NOVELTY - A disposable sterile syringe piston comprises 1.0-2.5 pts. wt. activated zinc oxide, 0.5-1.5 pts. wt. stearic acid, 1.0-2.0 pts. wt. environment-protecting antioxidant 1010, 10-15 pts. wt. carbon black N330, 50-60 pts. wt. calcined clay, 1.5-3.0 pts. wt. Vaseline (RTM: petroleum jelly based product), 0.2-0.6 pt. wt. accelerant tetramethylthiuram monosulfide (TMTM), 0.2-0.5 pt. wt. accelerant TRA, 1.0-2.0 pts. wt. sulfur, and 100 pts. wt. isoprene synthetic rubber.    USE - Disposable sterile syringe piston.    ADVANTAGE - The piston has good biological performance index and antiaging performance, strong resilience force, and good sealing property. It saves great amount of energy and reduces environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of disposable sterile syringe piston comprising uniformly mixing raw materials except isoprene synthetic rubber to obtain mixture, plasticizing isoprene synthetic rubber, uniformly mixing with mixture, preparing into film, molding, vulcanizing at 165-175 degrees C for 210-240 seconds to prepare semi-finished product, drying, detecting qualified products, packing and storing in storehouse.
NOVELTY - An orange fluorescence-emitting nitrogen-sulfur co-doped carbon quantum dot is synthesized by stirring L-cystine and L-serine in purified water to dissolve and obtain precursor solution in which molar ratio of L-cystine:L-serine is 1:0.5-2 and mole-to-volume ratio of L-cystine:purified water is 5 mmol:15-25 ml, placing in reaction vessel, sealing reaction vessel, reacting at 160-220 degrees C for 2-8 hours, cooling at room temperature to obtain reddish brown turbid solution, and centrifuging.    USE - Synthesis of orange fluorescence-emitting nitrogen-sulfur co-doped carbon quantum dot used in biological imaging, cell labeling, and security study.    ADVANTAGE - Synthesis is simple and environment-friendly and has low cost, short period, and good repeatability.    DESCRIPTION OF DRAWING(S) - The drawing shows a transmission electron microscope image of an orange fluorescence-emitting nitrogen-sulfur co-doped carbon quantum dot.
NOVELTY - This utility new type claims a a stack fertilizer machine, comprising the fermentation chamber, the fermentation chamber upper end orderly provided with feeding wherein a discharge wherein, conveying device, stirring device, the stirring device is set on the bottom of the fermentation cabin ventilation device, said ventilation device is set below said stirring device, water heating device, comprising solar energy heat-collecting plate, a water pipe b is inner the fermenting chamber inner wall is set up a fermenting chamber and inner surface of spray head, a solar energy heat-collecting plate, a water pipe and a spray head connected in turn, the solar energy heat collecting plate connected the outside water source, tail pneuma treatment device, and a connection port. Through a solution, in the existing technology is a constant temperature hot water insulating layer a modify to make it ferment cabin for a water supply, a humidity water satisfy claim when organic matter fermentation, and water through a solar energy heating, energy-saving and environment-friendly, and the added tail pneuma treatment device, the machine tail pneuma compost discharging clean without pollute.
NOVELTY - Biogas recycling method involves pressing biogas containing methane and carbon dioxide primarily, supplying methane with purity of more than 97% through membrane for biogas, separating mixed gas of methane and carbon dioxide to permeate membrane primarily, pressing mixed gas secondarily, and separating carbon dioxide in mixed gas by fixed reaction with calcium carbonate secondarily. The methane separated in secondary separation has purity of more than 97%. The membrane is made of polysulfone and/or polyimide. The pressing is carried out at pressure of less than 2 bar.    USE - Biogas recycling method (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for recycling biogas.
NOVELTY - A refreshing air purification liquid comprises 3-6 pts. wt. diatomite, 5-7 pts. wt. sodium polyphosphate, 2-8 pts. wt. sepiolite clay powder, 1-5 pts. wt. gallium oxide, 3-9 pts. wt. modified soybean phospholipid, 2-5 pts. wt. cypress, 1-5 pts. wt. Ginkgo, 2-8 pts. wt. citric acid, 4-9 pts. wt. sandalwood oil, 3-8 pts. wt. tartaric acid, 2-6 pts. wt. sodium fluoride, 1-4 pts. wt. butane, 6-11 pts. wt.attapulgite clay, and 4-7 pts. wt. Angelica dahurica.    USE - Refreshing air purification liquid used for killing and inhibiting bacteria in air.    ADVANTAGE - The purification liquid has good refreshing effect and good smell.
NOVELTY - The system has a dirt suction pump station connected to a bottom suction sewage biogas pool. A separated sewage dewatering machine comprises a machine framethat is connected with a memory preheating slag. A slurry storage tank is provided with a sieving machine. The memory preheating slag is provided with a guide chute, an overflow pipe, a drain pump, a seri-flux stir device and a sedimentation dung dirt diluting device. An upper part of the slurry tank is welded with a distributor fixing frame.    USE - Marsh gas fermentation pool silt cleaning device system.    ADVANTAGE - The system performs sedimentation dirt cleaning process in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a marsh gas fermentation pool silt cleaning device system construction method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a marsh gas fermentation pool silt cleaning device system.
NOVELTY - Removing heavy metal from industrial wastewater involves grinding industrial waste and then absorbing it in an absorbing pool through solid-liquid separation process. Wastewater is filtered, where leaching process is carried out in a biological leaching filter chamber, and heavy metal is removed from sludge by a filter press. Alkali is added in the sludge to neutralize pH value (6-7) and then electric flocculation and floating process are carried out by using a floating device to obtain supernatant. A sludge disposal device is utilized for removing harmful content of solid waste.    USE - Method for removing heavy metal from industrial wastewater (claimed).    ADVANTAGE - The method enables to remove heavy metal from industrial wastewater in a simple manner.
NOVELTY - Producing organic fertilizer from domestic garbage involves sorting of household garbage, such as organic matter, low water containing sludge, manure, crushed plant straw, nitrogen ( greater than or equal to 1%), potassium ( greater than or equal to 2%) and phosphorus ( greater than or equal to 1.5%) elements. Anaerobic fermentation is carried out of the household garbage at 35-37 degrees C for 20-30 minutes to evolve marsh gas and then composting for 9-10 days.    USE - Method for producing organic fertilizer from domestic garbage (claimed).    ADVANTAGE - The method enables to produce high quality organic fertilizer garbage.
NOVELTY - 1-Methoxynaphthalene and succinic anhydride are dissolved in dichloromethane, stirred, and cooled to 1-3 degrees C. Aluminum chloride is dripped to solution. The solution is heated at 35 plus minus 2 degrees C for 5.5-6.5 hours, to obtain menbutone.    USE - Synthesis of menbutone (claimed).    ADVANTAGE - The method enables environmentally-friendly and economical synthesis of menbutone with reduced toxicity and yield of 86.4%, by simple method. The solvent used during synthesis of menbutone is efficiently recycled.
NOVELTY - Preparation of florfenicol involves adding crude florfenicol to N,N-dimethylformamide, heating at 40-80 degrees C for 3-6 hours, cooling to room temperature, crystallizing, filtering, washing, and vacuum-drying for 4-8 hours. The mass ratio of crude florfenicol and N,N-dimethylformamide is 1:3-4.    USE - Preparation of florfenicol (claimed).    ADVANTAGE - The florfenicol having excellent stability and quality is prepared with high yield and purity by environmentally-friendly, economical and simple process.
NOVELTY - Nondestructive continuous pyrolysis of hardwood chips involves introducing wood chips into tube-type screw conveyor which has external jacket for progressive heating uniformly propelled charge using volatile products of pyrolysis, withdrawing and cooling of product of reaction instantaneously in countercurrent manner to affect cooling and provide heat for incoming charge, isolating volatile products of pyrolysis by rotary valves, and direct-and-indirect heating of woodchips in a countercurrent manner using hot gases generated by combustion of methanol.    USE - Nondestructive continuous pyrolysis of hardwood chips for use in production of methanol used as fuel.    ADVANTAGE - The method is carried out efficiently at high temperature in absence of oxygen.
NOVELTY - Organic fertilizer comprises 5-20 pts. wt. or 5-10 pts. wt. chicken manure, 5-20 pts. wt. or 8-12 pts. wt. peanut bran, 2-10 pts. wt. or 3-6 pts. wt. soybean flour, 3-15 pts. wt. or 2-5 pts. wt. oatmeal, 1-10 pts. wt. or 2-5 pts. wt. fish meal, and 50-200 pts. wt. or 100-150 pts. wt. water, where the organic fertilizer is prepared by evenly mixing the above-mentioned materials in fermentation vessel, performing fermentation at 20-30 degrees C, and sealing the vessel for 25-30 days.    USE - The organic fertilizer is useful for growth of D.candidum (claimed).    ADVANTAGE - The organic fertilizer has enriched content of nitrogen, phosphorus, potassium and protein content, and increases crude polysaccharide content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for applying the organic fertilizer to Dendrobium candidum, which involves diluting organic fertilizers for 50-fold, and spraying diluted product on plants, during growing season of D.candidum, where spraying is performed once in every 10 days.
NOVELTY - Method for preparing fertilizer, involves uniformly mixing dried wheat bran and soybean, adding Bacillus subtilis and Aspergillus niger to obtained mixture, aerobically fermenting the mixture, regulating moisture content of the mixture at 45-55% on third day, fermenting the mixture for 5-7 days, adding water to fermented product, performing primary extraction of obtained mixture to obtain extract (A), then performing secondary extraction to obtain extract (B), and mixing the extract (A) and extract (B) to obtain product.    USE - The method is useful for preparing fertilizer (claimed), preferably foliar fertilizer.    ADVANTAGE - The method prepares fertilizer which promotes growth of seedling. The fertilizer improves yield of crops, and reduces incidence of disease of crops.    DETAILED DESCRIPTION - Method for preparing fertilizer, involves uniformly mixing dried wheat bran and soybean, adding Bacillus subtilis and Aspergillus niger to obtained mixture, maintaining moisture content of the mixture at 50-65%, aerobically fermenting the mixture, regulating moisture content of the mixture at 45-55% on third day, turning the mixture, continuously fermenting the mixture for 5-7 days, adding water to fermented product, performing primary extraction of obtained mixture to obtain extract (A), then performing secondary extraction to obtain extract (B), and mixing the extract (A) and extract (B) to obtain product.
NOVELTY - Method for preparing organic fertilizer, involves weighing rice hull, duck excrement, wine residue, bean dregs, starch and traditional Chinese medicine additive, where the traditional Chinese medicinal additive comprises honeysuckle, purslane, plantain, medicated leaven and radix phytolaccae, mixing weighed materials, performing fermentation at 22-25 days, adding calcium chloride powder, mixing materials, drying fermented product at 120 degrees C for 8 minutes, crushing dried material, and granulating crushed product.    USE - The method is useful for preparing organic fertilizer (claimed) which is useful for controlling fungi and nematodes, preventing root rot disease, and increasing soil fertility.
NOVELTY - Preparing fertilizer granule involves fermenting liquid culture inoculated with micro-organism. The fermented slurry is freeze-dried in vacuum to obtain solid block that is pulverized to obtain powder. The obtained powder is mixed with additive and bulking agent to obtain mixture that is granulated to obtain product.    USE - Method for preparing fertilizer granule (claimed).
NOVELTY - Preparing biofertilizer involves (a) mixing 20-35 pts. wt. Lactobacillus plantarum, 1-2 pts. wt. phosphate-solubilizing bacteria, 2-4 pts. wt. potassium solution, 10-15 pts. wt. Bacillus subtilis, and 8-15 pts. wt. Aspergillus awamori, and (b) granulating the mixture using a granulator into granules having particle size of 0.5-2 mm, adding 5-8 pts. wt. polyglutamic acid into fertilizer particles, and maintaining temperature at 30-40 degrees C for 1-3 hours.    USE - The method is useful for preparing biofertilizer (claimed).    ADVANTAGE - The prepared biofertilizer increases soil fertility, and drought resistance property food plants, regulates acid-base balance of soil, and reduces harmful substance such as nitrite in soil.
NOVELTY - Method for pre-treating lignocellulose raw material involves soaking lignocellulose raw material in diluted acid solution at room temperature, performing steam explosion of soaked lignocellulose raw material at 180-220 degrees C and 1.2-1.6 MPa, and adding calcium hydroxide, performing high temperature cooking process, reacting calcium hydroxide and carbon dioxide in the cooked mixture, and reducing pH of the reacted product.    USE - The method is useful for pre-treating lignocellulose raw material (claimed).    ADVANTAGE - The method enables to pre-treat lignocellulose raw material in a simple and cost-effective manner.
NOVELTY - Fertilizer composition preparation involves taking 30-32% dry pig manure, 16-18% pond mud, 10% peanut straw stick, 6% rapeseed cake, 10% lees, 6% pulp, 5% mildew feed, 1% organic fertilizer leavening agent, 7% amino acid waste liquid, 6% diammonium phosphate, 0.4% humic acid chelated iron, 0.4% humic acid chelated calcium and 0.2% humic acid chelated magnesium, and then crushing pig manure, pond mud, peanut straw stick, rape seed cake, lees, pulp, mildew feed, organic fertilizer leavening agent. The crushed material is fermented for 31-33 days.    USE - Method for preparing fertilizer composition used for cultivating Lepidogrammitis drymoglossoides (claimed).    ADVANTAGE - The method enables to prepare fertilizer composition, which ensures improved disease resistance, drought resistance and cold resistant abilities, and quality and yield of the tree.    DETAILED DESCRIPTION - Fertilizer composition preparation involves taking 30-32% dry pig manure, 16-18% pond mud, 10% peanut straw stick, 6% rapeseed cake, 10% lees, 6% pulp, 5% mildew feed, 1% organic fertilizer leavening agent, 7% amino acid waste liquid, 6% diammonium phosphate, 0.4% humic acid chelated iron, 0.4% humic acid chelated calcium and 0.2% humic acid chelated magnesium, and then crushing pig manure, pond mud, peanut straw stick, rape seed cake, lees, pulp, mildew feed, organic fertilizer leavening agent. The crushed material is fermented for 31-33 days. The obtained material is mixed with crushed diammonium phosphate, humic acid chelated with iron, humic acid chelated with calcium , humic acid chelated with magnesium. The obtained mixture is mixed with filtered amino acid waste liquid, and then pH of the obtained mixture is adjusted to 7 by using alkali to obtain the finished product.
NOVELTY - Preparation of saxagliptin intermediate (VIII) involves deprotecting adamantane carboxylic acid intermediate (VII) in presence of nitrogen, and subjecting to tert-butoxycarbonyl protection.    USE - Preparation of saxagliptin intermediate (claimed).    ADVANTAGE - The method enables economical, easy and environmentally-friendly preparation of saxagliptin intermediate having high optical purity and chemical purity under mild reaction conditions.    DETAILED DESCRIPTION - Preparation of saxagliptin intermediate of formula (VIII) involves deprotecting adamantane carboxylic acid intermediate of formula (VII) in presence of nitrogen, and subjecting to tert-butoxycarbonyl protection.    Rl=optionally substituted phenyl;and    R2=hydroxy or alkoxy.
NOVELTY - Perishable organic oxidizing agent comprises 10-35% hydrogen peroxide solution and alkaline protecting agent.    USE - Perishable organic oxidizing agent used for processing organic waste and agricultural fertilizer.    ADVANTAGE - The perishable organic oxidizing agent is eco-friendly in nature, and ensures improved degradation of heavy metal from organic waste.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a perishable organic oxidizing agent processing system, which comprises oxidation unit (1), biological acidification unit (2) and solid-liquid separating machine (4), where oxidation unit and biological acidification unit are connected, and biological acidification unit and solid-liquid separating machine is connected; and    (2) a method for preparing perishable organic oxidizing agent, which involves mixing hydrogen peroxide solution and alkaline protecting agent, and then adjusting pH of the obtained mixture to 6.5, where temperature is maintained at 60-110 degrees C; processing the obtained material through perishable organic oxidizing agent processing system, and then performing solid-liquid separation to obtain 50-70% solid matter, which comprises solid matter, nitrogen fertilizer, phosphorus fertilizer, potassium fertilizer and humic acid in 10-79.5:10-50:5-27:5-20:0.5-3 mass ratio to obtain the finished product.
NOVELTY - A methanol gasoline composite additive comprises 5-30 vol.% hydrocarbon compound, 5-15 vol.% ether-type compound, 5-30 vol.% alcohol compound, 5-15 vol.% ester compound, 0-5 vol.% high energy agent, 5-15 vol.% plasticizer, 5-15 vol.% cleaning agent, 0.01 vol.% nano-catalyst, and 1-15 vol.% antioxidant preservative.    USE - Methanol gasoline composite additive (claimed).    ADVANTAGE - The additive has easily available raw materials, low toxicity, increased explosive combustion efficiency and heat value, high stability and quality, good startability, performance, and water resistance, long-term storing property, and no sulfur, phosphorus, benzene, and heavy metals, is economic and environment-friendly, improves oil cleanness, and restrains metal corrosion.
NOVELTY - A mushroom cultivation base material comprises 52-58 pts. wt. biogas fermented residue, 3-4 pts. wt. urea, 2-5 pts. wt. calcium superphosphate, 10-12 pts. wt. rapeseed shell, 1-3 pts. wt. rapeseed cake fertilizer, 0.2-0.4 pt. wt. lime and 1.8-2.2 pts. wt. gypsum.    USE - Mushroom cultivation base material.    ADVANTAGE - The base material utilizes waste from biogas fermentation, thus it is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mushroom cultivation base material comprising spreading plastic film pad on ground, spreading rapeseed shell, pouring water until wet, covering thin film, spreading biogas fermented residue on surface of rapeseed shell, overlapping until thickness is 20-25 cm, stacking for 10 days until temperature is 75 degrees C , turning, spreading gypsum and lime, uniformly turning, stacking for 7-8 days until temperature is 80 degrees C, turning, adding urea, calcium superphosphate and rapeseed cake fertilizer, spreading and stacking for 3-4 days.
NOVELTY - A high-density polyethylene regenerated material is baked at 80-90 degrees C for 4 hours. 40-60 %mass High-density polyethylene regenerated material, 10-30 %mass high-density polyethylene, 10-20 %mass linear low-density polyethylene, 1-10 %mass antimicrobial masterbatch and 0.5-1 %mass mixed masterbatch are mixed, heated, plasticized, added to mold and the mold is closed and the mixture is injection-molded, packed and cooled, to obtain antimicrobial drip irrigation emitter.    USE - Production of antimicrobial drip irrigation emitter (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly production of drip irrigation emitter having excellent antimicrobial property, dispersion property, anti-clogging property, anti-mold property and anti-aging property.    DETAILED DESCRIPTION - A high-density polyethylene plastic is cleaned, sorted, crushed, granulated and dehydration, to obtain high-density polyethylene recycled material. The high-density polyethylene regenerated material is baked at 80-90 degrees C for 4 hours. 40-60 %mass High-density polyethylene regenerated material, 10-30 %mass high-density polyethylene, 10-20 %mass linear low-density polyethylene, 1-10 %mass antimicrobial masterbatch and 0.5-1 %mass mixed masterbatch are mixed, heated, plasticized, added to mold and the mold is closed and the mixture is injection-molded, packed and cooled, to obtain antimicrobial drip irrigation emitter.
NOVELTY - This utility new type belongs to low methanol emulsify diesel oil production of technology field, specific relates to a one continuous a methyl alcohol diesel oil emulsify a single reflection super-gravity device, solves the problem that the existing methanol diesel oil liquid of a process material in volume rate of flow than larger difference of condition, mix effect is not ideal, uniformity is not a problem. A super-gravity, impact flow structure comprising a rotary filler bed, flow structure is non-impact flow structure, comprising different pipe diameter of main feeding pipe and sleeve and a liquid baffle plate, a sleeve opening end part and main feeding pipe nozzle end part form ring joint, an impact flow structure b. inner cavity of the rotor along the rotor axis direction and set. This utility new type two-phase flow change of impact, increase two phase flow impact of effect, at the same time can realize a liquid continuous operation of a large flow amount.
