaft configured to rotate both end parts of the carbonization furnace, an insulation unit for covering an external side of the carbonization furnace, a pipe for circulating hot air through the rotary shaft and the carbonization furnace, and a unit for preventing leakage of carbon gas in the carbonization furnace. The carbonization furnace comprises a dome valve installed at an exhaust pipe in order to prevent the carbon gas leakage, and is provided with a recycle pipe and a hot air pipe to pass through the rotary shift. The rotary shaft is connected with the carbonization furnace. A jacket is connected to the carbonization furnace including organic toxic gas and carbon gas. The carbon gas is supplied by an air fan or an air duct. The hot air pipe is connected with the rotary shaft.
NOVELTY - Decomposing biomass involves using ionic liquid to dissolve cellulose and remove lignin.    USE - Method used for decomposing biomass (claimed).    ADVANTAGE - The method enables to decompose cellulose in an effective manner.
NOVELTY - Converting biomaterials into structural carbon products or their aggregates, comprises a pressurized hydrothermal treatment step of an organic starting material having a carbon content of greater than 40 wt.% of the dry matter.    USE - The process is useful for converting biomaterials into structural carbon products or their aggregates which is used in manufacturing rubber, plastic product or pigment (all claimed).    ADVANTAGE - The process provides carbon product which has: carbon contents of greater than 40 wt.% of the dry matter (claimed); and which has well-defined physico-chemical properties e.g. surface area, carbon content, density, size and shape.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a carbon product, comprising carbon particles having a surface area of greater than 500 m2/g, and an average pore volume of less than 1 ml/g, which in turn are obtained from primary particles, including aggregates, having an average particle size of less than 250 nm.
NOVELTY - Enzymatic hydrolysis of cellulose, comprises: (a) extracting biomass containing both protein and cellulose with an aqueous liquid to produce an extracted biomass and an aqueous extract; (b) mechanically, chemically and/or thermally pretreating cellulose-containing biomass; and (c) contacting biomass pretreated in step (b) with (i) an enzyme capable of hydrolyzing cellulose, and (ii) the aqueous extract obtained in step (a), optionally after concentration.    USE - The process is useful for enzymatic hydrolysis of cellulose.    ADVANTAGE - The process is cost effective.
NOVELTY - Invention can be used in the chemical industry. A method of obtaining a hydrogen-methane mixture includes application of two parallel flows, which contain lower alkanes, as a source of raw material. The first flow is directed to partial oxidation with oxygen containing gas. Products of the first flow oxidation are supplied to cooling by means of the second flow heating, and after that, to catalytic conversion of carbon monoxide. After that, hydrogen is separated from the first flow. The second flow is mixed with water vapour and successively passed through a series of successive stages, each of which includes heating in a heat exchanger due to discharge of heat from the process of the partial first flow oxidation, and then through an adiabatic conversion reactor, filled with a catalyst filling. Products of the second flow conversion after separation of water vapour are mixed due to ejection with hydrogen, discharged from the first flow.    USE - Chemistry.    ADVANTAGE - Invention makes it possible to increase a coefficient of conversion of low alkanes and reduce the content of ballast gases, such as nitrogen and argon, in produced gas.15 cl, 1 dwg, 1 tbl
NOVELTY - Escherichia coli 0127:H6 for producing a hydrogen gas and methane gas from marine algae, is new.    USE - The Escherichia coli 0127:H6 is useful in production of biogas such as methane gas and hydrogen gas from marine algae (all claimed).    ADVANTAGE - The Escherichia coli 0127:H6 produces the hydrogen gas and the methane gas in an efficient, environment-friendly and economical manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) a biocatalizer comprising a strain, a culture fluid of the strain, and a concentrate of the culture fluid; and (2) producing a biogas including adding the biocatalizer having a biogas productive capacity in the marine algae and reacting the mixture at 30-40 degrees C in an anaerobic condition using Escherichia coli 0127:H6.
NOVELTY - The device has a container located on an inner side of a heat exchanger that is connected to pipes through a nipple. The container is provided with the pipes that are connected to a fermentation tank. A lower part of a drain valve is connected to a digestate reservoir. The container is mounted on a metal frame structure and covered with an upper cover roof. The metal frame structure is attached to a bracket during attaching the cover with a collective part.    USE - Device for treating organic fertilizer in agricultural biogas.
NOVELTY - The method involves preparing two electrolyte green sheets (2a,2b) that contain an electrolyte material. A green-sheet laminated body (3) is formed with an electrode green sheet and accommodated with a fuel electrode (11) or an air electrode. An electrode laminated body is accommodated with an electrolyte (21a). A part of the electrolyte is removed from a battery part (5) i.e. fuel cell part. An electrode i.e. air electrode green sheet (4), is arranged on the electrolyte of the battery part. The electrode green sheet is stacked on the green-sheet laminated body.    USE - Method for manufacturing a solid oxide fuel cell.    ADVANTAGE - The air electrode green sheet is arranged on the electrolyte of the battery part, so that damage and failure of the cell can be prevented and productivity and yield of the cell can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrolyte.    DESCRIPTION OF DRAWING(S) - The drawing shows a process diagram illustrating a solid oxide fuel cell manufacturing method.    Electrolyte green sheets (2a,2b)    Green-sheet laminated body (3)    Air electrode green sheet (4)    Battery part (5)    Fuel electrode (11)    Electrolyte (21a)
NOVELTY - Two-component fertilizer tablet or fertilizer-pad for long-term action on all pot-, balcony-, and potted-plants, comprises a mineral component of clay.    USE - The two-component fertilizer tablet or fertilizer-pad is useful for long-term action on all pot-, balcony-, and potted-plants (claimed).    ADVANTAGE - The two-component fertilizer tablet or fertilizer-pad: is completely natural; and allows the plants to optimally absorb nutrients and minerals.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the two-component fertilizer tablet or fertilizer-pad.