NOVELTY - Method for controlling gray mold disease of grape vine, involves (a) selecting disease-resistant varieties of grape vine for cultivation, and timely pruning the grape vine, (b) timely removing burned flower spikes of grape vine during spring, and reducing secondary pollution, (c) timely managing water drainage in grape orchard during rainy season, and timely pruning the grape vine, (d) removing wounded grape fruit, (e) picking the grape fruit, (f) spraying lime sulfur to the grape vine, and (g) spraying e.g. Bordeaux mixture to the grape vine.    USE - The method is useful for controlling gray mold disease of grape vine (claimed).    ADVANTAGE - The method is simple to perform, and promotes growth of grape vine.    DETAILED DESCRIPTION - Method for controlling gray mold disease of grape vine, involves (a) selecting disease-resistant varieties of grape vine for cultivation, timely pruning the grape vine, and removing plant debris, dry branches and fallen leaves of grape vine, (b) timely removing burned flower spikes of grape vine during spring, and reducing secondary pollution, (c) timely managing water drainage in grape orchard during rainy season, timely pruning the grape vine, and controlling spreading and growth of damaged grape vine, (d) removing wounded grape fruit, (e) picking the grape fruit during sunny day, and storing the grape fruit in a cool place provided with ventilation, (f) removing grape vine affected with pests, and spraying lime sulfur having 6-8 degrees Baume to the grape vine, and (g) spraying 1:3:200 times Bordeaux mixture, 50% carbendazim wettable powder (diluted for 900 times), 75% thiophanate-methyl wettable powder (diluted for 900 times), and 50% fluopicolide wettable powder (diluted for 900 times) to the grape vine.
NOVELTY - Method for using agent for improving cold resistance of crops, involves (a) spraying 800 times agent diluted with water to crops during late autumn, (b) spraying 600 times agent diluted with water to the crops before 3-7 days of frost or cold season, (c) spraying 1000 times agent diluted with water to the crops before transplantation, and (d) spraying 50-80 times agent diluted with water to trunk or branches the crops before winter season. The agent contains paraffin wax, vegetable oil, glycerol, and acetic acid.    USE - The method is useful for improving cold resistance of crops using agent (claimed).    ADVANTAGE - The method is simple to perform. The agent is convenient to use, and reduces damage of crops.    DETAILED DESCRIPTION - Method for using agent for improving cold resistance of crops, involves (a) spraying 800 times agent diluted with water to crops during late autumn, (b) spraying 600 times agent diluted with water to the crops before 3-7 days of frost or cold season, (c) spraying 1000 times agent diluted with water to the crops before transplantation, and (d) spraying 50-80 times agent diluted with water to trunk or branches the crops before winter season. The agent comprises paraffin wax, vegetable oil, glycerol, acetic acid, salicylic acid, coupling agent, amino acid, bamboo leaves, ochre, Elsholtzia and pine needle.
NOVELTY - Preparing active pillared synthetic pesticidal sustained-release agent comprises slowly adding hydrated calcium chloroaluminate mixed salt solution into sodium dodecyl sulfate under room temperature, adjusting the pH of the solution, stirring, placing in an oven, filtering, washing with deionized water and ethanol to obtain modified sodium dodecyl sulfate hydrated calcium chloroaluminate, preparing modified hydrotalcite and dispersing in toluene and ethanol mixed solution of imidacloprid solution taken in a three-necked flask, heating, centrifuging, washing and drying.    USE - The method is useful for preparing active pillared synthetic pesticidal sustained-release agent (claimed).    ADVANTAGE - The method does not generate secondary pollution. The sustained-release agent has good slow-releasing effect under alkali, acidic and neutral conditions.    DETAILED DESCRIPTION - Preparing active pillared synthetic pesticidal sustained-release agent comprises slowly adding hydrated calcium chloroaluminate mixed salt solution into sodium dodecyl sulfate under room temperature, simultaneously adjusting the pH of the solution to 9.8-10.2 using sodium hydroxide solution, continuously stirring for a day, then placing in an oven at 65 degrees C for 3 days, filtering, then washing 2-3 times with deionized water and 2-3 times with ethanol to obtain modified sodium dodecyl sulfate hydrated calcium chloroaluminate, then preparing modified hydrotalcite using modified sodium dodecyl sulfate hydrated calcium chloroaluminate, dispersing the hydrotalcite in toluene and ethanol mixed solution of imidacloprid solution in a three-necked flask under magnetic stirring condition for 2-72 hours, heating to 70 degrees C for 4 days, centrifuging at 3000 rotations/minute for 20 minutes, then washing once with ethanol and drying at 80 degrees C for 12-48 hours to obtain different drug-loading nano-hybrid pesticidal sustained-release agent.
NOVELTY - Chinese herbal pesticide is prepared by using 20-30 pts. wt. radix sophorae flavescentis, 22-30 pts. wt. cortex meliae, 8-10 pts. wt. herba houttuyniae, 7-10 pts. wt. Pteris multifida, 5-13 pts. wt. lotus seed, 12-15 pts. wt. Wu Chia Pee, 5-8 pts. wt. turmeric, 6-10 pts. wt. Aconitum, 3-5 pts. wt. Chrysanthemum, 2-6 pts. wt. Euphorbia, and 2.5-5 pts. wt. pomegranate rind.    USE - As Chinese herbal pesticide.    ADVANTAGE - The Chinese herbal pesticide is cost-effective, and simple to prepare, does not cause toxic side effects to human and animals, and can be prepared in a environmentally-friendly manner.
NOVELTY - Fertilizer is prepared using humic acid, clay, peat, ammonium nitrate, calcium dihydrogen phosphate, ferrous sulfate, organic fertilizer, manganese sulfate, Aschersonia shell powder, soybean hull powder, sugar residue, agar, zinc sulfate, Phellodendron, sodium humate, stone powder, gypsum, and Lactobacillus.    USE - As fertilizer for tea trees.    ADVANTAGE - The fertilizer ensures to improve soil fertility and quality of tea.    DETAILED DESCRIPTION - Fertilizer is prepared using 8-14 pts. wt. humic acid, 3-7 pts. wt. clay, 4-9 pts. wt. peat, 4-10 pts. wt. ammonium nitrate, 6-12 pts. wt. calcium dihydrogen phosphate, 4-8 pts. wt. ferrous sulfate, 5-9 pts. wt. organic fertilizer, 1-4 pts. wt. manganese sulfate, 1-5 pts. wt. Aschersonia shell powder, 5-10 pts. wt. soybean hull powder, 1-3 pts. wt. sugar residue, 3-5 pts. wt. agar, 2-7 pts. wt. zinc sulfate, 4-8 pts. wt. Phellodendron, 2-7 pts. wt. sodium humate, 3-8 pts. wt. stone powder, 4-9 pts. wt. gypsum, and 2-6 pts. wt. Lactobacillus.
NOVELTY - Method for preparing insecticidal organic fertilizer, involves (a) mixing biogas, lime and agent in a weight ratio of 100:1:0.1 (moisture content of 40-60%), fermenting mixture at 50-60 degrees C for 1-2 days, and maintaining mixture for 15-20 days, (b) mixing 19-30 wt.% fermented biogas, 49-60 wt.% soil, 5-10 wt.% wood flour, 0.1-2 wt.% fertilizer and trace elements, and 15 wt.% tobacco slag powder with peat, and (c) reacting obtained mixture for 4 hours, adding peat, palm ash and monosodium glutamate in a ratio of 7:1:2 to reacted mixture, and granulating mixture.    USE - The method is useful for preparing insecticidal organic fertilizer (claimed).    ADVANTAGE - The method is cost-effective and environmentally-friendly, and improves soil.    DETAILED DESCRIPTION - Method for preparing insecticidal organic fertilizer, involves (a) mixing biogas, lime and agent in a weight ratio of 100:1:0.1 (moisture content of 40-60%), fermenting mixture at 50-60 degrees C for 1-2 days, and maintaining mixture for 15-20 days, where the agent is prepared by mixing 2.5 billion/g Bacillus subtilis and auxiliary materials in a ratio of 1:10, and auxiliary materials are straw powder, rice bran powder or wood powder, (b) mixing 19-30 wt.% fermented biogas, 49-60 wt.% soil, 5-10 wt.% wood flour, 0.1-2 wt.% fertilizer and trace elements, and 15 wt.% tobacco slag powder with peat, where the fertilizer is nitrogen fertilizer, phosphorus fertilizer and potassium fertilizers, and (c) reacting obtained mixture for 4 hours, adding peat, palm ash and monosodium glutamate in a ratio of 7:1:2 to reacted mixture, and granulating mixture.
NOVELTY - Microbial pesticide comprises 30-50 wt.% Bacillus thuringiensis solution, 30-50 wt.% Beauveria bassiana solution, 5-9 wt.% photosynthetic bacteria solution, 5-9 wt.% yeast solution, 5-7 wt.% chelated tobacco leaves solution, 1-3 wt.% potassium dihydrogen phosphate, 0.05-0.2 wt.% diethyl aminoethyl hexanoate, 0.05-0.3 wt.% sodium nitrophenolate and 0.1-0.4 wt.% organosilicon.    USE - The microbial pesticide is useful as fertilizer, which is useful for providing required amount of nitrogen, phosphorus and potassium to the crop.    ADVANTAGE - The microbial pesticide is cost-effective and environmentally-friendly, and exhibits broad spectrum pesticidal activity for prolonged time period, without any adverse effects.
NOVELTY - Device for separating ethanepropionic fraction, comprises supply conduit of ethanepropionic fraction in rectifying column, supplied with withdrawal of gas of deethanation in upper part, and with withdrawal of propionic fraction in the bottom part and with irrigation unit; heat exchanger, connected along the first heat-transfer agent with the withdrawal of gas of deethanation; and container with withdrawal of non-condensed gas of deethanation and withdrawal of condensate using pump.    USE - The device is useful for separating ethanepropionic fraction (claimed).    DETAILED DESCRIPTION - Device for separating ethanepropionic fraction, comprises supply conduit of ethanepropionic fraction in rectifying column, supplied with withdrawal of gas of deethanation in upper part, and with withdrawal of propionic fraction in the bottom part and with irrigation unit; heat exchanger, connected along the first heat-transfer agent with the withdrawal of gas of deethanation; and container with withdrawal of non-condensed gas of deethanation and withdrawal of condensate using pump. The device is supplied with supply conduit of propionic fraction, connected through additionally installed heat exchanger and expansion device to a heat exchanger of the unit of irrigation along the second heat-transfer agent and further with further installed compressor. The output of propionic fraction from the compressor is connected to by the bottom part of rectifying column and supplied with additional withdrawal of propionic fraction, and the withdrawal of the non-condensed gas of deethanation from the container for the irrigation is connected to heat exchanger and further with the user.
NOVELTY - Producing fuel pellets from lignin comprises: gradual drying of raw exhaust gases to the required humidity, molding, final drying and cooling of pellets, where the first phase comprising 20-30% of the total lignin is dried to a moisture content of 35-40%; selecting and directing the remaining 70-80% of the lignin pellet form to the heat source for combustion and drying to a residual humidity of 14-16%; before forming the pellets, mixing the raw material in a mixer in the presence of water-soluble additives; and forming the pellets of 6-10 mm by pressing them at low specific energy consumption.    USE - The method is useful for producing fuel pellets from lignin.
NOVELTY - The tank has a mixer rotatably mounted in the tank about an axis along a main direction, where the tank extends in the main direction. The mixer is provided with a stirring element for homogenizing contents of the tank, where the stirring element comprises a beater (72) having a constant section and an open section. The beater comprises a leading edge (721) that is extended along a rotation direction of the mixer, where the beater comprises multiple apertures (723). The apertures are distributed along the leading edge for communicating an upstream face (725) and a downstream face (726).    USE - Biogas tank for treating liquid manure produced by livestock.    ADVANTAGE - The beater comprises the leading edge that is extended along the rotation direction of the mixer, where the beater comprises multiple apertures, which are distributed along the leading edge for communicating the upstream face and the downstream face, thus ensuring better population of bacteria, and hence allowing liquid manure to be treated in an efficient manner without disturbing environments.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas installation.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a beater.    Beater (72)    Leading edge (721)    Apertures (723)    Upstream face (725)    Downstream face (726)
NOVELTY - The method involves generating boil-off gas temporarily, and maintaining liquefied gas permanently in supercooled state. The liquefied gas is cooled so far below an enthalpy to boiling point of liquefied gas at maximum permissible operating pressure of storage container (S), which is sufficiently large to boiling point of generating boil-off gas in order to back liquefy the boil-off gas.    USE - Method for operating storage container storing liquefied gas such as liquefied natural gas (LNG). Can also be used in storing liquefied oxygen, liquefied nitrogen, liquefied Carbon dioxide, liquefied noble gas, and liquefied hydrocarbon.    ADVANTAGE - The operation of storage container storing the liquefied gas is enabled to limit and control the formation of boil-off gas in improved and effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram showing the arrangement of storage container storing liquefied gas.    Spacer (1,2)    Refrigerant cycles (3,4)    Liquid phase (F)    Gas phase (G)    Storage container (S)
NOVELTY - Method (M1) for performing a hydrolysis of a cellulosic biomass, comprises: providing the cellulosic biomass; providing a cellulase; providing a strain of Bacillus subtilis SH44; and mixing the cellulosic biomass, the cellulase and the strain of Bacillus subtilis SH44 to perform the hydrolysis.    USE - The method is useful for performing a hydrolysis of a cellulosic biomass for producing a product which is a glucose (claimed).    ADVANTAGE - The method increases the yield and efficiency of generation of glucose (claimed).    DETAILED DESCRIPTION - a method (M2) for cutting a cellulose, comprising: providing the cellulose; providing a cellulase; providing a strain of Bacillus subtilis SH44; and mixing the cellulose, the cellulase and the strain of Bacillus subtilis SH44 to cut the cellulose; and #a method (M3) for preparing a raw composition for producing a glucose by a hydrolysis, comprising: providing a cellulose; providing a biologically pure culture of strain Bacillus subtilis BCRC 910566; providing a cellulase comprising an exoglucanase and beta-glucosidase, where neither the exoglucanase nor the beta-glucosidase is produced by the biologically pure culture of strain Bacillus subtilis BCRC 910566; and mixing the cellulose, the biologically pure culture of strain Bacillus subtilis BCRC 910566, the exoglucanase and the beta-glucosidase.
NOVELTY - The method involves monitoring the power supplied by an energy source (E41). A portion of the power supplied by the energy source is deviated (E42) upstream of the electrolyzer for the heating of a stack of cells in a high-temperature electrolyzer when the value of the power supplied becomes lower than a previously determined limit value. The portion of the power supplied by the energy source is not deviated when the value of the power supplied is not less than the previously determined limit value, where the energy source is an intermittent and/or fluctuating energy source.    USE - Method for controlling a high-temperature electrolyzer in a hydrogen or syngas producing system (claimed).    ADVANTAGE - The portion of the power supplied by the energy source is deviated upstream of the electrolyzer for the heating of the stack of cells in the high-temperature electrolyzer when the value of the power supplied becomes lower than the previously determined limit value, thus enabling the electrolyzer to be operated in a wide range of powers.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a system for controlling a high-temperature electrolyzer    (2) a system for producing hydrogen or syngas.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a method for controlling a high-temperature electrolyzer.'(Drawing includes non-English language text)'    Step for monitoring the power supplied by an energy source (E41)    Step for deviating portion of the power supplied by the energy source upstream of the electrolyzer for the heating of the stack of cells in the high-temperature electrolyzer (E42)
NOVELTY - Preparing an oil composition from a grain material comprises incubating the grain material with a proline-specific endoprotease and preparing the oil composition.    USE - The process is useful in an ethanol fermentation process.    ADVANTAGE - The process is an improved oil recovering process, and provides 10-20% higher yield of oil compared to a process that does not using the proline-specific endoprotease.    DETAILED DESCRIPTION - AN INDEPENDENT CLAIM is also included for the oil composition obtainable by the process.
NOVELTY - Refrigerant composition consisting essentially of 3-9 wt.% 1,1,1,2,3,3,3-heptafluoropropane ( R227ea), 25-70 wt.% 1,1,1,2-tetrafluoroethane (R134a), 3-35 wt.% 1,1,1,2,2-pentafluoroethane (R125) and 10-35 wt.% difluoro methane (R32) together with an optional hydrocarbon component.    USE - The composition is useful in thermal pump, refrigeration and air conditioning.    ADVANTAGE - The composition: is utilized as replacement for R22 in existing equipment and non-flammable and have a global warming potential less than 2200; provides pressure not greater than pressure of R22 and lower than the pressure for R407C which is used as an R22 replacement; reduces the decomposition of lubricating oil, resulting in less formation of decomposition products at the discharge outlet during prolonged use; and utilizes low toxic refrigerants.
NOVELTY - 2-Methyl-3-nitrobenzoic acid methyl ester is brominated with N-bromosuccinimide in methyl acetate. The obtained 2-(bromomethyl)-3-nitrobenzoic acid methyl ester is reacted with 3-aminopiperidine-2,6-dione. The obtained 3-(4-nitro-1-oxo-,3-dihydro-2H-isoindol-2-yl)piperidine-2,6-dione is reduced to 3-(4-amino-1-oxo-1,3-dihydro-2H-isoindol-2-yl)-piperidine-2,6-dione with an iron and ammonium chloride reducing system.    USE - Preparation of lenalidomide useful as anticancer agent.    ADVANTAGE - The method enables economical and environmentally-friendly preparation of lenalidomide which is more accessible to cancer patients in short reaction time of 4 hours with high yield of 80% and purity of 98%, by simple process.
NOVELTY - Domestic garbage processing machine comprises a pre-processing unit, an aerobic biological leaching filter (5), pool (10) and aerobic bioreactor (13). Pre-processing unit and aerobic biological leaching filter are connected to feeding outlet. The aerobic bioreactor is provided with liquid inlet, liquid outlet and circulation fan. The aerobic biological leaching filter comprises air blower (8), air outlet, filter nozzle (6), spraying filter pump (14) and shower nozzle. The aerobic bioreactor is provided with dewatering machine (7).    USE - Domestic garbage processing machine.    ADVANTAGE - The domestic garbage processing machine does not pollute environment and protects the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a domestic garbage processing machine.    Aerobic biological leaching filter (5)    Filter nozzle (6)    Dewatering machine (7)    Air blower (8)    Pool (10)    Aerobic bioreactor (13)    Spraying filter pump (14)
NOVELTY - Heating network rapid biomass pyrolysis device comprises flange blind plate, lower flange blind plate, organic glass cylinder, block electric wood plate, fixed electrode A, movable electrode, silk screen with mounting biological oil collector, thermocouple, acquisition card, and computer equipped with proportional-integral-derivative controller.    USE - Heating network rapid biomass pyrolysis device.    ADVANTAGE - The device is small, easy to realize and inexpensive. It can change flow rate of helium, reduces volatile residence time in high temperature area, and restrains bio-oil (tar) vapor thermal disintegration.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the heating network rapid biomass pyrolysis comprising taking biomass sample, carrying out grinding, sieving, drying and sealing; secondary heating, cutting square stainless steel wire net, drying, weighing screen, fixing on one side, taking 3-5 mg microsample, spreading uniformly between screens, clamping and holding, fixing other side of screen between movable electrode, removing fine dust, drying coal sample, fixing sample between electrodes, flattening, rotating; cutting K-type thermocouple wire anode and cathode, passing through two layers of screens, passing through silk screen, knotting, downward pulling, sealing, ensuring reliable contact of thermocouple and wire net, closing two layer folding screen to prevent moving sample, pushing honeycomb ceramic into air flow stabilizer, mounting organic glass cylinder and flange blind plate, taking filter film into closing seal in biological oil collector outlet; vacuumizing; and heating.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of heating network rapid biomass pyrolysis device (Drawing shows non-English language text).
NOVELTY - The biomass molding fuel comprises a base fuel layer and waterproof fuel layer, where the base fuel layer is a rectangular block. The base fuel layer has a waterproof pressing fuel layer, where the biomass of the base fuel layer is agricultural waste. The waterproof layer of the biomass fuel is lignin or oil crops waste.    USE - Biomass molding fuel.    ADVANTAGE - The biomass molding fuel has strong workability and good waterproofing property, and can be prepared in a simple and cost-effective manner with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biomass molding fuel, which involves:    (A) smashing agricultural waste as a biomass raw material;    (B) drying the pulverized material naturally;    (C) adding a certain proportion of waste paper pulp or hydrolysis fiber and quicklime with uniform stirring in extrusion molding machine to obtain a base fuel layer;    (D) smashing lignin or oil crops waste;    (E) drying the pulverized material naturally;    (F) adding a certain proportion of thermosetting resin with uniform stirring in extrusion molding machine to obtain a waterproof fuel layer;    (G) coating thermosetting resin on lower surface of the base fuel layer;    (H) providing base fuel layer between the waterproof fuel layer and base fuel layer; and    (I) pressing the formed layer in double-roller machine to obtain a waterproof biomass molding fuel.
NOVELTY - Producing biodiesel involves adding raw material i.e. animal fat and short chain alcohol into a conical screw extruder, where the mixture is dispersed, compressed and de-volatilized to obtain biodiesel. The animal fat and short chain alcohol is processed in multiple sections of a conical screw extruder at 80-110 degrees C, 100-110 degrees C, 100-120 degrees C and 110-110 degrees C respectively, where a chemical reaction is performed to obtain oil. Short-chain alcohol are short-chain fatty acid are further added to obtained oil, and then processed to obtain homogeneous solution.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method enables to produce biodiesel with high purity and quality stability.    DETAILED DESCRIPTION - Producing biodiesel involves adding raw material i.e. animal fat and short chain alcohol into a conical screw extruder, where the mixture is dispersed, compressed and de-volatilized to obtain biodiesel. The animal fat and short chain alcohol is processed in multiple sections of a conical screw extruder at 80-110 degrees C, 100-110 degrees C, 100-120 degrees C and 110-110 degrees C respectively, where a chemical reaction is performed to obtain oil. Short-chain alcohol are short-chain fatty acid are further added to obtained oil, and then processed to obtain homogeneous solution. The trans-esterification of homogeneous solution is carried out, and the de-volatilized in a vacuum de-volatilizer. The obtained product is distillated in a vacuum distillation chamber at 150-200 degrees C to obtain biodiesel.
NOVELTY - This utility new type claims a marsh gas application of a heating system, comprising heating furnace, gas storage cabinet, a marsh gas pool, heating furnace and between the marsh gas pool set has circulation heat exchange tube, the heat exchange tube from a circulation heating furnace end side wall is connected after connecting to marsh gas pool inside winding number from marsh gas pool join the connection to the following heating furnace side wall upper end of the marsh gas pool through a biogas input pipe and gas storage cabinet connected, a gas storage cabinet through air conveying pipe heating furnace and the bottom of a combustion chamber. The effective marsh gas pool and a heating furnace combine together through this utility model, through a circulation tube for heating a hot water inner furnace introduced in marsh gas pool, after the temperature of inner marsh gas pool, so as to fully give play to a combustible gas inner marsh gas pool, increase the methane yield, and heat exchange of residual heat by water circulation heat exchange tube to connect heating furnace in, so as to reduce the heat energy consumption, realize the energy of marsh gas pool heating furnace and fully apply.
NOVELTY - Producing a biomass-derived product comprises subjecting a primary whole stillage to fermentation to produce a fermentation product comprising a secondary whole stillage and ethanol. The whole stillage has a starch content of at least 15 wt.% on a dry matter basis.    USE - The method is useful for producing ethanol from a biomass feedstock.    ADVANTAGE - The method improves ethanol production using a biomass feedstock comprising high amounts of solids and starch.
NOVELTY - A yeast, where the yeast lacks a gene encoding hexadecanal dehydrogenase (HFD1) or comprises a disrupted gene encoding HFD1; and the yeast comprises at least one heterologous gene encoding an enzyme involved in a pathway of producing hydrocarbons, is new.    USE - The yeast and method are useful producing hydrocarbons, where the hydrocarbons are a fatty acid derivative selected from an alkane, an alkene and a fatty alcohol, preferably selected from an alkane and an alkene (claimed).    ADVANTAGE - The yeast and method can produce hydrocarbons in a controllable and economic fashion, and efficiently produces hydrocarbons, for instance liquid alkanes and alkenes, that can be used for liquid transportation fuels, specialty chemicals, or feed stock for further chemical conversion having low environmental impacts.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing hydrocarbons, which involves: culturing a yeast lacking a gene encoding HFD1 or comprising a disrupted gene encoding HFD1 in culture conditions suitable for production of the hydrocarbons from the yeast; and collecting the hydrocarbons from the culture medium in which the yeast is cultured and/or from the yeast.
NOVELTY - The catalyst comprises an inorganic oxide support, and 7-30 wt.% mixture of oxides of nickel, cerium and lanthanum in the form of their oxides (nickel oxide, lanthanum (III) oxide and cerium (III) oxide), which are simultaneously impregnated with inorganic oxide support. The mixture of nickel oxide and lanthanum (III) oxide has a ratio of 6:1 to 15:1 (w/w). The mixture of lanthanum (III) oxide and cerium (III) oxide has a ratio of 2:1 to 4:1 (w/w). 0.3-2.0 wt.% promoter element is also included in the catalyst.    USE - Catalyst for producing synthesis gas for use in petrochemical industry for producing synthetic fuels, methanol, ammonia or urea.    ADVANTAGE - The catalyst facilitates acceptable activity during the entire steam reforming process, and has a lower production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing catalyst for producing synthesis gas, which involves:    (A) preparing an aqueous impregnating solution of an inorganic nickel salt, preferably nickel nitrate, nickel acetate or nickel carbonate, lanthanum and cerium, preferably in the form of nitrate;    (B) impregnating the inorganic oxide support through damp point technique or through placing the inorganic oxide support in an excess of solution;    (C) drying the impregnated material in air at 50-150 degrees C for 1-24 hours;    (D) calcining the impregnated material to a static air or to air flow at 250-650 degrees C for 1-4 hours;    (E) adding a promoter element to the calcined material by using impregnation method;    (F) drying the impregnated material in air at 50-150 degrees C; and    (G) calcining the impregnated material in air at 250-650 degrees C.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical representation depicting rate of carbon deposition on various commercial pre-reforming catalysts. (Drawing includes non-English language text).
NOVELTY - The device has a masticating device provided with a first granulator (5). A tank (4) is used for homogenizing fine and purified raw materials. The first granulator is connected with a second granulator (6), where outlets of the granulators are connected with a conveying equipment (7) and a cooling system (8).    USE - Device for preparing feed pellets from biodegradable material.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a device for preparing feed pellets.    Tank (4)    Granulators (5, 6)    Conveying equipment (7)    Cooling system (8)
NOVELTY - Carbon dioxide stemming from industrial process as synthetic or substitute natural gas is stored by separating carbon dioxide containing gas mixture from flue gas stemming from industrial combustion or calcination step or metallurgical process, splitting water by electrolysis to produce hydrogen gas and oxygen gas and converting carbon dioxide containing gas mixture and hydrogen gas by methanation reaction to methane rich gas which can be used as or upgraded to synthetic natural gas.    USE - Storing process for carbon dioxide stemming from industrial process as synthetic or substitute natural gas (claimed).    ADVANTAGE - Efficiency of water electrolysis is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a carbon dioxide storage plant comprising industrial operation plant which generates carbon dioxide in flue gas and performs industrial combustion or calcination process or metallurgical process, carbon dioxide separating unit which separates carbon dioxide containing gas mixture from flue gas, electrolysis unit which splits water by electrolysis to produce hydrogen gas and oxygen gas, and methanation unit which converts carbon dioxide containing gas mixture and hydrogen gas to methane rich gas by methanation reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the synergetic effects of combining diverse industrial processes.
NOVELTY - A a water-coal-slurry desulfurizing electrolytic hydrogen making device, a coal desulphurization at the same time in a hydrogen and desulfurizing.. This utility new type comprising ingredients a, b, gas recovery system, the recovery system, dosing system comprising has funnel feeder, a microwave dryer, belt conveyor, flour mill, hopper, a dry powder mixer, mixer seriflux; electrolytic system comprises stirring tank, an electrolytic groove, a direct current pulse electric source cabinet, a microwave radiation device, an ultrasonic vibration rod, and a tube network, in a plate of two stirring tank is equipped with the middle liquid lower pump, pump outlet by electrolyte pipe and electrolysis groove bottom of pipe network connected, a vertical to the electrolytic groove in center, is a four group by a plate form a close wherein character shape; inner electrolytic groove of two side is equipped with a ultrasonic vibration rod, a gas comprising has a carbon dioxide storage tank, a hydrogen storage tank and pressure table, a flow meter, a one-way valve, a stop valve, a gate valve, a hydrogen analyzer, an emptying valve, buffer tank, a booster pump.
NOVELTY - A artificially constructing a biological carrier filler combination, comprising upper and lower hemispherical shell, surface of upper and lower shell set with mutually connected has a buckle, composed of a ball type structure, the upper and lower shell surface is grid-shaped, the upper lower inner housing fill has a filler, a filler is a whole block fill b and inner shell or a irregular multi-hung upper and lower inner shell, said each block filler surface are provided has a " Z "-shaped groove, a filler are provided center has through hole, inner through hole is inserted a filler wire winding fixing block b and a housing. Structure is simple, compact and reasonable structure, convenient and fast assembly, convenient attachment of microorganism and waste water in a filler fully contact, at the same time it can intercept and water together out of microorganism.
NOVELTY - This utility model new supply of one of biomass cracking carbonization gasification device, including pulverizer, drying device, forming machine and splitting are orderly connected through pipeline and device, one level tank, rough purifier, acid washing tank, cooling separating device, gas liquid separating device, alkali washing tank, a fan, a decoking device, one grade gas phase purifier, desulfurizer, remove , gas filter, second level gas phase purifier and second level tank, air storage tank, also comprising oil liquid separator, wood vinegar, wood tar, wood tar distillation device. This new utility model enlarging of production scale, using biomass cracking product, biomass resource for full use, use multiple continuous purification device, removing each kind of impurities in the gas, with suitable gas specified quality of fuel gas, and the whole production process without waste gas, waste residue and waste liquid discharging, not only does not cause pollute, but also ensures the yield and quality of the fuel gas, promoting of environment protection and economic coordinate.
NOVELTY - This new utility model relates to one kind of crop splitting system, comprising material chamber, feeding device, motor, and heater reactor, feeding the two terminal device respectively connected with material chamber and reactor, feeding chamber through transmission belt and motor connected with the heater set in the reactor below the crop splitting system also comprises the first cyclone separator and the second cyclone separator under the first, the second cyclone separator respectively equipped with the first, the second coal tank, the second cyclone separator and the concentration chamber connected, in concentrate chamber provided with coolant chamber upper part and lower part respectively provided with material port and discharge port enter, enter material port and the second cyclone separator connected, discharging port and collecting chamber connected, collection chamber through circulation pump and enter material port connect. This new utility model through multi-time separation and circulation condensation filter, make cracking product of biologic oil can further obtain full collecting, increase of use rate of crops, at the same time through multiple filtering, reducing cracking system discharging of harmful substance.
NOVELTY - This utility model new supply of one of biomass cracking carbonization gasification device, comprising orderly connected by pipeline and pulverizer, drying device, molding machine, splitting device, the first tank, rough purifier, acid washing tank, cooling separating device, gas liquid separating device, alkali washing tank, a fan, a decoking device, the first gas phase purifier, desulfurizer, remove , gas filter, the second gas phase purifier, the second tank, an air storage tank, also comprising coke activator oil liquid separator, wood vinegar, wood tar, wood tar distillation device, water circulation pool. The utility model use new coke activator to produce the coke by cracking activate, increase coal quality condition, and removing each kind of impurities in the fuel gas, the yield and quality of the fuel gas, and the whole production process without waste gas, waste residue and waste liquid discharging, it will not cause polution, as one of fuel gas, active coal and liquid fuel and biomass cracking carbonization gasification cogeneration device.
NOVELTY - This utility new type provide the one a simple marsh gas fermenting device, comprising a fermenting box body, comprising a box body set with feeding channel and has liquid discharging channel, the top of the box body has set with marsh gas outlet, a box body has set with liquid level display window, the bottom of the box body has set with a slag tank body in section set has rows of oil wherein, the feeding channel is channel of upper end opening, a drain channel end, the top end has set, this device a fermentation that pollute the kitchen garbage, the kitchen waste into a sewage gas energy source, and a valid is a oil water separating, a Fischer-Tropsch oil is the following one step process making preparation, this device structure is simple and reasonable, using rubber integrated injection molding cost low, convenient to popularize, integrated structure has good air tightness, simple and safe operation, it is suitable for family and restaurant use.
NOVELTY - A volatility organic waste pneuma biological dropping filter purification integrated device is used for removing a waste in pneuma of volatile organic matter (VOC) and PM2.5. This utility new type a trickling filter 1, air inlet system, a water inlet system, nutrition liquid adding system, a system 4 one part. This utility new type HEPA for a material application b advanced biological trickling filter device in the removing of VOC at the same time removing PM2.5 pollute a; and removing dampness network, HEPA network a disassembled, convenient to maintain, install the pneuma, bottom water washing is combined on-line clean system, active filler solves the blocking problem of dripping part. the filter chamber, saves the water storage tank form. equipped with the hot water heat preservation device, a cold climate and area provide biochemical needed temperature, according to REQUIREMENT match a different property selecting different filter material, a filter change, so it can take the tower body standardization manufacture, reduce cost, increase quality.
NOVELTY - This utility model relates to the coal chemical industry technology field, especially relates to a radial flow by-product steam temperature methanation furnace. This utility model claims a radial flow by-product steam temperature methanation furnace, it comprises a furnace body, a pressed catalyst bed layer, a gas distribution roller, a gas collector, wherein the pressed body part is provided with a feed gas entrance and a water exit, the feed gas entrance inner furnace body is provided with a gas distributor, the lower pressed part is set with a transformation gas furnace body outlet and a water entrance, between the pressed body inner wall and catalyst bed layer is equipped with a gas distribution, the pressure shaft center part is set with a furnace body gas; in the catalyst bed layer is set with a lengthways heat taking device, a lengthways heat taking device for catalyst bed layer of each upper, lower part is set with one annular tube tank, between two annular pipe tanks is connected by multiple lengthways pipes, across the catalyst bed layer, the upper annular pipe water tank is connected with the outlet, the lower annular tube water tank s connected with the entrance.
NOVELTY - Safe treatment device comprises liquid collecting mechanism (1), feeding mechanism (2), heating body (3), stirring device (4), pulley (5), housing (6), buckets (101), funnel (102), rotary screen (103), bracket (104), feeding pipe, belt conveyor, hollow belt, box heater, heater blades, motor, valve, discharge tube, blades, rotating shaft, mixing box, feeding mouth, grooves, top cover and handle.    USE - Safe treatment device for human and animal excreta (claimed).    ADVANTAGE - The device has improved efficiency and is environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of safe treatment device.    Liquid collecting mechanism (1)    Feeding mechanism (2)    Heating body (3)    Stirring device (4)    Pulley (5)    Housing (6)    Buckets (101)    Funnel (102)    Rotary screen (103)    Bracket (104)
NOVELTY - Simple device comprises liquid fermentation room (1), dredging port (2), solid fermentation room (3), tank (4), handle cover (5), cover plate (6), garbage entrance (7), cover shaft (8), gas and liquid guiding tube (9), first gas and liquid hole (10), helical baffle, second gas and liquid hole, solid outlet, door plate, door plate fixing groove, liquid discharge valve and fixed pins.    USE - Simple device for rapid treatment of domestic waste (claimed).    ADVANTAGE - The device is simple, space-saving and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of simple device.    Liquid fermentation room (1)    Dredging port (2)    Solid fermentation room (3)    Tank (4)    Handle cover (5)    Cover plate (6)    Garbage entrance (7)    Cover shaft (8)    Gas and liquid guiding tube (9)    First gas and liquid hole (10)
NOVELTY - Municipal solid waste simple treatment method comprises carrying out solid-liquid separation of garbage, entering wastes from the feed port into the tank body, mixing solid waste with bacteria, setting off gas and liquid in solid fermentation room, taking solid organic fertilizer from the discharge port, carrying out solid biological fermentation, sieving to obtain fermented solid biological organic fertilizer, introducing waste liquid through gas-liquid pipe and gas-liquid hole, carrying out liquid fermentation in liquid fermentation room and discharging.    USE - Method for treating municipal solid waste (claimed).    ADVANTAGE - The method is environment-friendly.    DETAILED DESCRIPTION - Municipal solid waste simple treatment method comprises carrying out solid-liquid separation of garbage, entering wastes from the feed port into the tank body, mixing solid waste with bacteria, setting off gas and liquid in solid fermentation room through gas and liquid pipe and gas and liquid holes, taking solid organic fertilizer from the discharge port, carrying out solid biological fermentation, sieving to obtain fermented solid biological organic fertilizer, introducing waste liquid by gas-liquid pipe gas-liquid hole, carrying out liquid fermentation in liquid fermentation room and discharging biological fermentation liquid in discharge valve.
NOVELTY - Turning plate comprises plate leaves (1) having working surface (2) provided with reinforcing ribs (4), and assembling hole (3).    USE - Turning plate used for biological organic fertilizer fermentation material turning mechanism (claimed).    ADVANTAGE - The turning plate has unique structure design, good reliability, and stable turning operation transition, provides high turning efficiency, and is suitable for large-scale and high-volume turning operation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biological organic fertilizer fermentation material turning mechanism.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic view of turning plate.    Plate leaves (1)    Working surface (2)    Assembling hole (3)    Reinforcing ribs (4)
NOVELTY - Cultivation of Cordyceps sinensis comprises cultivating soil land and adding 20-100 kg effective microorganism (EM) bacteria compost per acre with fertilization depth of 15-25 cm; cutting ginseng into 4-7 cm long each with 3-5 buds, diluting with EM bacteria, soaking for 2-12 hours, planting, sprouting, spraying once with EM bacteria; and spraying 1-4 times dilution liquid in ginseng monthly.    USE - Method for cultivating Cordyceps sinensis (claimed).    ADVANTAGE - The method avoids the use of chemical fertilizer.
NOVELTY - Cultivation of mushroom comprises adding culture medium into culture bag and sterilizing; inoculating with hairy fungus, putting into culture bag, and maintaining culture medium culture bag temperature; maintaining room temperature and mycelium water content, maturing, and culturing under shed to change mushroom color; budding young mushroom and maintaining temperature; maintaining temperature and budding; cultivating and budding with light; and harvesting.    USE - Method for cultivating mushroom (claimed).    ADVANTAGE - The mushroom is tender and has aroma, big flower shape, strong stress resistance and yield of more than 59%.    DETAILED DESCRIPTION - Cultivation of mushroom comprises adding culture medium into culture bag and sterilizing; inoculating with hairy fungus, putting into culture bag at 22-26 degrees C, and maintaining culture medium culture bag temperature at 25-28 degrees C with air relative humidity of 60-70%; maintaining room temperature at 20-24 degrees C with relative humidity of 80-90% and mycelium water content of 50-55%, maturing, and culturing under shed to change mushroom color; budding young mushroom for 5-7 days and maintaining temperature at 8-16 degrees C with relative humidity of 80-90%; maintaining temperature at 8-10 degrees C and relative humidity of 65-70% when the bud is 1 cm, and budding for 4-7 days; cultivating at 8-16 degrees C with relative humidity of 50-70% and budding with light intensity of 1800-2000 LX; and harvesting. The culture medium comprises 60-65 pts. wt. cottonseed hull, 15-20 pts. wt. sawdust, 1-3 pts. wt. soybean meal, 15-17 pts. wt. bran, 1-3 pts. wt. sugar, 1-3 pts. wt. gypsum, and 1-3 pts. wt. lime.