NOVELTY - A catalyst (C1) for converting alcohols to higher alcohols comprises at least one metal or metal layer on support, where metal is selected from cobalt, nickel, palladium, platinum, iron, zinc, tin and copper; and support selected from Al2O3, ZrO2, MgO, TiO2, zeolite, and/or ZnO, where the catalyst is substantially free of alkali metals and alkaline earth metals.    USE - As catalyst (C1) for converting alcohols to higher alcohols such as butanol used as a fuel in an internal combustion engine; in the manufacture of pharmaceuticals, polymers, pyroxylin plastics, herbicide esters and butyl xanthate; as a solvent for the extraction of essential oils or as an ingredient in perfumes; as an extractant in the manufacture of antibiotics, hormones, and vitamins; as solvent for paints, coatings, natural resins, gums, synthetic resins, alkaloids, and camphor; and also used as swelling agent in textiles; as component of break fluids, cleaning formulations, degreasers, and repellents; and as component of ore floatation agents and of wood-treating systems.    ADVANTAGE - The catalyst system of metal coated on a support beneficially results in the improvement of ethanol conversion (at least 20%), and/or butanol selectivity (at least 20%). The catalyst oxidizes ethanol to form an intermediate aldehyde, which forms crotonaldehyde, which is reduced to butanol. The catalysts serve as a base to oxidize ethanol and to promote aldol condensation, and also as a hydrogenating site for crotonaldehyde to form butanol. The metal-coated support catalysts provide high butanol selectivity and yield in comparison to metal-free catalysts, which is accompanied by the decrease of selectivity to by-products, such as diethyl ether (DEE) and ethylene.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing butanol involving feeding a gaseous stream comprising ethanol over the catalyst (C1) in a reactor to form butanol.
NOVELTY - Controlling Perilla rust disease, involves diluting pyroligneous acid with water, and spraying before and after infection in the Perilla leaves.    USE - The method or pesticidal composition is useful for controlling the Perilla rust disease in Perilla leaves (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pesticidal composition, which comprises the above-mentioned pyroligneous acid as an active ingredient.
NOVELTY - Use of cyclohexene compounds (I) for modifying the behavior of insects of the order Thysanoptera (thrips), is claimed.    USE - (I) are useful: for modifying the behavior of insects of the order Thysanoptera (thrips); as an attractant; and for the control one or more of Thrips palmi, Thrips tabaci, Frankliniella fusca, Frankliniella schultzei, Frankliniella tritici or Frankliniella occidentalis (all claimed). Tests details are described but no results given.    ADVANTAGE - (I) have minimal impact on the environment, and effectively attract the thrips.    DETAILED DESCRIPTION - Use of cyclohexene compounds of formula (I) for modifying the behavior of insects of the order Thysanoptera (thrips), is claimed.    R1 = CH3;    R2, R5 = H;    R3 = ketone or H; and    R4, R6 = H, methyl or ethyl.    An INDEPENDENT CLAIM is included for a device for the control of insects of the order Thysanoptera, including (I).
NOVELTY - Experimental device comprises stirrer (1), motor (2), iron stand (3), three-mouth bottle (4), temperature sensor (5), controller (6), water bath tank (7) and solar water heater (8). The water bath tank is installed with hot insulating material. The temperature sensor through data wire is connected to controller. The controller is connected with electromagnetic valve.    USE - Experimental device used for preparing biodiesel (claimed).    ADVANTAGE - The device reduces biodiesel cost, and ensures environmental protection.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of experimental device (Drawing includes non-English language text).    Stirrer (1)    Motor (2)    Iron stand (3)    Three-mouth bottle (4)    Temperature sensor (5)    Controller (6)    Water bath tank (7)    Solar water heater (8)
NOVELTY - A fruit tree fertilizer comprises 45-49 pts. wt. calcium superphosphate, 45-48 pts. wt. urea, 30-34 pts. wt. potassium chloride, 14-17 pts. wt. potassium dihydrogen phosphate, 30-34 pts. wt. sawdust, 30-34 pts. wt. rhizome of rehmannia wine lees, 12-14 pts. wt. yellow powder and manure, 8-10 pts. wt. fulvic acid, 1-2 pts. wt. stonewort essential oil, 3-4 pts. wt. sodium carbonate, 3-4 pts. wt. borax, 3-4 pts. wt. calcium sulfate, 3-4 pts. wt. effective microorganisms (EM) microbial inoculum, and water.    USE - Fruit tree fertilizer.    ADVANTAGE - The fertilizer improves soil organic material content, improves nutrient component of soil, and improves yield and quality of plant.    DETAILED DESCRIPTION - Fruit tree fertilizer comprises 45-49 pts. wt. calcium superphosphate, 45-48 pts. wt. urea, 30-34 pts. wt. potassium chloride, 14-17 pts. wt. potassium dihydrogen phosphate, 30-34 pts. wt. sawdust, 30-34 pts. wt. rhizome of rehmannia wine lees, 12-14 pts. wt. yellow powder and manure, 8-10 pts. wt. fulvic acid, 1-2 pts. wt. stonewort essential oil, 3-4 pts. wt. sodium carbonate, 3-4 pts. wt. borax, 3-4 pts. wt. calcium sulfate, 3-4 pts. wt. EM microbial inoculum, and water. A coating agent comprises 10-12 pts. wt. dipentaerythritol hexa-acrylate, 2-3 pts. wt. silane coupling agent (KH-570), 0.1-0.2 pts. wt. nanocarbon, and 1-2 pts. wt. medical stone powder. It is prepared by mixing the raw materials, grinding, and dispersing. An INDEPENDENT CLAIM is included for preparing the fertilizer.
NOVELTY - Preparing modified raney nickel involves preparing modified Raney nickel catalyst by bulk and surface modification of raney nickel by using conventional process, where modified component include manganese, iron, chromium, molybdenum, titanium and tungsten, and modified component content is 0.5-10 wt.%.    USE - Method for preparing modified raney nickel used for preparing pyrogallol and phloroglucinol (claimed).    ADVANTAGE - The method enables to prepare modified raney nickel in eco-friendly, simple and convenient manner.
NOVELTY - This utility new type claims a one microorganism Household organic garbage processing device, comprise support legs, a shell, a cover, a charging barrel, a stirring device, stirring device of driving system driving the upper cover body is provided with a temperature control device, temperature control device include a heater, a controller, a temperature sensor, a heater control by the controller, temperature sensor is connected with the controller. This utility new type has simple structure, small volume, convenient to move, of stirring device, biological probiotics and garbage fully contact, to accelerate the speed of the garbage is set of temperature control device to make the material bucket temperature control of the best temperature of probiotic fermented and improves the processing speed, a shell and charging barrel separated more convenient processing; is set of timer, time waste can be multi-amount uniform treatment, using this utility new type garbage processing device a Household organic garbage, it not only can quickly valid Household organic garbage processing, at the same time, for the environment, water source, soil will not cause second pollution.
NOVELTY - Ionic membrane electric groove hydrogen recovery device, comprising a hydrogen pipeline, a cable, a upper pneumatic valve, fire arrestor, emptying tube, emptying valve, the pressure difference processor, lower pneumatic valve, hydrogen removing negative pressure valve, hydrogen pipe, dripping,, flange, by-pass pipeline, pressure regulating tube, a water tube, a hydrogen discharging, flange butterfly valve, cut-off pipeline, a worm wheel movable valve, and gas valve, wherein the upper end of upper side of water seal is dripping, dripping water tube connecting the hydrogen pipe, the centre of the bypass pipeline and the hydrogen valve is set, and two side gas valve is one of the worm wheel for the valve, pressure regulating tube left end connecting gas pipeline, gas pipeline connecting upper pneumatic valve, pneumatic valve of upper right emptying tube, emptying valve right end connecting pressure difference processor, hydrogen discharging device of the right side is provided with a water tube, the utility model is new type of structure is reasonable, regulating precision high, the hydrogen of emptying a part to a system, a high rate.
NOVELTY - The present invention discloses a process for preparation of Dorzolamide and its hydrochloride salt with high yield and high purity, wherein the reaction starts with 6-methyl thieno(2,3-b)thiopyran 4-one compound having desired chirality at C-6 position and nonchiralality at C-4 position.
NOVELTY - Obtaining a composition involves extracting grape juice and then treating the grape juice by alcoholic fermentation for 10-15 days, without adding sulfites. Sulfur, copper, iron in form of salt or solvate, and polyphenols and tannins are added to the fermentation materials. The fermentation process is performed in presence of microorganisms i.e. Mycoderma aceti for 30-40 days at 30-50 degrees C for obtaining a composition that comprises acetic acid.    USE - Method for obtaining a composition used as plant protection product such as pesticide, fungicide, insecticide, bactericide, miticide or anti-parasitic agent, pesticides and fertilizers and soil conditioners (claimed) for preventing and treatment of plant disease, such as iron chlorosis, downy mildew, powdery mildew, white root rot, Petri disease, Gummosis, anthracnose and fungus such as Colletotrichum gloeosporioides, Verticillium and Armillaria, Phytosphora, and for stimulating growth and germination of plants and for removing limescale from irrigation systems.
NOVELTY - The device comprises a raw material storage tank, a conical-shaped fermentation tank, and a microbial deodorization trough, where a conveying device is installed between the storage tank and the fermentation tank. A material refining machine is installed at a bottom of the fermentation tank. An odor collecting tube is installed on a top part of the fermentation tank. The whole device is controlled with a computer system. The fermentation tank comprises a cover, a beam support column, and a cylinder tube. The bottom of the tube is formed with a discharge opening.    USE - Sludge treatment device.    ADVANTAGE - The device exhibits short fermentation time, less equipment failures, good deodorizing effect and low energy consumption, and has reduced labor intensity.    DETAILED DESCRIPTION - The device comprises a raw material storage tank, a conical-shaped fermentation tank, and a microbial deodorization trough, where a conveying device is installed between the storage tank and the fermentation tank. A material refining machine is installed at a bottom of the fermentation tank. An odor collecting tube is installed on a top part of the fermentation tank. The whole device is controlled with a computer system. The fermentation tank comprises a cover, a beam support column, and a cylinder tube. The bottom of the tube is formed with a discharge opening. A ventilation duct is formed at a lower part of the fermentation tank. The device further comprises a vertical lifting machine, a discharge baffle and a turner baffle. A bracket is installed in the discharge baffle. A distance between ends of the discharge baffle is 10-30cm. The turner baffle is fixed to the lifting machine at an inclined angle of 10-30 degrees . A bottom of the deodorization trough is set with an atomizing spraying device, a material layer of 40-50 cm thickness, and a filtering layer set with a filter screen. The filter layer is made wood, ceramic balls or fiber balls.
NOVELTY - Manufacture of cyclic unsaturated compound having fluorine atom-containing organic group involves irradiating light ray which excites photosensitizer (C) with respect to cyclic unsaturated compound (A) having unsaturated bond(s) in a ring in presence of sulfinate (B) (I) having fluorine atom-containing organic group and photosensitizer (C).    USE - Manufacture of cyclic unsaturated compound used in agricultural field and pharmaceutical field.    ADVANTAGE - The cyclic unsaturated compound having favorable stability is efficiently and safely manufactured by simple and environmentally-friendly method.    DETAILED DESCRIPTION - Manufacture of cyclic unsaturated compound having fluorine atom-containing organic group involves irradiating light ray which excites photosensitizer (C) with respect to cyclic unsaturated compound (A) having unsaturated bond(s) in a ring in presence of sulfinate (B) of formula: (RfSO2)nM (I) having fluorine atom-containing organic group and photosensitizer (C).    Rf=fluoro-containing organic group having at least one fluoro;    M=alkali-metal atom, alkaline-earth metal atom or zinc;and    n=1 or 2.    INDEPENDENT CLAIMS are included for the following:    (1) aromatic compound has fluorine atom-containing organic group, and is of formula (II); and    (2) cyclic unsaturated compound of formula (III) having fluorine atom-containing organic group.    R31-R33=alkoxy or alkyl;    Rf1=fluorine atom-containing 2-20C alkyl having at least one fluoro;    R34=alkoxy or alkyl;and    Rf2=fluorine atom-containing 1-20C alkyl having at least one fluoro.
NOVELTY - Cerium-lanthanum complex oxide desulfurizing agent prepared by mixing lanthanum as an oxidation enhancement component with a cerium group desulfurizing agent, is claimed.    USE - The cerium-lanthanum complex oxide desulfurizing agent is useful in a biomass gasification process, an integrated gasification combined cycle, and a heavy crude oil reforming process.    ADVANTAGE - The desulfurizing agent has excellent desulfurization capacity and sulfur recovery efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing cerium-lanthanum complex oxide desulfurizing agent including mixing a lanthanum precursor solution and a cerium precursor solution to prepare a mixed solution, adding ammonium hydroxide in the mixed precursor solution to adjust the pH value of the mixed precursor solution to 8-13, precipitating a slurry, and filtering the precipitated slurry to prepare a cerium-lanthanum complex oxide particle.
NOVELTY - Preparing a fertilizer, comprises adding 50-60 wt.% of coal pumice stone, 30-40 wt.% of sericite and 10-20 wt.% of clay powder, adding 10-30 wt.% of water to the mixture, extruding the mixture by compression molding and cutting into pellets, drying the obtained pellets, calcining the dried pellets in a calcination furnace to obtain a carrier, immersing the carrier in a microbial culture, soaking the microorganisms fixed carrier in contaminated river, purifying the river water using nitrogen, collecting out the carrier from the river, and drying the collected carrier.    USE - The method is useful for preparing a fertilizer (claimed).    ADVANTAGE - The method is capable of economically and eco-friendly preparing the fertilizer that improves the quality of soil and enhances the crop production.    DETAILED DESCRIPTION - Preparing a fertilizer, comprises adding 50-60 wt.% of coal pumice stone, 30-40 wt.% of sericite and 10-20 wt.% of clay powder, adding 10-30 wt.% of water to the mixture, extruding the mixture by compression molding and cutting into pellets, drying the obtained pellets, calcining the dried pellets in a calcination furnace to obtain a carrier, immersing the carrier in a microbial culture, soaking the microorganisms fixed carrier in contaminated river, purifying the river water using nitrogen, collecting out the carrier from the river, drying the collected carrier, and crystallizing the obtained carrier into granular powder to obtain a fertilizer.