NOVELTY - Cultivation of melon comprises selecting nutrition bowl, adding peat soil, red soil, bentonite and base fertilizer, adding water, and maintaining water content; sowing, adding pumpkin seedlings, planting sweet melon seedling, and grafting muskmelon leaf; digging up growing point of pumpkin seedling with two cotyledons, cutting, and adjusting pumpkin cotyledons with melon cotyledon; and grafting, maintaining water content, removing nutritional bowl, transplanting seedling into field with underlying nutritional soil, controlling spacing per plant, and spraying roots with topdressing.    USE - Method for cultivating melon (claimed).    ADVANTAGE - The method enhances survival rate of melon, ensures rich organic matter content in root during whole growth period, and increases soil nutrient adsorption. The borax and agar added in base fertilizer has slow release effect.    DETAILED DESCRIPTION - Cultivation of melon comprises selecting 12x 1 cm nutrition bowl, adding peat soil, red soil, bentonite and base fertilizer at ratio of 2:6:3:4, adding water, and maintaining water content of 60%; sowing after 12 months, adding pumpkin seedlings, planting sweet melon seedling about 1.5 cm in the center, and grafting muskmelon leaf; digging up growing point of pumpkin seedling with two cotyledons, cutting, and adjusting crosswise pumpkin cotyledons with melon cotyledon; and grafting at 25-27 degrees C during daytime and 15 degrees C at night, maintaining water content to 60%, removing nutritional bowl, transplanting seedling into field with underlying nutritional soil, controlling spacing per plant, and spraying roots with 2-3 times topdressing each with 2-3 kg/strain.
NOVELTY - Reduction of acid-value involves reducing acid value of edible oil of 10 mg potassium hydroxide/g or less to 5 mg potassium hydroxide/g or less by adding 0.1-50 pts. wt. bentotite with respect to 100 pts. wt. edible oil.    USE - Reduction of acid-value of edible oil used in manufacture of biodiesel fuel (claimed). Can also be used for tempura, side dishes, instant noodles, and oil confectioneries.    ADVANTAGE - The method enables reduction of acid-value of edible oil without producing soap component, and the bentonite contained in the edible oil can be removed easily by filtration or centrifugation.
NOVELTY - This utility new type claims a a peristaltic solid phase reactor, comprising furnace main body, furnace main body comprises outside tube, set with a stirring shaft in coaxial outside cylinder body inner, driving stirring shaft of rotating driving unit, the outside tube and between the stirring shaft form reaction cavity, one end outside is set with tube has feeding port, and the other end has set with cabin, when comprising a discharging bin, a discharging cavity and react cavity has set the gate unit, a gate unit open, reaction cavity and discharging cavity; when gate unit is closed, the reaction cavity and discharging cavity. Gate unit through a inner furnace into reaction chamber and a separating chamber, separate increase of efficiency and reliability, inclined angle of blade of the feeding section is more than inclination angle of blade is reaction section, which not only ensure smooth feeding, and increasing a furnace inner material of reaction time, increase efficiency, using mode of this reactor can be combined for a garbage is pneuma, oil, carbon, A is a change process of the waste is valuable, energy regeneration, suitable for popularization and application.
NOVELTY - Special fertilizer comprises 60-80 pts. wt. yellow phosphorus slag, 200-210 pts. wt. organic fertilizer, 0-150 pts. wt. yellow sludge, 170-180 pts. wt. urea, 0-220 pts. wt. urea formaldehyde, 50-170 pts. wt. potassium chloride, 0-150 pts. wt. potassium sulfate, and 180 pts. wt. monoammonium phosphate.    USE - Special fertilizer used for Chinese gooseberry (claimed).    ADVANTAGE - The method is environment-friendly, improves utilization rate of yellow phosphorus slag, and reduces waste emission of yellow phosphorus slag and consumption of resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of special fertilizer comprising adding yellow phosphorus slag into crusher, crushing into 90-100 meshes powder, placing into pretreatment tank, adding nitric acid at weight ratio of 3-6:2, stirring at 60-90 revolutions/minute (rpm) for 20-30 minutes, adjusting temperature to 30-45 degrees C, static processing for 23-25 hours, drying at 60-70 degrees C until water content of 5-10% to obtain activated phosphorus slag; adding activated phosphorus slag into mixer, stirring at 70-120 rpm, adding remaining raw materials, stirring, controlling temperature at 30-40 degrees C, stirring for 20-30 minutes, and storing at room temperature for 2-5 hours to obtain raw material mixture; and placing into granulator and granulating into 70-90 meshes.
NOVELTY - Production of bioorganic fertilizer includes crushing mulberry stems and leaves, animal manure and pond sludge into powder respectively, mixing, stirring, adding microbial strains and water, stirring, and adjusting water content; and piling, fermenting until material turns brown or dark brown and soft, ambient drying, and packaging.    USE - Method for production of bioorganic fertilizer (claimed).    ADVANTAGE - The fertilizer increases soil organic matter content, improves soil structure, promotes soil microorganism activity, increases product quality and yield, increases income of farmers, and it has wide source of raw materials, low cost, simple manufacturing technique, high organic matter and microbial strains contents, and nitrogen, phosphorus and potassium nutrient contents.    DETAILED DESCRIPTION - Production of bioorganic fertilizer comprises:    (A) washing 64.8 wt.% mulberry stems and leaves, drying until moisture content is less than 15-18%, and crushing into 20-30 mesh powder;    (B) drying 20 wt.% animal manure until moisture content is less than 15-18%, and crushing into 50-60 mesh powder;    (C) drying 15 wt.% pond sludge until moisture content is less than 15%, and crushing into 100-120 mesh powder;    (D) mixing obtained powders, stirring, adding 0.2 wt.% microbial strains and right amount of water, stirring, and adjusting water content to 55-65%; and    (E) piling, fermenting until material turns brown or dark brown and soft, ambient drying to 70 degrees C until moisture content is below 10%, and packaging.
NOVELTY - A fuel oil additive comprises 0.5-2.3 wt.% nano silver powder, 1.5-18 wt.% coconut oil, 1.3-3 wt.% silver oxide or silver nitrate, and balance anhydrous ethyl alcohol.    USE - A fuel oil additive for fuel, gasoline, diesel oil, mixed fuel, heavy oil, and biological oil (all claimed).    ADVANTAGE - Product reduces cost, oil pipeline corrosion, exhaust gas discharge, and noise, eliminates carbon deposit, prolongs service life of engine, and increases fuel efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of fuel oil additive which involves weighing components and uniformly mixing; and    (2) fuel comprising fuel additive.
NOVELTY - Preparing short chain fatty acids involves collecting kitchen garbage and then removing oil form kitchen garbage. The garbage is crushed, water is added into crushed garbage and then mixed to obtain mixture. The mixture is processed by ultrasonic wave and then fermented under anaerobic condition to obtain the product.    USE - Method for preparing short chain fatty acids (claimed).    ADVANTAGE - The method enables to convert 70% dissolved organic matter into short chain fatty acids, reduces production cost and does not utilize chemical reagent.
NOVELTY - Preparing microorganism lipid involves culturing microorganism in fermentation culture medium to obtain fermentation culture. The fermentation culture is added into volatile fatty acids, ammonium sulfate and potassium nitrate and then fermented to obtain the product.    USE - Method for preparing microorganism lipid used for treating waste water and biological diesel oil.
NOVELTY - Extracting insect polypeptide involves injecting insect virus into insect and then multiplying virus in insect to obtain hydrolase enzyme. Structural protein of insect is hydrolyzed by hydrolase enzyme to obtain hydrolyzed liquid. The hydrolyzed liquid is filtered to obtain filtrate. The filtrate is centrifuged to obtain the product.    USE - Method for extracting insect polypeptide used as plant foliar fertilizer (claimed).    ADVANTAGE - The method enables to prepare insect polypeptide in a simple, cost-effective and eco-friendly manner.
NOVELTY - The device has a tank body whose lower end is connected with a supplement water inlet. An inner end of the tank body is connected with a return mechanism that is fixed with a bubble refining network. A middle part of the bubble refining network is fixed with a flow component that is mounted in an inner end of the tank body. A three-layer sleeve is fixed with a gas return pipe that is fixedly mounted in a lower end of a substrate. End of the substrate is formed in a through-hole. The three-layer sleeve is fixed with a supplement water overflow pipe that is formed in the through-hole.    USE - Water electrolysis hydrogen comprehensive processing device.    ADVANTAGE - The device occupies less floor space, and has low production cost and better cooling effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a water electrolysis hydrogen comprehensive processing device.
NOVELTY - The method involves entering liquefied natural gas sample through a sampling valve into a valve. Three different pneumatic ways for liquefied natural gas sample are detected. Carrier nitrogen gas is pushed from a first chromatographic column to a second chromatographic column. Small molecule component of carbon dioxide is detected by a detector through a third chromatographic column. Carbon dioxide is completely flowed when another valve is closed. Remaining component of carbon dioxide is flowed through the third chromatographic column to perform a detection process.    USE - Liquefied natural gas component measured multi-dimensional pneumatic phase chromatography method.    ADVANTAGE - The method enables simplifying detection operation and satisfying rapid gas detection process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a liquefied natural gas component measured multi-dimensional pneumatic phase chromatography method.
NOVELTY - The transportation method involves selecting fish having weight of 0.5-1 kilogram, and which does not have disease and damage then killing fish in cold water treatment. The fish is bent by fixing fish mouth and gills with the fish tail by ring. The transport tank is filled with saline water with temperature 10-15 degrees centigrade and potential of hydrogen of 7.6-8.2. The temperature inside the tank is controlled to be at 15-20 degrees centigrade in transporting process.    USE - Long distance transportation method of live fish e.g. jewfish.    ADVANTAGE - Enables simple, natural and environment-friendly operation which allows high density transporting with high survival rate without using any drug since fish is bent to expose the organs. Prevents damage caused by jumping since fish movement is limited. Suitable for commercial transport, and increases sales. Promotes healthy development of the jewfish cultivation industry.    DESCRIPTION OF DRAWING(S) - The drawing shows a photograph of a jewfish.
NOVELTY - Production of selenium-enriched egg involves feeding laying chickens with mixed feed containing selenium-enriched corn, and fermenting chicken excrement to obtain biogas and organic manure slurry. The biogas and organic manure slurry are used for producing energy and fertilizer for growing selenium-enriched corn, respectively.    USE - Method for producing selenium-enriched egg.    ADVANTAGE - The method is inexpensive, safe and environmental-friendly.
NOVELTY - The ecological breeding method involves fermenting excrement of yellow mealworm then added to wheat bran and green vegetable to become feed for goldfish. The goldfish manure is fermented then fed to yellow mealworm.    USE - Yellow mealworm and goldfish ecological breeding method.    ADVANTAGE - The circulation effect provides an environment-friendly cultivation which does pollute the environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of the breeding method. (Drawing includes non-English language text).
NOVELTY - Preparing peppermint water involves mixing anhydrous ethyl alcohol solvent and propylene glycol in weight ratio of 1:1-1:8 to obtain a solution. The obtained carrier solution is added with balance amount of peppermint and then stirring the obtained material to dissolve, where the weight ratio of carrier solution and distilled water is 20-35:50-70. The dissolved material is stirred and then the stirred material is added with balance amount of distilled water to obtain the colorless or light yellow peppermint water.    USE - Method for preparing peppermint water (claimed) used in food, beverages, candy, cosmetics and pharmaceutical industries.    ADVANTAGE - The method enables to prepare peppermint water in environment friendly manner, and without impurity and side effect.
NOVELTY - The system has a fat heat exchanger (10) connected with a liquid mixing unit (4) through a carbon-lean biogas liquid conveying pump (13). The biogas slurry mixing device is provided with an exogenous additive inlet (4.1). An absorption device (6) is fixed with a rich gas inlet (6.1) and a mixed liquid input (6.3). The liquid mixing unit is connected with the absorption device through a heater (5). A carbon-rich biogas liquid regeneration device (11) is provided with an air inlet (11.3) and a regeneration pneuma exhaust port (11.4).    USE - Anaerobic fermentation biogas slurry carbon dioxide absorption and storage system.    ADVANTAGE - The system reduces carbon dioxide regeneration energy consumption, and has wide application range.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an anaerobic fermentation biogas slurry carbon dioxide absorption and storage method.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic block diagram of an anaerobic fermentation biogas slurry carbon dioxide absorption and storage system.    Liquid mixing unit (4)    Exogenous additive inlet (4.1)    Heater (5)    Absorption device (6)    Rich gas inlet (6.1)    Mixed liquid input (6.3)    Fat heat exchanger (10)    Carbon-rich biogas liquid regeneration device (11)    Air inlet (11.3)    Regeneration pneuma exhaust port (11.4)    Carbon-lean biogas liquid conveying pump (13)
NOVELTY - The method involves feeding municipal organic waste and agricultural organic waste into a garage-type anaerobic fermentation chamber. A liquid is sprayed into a percolate processing section through an opening. Aerobic reaction and anaerobic fermentation reaction process are performed after starting an aeration system. A filter liquid is entered into a filter liquor pool through a water collection groove. A sprinkle head is mounted at a top part of the garage-type anaerobic fermentation chamber. Material timing spraying process is carried out.    USE - Municipal organic waste and agricultural organic waste biologically processing method.    ADVANTAGE - The method enables biologically processing municipal organic waste and agricultural organic waste in a simple and convenient manner. The method enables increasing practicability and resource utilization rate. The method enables solving environment problem.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a municipal organic waste and agricultural organic waste biologically processing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a municipal organic waste and agricultural organic waste biologically processing method.
NOVELTY - Method for enhancing growth capabilities of microalga, involves increasing activity of nicotinamide adenine dinucleotide phosphate-oxygen (NADPH-O2) oxidoreductase of microalga.    USE - The method is useful for enhancing growth capabilities of microalga (claimed) which is useful in producing bioenergy or biofuels, such as ethanol, and for raising reproduction potency of microalga.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing microalga in which growth capability is enhanced; and    (2) processed biomass material.
NOVELTY - Method (M1) for binding a particulate material involves (a) providing a lignocellulosic syrup, and (b) providing at least one particulate material contacting the particulate material of (b) with the syrup of (a).    USE - The method is useful for binding a particulate material chosen from animal feed ingredients, carbon black, and fly ash (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for adhering two surfaces; and    (2) composition.
NOVELTY - This utility new type relates to dewatering device of biomass gas, specifically a biomass for a gas composite dehydration device, comprising a coil (1), a folding plate dehydrating device I (2), pneuma cabinet (3), a Roots blower (4), a folding plate dehydrating device II (5), a condensed water storage device (6), the coil (1) end and a folding plate dehydrating device I (2) is a connecting side, and the folding plate dehydrating device I (2), and the other side and the pneuma cabinet (3) one side a, the gas storage cabinet (3), and the other side through Roots blower (4) and folding plate dehydrating device II (5) are connected, and the folding plate dehydrating device II (5) through condensing water storage device (6) and cooling coil (1), and the other end connected. The beneficial effect is that the increase of inner water gas of a removing efficiency and reduces a secondary carrying liquid drop phenomenon, reduces operation cost, increase thermal value.
NOVELTY - The device has a reactor in which the synthetic natural gas including methane is generated from a source gas. The lower portion of internal vessel is arranged with outer container. The separation distance is comprised among outer container and internal vessel. A power supply unit is electrically connected to outer container and internal vessel.    USE - Synthetic natural gas manufacturing device.    ADVANTAGE - The mixing gas is injected in upper portion of reactor, such that the production efficiency of methane is increased effectively. The quantity of injected gas is improved reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the synthetic natural gas manufacturing device using plasma.    Synthetic natural gas manufacturing device (100)    Reaction gas mixing vessel and igniter (110)    Reactor (120)    Gas mixing injector (130)    Main portion stream line (150)
NOVELTY - The system has a pre processor for boosting voltage. A first line part reduces siloxane concentration of biogas. An electric power generator discharges exhaust gas. A second line part reduces siloxane concentration in the exhaust gas. A siloxane remover is fixed with a catalyst oxidation apparatus. A selective catalytic reduction (SCR) apparatus reduces nitrogen oxide in the exhaust gas. The siloxane remover is equipped with the SCR apparatus. The SCR apparatus is connected with a third line part through a fourth line part.    USE - Biogas utilized electric power generation system.    ADVANTAGE - The system effectively prevents inflow of siloxane into an inner side of catalyst facility of the electric power generator. The system is inexpensive and easy to operate. The system has better cleaning effect. The system facilitates easy replacement of the siloxane remover. The system reduces power consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a siloxane removal method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biogas utilized electric power generation system.
NOVELTY - Isolated nucleic acid having: a nucleotide sequence of SEQ ID NO: 2 or SEQ ID NO: 3 (Sequences not defined here may be found at http://seqdata.uspto.gov/?pageRequest=docDetailandDocID=U520150104841A1); or a nucleotide sequence that hybridizes under stringent conditions to SEQ ID NOs: 2 or 3 or to a fully complementary nucleotide sequence of SEQ ID NOs: 2 or 3, is new, where over-expression of the isolated nucleic acid in yeast provides increased xylose fermentation in the yeast relative to a control yeast lacking over-expression of the isolated nucleic acid.    USE - The isolated nucleic acid is useful in a recombinant yeast for producing ethanol (claimed), where the produced ethanol is useful as a fuel for vehicles, or as gasoline additive.    ADVANTAGE - The isolated nucleic acid provides increased xylose fermentation in yeast, as compared to a control yeast lacking over-expression of the isolated nucleic acid (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) a recombinant yeast comprising the isolated nucleic acid; (2) producing ethanol by fermentation of xylose in yeast, comprising: culturing the recombinant yeast (comprising the isolated nucleic acid encoding an aldo/keto reductase (AKR) or a nucleotide sequence that hybridizes under stringent conditions to the isolated nucleic acid encoding AKR, or to a fully complementary nucleotide sequence of isolated nucleic acid) under ethanol-producing conditions; and isolating ethanol produced by the recombinant yeast; and (3) a recombinant Saccharomyces cerevisiae strain, comprising: the isolated nucleic acid encoding the AKR or a nucleotide sequence that hybridizes under stringent conditions to the isolated nucleic acid or its fully complementary nucleotide sequence, operably linked to the heterologous promoter; and xylose reductase (XYL)-1, XYL-2 and XYL-3 genes from Pichia stipitis.
NOVELTY - Invention relates to the field of power engineering and can be used for partial or full replacement of hydrocarbon fuel in various modes of transport, in heating systems of residential and industrial premises, in steam generators and for separate generation of pure oxygen and hydrogen for industrial, medical and other applications. The method of generation of hydrogen and oxygen from water vapour includes passing of superheated steam with the temperature 500-550 degrees C through high voltage DC electric field, meanwhile the superheated steam is passed simultaneously through the gravitational (inertial) field created by steam itself during its movement in electric gravitational hydrogen cell, and separation of hydrogen and oxygen mix. For generation of gravitational (inertial) field the electric gravitational hydrogen cell is designed as a set of the disk plates with the central hole which are used as electrodes and guides for movement of water steam along screw trajectory, and collected in such a manner that disk plates form the double screw, and homonymous ones - even, odd disk plates are connected among themselves and electrically insulated from the heteronymic ones.    USE - Power industry.    ADVANTAGE - Invention allows to reduce considerably dimensions and to increase productivity of units.2 cl, 3 dwg
NOVELTY - Reduction of water and carboxylic acid content in alcohol composition involves contacting alcohol composition comprising 1-4C alcohol(s), water and 1-4C carboxylic acid(s) with a desiccant bed comprising porous inorganic oxide material(s) at elevated temperature. The porous inorganic oxide material(s) contains Bronsted acid portion and/or neutralized Bronsted acid portion.    USE - Reduction of water and carboxylic acid content in alcohol composition e.g. gasoline composition.    ADVANTAGE - The method enables efficient reduction of water and carboxylic acid content in alcohol composition without coproduction of ether.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage of desiccant chosen from molecular sieve 3A and molecular sieve 4A for reducing carboxylic acid content in alcohol composition.