NOVELTY - The device has conveying unit (200) that transfers livestock excretions supplied from supply unit (100). An agitator (300) mixes additive with excretions supplied from conveying unit. The amount of administration is controlled so that control unit receives weight detection signal of the excretions supplied to mixer from the weight perception sensor. The livestock excretions, rice hulls and medicinal herbs are mixed at a rate of 6:3:1 in order to sterilize the mixed content in heater to high temperature. The sterilizing disinfectant is injected by injection control portion.    USE - Device for manufacturing solid fuel using livestock excretions.    ADVANTAGE - The bad smell of livestock excretions generated during the combustion process of the solid fuel can be removed, so that the incense or characteristic of Chinese medicine ingredient of medicinal herbs is seasoned in order to completely remove the bacteria or the harmful microorganism through sterilization. The garbage is reduced and the device is environment-friendly.    DETAILED DESCRIPTION - A compressor compresses the livestock excretions agitated in agitator and the additive supply unit (400) supplies the rice hulls and medicinal herbs to the agitator for fire and reduces odor of solid fuel to agitator. A control unit receives the sensing signal of weight perception sensor and temperature sensor and controls the heater and blower. An injection nozzle sprays fungicide on mixer and a blower discharges the gas generated within the mixer to outside. The solid fuel mixture agitated in the mixer is crushed. An INDEPENDENT CLAIM is included for a method for manufacturing solid fuel using livestock excretions.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the device for manufacturing solid fuel using livestock excretions. (Drawing includes non-English language text)    Supply unit (100)    Conveying unit (200)    Agitator (300)    Additive supply unit (400)    Pellet (500)
NOVELTY - The present invention provides a biological method for the preparation of a compound of formula I; said method comprising the following steps: inoculating the Streptomyces violaceorubidus strain into at least one nutrient medium comprising at least one carbohydrate source to obtain an inoculum, fermenting the, inoculum at a. pH ranging-between .5.5 and 9.0 to obtain a bio-mass comprising 2-chlorobenzene-1,4-diol, adjusting the pH of the bio-mass in the range of 4.5 to 5.5 followed by centrifuging to obtain a separated mass containing mycelia biomass and supernatant, extracting supernatant with at least one organic solvent to obtain a solution containing a mixture of 2-chlorobenzene-1,4-diol and impurities, and purifying the mixture to obtain the compound of formula I.
NOVELTY - The food waste destruction device comprises a unit for stirring the food waste with the speed of 10 revolutions per minute, where the food waste is fermented with sawdust and Bacillus subtilis at 30 degrees C with reduced moisture content of 40%.    USE - Food waste destruction device.    ADVANTAGE - The device effectively treats the food waste.
NOVELTY - Preparing feed cereals comprises: selecting wheat as a raw material; immersing the wheat in water; steaming the wheat; inoculating the strain to perform a fermentation process; performing an enzyme treatment; and drying the wheat.    USE - The method is useful for preparing feed cereals (claimed) for domestic animals including pig and cow.    ADVANTAGE - The feed cereals are prepared in an environment-friendly manner, and can improve physiological function, enzyme activity, growth and digestion rate of the domestic animals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for feed cereal with sugar content of greater than or equal to 35 mg/g.
NOVELTY - This new type utility claims one a vehicle decarbonizing removing, include the hydrogen oxygen generating device, box body is of a rectangular structure, the vertical between hydrogen oxygen generating device is installed in the box body, and the upper surface and the front side surface of the box body is one inclined surface, the air hole, the lower part of the front side surface, water injection hole, upper box body upper surface, water level meter, the front side surface of middle part, used for water level in device identification of hydrogen oxygen generating, operation button, the inclined surface of the box body up, operation for hydrogen oxygen generating device, an air pressure gauge, the inclined surface of upper box body, used for identification of hydrogen oxygen generating device to generate gas of pressure, indicating lamp, the inclined surface of upper box body, used for status of mark hydrogen oxygen generating device, display, the inclined upper surface of the box body, the operation parameter of device identification used for hydrogen oxygen generating, moving wheel, set on upper surface of lower box body. This utility new type not only has compact structure, is easy to move, and operation is convenient, use safety.
NOVELTY - Biogas upgrading process involves filling space of absorbing module with absorbent, injecting bubbling gas to hydrophobic porous hollow fiber membrane, controlling pressure of module by dissolving carbon dioxide of biogas in absorbent, and separating undissolved gas.    USE - Biogas upgrading process (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus for biogas upgrading process.
NOVELTY - L-chloperastine fendizoic acid salt (I) is prepared by reacting isopropyl titanate, methylene dichloride and phenyl Grignard reagent ethyl ether solution to obtain organic titanium reagent; adding organic titanium reagent into mixed solution of chiral ligand (R)-diphenylphenyl-H8-binol, 4-chlorobenzaldehyde, isopropyl titanate and dichloromethane, and reacting to obtain L-4-chlorobenzhydrol; reacting L-4-chlorobenzhydrol with N-(2-chloroethyl)piperidine hydrochloride to obtain L-chloperastine; and adding L-chloperastine and fendizoic acid to obtain compound (I).    USE - Method of preparing L-chloperastine fendizoic acid salt (claimed).    ADVANTAGE - The method has simple operation, reduced cost and reduced three wastes, and actual yield of more than 95%, and is suitable for industrial production. Further, the chiral ligand can be used repeatedly.    DETAILED DESCRIPTION - Preparation of L-chloperastine fendizoic acid salt of formula (I) having measured optical rotation ( alpha ) of -48 to 56 degrees and melting point of 116-124 degrees C at concentration of 0.02 g/ml using chloroform as solvent at 28 degrees C, the method comprises:    (A) reacting isopropyl titanate, methylene dichloride and phenyl Grignard reagent ethyl ether solution to obtain organic titanium reagent;    (B) adding the organic titanium reagent into mixed solution of chiral ligand (R)-diphenylphenyl-H8-binol, 4-chlorobenzaldehyde, isopropyl titanate and dichloromethane, and reacting to obtain L-4-chlorobenzhydrol;    (C) reacting L-4-chlorobenzhydrol with N-(2-chloroethyl)piperidine hydrochloride to obtain L-chloperastine; and    (D) adding L-chloperastine and fendizoic acid to obtain L-chloperastine fendizoic acid salt.
NOVELTY - Method for purifying contaminated underground water using microorganism, involves measuring concentration of pollution, and velocity in trichlorethylene (TCE) contaminated groundwater areas, performing aerobic co-metabolism on path of movement of ground water to cover the micro-organisms in the fixed charge carriers to install permeable reactive barrier, inhaling toluene through the substrate return duct installed at the opposite side of the permeable reactive barrier, adding hydrogen peroxide to permeable reactive barrier, and collecting toluene using suction tube.    USE - The method is useful for purifying contaminated underground water using microorganism (claimed).    DETAILED DESCRIPTION - Method for purifying contaminated underground water using microorganism, involves measuring concentration of pollution, and velocity in trichlorethylene (TCE) contaminated groundwater areas, where the ratio of primary substrate of trichlorethylene and toluene is 1:50-1:70, determining the concentration of the input, performing aerobic co-metabolism on path of movement of groundwater to cover the microorganisms in the fixed charge carriers to install permeable reactive barrier, inhaling toluene through the substrate return duct installed at the opposite side of the permeable reactive barrier, adding 70 mg/l hydrogen peroxide to the permeable reactive barrier, ensuring the circulation of the primary substrate of the permeable reactive barrier installed on the opposite side of the substrate, and collecting toluene using suction tube.
NOVELTY - An osthol botanical insecticide emulsifiable concentrate comprises 10-14 wt.% osthol, 4-8 wt.% anonaine, 2-4 wt.% emulsifier and balance solvent.    USE - Osthol botanical insecticide emulsifiable concentrate.    ADVANTAGE - The insecticide is purely sourced from plants, safe, and environment-friendly.
NOVELTY - The method involves allowing electrolyte to pass through electrolyte pervious inert membranes (16,18) forming boundaries to a first compartment (20) of electrolysis cell (10) into second and third compartments (22,24) of electrolysis cell. A potential difference is applied across a pair of electrodes located in the second and third compartments. The electrolysis products are produced in the second and third compartments through electrolysis of electrolyte in respective compartments. The electrolysis products are withdrawn from second and third compartments of electrolysis cell.    USE - Method for producing electrolysis products such as sodium hydroxide, hydrogen gas, sulphuric acid and oxygen gas using electrolyte such as sodium sulphate (all claimed) for production of metal such as aluminum.    ADVANTAGE - The efficiency of electrolytic cells can be improved, thereby enabling electrolysis products to be produced more efficiently and cost effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the electrolytic cell.    Electrolytic cell (10)    Outer wall (12)    Electrolyte pervious inert membranes (16,18)    Compartments (20,22,24)    Anode (26)
NOVELTY - Fractionating lignocellulosic biomass, involves: (a) providing a feedstock comprising lignocellulosic biomass; (b) contacting the feedstock with sulfur dioxide, water, and optionally a first solvent for lignin; (c) contacting the intermediate solids with sulfur dioxide, water, and a second solvent for lignin; (d) separating and recovering the cellulose-rich solids from the liquid phase; (e) hydrolyzing the hemicelluloses to produce monomeric sugars; and (f) recovering the monomeric sugars.    USE - The process is useful for fractionating lignocellulosic biomass (claimed), preferably for converting biomass into fermentable sugars, cellulose, and lignin.    ADVANTAGE - The process provides fractionated cellulosic products with high purity, and produces cellulose with very low hemicellulose content and/or very low lignin content in an economical manner.    DETAILED DESCRIPTION - Fractionating lignocellulosic biomass, involves: (a) providing a feedstock comprising lignocellulosic biomass; (b) in a first digestor stage, contacting the feedstock with sulfur dioxide, water, and optionally a first solvent for lignin, where the sulfur dioxide is present at a first concentration, to produce intermediate solids and a first liquid phase comprising hemicelluloses and lignin; (c) in a second digestor stage, contacting the intermediate solids with sulfur dioxide, water, and a second solvent for lignin, where the sulfur dioxide is present at a second concentration i.e. different than the first concentration, to produce cellulose-rich solids and a second liquid phase comprising hemicelluloses and lignin; (d) separating and recovering the cellulose-rich solids from the liquid phase; (e) hydrolyzing the hemicelluloses to produce monomeric sugars; and (f) recovering the monomeric sugars.
NOVELTY - Special grain complex biological liquid fertilizer comprises, but not limited to, 6.2-7.2 wt.% EDTA-calcium (Ca); 0.015-0.020 wt.% EDTA-copper (Cu); 7.25-8.32 wt.% EDTA-magnesium (Mg); 0.15-0.25 wt.% EDTA manganese (Mn); 0.042-0.051 wt.% EDTA-zinc (Zn); and 0.15-0.24 wt.% EDTA-iron (Fe).    USE - The special grain complex biological liquid fertilizer is useful in cereal crops for preventing pest, improving soil composition, enhancing crop resistance, enhancing fixed carbon, enhancing soil fertility, and for stimulating crop growth.    ADVANTAGE - The special grain complex biological liquid fertilizer has reasonable grain nutrients for growth cycle to extend and maintain a sustained release through long-lasting supply of microbial fertilizers.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a method of using special grain complex biological liquid fertilizer comprising taking special grain complex biological liquid fertilizer at 2 ml, diluting for 500 times, spraying up just the oat seedling of bud, oat seedling to 20 to 325 cm, then fertilizing one time, and applying at last one time.
NOVELTY - Garage-type dry fermentation of food waste and organic waste involves performing dehydration degreasing pretreatment of food waste, mixing with organic waste, and subjecting to garage-type dry fermentation by mixing food waste and organic waste with fermented raw materials, supplying into anaerobic tank, subjecting to anaerobic fermentation by providing anaerobic environment by supplying inert gas, heating, inoculating, producing biogas, feeding biogas into gas turbine for power generation, recovering waste heat, and discharging after completing anaerobic fermentation.    USE - Garage-type dry fermentation of food waste and organic waste (claimed).    ADVANTAGE - The garage-type dry fermentation of food waste and organic waste is performed by simple and economical method.    DETAILED DESCRIPTION - Garage-type dry fermentation of food waste and organic waste involves collecting food waste, subjecting to dehydration degreasing pretreatment, mixing with organic waste, and subjecting to garage-type dry fermentation by mixing food waste and organic waste with fermented raw materials, such that the ratio of waste and fermented materials is 40:60-60:40, supplying into anaerobic tank and into garage, subjecting to anaerobic fermentation by closing hydraulic doors, providing anaerobic environment by supplying inert gas, heating at 36-40 degrees C, providing liquid spray system on the top of tank for uniformly spraying materials, inoculating, collecting inoculum for recycling through tank bottom drain system, producing biogas by anaerobic fermentation before dehydration and desulfurization process, feeding purified biogas into gas turbine for power generation, recovering waste heat for heating anaerobic tank and for drying biogas, and discharging after completing anaerobic fermentation. The fermentation is repeated for new batch materials. The organic waste comprises garden waste, sewage treatment plant sludge, straw, animal waste and/or sawdust.