NOVELTY - High growth rate sweet potato compound fertilizer includes 40-50 pts. wt. potassium sulfate, 15-20 pts. wt. ammonium sulfate, 10-15 pts. wt. sodium humate, -15 pts. wt. monoammonium phosphate, 5-10 pts. wt. diammonium phosphate, 10-15 pts. wt. calcium formate, 20-25 pts. wt. ferrous sulfate, 2-3 pts. wt. zinc sulfate, 2-4 pts. wt. sodium molybdate, 5-8 pts. wt. borax, 15-20 pts. wt. urea, 1-3 pts. wt. tung oil, 4-7 pts. wt. lignin sulfonate, 2-6 pts. wt. polyvinyl alcohol, 5-8 pts. wt. carboxymethyl cellulose, 2-2.5 pts. wt. proline, 1.5-2 pts. wt. glycine and 1-1.6 pts. wt. tyrosine.    USE - High growth rate sweet potato compound fertilizer.    DETAILED DESCRIPTION - High growth rate sweet potato compound fertilizer comprises 40-50 pts. wt. potassium sulfate, 15-20 pts. wt. ammonium sulfate, 10-15 pts. wt. sodium humate, -15 pts. wt. monoammonium phosphate, 5-10 pts. wt. diammonium phosphate, 10-15 pts. wt. calcium formate, 20-25 pts. wt. ferrous sulfate, 2-3 pts. wt. zinc sulfate, 2-4 pts. wt. sodium molybdate, 5-8 pts. wt. borax, 15-20 pts. wt. urea, 1-3 pts. wt. tung oil, 4-7 pts. wt. lignin sulfonate, 2-6 pts. wt. polyvinyl alcohol, 5-8 pts. wt. carboxymethyl cellulose, 2-2.5 pts. wt. proline, 1.5-2 pts. wt. glycine, 1-1.6 pts. wt. tyrosine, 3-5 pts. wt. river sand, 5-8 pts. wt. bentonite, 8-11 pts. wt. activated carbon, 20-30 pts. wt. peanut cake, 20-30 pts. wt. bean meal, 30-40 pts. wt. corn rice stalk, 25-30 pts. wt. rice bran, 2-5 pts. wt. probiotics, 1-3 pts. wt. Bacillus spore and 1-3 pts. wt. radix stemonae powder. An INDEPENDENT CLAIM is included for the sweet potato planting method comprising taking sweet potato seedling, applying high growth rate compound fertilizer and spraying paclobutrazol solution.
NOVELTY - The plant has a filtering assembly (15), a solid phase separator and a liquid phase separator that are formed with a substrate (16) and a base of a bioreactor tank (1). The filtering assembly includes outlets for separating materials. A tube (17) is attached to a liquid intermediate tank (18) and placed on another tube (19). A conveyor (20) is attached to a solid phase tank (21) for a transport unit. The bioreactor tank and a biodigest pond (2) are provided with superior output tubes (22) for conducting biogas to a consumer unit (23).    USE - Biological waste water treatment plant for recycling vegetable waste from sugarcane for use in sugar and alcohol sector.    ADVANTAGE - The plant reduces environmental influences and reduces carbon di oxide in an easy manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biological waste water treatment plant.    Bioreactor tank (1)    Biodigest pond (2)    Filtering assembly (15)    Substrate (16)    Tubes (17, 19)    Liquid intermediate tank (18)    Conveyor (20)    Solid phase tank (21)    Superior output tubes (22)    Consumer unit (23)
NOVELTY - The device has discharging cyclone separator (17) whose air outlet and material discharging fan (15) is connected with air inlet. A heat carrier outlet is connected with a ball room (19). A spiral material conveying device (110) is connected with reactor (111). A gas discharge cyclone separator (118) of air outlet is connected with tail pneuma water seal (119). A roots blower (120) and the combustion bed (116) are connected with gas ash discharging cyclone separator. The lower end of cooling tower (117) is provided for supplying redundant biological oil provided in a row of oil.    USE - Biomass thermal cracking oil device.    ADVANTAGE - The stable performance of biomass thermal cracking oil device is ensured effectively with long-term operation so as to increase the efficiency of the biomass thermal cracking oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass thermal cracking oil method.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the biomass thermal cracking oil device.    Material discharging fan (15)    Discharging cyclone separator (17)    Ball room (19)    Spiral material conveying device (110)    Reactor (111)    Combustion bed (116)    Cooling tower (117)    Gas discharge cyclone separator (118)    Pneuma water seal (119)    Roots blower (120)
NOVELTY - The method involves supplying hydrogen in a solvent under a hydrogen or without low hydrogen pressure condition. Lipid raw material is provided to metal catalyst catalysis. A product biological jet coal is obtained, where the product biological jet coal is mixture of C9-C18 alkane, isoparaffin and aromatic hydrocarbon.    USE - Method for production of hydrogen solvent coactivate biological model of coal.    ADVANTAGE - The method enables providing wide application prospect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of coal.
NOVELTY - Liquid fuel comprises 52-88 wt.% methanol, 1-10 wt.% ethanol, 1-10 wt.% acetone, 0.5-5 wt.% hydrogen peroxide, 3-20 wt.% fuel oil and 0.5-1 wt.% inorganic oxidizer.    USE - Used as liquid fuel.    ADVANTAGE - The liquid fuel is safe, and has steady performance.
NOVELTY - A fuel comprises 40-55 wt.% methanol, 30-40 wt.% gasoline, 20-30 wt.% dimethylbenzene, and 0.1-10 wt.% isopropyl alcohol.    USE - Fuel.    ADVANTAGE - The fuel has ideal performance and high safety.
NOVELTY - Alcohol ether fuel comprises 15-50 pts. wt. industrial methanol, 1-3 pts. wt. triethylchlorosilane, 0.05-0.2 pts. wt. catalyst, 1-3 pts. wt. methyl tertiary butyl ether, 1-5 pts. wt. diisopropyl ether, 1-2 pts. wt. isopropanolamine, and 1-2 pts. wt. diethyl carbonate.    USE - Used as alcohol ether fuel.    ADVANTAGE - The fuel saves energy.
NOVELTY - Improving cold flow properties of biodiesel involves stirring component A, B and C with organic solvent in vacuum box at 30-80 degrees C for 2-15 hours to obtain active ionic liquid catalyst. The component A is halogenated alkyl pyridine, 1,2-dialkyl-imidazole or quaternary phosphonium salt. The component B is alkyl aluminum compound (I), nano-silica, anhydrous alumina, chlorinated alkyl aluminum compound (II). The component C is aluminum chloride, zinc chloride, titanium trichloride, titanium tetrachloride, copper(II) chloride or magnesium chloride.    USE - Method for improving cold flow properties of biodiesel (claimed).    ADVANTAGE - The method enables to effective reduce the solidifying point of biodiesel.    DETAILED DESCRIPTION - Improving cold flow properties of biodiesel involves stirring component A, B and C with organic solvent in vacuum box at 30-80 degrees C for 2-15 hours to obtain active ionic liquid catalyst. The component A is halogenated alkyl pyridine, 1,2-dialkyl-imidazole or quaternary phosphonium salt. The component B is alkyl aluminum compound of formula AlEt2Cl-AlR3 (I), nano-silica, anhydrous alumina, chlorinated alkyl aluminum compound for formula RnAlX3-n (II). The component C is aluminum chloride, zinc chloride, titanium trichloride, titanium tetrachloride, copper(II) chloride or magnesium chloride. Active ionic liquid catalyst, organic solvent and ethylene are added into autoclave, where the mixture is stirred in inert atmosphere with speed of 100-400 revolutions per minute at 30-100 degrees C and 0.1-6 megapascal for 2-24 hours. The obtained mixture is hydrogenated with hydrogenation catalyst in an evacuated autoclave, and then stirred with speed of 400-700 revolutions per minute at 1-1.2 megapascal and 15-80 degrees C for 2-48 hours to obtain hydrogenated polyolefin. The biodiesel is processed with hydrogenated polyolefin at normal temperature and normal pressure.    X=F, Cl, Br, or I;R and R3=undefined; and    n=1-3.
NOVELTY - A Saccharomyces cerevisiae yeast strain with preservation number CCTCC M 201463 is new.    USE - Saccharomyces cerevisiae yeast strain with preservation number CCTCC M 201463 for potable spirit, corn raw material, brewing fruit raw material, beverage wine production, and ethyl alcohol fuel production (all claimed).    ADVANTAGE - The strain has high temperature resistance, acid component, and ethyl alcohol component, rich flavor metabolism ability, and good brewing property.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) application of S. cerevisiae yeast strain for potable spirit, corn raw material to saccharify polysaccharide liquid or solid matrix as substrate, and brewing fruit raw material; (2) application of S. cerevisiae yeast strain for beverage wine production which involves using liquid microbial inoculum or solid microbial inoculum production system; and (3) application of S. cerevisiae yeast strain for ethyl alcohol fuel production which involves inoculating S. cerevisiae yeast strain in starch raw material and saccharifying cellulose-containing raw material and fermenting with polysaccharide liquid or solid matrix in which polysaccharide is any polysaccharide component.
NOVELTY - A Saccharomyces cerevisiae NT102002 strain (CCTCC NO: M2014312), is new.    USE - The S.cerevisiae NT102002 strain is useful in composition, which is useful for simultaneous saccharification and fermentation of ethanol using lignocellulosic raw material (all claimed).    ADVANTAGE - The S.cerevisiae NT102002 strain has excellent thermal resistance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of S.cerevisiae NT102002 strain for simultaneous saccharification and fermentation of ethanol fuel, using lignocellulosic raw material.
NOVELTY - Preparation of porous metal organic framework material comprises taking metal compound containing metal ion, mixing metal ion, organic ligand and slow-release alkali in solvent, performing coordination complex reaction to form self-assembled supramolecular network structure, filtering, washing, drying and activating. The metal ion is copper ion (Cu(II)), aluminum ion (Al(III)), magnesium ion (Mg(II)), manganese ion (Mn(II)), iron ion (Fe(III)), nickel ion (Ni(II)), cobalt ion (Co(II)) and/or zinc ion (Zn(II)). The organic ligand contains atom of oxygen, sulfur and/or nitrogen.    USE - Method for preparing porous metal organic framework material used for catalyst, sensor or ionic conductor, or optical or magnetic material for absorbing and separating natural gas, air and inert gas (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for porous metal organic framework material comprising metal ion and organic ligand.
NOVELTY - This utility new type claims a a high ammonia nitrogen organic waste water of a device, including Anaerobic pool, stripping tower and absorption tower, Anaerobic pool. Anaerobic through the water pipeline and a stripping tower, a stripping tower through stripping tower air outlet pipeline and a absorption tower, in the Anaerobic pool provided with gas collection device, a marsh gas collection device through Anaerobic gas pipeline and a stripping tower, a gas collection device of collection as gas stripping tower for blowing off; the Anaerobic pool and between the tower provided with a pH regulating device, a pH regulating device one side set with alkali liquid pipeline, a stripping tower in tower provided with water distribution device, a tower water distribution device and a pH regulating device connected. This utility new type methane generated Anaerobic pool for stripping tower for blowing off; a gas stripping tower, an absorbing tower repeatedly purification, can reduce the impurity of methane; inner of marsh gas after absorption tower enter into subsequent gas purification using technology, the comprehensive treatment waste water and a gas.
NOVELTY - A biochemical exhaust gas treatment system, wherein it is a biochemical waste gas incineration-waste heat recovery system and absorbing system, a biochemical waste gas incineration-waste heat recovery system including biochemical waste gas buffer tank (1), air air blower (2), a biochemical waste gas incinerator (3), a waste heat boiler (4) and super-heater (5). This utility new type of biochemical treatment system of the exhaust gas system using a biochemical waste gas incineration technology, equipped with waste heat boiler, a steam over-heater and a for a can, a over-heat steam or saturated steam. Heat-insulating full-closed washing, full closed. The biochemical treatment system of the exhaust gas system is environment-friendly, safe treatment and comprehensive using engineering, a treating method by using a practical, a. to pollute environment, clean production device, at the same time a energy, energy-saving and environment-friendly.
NOVELTY - The biodiesel fuel blend composition includes diesel, ethanol and prickly poppy methyl ester in a proportion of 50 percent diesel, 30 percent ethanol and 20 percent prickly poppy methyl ester.    USE - Biodiesel fuel blend composition for use in diesel engine, such as single cylinder, water-cooled, four-stroke, direct injection diesel engine (claimed).    ADVANTAGE - Prickly poppy plants are used to obtain the methyl ester for the biodiesel fuel blend, making the blend more economical compared to other biodiesel alternatives. The use of poppy plants contributes to strengthening of the rural agricultural economies as it creates employment opportunities for people. The biodiesel fuel blend also aids in conserving fossil fuel reserves, degrades four times faster than diesel, has 80 percent heating value compared to that of diesel, is eco-friendly, and can be used directly with compression ignition engines with no engine modifications. The blend also has higher flash point, making storage safe.
NOVELTY - The apparatus (31) has bypass line which supplies source gas to modification unit (3) through desulfurization unit (2). A switch unit (7) switches supply route of source gas between desulfurization line and bypass line. A recycle line supplies portion of reformed gas to desulfurization unit (2). An obstruction detection unit (6) detects obstruction of the recycle line. A control unit (9) is comprised so that desulfurization line is made to switch from the bypass line to the switch unit when the source gas is supplied through bypass line and the obstruction is detected by detection unit.    USE - Apparatus for producing gas e.g. town gas and liquefied petroleum gas (LPG) containing high concentration hydrogen.    ADVANTAGE - The poisoning by a sulfur compound is prevented even if recycle sign is obstructed. The cross-sectional area of flow path is reduced, and the flow volume of reformed gas is reduced. The quantity of adsorbent desulfurizing agent is reduced. The stable operationis hydrogen-producing apparatus is continued, without stopping the hydrogen-producing apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of the hydrogen-producing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hydrogen-producing apparatus. (Drawing includes non-English language text)    Desulfurization unit (2)    Modification unit (3)    Obstruction detection unit (6)    Switch unit (7)    Control unit (9)    Hydrogen-producing apparatus (31)
NOVELTY - Producing biodiesel oil involves grinding waste shell of microalgae into powder and then heating the powder at 800-1000 degrees C. The heated material is sintering for 3-4 hours to obtain the lime powder. The microalgae powder is mixed with organic solution in mass volume ratio of 1g:3ml-1g:6ml and then the mixed material is heated at 60-100 degrees C and at ultrasonic frequency of 20-30 kilohertz to obtain solid-liquid mixed phase. The solid-liquid mixed phase is subjected to centrifugal separation to remove the algae residue and then the separated material is kept to obtain upper layer.    USE - Method for producing biodiesel oil (claimed).    ADVANTAGE - The method enables to produce biodiesel oil has improved oil extraction rate and reduced the added amount of the organic solution and catalyst.    DETAILED DESCRIPTION - Producing biodiesel oil involves grinding waste shell of microalgae into powder and then heating the powder at 800-1000 degrees C. The heated material is sintering for 3-4 hours to obtain the lime powder. The microalgae powder is mixed with organic solution in mass volume ratio of 1g:3ml-1g:6ml and then the mixed material is heated at 60-100 degrees C and at ultrasonic frequency of 20-30 kilohertz to obtain solid-liquid mixed phase. The solid-liquid mixed phase is subjected to centrifugal separation to remove the algae residue and then the separated material is kept to obtain upper layer of liquid phase oily organic solution. The lime powder is added with oily organic solution and then the obtained material is heated at 60-100 degrees C to obtain solid-liquid mixed phase. The solid-liquid mixed phase is subjected to centrifugal separation to recover lime and then the liquid phase is distilled under reduced pressure to remove organic solution and to obtain biodiesel oil.
NOVELTY - Producing biodiesel oil involves taking Paulownia seed oil and then extracting the Paulownia oil with anhydrous methanol or ethanol solvent to reduce the acid value of oil to 1 milligrams of potassium hydroxide per gram. The obtained low acid value Paulownia oil is added with 15-25% anhydrous methyl alcohol or ethyl alcohol and 1.5-2.5 wt.% potassium hydroxide to perform transesterification reaction. The obtained material is stand for layering, where the upper layer contains glycerol and then lower solvent phase containing supernatant liquid phase and biodiesel oil.    USE - Method for producing biodiesel oil (claimed).    ADVANTAGE - The method enables to produce biodiesel oil good applicability, good effect and high purity.    DETAILED DESCRIPTION - Producing biodiesel oil involves taking Paulownia seed oil and then extracting the Paulownia oil with anhydrous methanol or ethanol solvent to reduce the acid value of oil to 1 milligrams of potassium hydroxide per gram. The obtained low acid value Paulownia oil is added with 15-25% anhydrous methyl alcohol or ethyl alcohol and 1.5-2.5 wt.% potassium hydroxide to perform transesterification reaction. The obtained material is stand for layering, where the upper layer contains glycerol and then lower solvent phase containing supernatant liquid phase and biodiesel oil. The layer containing biodiesel oil is distilled and then the distilled material is stirred with silicon glue or active carbon. The obtained material is filtered to remove silicon glue or activated carbon. The filtered material is dried over anhydrous sodium sulfate or activated alumina to obtain fatty acid methyl ester or ethyl ester. The obtained material is filtered to remove sodium sulfate or active aluminum oxide and to obtain biodiesel oil.
NOVELTY - Biodiesel oil heating flash device comprises upper, middle and lower parts connected through a flange to form an integrated device. The upper part includes a liquid distributor, whose bottom is set with cleaning disk pipe. The top of the disk pipe is set with a liquid inlet distributor and the bottom of the inlet distributor is set with a falling film tubular heater. The middle of the falling film tubular heater is set with a liquid collector. A gas-liquid separator is set between the cleaning disk pipes. The bottom part is uniformly set with multiple flash distribution plates.    USE - Used as biodiesel oil heating flash device.    ADVANTAGE - The device: reduces cleaning labor intensity; ensures continuous production; has high efficiency; and saves energy.    DETAILED DESCRIPTION - Biodiesel oil heating flash device comprises upper, middle and lower parts connected through a flange to form an integrated device. The upper part includes a liquid distributor, whose bottom is set with a cleaning disk pipe. The top of the disk pipe is set with a liquid inlet distributor and the bottom of the inlet distributor is set with a falling film tubular heater. The middle of the falling film tubular heater is set with a liquid collector. A gas-liquid separator of the belt filter disk is set between the cleaning disk pipe. The bottom part is uniformly set with multiple flash distribution plates based on the height direction, where inner part of each plate is set with a steam guide pipe.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biodiesel oil heating flash device.
NOVELTY - Preparing solid alkali catalyst, comprises (i) drying natural sepiolite, acidifying by adding sulfuric acid solution into dried sepiolite, washing until the filtrate gets neutralized, drying to remove moisture content, and grinding into powder, to obtain acidified sepiolite powder; (ii) soaking acidified sepiolite powder in potassium carbonate solution, stirring while soaking, allowing to stand, filtering, and drying, and placing the mixture into a muffle furnace at 300-500 degrees C, and calcining, to obtain solid base catalyst; and (iii) grinding the solid base catalyst into powder.    USE - The solid base catalyst is useful for producing biodiesel by heterogeneous transesterification reaction (claimed).    ADVANTAGE - The method produces product: having molar conversion rate of biodiesel by 85-98% after carrying out four reactions (claimed), and high catalytic efficiency, and which can be easily recovery, and repeatedly utilized; has simple preparation procedure; and does not produces toxic substances.
NOVELTY - Method for preparing organic fertilizer involves drying chicken manure, uniformly mixing dried chicken manure with water, where moisture content of mixture is 60-70%, adding zeolite powder and calcium chloride to mixture in a weight ratio of 100:3:3, stirring mixture, performing primary fermentation at 60-70 degrees C for 10 days, adding 20-25 wt.% plant ash powder to fermented product, and performing secondary fermentation at 60-70 degrees C for 4-5 days.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare product within short period of time of 40 days as compared to existing method, and has total nutrient content of 10% and nitrogen content of more than 3%.
NOVELTY - The bottom of this utility new type refers to a convenient to regulate a liquid level of biogas pneuma water sealing device, comprising a closeness water tank with a top cover (1), a top cover set with a water supplement pipe (2), air inlet pipe (4) and air outlet pipe (3), water tank (1) is set with an external visual liquid level device and emptying pipe (8), a visual liquid level device comprising connected water tank (1) pipe A of the upper part (5) and connected water tank (1) of the pipe B (7), a thin pipe A (5) and the pipe B (7) through a pipe (6) connected. This utility new type using connector principle, in a water tank through a tube directly observe external water tank in liquid level, and through scave accurate time known amount of internal liquid through regulating the internal liquid level, adjusting pipeline pressure to prevent the air inlet pressure low other illegal input, obviously increase security. The utility model is new type structure is simple, the cost is low, operation is convenient, fit to popularize application.
NOVELTY - Fermentation reactor comprises a fermentor (1), a filter unit (2), a fluid pumping apparatus (3), a molecular sieve separator (4), an inlet (5) for hot water tank, a pressure sensor (6), a stirring blade (7), clip sets (91), a jacket unit (8) and peristaltic pumps (92). The fermentor is connected to the molecular sieve separator and to a filter unit for discharging the purified fermented product. The molecular sieve separator comprises inlet hot water tank for the delivery of fermented product to the feed outlet channel.    USE - Fermentation reactor used for producing fuel.    ADVANTAGE - The fermentation reactor effectively recycles cellulase and xylanase to reduce production costs for generating fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing fuel, which involves:    (A) crushing cleaned fresh corn or rice straw to obtain pulverized straw powder, and then performing biological pretreatment process to degrade lignin of pulverized straw powder using white rot fungi;    (B) performing fermentation by inoculating Saccharomyces cerevisiae into the straw powder, followed by addition of cellulase to perform double enzymatic hydrolysis in the presence of balanced amount of water; and    (C) separating the obtained residues through an ultrafiltration membrane to obtain filtrate, which is distilled to obtain alcohol as fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermentation reactor. (Drawing includes non-English language text).    Fermentor (1)    Filter unit (2)    Fluid pumping apparatus (3)    Molecular sieve separator (4)    Inlet (5)    Pressure sensor (6)    Stirring blade (7)    Jacket unit (8)    Clip sets (91)    Peristaltic pump (92)
NOVELTY - Apparatus comprises fermentation groove (1), crushers (2,3,4), fermenting tank (3), mill (4), mixing machine (5), granulator (6), drier (7) and conveyor (9) where the fermentation groove is connected with a raw material inlet (8), and fermenting groove and the mixing machine are connected with former conveyor. The former crusher is connected with a raw material inlet. The latter crusher and the fermentation tank are with latter conveyor. The fermentation tank is connected with a water inlet (12). The latter crusher and mixing machine are connected with conveyor.    USE - Apparatus used for preparing fertilizer for cultivating persimmon tree (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus.    Fermentation groove (1)    Crushers (2,3,4)    Fermenting tank (3)    Mill (4)    Mixing machine (5)    Granulator (6)    Dryer (7)    Raw material inlet (8)    Conveyor (9)    Water inlet (12)
NOVELTY - Double-layer slow release fertilizer and polyethylene film comprises 45-75 wt.% urea, 7-9 wt.% ferrous sulfate, 15-20 wt.% lime nitrogen, 6-8 wt.% borax, 8-10 wt.% ammonium chloride and 15-19 wt.% slow release silicon fertilizer, and is prepared by heating urea, ferrous sulfate and lime nitrogen to obtain melted mixture that is cooled to obtain fertilizer granule. Slow release silicon fertilizer, ammonium chloride and aqueous solution of borax are mixed to obtain solution that is sprayed on surface of fertilizer granule. The coated fertilizer granules are dried, screened and cooled to obtain product.    USE - Double-layer slow release fertilizer and polyethylene film used for removing pests from peanut (claimed).    ADVANTAGE - The fertilizer ensures long term effect and labor saving, and is prepared in eco-friendly manner.
NOVELTY - Brown coal mine waste recycling process involves crushing brown coal mine waste such as lignite carbon gray mud, brown red clay and sand, and then adding water to the obtained material, which contains 10-40% humic acid. The obtained material is mixed with organic matter, and then the obtained mixture is fermented at 40-60 degrees C for 10-15 days to obtain the finished product, where the obtained material contains 40-70% humic acid.    USE - Method for recycling brown coal mine waste (claimed).    ADVANTAGE - The method enables to recycle brown coal mine waste, ensures improved recovery of brown coal mine product.
NOVELTY - Preparing base fertilizer involves utilizing fresh pig manure 47-49%, nitrogen-fixing bacteria 0.2%, ammonifying bacteria 0.2%, decomposed organic phosphorus 0.2%, yeast 0.2%, potassium solubilizing bacteria 0.2%, straw 10-12%, peanut shell 7%, fruit 3%, lees 10%, seaweed shell 3%, monosodium glutamate 2%, Phellodendron 4%, leavening agent 1%, diammonium phosphate 4%, potassium sulfate 5%, iron amino acid chelate 0.3%, humic acid chelated calcium 0.4% and humic acid chelated copper 0.3%.    USE - Method for preparing base fertilizer used for persimmon tree fruit (claimed).    ADVANTAGE - The method enables to prepare base fertilizer that has drought resistant and cold resistant abilities, and improves quality and yield of persimmon tree fruit.    DETAILED DESCRIPTION - Preparing base fertilizer involves utilizing fresh pig manure 47-49%, nitrogen-fixing bacteria 0.2%, ammonifying bacteria 0.2%, decomposed organic phosphorus 0.2%, yeast 0.2%, potassium solubilizing bacteria 0.2%, straw 10-12%, peanut shell 7%, fruit 3%, lees 10%, seaweed shell 3%, monosodium glutamate 2%, Phellodendron 4%, leavening agent 1%, diammonium phosphate 4%, potassium sulfate 5%, iron amino acid chelate 0.3%, humic acid chelated calcium 0.4% and humic acid chelated copper 0.3%. Pig manure is cleaned to remove impurity and then nitrogen-fixing bacteria, ammonifying bacteria, decomposed organic phosphorus, yeast and potassium solubilizing bacteria are added to carry out fermentation in a sealed container for 16-18 days. Remaining components are crushed to obtain powder, and then powder is mixed with water and then added in fermentation pool and kept for 26-28 days to obtain a product. The product is dried at 351-371 degrees C by using a dryer and granulated and pelletized by using a pelletizer.
NOVELTY - Method for extracting biodiesel convertible lipid from microalgae, involves introducing methanol as cosolvent and supercritical carbon dioxide into reactor, adding microalgae, and extracting mixture at 50 degrees C and 300 bar to obtain the product, where the flow rate of supercritical carbon dioxide and methanol is 1:0.1.    USE - The method is useful for extracting biodiesel convertible lipid from microalgae (claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biodiesel convertible lipid which is produced by performing the above-mentioned method.
NOVELTY - A layered-structured semiconductor photocatalyst contains semiconductor material having layered structure comprising group (VIB) metal element, group (VIIB) metal element, group (VIII) metal element, group (IIB) metal element or group (IIIA) metal element, and group (IIA) metal element, group (IB) metal element and group (VIA) metal element. The molar ratio of group (IIA) metal element and group (IB) metal element is 2:1 or 1:1. The molar ratio of group (IIA) metal element and group (VIA) metal element is 1:2.    USE - Layered-structured semiconductor photocatalyst is used as photocathode material in photoelectrochemical-decomposing water system (claimed).    DETAILED DESCRIPTION - A layered-structured semiconductor photocatalyst contains semiconductor material having layered structure comprising group (VIB) metal element, group (VIIB) metal element, group (VIII) metal element, group (IIB) metal element or group (IIIA) metal element, and group (IIA) metal element, group (IB) metal element and group (VIA) metal element. The molar ratio of group (IIA) metal element and group (IB) metal element is 2:1 or 1:1. The molar ratio of group (IIA) metal element and group (VIB) metal element, group (VIIB) metal element, group (VIII) metal element, group (IIB) metal element or group (IIIA) metal element is 2:1. The molar ratio of group (IIA) metal element and group (VIA) metal element is 1:2. An INDEPENDENT CLAIM is included for preparation of photocatalyst, which involves placing raw materials comprising metal element, bimetallic oxide, metal sulfide or bimetallic sulfide in quartz tube, and heating at 500-1200 degrees C for 5-20 hours in protecting argon atmosphere.
NOVELTY - A fuel reducing agent comprises biofuel and blended diesel oil having volume ratio of 9:1-1:9.    USE - A fuel reducing agent for pyrometallurgical process (claimed).    ADVANTAGE - Reducing agent is energy-saving and safe, saves diesel oil, reduces toxic organic matter discharge and carbon monoxide emission, and has excellent combustion property, improved thermal efficiency, and high flash point.
NOVELTY - An environment-friendly oil comprises 75-85 wt.% methyl alcohol, 0.2-0.3 wt.% ethyl alcohol, 0.025-0.05 wt.% sodium hydroxide, 0.05-0.08 wt.% hydrogen peroxide, 0.001-0.002 wt.% sodium nitrate, 0.01 wt.% dicyclopentadienyl iron, and water.    USE - An environment-friendly oil for diesel engine.    ADVANTAGE - Oil is low cost and energy-saving and has excellent performance.
NOVELTY - An alcohol ester fuel comprises 3-10 vol.% methyl acetate, 5-12 vol.% methyl formate, 15-85 vol.% alcohol, 0-5 vol.% power reinforcing agent, 0-65 vol.% gasoline, 0.05-0.1 vol.% metal corrosion inhibitor, and 0.05-0.1 vol.% rubber anti-swelling agent.    USE - An alcohol ester fuel for vehicle engine in mountain or plateau area (claimed).    ADVANTAGE - Fuel does not easy to deteriorate and has long-term use, air resistance, improved acceleration performance, and high stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of alcohol ester fuel which involves pumping each raw material into tubular mixer using pump and uniformly mixing.
NOVELTY - Preparation of a rosuvastatin intermediate (I) comprises adding a chloro-containing compound (II), water, glucose, carbonyl reductases, ethanol dehydrogenase, and a coenzyme in a reactor, controlling temperature at 10-30 degrees C, maintaining temperature for 10-20 hours, and treating; adding 2,2-dimethoxypropane and methanesulfonic acid at 20-25 degrees C, reacting for 1-3 hours, extracting, and concentrating; and reacting with dimethylformamide (DMF) solvent, anhydrous sodium acetate, and tetrabutylammonium bromide at 130-140 degrees C, stirring for 22-28 hours, crystallizing, and drying.    USE - Method for the preparation of a rosuvastatin intermediate (I) (claimed).    ADVANTAGE - The method has mild reaction conditions, has no ultra-low temperature reactions, reduces solvent consumption, has improved yield, and is inexpensive.    DETAILED DESCRIPTION - Preparation of a rosuvastatin intermediate of formula (I) comprises adding a chloro-containing compound of formula (II), water, glucose, carbonyl reductases, ethanol dehydrogenase, and a coenzyme in a reactor, controlling temperature at 10-30 degrees C, regulating pH to 6.5-7.5 using a base, maintaining the temperature in the reaction for 10-20 hours, and treating to obtain chloro-containing compound of formula (III); adding 2,2-dimethoxypropane to (III), dropwise adding methanesulfonic acid at 20-25 degrees C, reacting for 1-3 hours, regulating pH at 7.5-8.5, extracting using n-hexane, washing with saturated brine, and concentrating using solvent to obtain chloro-containing compound of formula (IV); and adding (IV), DMF solvent, anhydrous sodium acetate, and tetrabutylammonium bromide to a reactor, heating to 130-140 degrees C, stirring for 22-28 hours, evaporating DMF under reduced pressure, adding n-hexane, washing with saturated brine, removing solvent, freezing and crystallizing, and drying.
NOVELTY - A one of sludge from paper mill sewage purification processing device, comprising sewage and combustion product purification device, comprising an air inlet, paper-making sludge burning device, and paper making sludge combustion device of smoke and high pressure fan air inlet of exhaust port is connected, wherein and sewage discharge and combustion product purification device is high pressure blower connected. A harmful substance using high pressure fan in the relatively high temperature of smoke gas transporting to purification groove in, for sewage and combustion product to a purification in a purification groove of sewage process heating to make sewage smoothly carry on Anaerobic fermentation, at the same time use sewage absorbing flue gas, such that when in a paper making waste, can realize sewage purification effect and reduce air pollution.
NOVELTY - Microalgae Tetraselmis suecica is preserved in Spanish algae bank with accession number BEA D0111.    USE - Microalgae Tetraselmis suecica used for producing biofuel (claimed).    ADVANTAGE - The microalgae Tetraselmis suecica enables to produce biofuel in eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing biofuel, which involves:    (A) culturing microalgae Tetraselmis suecica and then extracting fatty acid produced by algae; and    (B) performing transesterification process or hydrogenation of fatty acids to obtain the product.
NOVELTY - A polycyclic aromatic hydrocarbons anaerobic fermentation degradation promoting method involves charging polycyclic aromatic hydrocarbons-containing sludge into an anaerobic reactor, controlling the pH value of fermentation to be alkali by adding a biosurfactant, followed by performing mechanical stirring so that materials of the reaction system are mixed uniformly, and controlling the fermentation temperature.    USE - Method for promoting anaerobic fermentation degradation of polycyclic aromatic hydrocarbons in sludge, and for removing other refractory organic pollutants from the sludge.    ADVANTAGE - The method enables promoting anaerobic fermentation degradation of polycyclic aromatic hydrocarbons with reduced environmental pollution caused by the polycyclic aromatic hydrocarbons, and better land utilization of sludge by anaerobic digestion, in an effective manner.
NOVELTY - A Nannochloropsis mutant strain ENN11-4 (CGMCC No 9320), is new.    USE - The Nannochloropsis mutant strain ENN11-4 is useful for preparing pesticide, and feed, producing fatty acid, and biofuel, and breeding Nannochloropsis (all claimed).    ADVANTAGE - The strain has excellent stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for culturing Nannochloropsis mutant strain ENN11-4, involves inoculating Nannochloropsis mutant strain in culture medium and performing culturing process at 25-42 degrees C and pH of 7-9; and (2) use of Nannochloropsis mutant strain for breeding Nannochloropsis at high temperature, and preparing pesticide.
NOVELTY - Microbial composition comprises Bacillus cereus, B.subtilis, Clostridium pasteurianum, Phanerochaete chrysosporium, Aspergilus oryzae, and Trichoderma viride.    USE - The microbial composition is useful for decomposing crop straw (claimed).    ADVANTAGE - The microbial composition rapidly decomposes crop straw, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the above-mentioned agent for decomposing crop straw, which is performed by mixing the above-mentioned agents and water, stirring the mixture, naturally fermenting the mixture and mixing the obtained fermented mixture and the straw.
NOVELTY - The method comprises: collecting food garbage by sorting wastewater and removing foreign substances; reducing water content of the food garbage to 40-45%; adding 40-65 pts. wt. monoammonium phosphate, 20-40 pts. wt. diammonium phosphate and 10-15 pts. wt. alpha -amylase to 2000-3500 pts. wt. of the food garbage and then stirring; fermenting the stirred mixture and then drying; and powdering the fermented mixture using 100-200 mesh. The fermenting step is accomplished in a fermentation tank at a temperature of 40-55 degrees C for 65-72 hours.    USE - The method is useful for pulverizing fermented food garbage, which is useful in the production of solid biofuel (all claimed).    ADVANTAGE - The method is capable of pulverizing the fermented food garbage in an economical and environmentally-friendly manner. The fermented food garbage improves calorific value of the solid biofuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing a solid biofuel.
NOVELTY - Catalyst obtained by mixing or impregnating reactive metal in metal titanium oxide (I) having perobskite structure, is claimed.    USE - The catalyst is useful for reforming hydrocarbon and synthesizing hydrocarbon using steam (all claimed).    ADVANTAGE - The method shortens processing time and is economical.    DETAILED DESCRIPTION - Catalyst obtained by mixing or impregnating reactive metal in metal titanium oxide of formula (MTiO3) (I) having perobskite structure, is claimed.    M = Sr, Ca, Ma, Ba, La, Y, Ce or Sc.    An INDEPENDENT CLAIM is also included for producing catalyst, comprising either impregnating precursor compound including reactive metal in (I), or mixing active metal or oxide of active metal with (I), and reducing.
NOVELTY - Preparation of biodiesel complex using non-edible oil seeds is claimed.    USE - The biodiesel complex is useful for power generation, and for the manufacture of bio-fertilizers in pellet form, and bio-products in liquid emulsifiable concentrate for agricultural plant protection. No biological data given.    ADVANTAGE - The residues and wastes generated in the process can be efficiently used without discarding to make the high value added product. The process does not need fossil fuel including coal and electric power as they are in-house produced, where the produced power can be used in the process and additional power generated can be sold to the electricity board. The process does not release any effluent discharge since the released effluent is evaporated and recovered back as distilled water for re-use. The process has more opportunities to further increase the profits by adding more processes in the process. The process reduces the manufacturing cost below 50% by reducing the cost of power and fuel. The process has good carbon credit as no fossil fuel is used.
NOVELTY - A pidotimod injection liquid comprises pidotimod, pH-adjusting agent, and injection water in which pH-adjusting agent is sodium hydroxide and disodium hydrogen phosphate, sodium dihydrogen phosphate, sodium carbonate, and/or sodium citrate.    USE - A pidotimod injection liquid (claimed).    ADVANTAGE - Pidotimod injection liquid is stable and does not contain stabilizer or additive, and preparation is environment-friendly.
NOVELTY - Bioorganic fertilizer comprises 22.5-36% castor meal, 20.5-25.5% feather, 16-26.5% meat and bone meal, 8-15% waste wooden meal, 26-33% coffee residue and 0.06% complex microbial inoculum.    USE - Used as bioorganic fertilizer.    ADVANTAGE - The fertilizer comprises high content of organic substances; has low production cost; improves soil; degrades chemical toxins; and removes bacteria to increase product yield and variety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing bioorganic fertilizer comprising (a) screening raw materials, taking feather and meat and bone meal in a concentrating workshop, and placing castor meal, waste wooden meal and coffee residue into another plant, (b) preparing complex microbial inoculum comprising 26% fungi, 14% bacteria, 38% actinomycetes, 5% salt, 6% rice vinegar, 9% rice koji and 2% sugar, (c) allowing decomposition of feather at room temperature in a weight ratio of 1:100, adding complex bacteria, mixing uniformly, concentrating, turning once in 2 days, and aging for 30 days at 28 degrees C, (d) crushing castor meal, waste wooden meal and coffee residue in a crusher, (e) fermenting by adding 0.05% complex microbial inoculum, turning for one time and aging at normal temperature for 8-10 days, and (f) granulating the mixed concentrate, in a ratio of 4:6, stirring uniformly and granulating.