NOVELTY - Manufacture of biodiesel involves mixing waste cooking oil, catalyst, and sodium hydroxide or alcohol, heating at 40-60 degrees C, maintaining the resultant mixture, obtaining lower layer of glycerine and upper layer of biodiesel and separating the upper layer of biodiesel.    USE - Manufacture of biodiesel (claimed).
NOVELTY - Biodegradation process for generating biogas and composting biogas from material including agricultural waste, comprises performing pretreatment step by aerobic composting a material on an open platform, and performing anaerobic methanization of the pretreated material in a methanizer.    USE - The biodegradation process is useful for the generation of biogas and composting biogas from material including agricultural waste derived from small farms with no regular production and different activities depending on the season (all claimed), where the biogas is useful as thermal energy, electrical generation energy or biofuel.    ADVANTAGE - The biodegradation process ensures simple, efficient and economical generation of biogas with good quality and without environment pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for biodegradation process, comprising a sealed composting platform provided with a unit for recovering juice and a device (such as methanizer) for anaerobic fermentation provided with biogas outlet.
NOVELTY - Fuel in the form of compacted granules, comprises 40-60 mass% of wood particles, 20-30 mass% of two mixtures derived from sorting, grading and sieving of agricultural production of cereals, oilseeds or protein crops, and 10-25 mass% of fine fossil coal or wood charcoal.    USE - The fuel is useful in boiler or industrial coal furnace (claimed), where the boiler is a thermal power plant.    ADVANTAGE - The fuel prevents the heat exchangers and/or superheater of the boiler against rapid corrosion thus improving the life of the boiler without increasing the maintenance costs of the boiler, is economical to produce, and has high stability and quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the fuel comprises mixing wood particles, two mixtures derived from sorting, grading and sieving of agricultural production of cereals, oilseeds or protein crops and fine fossil coal or wood charcoal, crushing the mixture so as to from a homogenate powder, mixing the powdered homogenate, and compacting the mixed ground material so as to obtain compacted granules with a density of 450-650 kg/cm3.
NOVELTY - The method involves applying source at high temperature in the form of plasma which is generated with a plasma carrier. The starting material (23) is exposed to high temperature as long as the plasma exposed to high temperature is completely gasified. The starting material is supplied either in the form of plasma carrier substance or in the form of additional auxiliary material while the chemical elements for production of desired gas is provided in the required amount in the required state.    USE - Method for converting starting material e.g. carbonaceous feedstock, sand or carbon-containing starting material such as green waste, plastic waste into gas in treatment chamber. Can also be used in polyethylene terephthalate (PET) plastic waste such as shredded PET bottles.    ADVANTAGE - he supplied amount of energy for the conversion process is reduced. The resulting gaseous products are not toxic and ash formation is minimized. The conversion process can be controlled in simple manner. The equipment and energy cost are reduced. The erosion of the electrodes can be reduced. The additional compaction of the starting material can be achieved. The service life of the device for converting starting material into gas can be prolonged.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for converting starting material into gas in treatment chamber.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the treatment apparatus.    Treatment chamber (1)    Outside wall (2)    Energy delivery device (3)    Core (12)    Starting material (23)
NOVELTY - Method for culturing combination of facultative anaerobic bacterium and aerobic bacterium, involves using base material which disposes organic waste by decomposition.    USE - The method is useful for culturing combination of facultative anaerobic bacterium and aerobic bacterium (claimed).    ADVANTAGE - The method is rapid, and provides good quality manure. The manure has resource recycling effect.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for culturing microbe using aerobic bacterium and facultative anaerobe of Paenibacillus, Bacillus novalis, B.oleronius and Lactobacillus; and (2) method for culturing base material.
NOVELTY - The digester has a lifting steel structure provided with a vertical element that is provided with a circumference chamber. Shape of a wheel is same as that of the circumference chamber. The vertical element is placed in a steel disk. Motherboards are connected with connectors by the steel disk. Internal edge of the vertical element is provided with fixed structural vertical heating elements. A central portion of steel plates is mounted with a power valve. The upper part of an enclosure chamber is set with an overflow valve.    USE - Digester for a bio-gas power plant.
NOVELTY - The gasifier has a tar decomposition modification catalyst layer (6) which is arranged by the freeboard unit (5). A removal unit (7) removes the particulate-form deposit and precipitation carbon adhering to the tar decomposition modification-catalyst layer. A vapor is sprayed for the removal unit from a nozzle (7b) as an injection fluid with respect to the particulate-form deposit of the tar decomposition modification catalyst layer. Soot blower (7a) sprays air or oxygen from a nozzle with respect to the precipitation carbon of the tar decomposition modification-catalyst layer.    USE - Fluidized-bed gasifier for fuel gasification equipment using solid fuels, e.g., coal, biomass, waste plastic, or wet waste as fuel.    ADVANTAGE - Suppresses temperature fall of gasifying gas, modifies tar efficiently, and has simple structure at low cost since cyclone-type particle isolation unit in gasifier main body is not necessary to provide.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional side view of the fluidized-bed gasifier. (Drawing includes non-English language text).    Freeboard unit (5)    Tar decomposition modification catalyst layer (6)    Removal unit (7)    Soot blower (7a)    Nozzle (7b)
NOVELTY - The system (1) has a collection part (20) provided in a middle of a sample gas flow path (10), and collecting to-be-measured gas as a liquid or solid. A cooling unit (21) is provided in the collection part. The sample gas flow path conveys the sample gas. A heating part (25) heats and vaporizes liquid or solid. Carrier gas is supplied in the flow path. A carrier gas supply part (40) entrains a to-be-measured gas to the carrier gas, where the to-be-measured gas is introduced into a gas chromatograph (50).    USE - System for analyzing sample gas to measure quantity of to-be-measured gas e.g. gas of sulfur compound such as hydrogen sulfide and methyl mercaptan, hydrocarbon gas such as propane and butane, inorganic gas such as carbon dioxide and nitrous oxide.    ADVANTAGE - The system is highly sensitive, highly accurate, and measures quantity of the to-be-measured gas contained in sample gas by simple operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for analyzing a sample gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a system for analyzing a sample gas.'(Drawing includes non-English language text)'    System for analyzing sample gas (1)    Sample gas flow path (10)    Collection part (20)    Cooling unit (21)    Heating part (25)    Carrier gas supply part (40)    Gas chromatograph (50)
NOVELTY - The anaerobic digester apparatus comprises a gas jet agitator using streams of recycled methane gas injected from intake ports by a compressor, and a heater that is provided with heater pipes and maintains a temperature at 85-105 degrees F.    USE - The anaerobic digester apparatus is useful for producing methane-rich biogas from water lily (claimed).