NOVELTY - A hydrolytic acidification process in anaerobic tank promoting method involves subjecting sludge to anaerobic digestion in digestion pool and adding alkali to regulate pH of sludge. Sodium thiosulfate is added to the sludge with stirring, and the mixture is allowed to react under anaerobic condition. Ethanol is added to mixture and fermented for 3-5 days, and fermented product is introduced into the digestion pool followed by maintaining absolute anaerobic condition, regulating pH of fermented product using sodium hydroxide, regulating temperature to 5 degrees C/day and heating at 50-55 degrees C.    USE - Method for promoting hydrolytic acidification process in anaerobic tank.    DETAILED DESCRIPTION - A hydrolytic acidification process in anaerobic tank promoting method involves subjecting sludge to anaerobic digestion in digestion pool and adding alkali to regulate pH of sludge. Sodium thiosulfate is added to the sludge with stirring, and the mixture is allowed to react for 3-5 days under anaerobic condition. Ethanol is added to the resulting mixture and continuously fermented for 3-5 days, and the fermented product is introduced into the digestion pool followed by maintaining absolute anaerobic condition, regulating pH of fermented product using sodium hydroxide, regulating temperature to 5 degrees C/day and heating at 50-55 degrees C.
NOVELTY - Hydroxamic acid derivatives (I)-(IV) are new.    USE - New hydroxamic acid derivatives are useful in preparation of anticancer medicine for treating cancer including glioma in cell lines chosen from U251, MGR2, and U373, and lung cancer in cell lines chosen from SPC, LTEP, and H1650 (all claimed).    ADVANTAGE - The hydroxamic acid derivatives are manufactured by environmentally-friendly process with high yield and high purity.    DETAILED DESCRIPTION - Hydroxamic acid derivatives of formulae (I)-(VI) or their salts or solvates, are new. An INDEPENDENT CLAIM is included for preparation of hydroxamic acid derivatives. The hydroxamic acid derivatives are obtained by dissolving suberic acid in dichloromethane in ice-bath, adding aniline, filtering the resultant product to obtain 8-(cyclohexylamino)-8-oxooctanoic acid derivative of formula (i) as intermediate compound (A), dissolving resultant product in tetrahydrofuran and triethylamine in ice bath, adding isobutyl chloroformate to obtain N-cyclohexyl-8-(((2-methylpropoxy)carbonyl)oxy)-8-oxooctanamide compound of formula (ii) as intermediate compound (B), adding hydroxylamine solution, reacting the resultant product, evaporating, adding hydrochloric acid solution to adjust pH to 5-6, filtering the precipitate, adding saturated sodium bicarbonate solution, stirring the resultant product, filtering, washing, drying to obtain crude product, providing the resultant product in water, heating, adding ethanol, filtering the resultant product and precipitating the resultant product.
NOVELTY - Moisture controlling agent mixed with hydrophilic polymer swelling supplement having excellent water-absorption property including sawdust, peat, peat moss, coconut meal, sugar cane, mushroom waste material, wheat bran, bark, wood powder, activated charcoal, rice hulls or leaf mould, is claimed.    USE - The agent is useful for fermentation during organic waste composting process (claimed) including human excrement, livestock manure, food waste, wastes discharged from agricultural and aquatic processing, wastes discharged from food processing plants, and waste discharged from the slaughter plant.    ADVANTAGE - The agent is economical, and improves swelling property.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for composting organic waste using moisture controlling agent (Drawing includes non-English language text).    Scrambler (1)    Scrambler mixer (2)    Fermentation equipment supplying conveyor (3)    Fermentation equipment (4)    Rotary mixer (5)
NOVELTY - The reactor (1) has a rust plate arranged in a reactor inner space, and a muffle tube (12) whose inner wall is formed by a multipart muffle tube brick lining. An air feed device forms an air inlet opening for air supply to the muffle tube, and an exterior wall of the muffle tube brick lining is surrounded by a muffle tube housing. The exterior wall-side is opened into a muffle tube-housing-side. Air flowing in an air duct is distributed into the muffle tube over the air inlet opening.    USE - Fixed bed reactor for gasification of fuel i.e. biomass (claimed). Can also be used for gasification of waste materials i.e. timber.    ADVANTAGE - The reactor distributes the air flowing in the air duct into the muffle tube over the air inlet opening, so that the reactor is easy to construct, and efficiency of a reaction in an oxidation zone is increased in operator-safe way.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic perspective view of a fixed bed reactor.    Fixed bed reactor (1)    Reactor brick lining (7)    Muffle tube (12)    Reactor housing (22)    Head part (85)
NOVELTY - The device (10a) has a fuel cell unit (12a) provided with a reformer unit (14a). The reformer unit generates synthesis gas using two reactants, and is connected with the fuel cell unit through a fluid connection (16a). A sensor unit (18a) detects a formation of carbon black in an operating condition. A cathode (28a) of the fuel cell (24a) supplies an oxidizing gas e.g. air or oxygen, over a lead (30a). The oxidizing gas is introduced over a valve (32a) and compressed by a compressor (34a).    USE - Fuel cell device.    ADVANTAGE - The reformer unit generates the synthesis gas using the two reactants and is connected with the fuel cell unit through the fluid connection and the sensor unit detects the formation of the carbon black in the operating condition, so that efficiency of the fuel cell device can be increased favorably and service lifetime of the fuel cell device can be prolonged.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for operating a fuel cell device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fuel cell device with a fuel cell unit and a reformer unit.    Fuel cell device (10a)    Fuel cell unit (12a)    Reformer unit (14a)    Fluid connection (16a)    Sensor unit (18a)    Fuel cell (24a)    Cathode (28a)    Lead (30a)    Valve (32a)    Compressor (34a)
NOVELTY - Process (P1) for preparing isoxaflutole, which is (5-cyclopropylisoxazol-4-yl)(2-(methylsulfonyl)-4-(trifluoromethyl)phenyl)methanone (I), comprises mixing (5-cyclopropylisoxazol-4-yl)(2-(methylthio)-4-(trifluoromethyl)phenyl)methanone (II) with acetic acid, acetic anhydride, and hydrogen peroxide in the presence of a strong acid.    USE - The process is useful for preparing (I) (claimed), which is useful as a p-hydroxyphenylpyruvate dioxygenase inhibitor to inhibit carotenoid biosynthesis.    ADVANTAGE - The process: is highly efficient and environmentally friendly; provides a high yield in a short reaction time; avoids use of hazardous and expensive oxidizing reagents and solvent such as dichloromethane; utilizes hydrogen peroxide, thus reducing the cost of production, simplifying work-up, and minimizing any effluent disposal problems; and maintains high degree of selectivity of oxidation of (II).    DETAILED DESCRIPTION - Process (P1) for preparing isoxaflutole, which is (5-cyclopropylisoxazol-4-yl)(2-(methylsulfonyl)-4-(trifluoromethyl)phenyl)methanone of formula (I), comprises mixing (5-cyclopropylisoxazol-4-yl)(2-(methylthio)-4-(trifluoromethyl)phenyl)methanone of formula (II) with acetic acid, acetic anhydride, and hydrogen peroxide in the presence of a strong acid. An INDEPENDENT CLAIM is also included for a process (P2) for preparing (I), comprising mixing (II) with acetic acid and hydrogen peroxide in the presence of a strong acid.
NOVELTY - The apparatus has a heat absorption unit (9) for absorbing heat energy from the product gas (5), connected to a discharge device (7). A heat emission unit (10) is connected to feeding device (6), for emitting heat energy to raw material (2) in feeding device. A closed circuit (12) for a heat exchange medium (12') is formed between heat absorption unit and heat emission unit such that heat exchange medium is vaporized in heat absorption unit by heat exchange with the product gas. The heat exchange medium in heat emission unit is partially condensed by heat exchange with raw material.    USE - Apparatus for gasifying raw material e.g. biomass such as wood waste, straw, or organic waste.    ADVANTAGE - The raw material required heat energy is completely recovered. Thus, the energy losses of the gasification are reduced. The cold gas efficiency is improved. The economic efficiency of the gasification of biomass is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for gasifying raw material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for gasifying raw material. (Drawing includes non-English language text)    Raw material (2)    Product gas (5)    Feeding device (6)    Discharge device (7)    Heat absorption unit (9)    Heat emission unit (10)    Closed circuit (12)    Heat exchange medium (12')
NOVELTY - The system has a pump (8) and a reservoir tank (5) that is in fluid communication with a radiator (3) to pump the electrolytic solution from the radiator back to a HHO generator (1). A demister (9) is installed downstream of the HHO generator to remove steam from hydrogen and oxygen gas generated in the HHO generator, such that the Zeer pot has only water inside a region for water evaporation. The HHO generator is open to the environment in order to allow water vapor, hydrogen gas, and oxygen gas to exit the HHO generator.    USE - Hydrogen/oxygen (HHO) system.    ADVANTAGE - The system improves high production of hydrogen and oxygen gas compared to other HHO generators of the same size, by using a Zeer pot to cool the solution inside the HHO generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the HHO system comprising the HHO generator, the Zeer pot, and the radiator.    HHO generator (1)    Radiator (3)    Water reservoir (5)    Pump (8)    Demister (9)
NOVELTY - The system has a conversion reactor i.e. riser reactor, for thermally converting a biomass feedstock fraction into an initial conversion product. A residual solids separator removes residual solids (108) from a portion of the initial conversion product. A biomass feed system transports the biomass feedstock fraction from a splitter to the conversion reactor. A biomass filter aid transport mechanism transports a biomass filter aid (106) from the splitter to the residual solids separator.    USE - Biomass conversion system for removing residual solid particle e.g. forestry waste such as wood chip, saw dust, pulping waste and tree branche, agricultural waste such as corn stover, wheat straw and bagasse, and energy crop such as eucalyptus, switch grass and coppice, from bio-oil.    ADVANTAGE - The biomass filter aid transport mechanism transports the biomass filter aid from the splitter to the residual solids separator such that the spent biomass filter aid is recycled for bio-oil production, thus ensuring that the residual solids are removed from bio-oil in an efficient manner.    DETAILED DESCRIPTION - The residual solids separator is a centrifuge, a rotary filter, a plate filter and a bag filter.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a horizontal plate filter for use in conjunction with a biomass conversion system.    Horizontal plate filter (100)    Plate-type filter elements (102)    Filter housing (104)    Biomass filter aid (106)    Residual solids (108)
NOVELTY - Fermented waste disposal tank comprises a tank body (1), a solid fermentation room, a liquid fermentation room, and a support (12); where the tank body (1) is provided with feed inlet port (3), whose upper side is provided with rainproof plate (2), and the tank body port is welded with rainproof plate using the supporting rod. The outer wall of tank body has a supporting lug, and the bottom of the tank body has a swash plate (9) constituting solid fermentation room and liquid fermentation room. The swash plate and the tank body are welded together and the, supporting lug is fixed to support.    USE - Used as a fermented waste disposal tank.    ADVANTAGE - The tank has simple structure, requires small floor space, is non-polluting, and is suitable for rural area and town.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fermented waste disposal tank.    Tank body (1)    Rainproof plate (2)    Feed inlet port (3)    Swash plate (9)    Support (12)
NOVELTY - An easy-forming biomass fuel comprises 50-60 wt.% mulberry stalk, 30-40 wt.% rice hull, 5 wt.% clay and 5 wt.% biomass combustion-supporting adhesive. The easy-forming biomass fuel is obtained by crushing mulberry and rice husk, adding clay and adhesive, crushing the resultant product, drying, compressing, screening the resultant product, cooling and packaging.    USE - Easy-forming biomass fuel (claimed).    ADVANTAGE - The easy-forming biomass fuel is manufactured by environmentally-friendly and economical process with high yield.
NOVELTY - The electrolyzer has electrodes that are insulated by gasket and are held in between frames (9). Centre electrode (10) or gasket (8) and frame art of circular shape are provided with two holes at top and two holes at bottom, when assembled ducts for gases at top and ducts for electrolyte at bottom are formed. End electrodes (2a,2b) with pre-electrode fitted of one side only facing to cell battery are provided with electrical connection and are compressed between end boxes by tie bars (3), such that gas pressure is build up to 100 PSIG within cell.    USE - Filter press type circular bi-polar water electrolyzer for production of hydrogen and oxygen gas.    ADVANTAGE - The bi-polar water electrolyzer achieves less floor area, low electricity consumption, less raw material, maintenance free, less manpower and supervision, highly efficient and economical, easy operation, and compact and leak proof structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of the assembled plant.    End electrodes (2a,2b)    Tie bar (3)    Gasket (8)    Frame (9)    Centre electrode (10)
NOVELTY - Waste sewage treatment plant comprises briquette that is prepared by using 25 wt.% sludge, 3 wt.% natural oil, 4 wt.% water, 13.6 wt.% sawdust, 13.6 wt.% corn stover, 13.6 wt.% coal sludge, 13.6 wt.% poultry litter and 13.6 wt.% molasses.    USE - Waste sewage treatment plant.    ADVANTAGE - The waste sewage treatment plant is eco-friendly.
NOVELTY - Organic material mixed biomass pellet fuel preparation involves weighing high-carbon black shale with 10-20% carbon, 1.0% sulfur, 0.5% nitrogen, 12% ash content, and 20-25% volatile matter. The weighed raw material is mixed uniformly.    USE - Method for preparing organic material mixed biomass pellet fuel (claimed).    ADVANTAGE - The method prepares organic material mixed biomass pellet fuel in a simple, cost-effective, and eco-friendly manner by saving agriculture and forestry resources.
NOVELTY - This utility new type relates to a a biomass combustion system, comprising a room, hopper, air blower group and injector, a set in a room of upper, lower room provided with a collection device, air blower group comprises the first air blower and the second air blower and third air blower, the first, the second air blower and a room connected, the first, second, third air blower are set with each other of a multi-section adjusting switch, a room through pipeline and purification room connected the lower part inner purification room set with blocking part, purification room set with containing room, an injector through air purification room and connected, third air blower and spraying l connected, thermal decomposition and injector of this utility new type biomass combustion system is through a first, second, third air blower capable of adjusting air control a rate of flow of room, at the same time through adjusting air rate of flow, effective to obtain each inner cleaning device a inner wall to avoid.
NOVELTY - Adjustment of pH of manure slurry is carried out providing manure slurry held in any manure retention structure; and mixing an aqueous alkaline solution directly into the manure slurry to adjust pH of the final mixture in the retention structure to within a desired predetermined pH range to make final mixture suitable for land application.    USE - Method for adjusting pH of manure slurry (claimed).    ADVANTAGE - The method provides safe, effective, and economical treatment and disposal of large volumes of manure wastes and other agricultural wastes, while minimizing liming applications in land-based disposal of anaerobically fermented agricultural and municipal waste. The adjustment of the pH of the manure slurry to within desired predetermined pH range reduces or eliminates further need for adjustment of soil pH due to manure acidity. Further, the method allows for sterilization of organic animal wastes including specified risk materials, can destroy transmissible spongiform encephalopathies (TSEs) and/or other pathogens by alkaline hydrolysis, and allows disposal of the sterilized end products by mixing the alkaline hydrolysis effluent into manure retention vessels prior to land application of the mixture.
NOVELTY - The method involves converting biomass or coke in influx of a gasification part (V) and an abeyance bed (12) into product gas (P), and operating a carrying layer (15) in an abeyance bed reactor (6) continuously in a structure mode. Degradation of the abeyance bed is performed by introduction of a supplementary gasification part (Vz), where the gasification part is designed as a nozzle or lance. The lance is injected into a non-load-bearing layer (16) of the abeyance bed. Filling height of the abeyance bed reactor is measured by a level sensor (13).    USE - Method for controlling operation of an abeyance bed reactor.    ADVANTAGE - The method enables ensuring reliable and safe long term operation of a plant with significant reduced requests to monitoring and trained interventions of monitoring personnel, and preventing efficiency reduction of gasification process or collapse of the abeyance bed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an abeyance bed reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a reduction unit, and a temperature gradient within the reduction unit.    Product gas (P)    Gasification part (V)    Supplementary gasification part (Vz)    Abeyance bed reactor (6)    Abeyance bed (12)    Level sensor (13)    Carrying layer (15)    Non-load-bearing layer (16)
NOVELTY - Method for preparing psychrophilic anaerobic digestion of ammonia-rich waste, involves (a) contacting the ammonia-rich waste to an adapted inoculum comprising anaerobic bacteria in a digester, and (b) reacting the ammonia-rich waste with the inoculum at less than 25 degrees C to allow digestion of the ammonia-rich waste.    USE - The method is useful for preparing psychrophilic anaerobic digestion of ammonia-rich waste. The ammonia-rich waste is liquid waste, semi-liquid waste or solid waste, chosen from animal manure, animal slurry, agrifood waste, slaughterhouse wastes, municipal waste, energy crops, or farm waste chosen from dairy manure, beef manure, poultry manure, spoiled hay, silage, swine manure or cash crops, preferably chicken manure or pig manure. The slaughterhouse wastes are feather, beef hoofs, blood, contaminated meat, rendering or their mixture (all claimed).    ADVANTAGE - The method he process offers the competitive advantages of great stability, robustness, maximum performance, and minimum supervision.
NOVELTY - The apparatus (1) has a to-be-measured liquid stirring chamber (30) to which hydrogen gas contained as dissolved hydrogen in to be-measured liquid is discharged from to-be-measured liquid. Fuel cell (2) makes hydrogen gas and in-air oxygen gas to discharge from to-be measured liquid react and generates electrical energy. A measurement unit (6) measures amount of electrical energy which is connected to fuel cell and generates energy from fuel cell.    USE - Measuring apparatus of dissolved hydrogen concentration used in health industry field and electronic industry field.    ADVANTAGE - The dissolved hydrogen concentration contained in the to-be-measured liquids in the time of use is quantified rapidly and easily. Measuring apparatus with the whole small apparatus and cost concerning apparatus is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a measuring method of dissolved hydrogen concentration.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the measuring apparatus. (Drawing includes non-English language text)    Measuring apparatus (1)    Fuel cell (2)    Measurement unit (6)    To-be-measured liquid stirring chamber (30)    Voltage measurement device (60)
NOVELTY - The electrolyzer (101) has electrolyte aqueous solution (107) that includes intermediate product repeating oxidation-reduction reaction, an electrolysis electrode (103) for electrolyzing water, a bipolar electrode (102) for performing oxidation-reduction reaction of the intermediate product, and an electrolytic cell (112). The intermediate product is maintained with a higher oxidation reduction potential than the hydrogen generation potentials of the bipolar electrode and the intermediate product and lower than hydrogen generation potential of electrolysis electrode.    USE - Water electrolyzer such as hydrogen-producing apparatus for use in energy storage and supply system (claimed).    ADVANTAGE - The intermediate product mediate product is maintained with a higher oxidation reduction potential than the hydrogen generation potentials of the bipolar electrode and the intermediate product and lower than the hydrogen generation potential of the electrolysis electrode. Thus, the water electrolyzer is provided with reduced installation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the water electrolyzer.(Drawing includes non-English language text)    Water electrolyzer (101)    Bipolar electrode (102)    Electrolysis electrode (103)    Electrolyte aqueous solution (107)    Electrolytic cell (112)
NOVELTY - Manufacture of high-quality biodiesel fuel involves hydrogenating biodiesel fuel by selectively converting unsaturated fatty acid monoglyceride, and removing fatty-acid monoglyceride.    USE - Manufacture of high-quality biodiesel fuel used for engine systems.    ADVANTAGE - The method enables simple manufacture of high-quality biodiesel fuel with improved oxidation stability.
NOVELTY - The fuel cell power generation system comprises a steam turbine generator (140), a condenser (150) and a fuel cell unit (110) that is arranged at the upper part of a waste heat boiler (120), where the waste heat boiler is provided for generating high pressure steam. The condenser is provided for liquidizing the high pressure steam. A hot-water tank (160) is installed with the waste heat boiler.    USE - System for generating power for fuel cell power by using exhaust gas.    ADVANTAGE - The fuel cell power generation system comprises a steam turbine generator, a condenser and a fuel cell unit that is arranged at the upper part of a waste heat boiler, where the waste heat boiler is provided for generating high pressure steam, and thus maximizes fuel cell power generation efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for generating power for fuel cell power by using exhaust gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a fuel cell power generation system. (Drawing includes non-English language text).    Fuel cell unit (110)    Waste heat boiler (120)    Steam turbine generator (140)    Condenser (150)    Hot-water tank (160)
NOVELTY - Manufacture of lignocellulosic biomass involves mixing wood powder or peat powder with molasses and diluting mixture using diluting agent and forming a paste, drying the paste at 80-250 degrees C, and carbonizing at 200-300 degrees C.    USE - Manufacture of lignocellulosic biomass (claimed).    ADVANTAGE - The method efficiently and economically provides lignocellulosic biomass having high hydrophobicity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for lignocellulosic biomass.