NOVELTY - Preparing fatty acid alkyl esters from Moringa oleifera seed oil involves: (a) base-catalyzed and acid-catalyzed transesterification of Moringa oleifera seed oil; (b) in situ transesterification of Moringa oleifera seeds using acid catalyst; (3) transesterification of Moringa oleifera seed oil using free enzyme; (d) transesterification of Moringa oleifera seed oil using immobilized enzymes employing sol-gel method and carbon nanoparticles immobilization technique.    USE - The method is useful for preparing fatty acid alkyl esters from Moringa oleifera seed oil (claimed).    ADVANTAGE - Immobilization and recycling methods for enzyme catalyst lead to alternative options for fatty acid alkyl ester production resulting in operationally easier and more efficient production routes that can generate less by-products and wastes and requires less energy.
NOVELTY - Silicon extraction from agro-industrial waste involves using the natural extractant citric acid that is derived from waste from the citrus industry. Silicon is extracted from rice husk leading to obtain silicate organic fertilizer.    USE - Method for extracting silicon from agro-industrial waste (claimed).    ADVANTAGE - The method enables to extract silicon from agro-industrial waste that is beneficial to agribusiness by producing organic fertilizer silicate, and is eco-friendly.
NOVELTY - Producing bio-gas comprises: introducing organic wastewater including sewage and livestock excretion into a sludge solubilization facility via a waterspout venturi tube; carrying out sludge solubilization process; measuring the sludge effluent in the solubilization facility and then settling, and supplying the obtained mixture to a flux control tank and then supplying into a digestion tank; and supplying a gas from an outerside of the digestion tank to the mixture and then purifying in a purification discharge facility, and recycling the remaining sludge.    USE - The method is useful for producing bio-gas (claimed) such as methane gas.    ADVANTAGE - The method is capable of rapidly and economically producing the bio-gas with less resource and energy consumption, high production efficiency and high dissolved organism concentration.
NOVELTY - Bioreactor has immobilized enzyme and reaction zone comprising heterocyclic compound comprising 5 or 6-membered ring of nitrogen and carbon, where enzymatic reaction is carried out at the reaction zone using the immobilized enzyme.    USE - The bioreactor is useful for e.g. preparing amino acid, peptide, and organic acid, and in petrochemical industry.    ADVANTAGE - The bioreactor is excellent in reaction efficiency in reaction zone. The bio-fuel cell has excellent battery characteristic, as enzyme activity of immobilized enzyme is significantly improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) enzyme activity improvement method of the above-mentioned immobilized enzyme; and    (2) bio-fuel cell.
NOVELTY - The method involves moving hydrocarbons-containing waste stock from a loading chamber (1) into a reactor chamber through a conveyor belt. The loading chamber is connected with a feed auger (2) that is connected to a compacting chamber (3) for removing air from the waste stock. The air removed stock from the compacting chamber is moved towards a stock grinder (4) for grinding the waste stock without supplying air. A degassing chamber (5) is provided with an upper bolt (6) and a lower bolt (7) that are closely connected with a gate valve.    USE - Method for preparing and feeding finely divided and sorted waste stock into a gas-tight waste incineration equipment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a gas-tight waste incineration equipment.    Loading chamber (1)    Feed auger (2)    Compacting chamber (3)    Stock grinder (4)    Degassing chamber (5)    Upper bolt (6)    Lower bolt (7)
NOVELTY - Method for producing fuel, involves using animal ruminant, preferably Bubalus bubalis.    USE - The method and system are useful for producing fuel, preferably ethanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for producing fuel.
NOVELTY - An activated sludge is reduced by cultivating in heterotrophy the algae which belong to the Parachlorella genus and adding the culture medium containing the algae or its dry body after cultivation to the aerator of a waste-water treatment plant.    USE - Reduction of activated sludge used for processing waste water (claimed).    ADVANTAGE - Amount of surplus sludge is reduced and cost of waste water treatment is lowered.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a processing of waste water which involves reducing activated sludge.
NOVELTY - Multi-component- and multi-phase nozzle for treating biomass for a biogas plant comprises a central tube (17), which ends with a nozzle in the mouth area of a mixing chamber (35), and a gap, which annularly surrounds the mouth of the central tube. A cleaning device (18) is introduced in the central tube up to a nozzle mouth (20).    USE - The multi-component- and multi-phase nozzle is useful for treating biomass for biogas plant.    ADVANTAGE - The multi-component- and multi-phase nozzle is operated in a cost efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for treating organic waste in a biogas plant with a storage container (5) for the preparation of a mixture and the multi-component- and multi-phase nozzle for treating the prepared mixture, comprising temporarily storing an inoculum suspension as a microbial seed carrier in a separate container for the incubation and proliferation of microorganisms and injecting as a vaccine into the mixture.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Storage container (5)    Central tube (17)    Cleaning device (18)    Nozzle mouth (20)    Mixing chamber (35)
NOVELTY - Cold temperature stable micro emulsion concentrate composition comprises: (a) 5-15 wt.% of an alkyl fatty acids mixture (I) consisting of 20-80 wt.% 8C fatty acids, 20-80 wt.% 9C fatty acids, 10-50 wt.% 10C fatty acids, and 0-30 wt.% 12C fatty acids, or an alkyl fatty acids mixture (II) consisting of 20-80 wt.% 9C fatty acids, 10-50 wt.% 10C fatty acids, and 10-30 wt.% 12C fatty acids; (b) 20-60 wt.% L(+)-lactic acid and/or 0-40 wt.% phosphoric acid; and (c) 20-40 wt.% 8-16C mono- and/or di-alkyldiphenyloxide disulfonate surfactants.    USE - The cold temperature stable micro emulsion concentrate composition is useful: for forming a ready to use product (when diluted with water) (claimed); and as bactericidal, fungicidal and virucidal compositions.    ADVANTAGE - The cold temperature stable micro emulsion concentrate composition: is environmentally safe; has low volatile organic compounds, and no maximum residue limit; and is safe for the end user.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a ready to use antibiotic cleaner comprising 0.02-0.2 wt.% 9C fatty acids, or 9C ,10C and 12C fatty acids, 0.5-2 wt.% L(+)-lactic acid, and 0.5-4 wt.% 8-16C mono- and/or di-alkyldiphenyloxide disulfonate or fatty alcohol ethoxylate surfactants, optionally an essential oil, and optionally a food flavoring.
NOVELTY - Preparing alkylate, comprises: (a) in a reaction zone, reacting a hydrocarbon mixture comprising at least an isoparaffin and an olefin with an ionic liquid catalyst to obtain an effluent comprising alkylate and solids; (b) separating, in a separator unit, a hydrocarbon-rich phase and an ionic liquid catalyst-rich phase which latter phase also comprises solids formed as side products during the alkylation reaction, from the effluent; and (c) separating the solids in ionic liquid catalyst-rich phase from the ionic liquid catalyst using a suitable separating device.    USE - The process is useful for preparing an alkylate using an ionic liquid catalyst (claimed).    ADVANTAGE - The process ensures much easier and more efficient solids removal from the ionic liquid by adding an organic solvent prior to the solids removal step, thus reducing the process time and energy.    DETAILED DESCRIPTION - Preparing alkylate, comprises: (a) in a reaction zone, reacting a hydrocarbon mixture comprising at least an isoparaffin and an olefin with an ionic liquid catalyst to obtain an effluent comprising alkylate and solids, which latter are formed as side products in an alkylation step; (b) separating, in a separator unit, a hydrocarbon-rich phase and an ionic liquid catalyst-rich phase which latter phase also comprises solids formed as side products during the alkylation reaction, from the effluent; and (c) separating the solids in ionic liquid catalyst-rich phase from the ionic liquid catalyst using a suitable separating device. The process further comprises, following the separation step (b) and prior to the solids removal step (c), adding an organic solvent to the ionic liquid catalyst-rich phase, which organic solvent has a viscosity which is significantly lower than that of the ionic liquid and which solvent is at least partially miscible with the ionic liquid.
NOVELTY - Telmisartan intermediate preparation involves treating 4-amino-3-methylbenzoic acid (I) in presence of sodium nitrite to obtain 4-amino-3-methyl-5-nitrosobenzoic acid (II), where 4-amino-3-methyl-5-nitrosobenzoic acid reacts with sodium dithionite to obtain 3,4-diamino-5-methylbenzoic acid (III). The obtained 3,4-diamino-5-methylbenzoic acid undergoes cyclization reaction with triethoxy-butane to obtain 4-methyl-6-(prop-1-en-2-yl)-2-propyl-1H-1,3-benzodiazole (IV).    USE - Method for preparing telmisartan intermediate (claimed).    ADVANTAGE - The method enables to produce telmisartan intermediate in a cost-effective and eco-friendly manner with improved yield of product.    DETAILED DESCRIPTION - Telmisartan intermediate preparation involves treating 4-amino-3-methylbenzoic acid of formula (I) in presence of sodium nitrite to obtain 4-amino-3-methyl-5-nitrosobenzoic acid of formula (II), where 4-amino-3-methyl-5-nitrosobenzoic acid reacts with sodium dithionite to obtain 3,4-diamino-5-methylbenzoic acid of formula (III). The obtained 3,4-diamino-5-methylbenzoic acid undergoes cyclization reaction with triethoxy-butane to obtain 4-methyl-6-(prop-1-en-2-yl)-2-propyl-1H-1,3-benzodiazole of formula (IV).
NOVELTY - Organic fertilizer comprises 80-120 pts. wt. of traditional Chinese medicine slag, 40-100 pts. wt. of straw, 10-40 pts. wt. of wheat bran, 1.5-8 pts. wt. of fungus liquid and 0.13-3 pts. wt. of bacteria liquid.    USE - The organic fertilizer is useful for planting vegetable (claimed).    ADVANTAGE - The organic fertilizer is eco-friendly, and has organic matter content of higher than 50%, nitrogen-phosphorus-potassium of more than 6% and improved soil property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing organic fertilizer comprising collecting traditional Chinese medicine dregs, straw and wheat bran, crushing the collected material into granule with grain diameter of 0.4-0.8 cm, crushing the traditional Chinese medicine dregs exposure for 10-12 hours in low light, then adding traditional Chinese medicine residue, straw and bran according to proportion, uniformly stirring and mixing, spraying fungus liquid, piling and fermenting at normal temperature for 5-10 days and 3-5 weeks, spraying the bacterial liquid, uniformly mixing, piling and fermenting at normal temperature for 3-5 days and 3-4 weeks, then air drying or drying.
NOVELTY - A gas introduction method involves introducing gas into the fuel cell system where the temperature of the solid oxide fuel cell part (2) is lower than the temperature of the fuel production unit. Fuel production unit (1) produces fuel gas by oxidation reaction and is reproducible by reduction reaction. Solid oxide fuel cell part produces electric power by reaction of oxidizing agent gas which contains oxygen and fuel gas supplied from the fuel production unit. Gas is circulated between the fuel production unit and the fuel electrode (2B) of the fuel cell part.    USE - Gas introduction method for fuel cell system (claimed).    ADVANTAGE - Oxidation of metal in the fuel electrode and performance reduction are suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel cell system structure. (Drawing includes non-English language text).    Fuel production unit (1)    Solid oxide fuel cell part (2)    Solid oxide electrolytic membrane (2A)    Fuel electrode (2B)    Oxidizing agent electrode (2C)
NOVELTY - A fertilizer comprises 30-70 pts. wt. nitrogenous fertilizer, 25-50 pts. wt. potash fertilizer, 10-20 pts. wt. phosphate fertilizer, 2.5-5 pts. wt. boron fertilizer, 2-7 pts. wt. calcium carbonate, 8-25 pts. wt. farm manure, 0-6 pts. wt. lime, and 0.5-8 pts. wt. fermented oil cake. The fermented oil cake is prepared by fermenting rapeseed oil, taking cake residue, adding water to form paste, and fermenting.    USE - Fertilizer used for mature orange tree (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fertilizing method comprising applying 10% total amount of fertilizer in germination period; applying 15% total amount of fertilizer in flowering period; applying 25% total amount of fertilizer when swelling fruit; applying 10% total amount of fertilizer in picking recovery period; applying 10% total amount of fertilizer during winter; applying 10% total amount of fertilizer and water mixture during spring and spraying 2-3 times on leaf surface; applying 10% total amount of fertilizer and water mixture during summer and spraying 2-3 times on leaf surface; and applying 10% total amount of fertilizer and water mixture during autumn and spraying 2-3 times on leaf surface.