NOVELTY - Hybrid fuel comprises coal, bio-solution and surfactant.    USE - The fuel is useful in power plant.    ADVANTAGE - The fuel burns in a continuous pattern which is identical with the combustion pattern of coal, utilizes hydrophobic bio-solution, improves the bonding strength of the bio-solution and coal, resolves the problem of power generating efficiency falling according to the generation of unburned carbon, and has increased calorific value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for manufacturing hybrid fuel, comprising (a) adding surfactant into the bio-solution, and forming bio-solution mixture by mixing with water, and (b) mixing coal in the bio-solution mixture, and preparing hybrid fuel by drying.
NOVELTY - Manufacture of hydrophobic coal-wood molded fuel involves mixing wood powder and coal, obtaining mixed fuel, molding, and carbonizing.    USE - Manufacture of hydrophobic coal-wood molded fuel (claimed).    ADVANTAGE - The method enables manufacture of hydrophobic coal-wood molded fuel having excellent fuel density and forming strength.
NOVELTY - This utility new type provide the A air-floating a biogas purification device, relating to a field of water, waste water, sludge or biogas purification device solves the problem that the current need either large land and fanancial, purification effect is not good, even with a further two times pollute cause equal, this device comprises the condensing mechanism, a water mechanism and air floating mechanism, this utility new type the device construction is simple, use is convenient, maintenance cost is low, small floor area, purification effect is good, safe and reliable operation, long service life and use for a large-scale cultivation field generating of biogas slurry mass process, reduce pollute of environment at the same time also promotes clean energy of popularization.
NOVELTY - One with a return line biogas manure. Anaerobic fermentation device, it relates to a A Anaerobic fermentation device, specifically relates to a a livestock Anaerobic fermentation device is provided with a liquid return line. This utility new type is that after Anaerobic fermentation of biogas slurry cannot be applied to direct use, need according to different need after blending into diluting liquid of different concentration or a sterilizing is using, and the long time use for a groundwater, air and natural cause two times pollute, using season, use a also comprises limitation problem. This utility new type the solid liquid separating machine and a strip biogas pipeline connected, solid-liquid separating machine further through one of the first pipeline biogas slurry and biogas storage tank connected, biogas storage tank and a biogas slurry of the second connected pipeline, the second pipeline and the slurry a third pipeline connected, the second pipeline is further connected through the liquid return pipeline and a feeding device. This utility new type used for agriculture marsh gas preparation.
NOVELTY - This utility new type provide the A garbage carbonization reaction kettle, comprising a kettle body and kettle cover, the kettle cover seal for a kettle, a kettle body equipped with a has gas inlet, gas discharge outlet, condensate discharge port, a pressure and temperature wherein a wherein, inner the kettle body has set along the length direction of the kettle body is a guide rail. The gas inlet comprises a gas entrance and join the second gas join entrance, wherein, the first gas. wherein set at lower side of the kettle body and the kettle body close to the middle position, the second gas. wherein a set with a seal head end of said kettle body. Further comprising , a heat insulation part set at inner side of said kettle body. A heat insulation part comprises a joint of asbestos and tin, a tin through the asbestos connecting the kettle body. This utility new type set in the length direction of the kettle body has a guide rail, a convenient loading and unloading of a reactant; in this utility new type has set, increase the heat insulating effect.
NOVELTY - A flue-cured tobacco for preparing fermentable reducing sugar from biomass a pneuma device, comprises hearth (2), a hearth (2) at the bottom has the air inlet ring channel (3) and groove (16), the air ring channel (3) and air inlet pipe (9) connected, a hearth (2) side part set with the gas pipe (8), the top has activity is equipped with seal cover (12), a hearth (2) is divided into a hearth (4), hearth (5) in a lower hearth (6), a hearth (4) is a small under a large frustum, lower hearth (6) is big end up frustum, in hearth (5), the upper part is cylindrical, the lower part is a big frustum, hearth (6) upper part. the pneuma has anti-blocking ring (7), a guide pneuma anti-blocking ring (7) and furnace wall between the pneuma ring composed of channel (14), gas outlet pipe (8) set up in a furnace wall inner poly pneuma ring channel (14). This utility new type gas stable, not easy to block, that is, using a biomass fuel, but also use a coal is fuel.
NOVELTY - A bottom of a preparing fermentable reducing sugar from biomass pneuma furnace is air inlet device, a hearth (1) set with air inlet ring channel (2), the air ring channel (2) and air inlet pipe (4), the air ring channel (2) of inner ring (5) is provided with a air inlet hole (3) and the hearth (1) is connected with the air inlet pipe (4) is connected the air inlet line type ring channel (2), an air inlet hole (3) is set with two more uniform. This utility new type can sufficiently uniform for a hearth oxygen supply, which is good for gas of biomass conversion, more stable, and a yield increase, and can use coal is fuel, which enlarges the furnace with fuel of a select range.
NOVELTY - Gathering anti-blocking device of a preparing fermentable reducing sugar from biomass pneuma a furnace, a hearth (1) in lower part is set with gas outlet pipe (2), a gas outlet tube (2) upper part is set with the pneuma anti-blocking ring (3), the pneuma anti-blocking ring (3) and furnace wall between the pneuma ring composed of channel (6), gas outlet pipe (2) of air inlet is located at the pneuma ring channel (6) inner. This utility new type for air outlet pipe set at lower part in the hearth, can make out a gas holding high temperature to prevent the tar condensed in to block the pipe, gathering anti-blocking ring can polymerization gas to gas outlet, and prevent the fuel entering into a gas outlet, gas so as to ensure smooth and stable in output.
NOVELTY - The module has a portable tank filled with mixed reagent i.e. oils or fats, with catalytic blend using a pump and a valve. Catalytic pumps (5, 6) are fed to a mixer (7) that mixes the reagent. The catalytic pump is connected with a reservoir (8) under a positive pressure condition. A sucked pump (9) is forwarded to an impeller (12), where an output part of the sucked pump is connected to another tank (14) that produces a vacuum space.    USE - Installation module for producing biofuels from vegetable and animal fats.    ADVANTAGE - The module has better mounting effect and portable structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic diagram of an installation module.    Catalytic pumps (5, 6)    Mixer (7)    Reservoir (8)    Sucked pump (9)    Impeller (12)    Tank (14)
NOVELTY - This utility new type relates to a crop a fuel preparation device, comprising a machine body, a transmission device and cavity body, the inner body provided with driving motor, driving motor and transmission mechanism connecting the cavity body set in the machine body, the cavity body comprises a bottom plate, a base, a bearing base set in the upper bottom plate, the motor shaft of the driving motor and a base, a transverse shaft set in bearing base a, a cross shaft set provided with a roller, a bottom plate provided with a discharge channel, the lower discharging channel provided with vibration. This utility new type of crop fuel preparation device capable of automatic feeding and discharging, it can automatic operation, at the same time it can through heating assistant device, and the device structure design is simple and convenient maintenance, manufacture and use cost low.
NOVELTY - Emission-free mobility with natural gas/methane, comprises (a) fueling natural gas from the natural gas grid or natural gas storage as fuel, (b) driving the natural gas into an internal combustion engine for mobility, (c) collecting and separating carbon dioxide from the exhaust gases of natural gas, (d) delivering the collected carbon dioxide to a collection point, (e) producing hydrogen by electrolyzing with energy from power grid or wind or solar plant,(f) converting the discharged carbon dioxide into methane with hydrogen, and (g) storing and dispersing methane into the a net.    USE - The method is useful for emission-free mobility with natural gas/methane (claimed).    DETAILED DESCRIPTION - Emission-free mobility with natural gas/methane, comprises (a) fueling natural gas from the natural gas grid or natural gas storage as fuel, (b) driving the natural gas into an internal combustion engine for mobility, (c) collecting and separating carbon dioxide from the exhaust gases of natural gas, (d) delivering the collected carbon dioxide to a collection point, (e) producing hydrogen by electrolyzing with energy from power grid or wind or solar plant,(f) converting the discharged carbon dioxide into methane with hydrogen, and (g) storing and dispersing methane into the a net. The step (a)-(d) are carried out in mobile phase and the step (e)-(g) are carried out in stationary phase.
NOVELTY - Device comprises organic feedstock low temperature gasifier (1) to generate tar-containing carbonization gas and solid organic feedstock, a high temperature gasifier (2) comprising an oxidation unit (21) and an endothermic reactor (22), where the carbonization gas is partially oxidized in the oxidation unit (21) and subsequently partially reduced to generate synthetic gas. The endothermic reactor conically extends in a vertical direction with at least one height. The device also comprises a unit for removing unwanted solid particles.    USE - The device is useful for partial gasification of solid (claimed).    ADVANTAGE - The device consumes less amount of feed and has high cold gas efficiency; and removes unwanted contaminants in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for partial gasification of solid, comprising introducing solid organic feedstock into organic feedstock low temperature gasifier to generate tar-containing carbonization gas, conveying the carbonization gas into an oxidation unit of the high temperature gasifier, for partial oxidation, subsequently partially reducing to generate synthetic gas in the endothermic reactor, where the endothermic reactor conically extends in a vertical direction with at least one height, and the synthetic gas in the endothermic reactor substantially flows upward in a vertical direction from below, allowing the predominant pyrolysis coke in the synthetic gas and unwanted solid particles at specific height to be removed from the side outlet.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the device for partial gasification of solid.    Low temperature gasifier (1)    High temperature gasifier (2)    Pressure regulator (19)    Oxidation unit (21)    Endothermic reactor (22)
NOVELTY - The system (101) has an anaerobic processing part for processing organic waste water utilizing anaerobic microorganisms. A water sprinkling part (9) sprinkles the treated water from the anaerobic processing part on a carrier part (10). Phosphorus adsorption agent is provided with calcium-type phosphorus adsorptive substance. A phosphorus process part makes phosphorus and the calcium-type phosphorus adsorptive substance to react with the treated water from the aerobic-treatment part react and produces crystallization of hydroxyapatite.    USE - Phosphorus elimination-type waste-water-treatment system.    ADVANTAGE - The system can easily perform removal of phosphorus from the organic waste water.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a phosphorus elimination-type waste-water-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a phosphorus elimination-type waste-water-treatment system.    Water supply apparatus (2)    Anaerobic-treatment tank (3)    Water sprinkling part (9)    Carrier part (10)    Phosphorus elimination-type waste-water-treatment system (101)
NOVELTY - Wood pellets (P) are obtained by compression-molding only woody raw material (M), and have a particle size of 1 mm or less and a bending strength of 80-110 kg/cm2.    USE - Wood pellets are used as solid fuel in pellet stoves and pellet boilers.    ADVANTAGE - The wood pellets have excellent bending strength and shape stability, and no swelling. Hence, the wood pellets do not condense or lose shape during storage. The fine wooden particles are firmly bonded by hardened lignin which is one of the components of woody raw material. Residue (cinder) hardly remains during combustion of wood pellets. Hence, combustion efficiency is high.    DESCRIPTION OF DRAWING(S) - The drawing shows a side surface sectional view of extruders used for manufacturing wood pellets.    Extruders (10,40)    Primary raw material (E)    Woody raw material (M)    Wood pellets (P)    Solid rod-shaped product (S)
NOVELTY - The method involves using a palm tree core housing of an average particle diameter (DA) as a raw material. The housing is heated and dry-distilled to adjust the particle size to 45.9-66.9%, and to manufacture palm tree core-housing carbon. The solid fuel for sintering is implemented without crushing housing carbon such that the average particle diameter of housing satisfies a predetermined relationship relating average particle diameter of housing carbon and particle size contraction rate of ratio of diameter of housing to diameter of housing carbon.    USE - Method for manufacturing sintered ore in blast furnace of iron mill.    ADVANTAGE - The palm tree core housing is heated and dry-distilled to adjust the particle size to 45.9-66.9%, and to manufacture palm tree core-housing carbon and the solid fuel for sintering is implemented without crushing housing carbon such that the average particle diameter of housing satisfies a predetermined relationship relating average particle diameter of housing carbon and particle size contraction rate of ratio of diameter of housing to diameter of housing carbon. Thus, the highly productive sintered ore is manufactured effectively by adjusting the particle diameter of palm tree core housing using the palm tree core-housing carbon manufactured to the appropriate particle size without performing crushing and sieving operations.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating the relationship between the particle size and sintering production rate of palm tree core-housing carbon by sintering pan test. (Drawing includes non-English language text)
NOVELTY - Objective of the invention is to convert an operable periodical biogenerator plant with manual charging-discharging for production of low-pressure biogas into an industrial continuous plant for production of biogas of high pressure (5-6 MPa) by installation of a bioreactor in the ground at the depth of around 1200 m, which will provide for optimal temperature conditions of reactions of anaerobic conversion of biomass, will develop conditions for self-flowing charging of a bioreactor with biomass and gaslift discharging of biogas and residual biopulp. Standard drilling equipment and materials may be used for arrangement of continuous underground generators of biogas.    USE - Power engineering.    ADVANTAGE - Invention is ideally energy-saving and environmentally safe.
NOVELTY - Objective of the invention is to convert an operable periodical biogenerator plant with manual charging-discharging for production of low-pressure biogas into an industrial continuous plant for production of biogas (biohydrogen) of high pressure (10-12 MSh) by installation of a bioreactor in the ground at the depth of around 2000 m, which will provide for optimal temperature conditions of reactions of anaerobic conversion of biomass, will develop conditions for self-flowing charging of a bioreactor with biomass, gaslift discharging of biogas and residual biopulp. For production of biohydrogen the following systems are provided: for biomass acidification up to pH=5.49: sowing of biomass with hydrogen-producing microorganisms; supply of biological catalyst into a zone of reaction of the bioreactor. Standard drilling equipment and materials may be used for arrangement of continuous underground generators of biogas (biohydrogen).    USE - Power engineering.    ADVANTAGE - Invention is ideally energy-saving and environmentally safe.
NOVELTY - This utility new type relates to a a sewage treatment process and a simulate device, provided with a sampling interface outside side wall at middle part of reaction cup body, cup body. outside side wall bottom end part is set with vent and air inlet interface, a cup bottom of a reaction cup body surface provided with air pipe and stirring rotor, set with a aeration head in the air tube, fixed hoop has a socket section inner wall of a reaction cup body, temperature probe provided with a lower part in inner wall of reaction cup body, a platform having a display screen, in a top surface of a table provided with protruding garter spring, an opening provided with a upper convex ring, a garter spring protruding outside and close to the top surface of a table is a convex ring set with temperature probe. This utility new type a rapid stimulate municipal sewage treatment plant for each biochemical reaction unit processing process, this utility new type is helpful in adjusting and optimizing sewage treatment plant operation parameter, scientifically guiding operation process and operation.
NOVELTY - Dual ring mould granule molding machine is a one outside a manufacturing wooden meal fuel and a molding device of a crop straw granule fuel, wherein each molding mould by large diameter ring mould (5) and small diameter ring die (4) constitute dual ring mould, mould upper dual ring set with ring mould protecting cover (10) and a feeding port (1), welding has annular die gap regulator dual ring mould outside a tank a (2), a ring module driving shaft (17) is set with a cooling water tank, a ring module driving shaft (17) and gear (3) fixed connected, it has small volume, simple structure, convenient and durable, high yield, use cost is low, the cost is low equal advantages of biomass molding machine. It integrates each type home and abroad preparing fermentable reducing sugar from biomass material machine has b, lighting, home audience, using the mould is mutually oust,, the force of pressure extrusion molding, after development, test is a multi year, a new technology product A is developed.
NOVELTY - A fire resistant a straw fuel block, relating to crop straw for the manufacture of fuel. Inner outside two layer comprises one of a fuel, said fuel a whole inside a straw powder by pressed by a filler, the fuel a whole outside is outside, the outside of a coal seam or the filler is covered in inner part provided with multiple expose a burning hole is square or circular inner filler is up at the outside of coal seam. The combustion hole area accounts for more than 3-5 outside the whole area of the coal bed. This utility new type is beneficial effect is: because of coal seam is covered outside a straw, increase the heat resistance of the whole burning effect.
NOVELTY - The device has a bioreactor for obtaining biogas. A supply conduit introduces the biogas in a bubble type mixing unit arranged in a bottom part of the bioreactor. The conduit includes a gas distributor with evenly arranged openings and a vertical spiral pipe bent in form of a cone and directed downward by a base.    USE - Device for obtaining biogas during anaerobic digest of organic waste.
NOVELTY - The method involves performing anaerobic and aerobic processes. Citric acid bacillus CYtroAacter StrainY9 liquid is added to di-potassium hydrogen phosphate according to volume ratio. Sodium citrate is mixed with a liquid culture medium that is heated at 10-30 degrees Celsius under an enriched culture condition. Tetravalent selenium i.e. receptor is added into sewage. 10 mmol/L of the sodium citrate is added to the sewage. Biochemical process is performed under 10-26 degrees Celsius. Citric acid bacillus is added to the sodium citrate. Tetravalent removing rate is calculated.    USE - Citrobacter containing tetravalent selenium sewage purification method.    ADVANTAGE - The method enables realizing simple process, convenient operation, low purification cost, environment-friendly effect and wide range of application.
NOVELTY - A bioorganic fertilizer is processed by crushing corn straw into 200 mesh, filtering, removing large granule impurity, taking 40 pts. wt. manure, 12 pts. wt. maggot, 2 pts. wt. ammonium citrate, 18 pts. wt. plant ash, 8 pts. wt. soybean, 20 pts. wt. corn straw and 26 pts. wt. canal mud, mixing uniformly, treating at 120 degrees C, cooling to room temperature, adding 1 pt. wt. strain, compost fermenting for 10-15 days, mixing uniformly, continuously compost fermenting for 15-20 days, spread drying, crushing, and packing.    USE - Method for processing bioorganic fertilizer (claimed).    ADVANTAGE - The method increases fertilizer nutrient, contains material that fully carries out fermentation, and promotes fermentation.
NOVELTY - An organic fertilizer bidirectional side turning machine comprises box body (1), turning main shaft (2), rotating shaft (4), spiral stirring blade (3), lifting belt (5), two exclusion material plate outlet, guide shaft, tension wheel, lateral conveying belt and front material input window.    USE - Organic fertilizer bidirectional side turning machine.    ADVANTAGE - The machine improves working efficiency and realizes fertilizer without resistance.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of organic fertilizer bidirectional side turning machine.    Box body (1)    Turning main shaft (2)    Spiral stirring blade (3)    Rotating shaft (4)    Lifting belt (5)
NOVELTY - Separation of lignin from garden waste comprises crushing garden waste into 100 mesh powder, mixing with water, stirring, cooking to 80-100 degrees C for 30-60 minutes, filtering, washing residue with water, and naturally drying; and mixing with mixed ethanol-water, cooking to 160-180 degrees C for 60-120 minutes, filtering, heating filtrate to remove moisture, and naturally drying.    USE - Method for separation of lignin from garden waste (claimed).    ADVANTAGE - The method is simple, uses simple device, effectively separates lignin, achieves high purity, solves difficult degradation and recycling of garden waste problem, and improves utilization of biomass resource.
NOVELTY - The device has a heat exchanger (14) connected with a gas purification system and a spiral feeder (1). An electronic gasification furnace (17) is mounted in an inner cylinder (2). A gas outlet of the electronic gasification furnace is connected with an outlet spraying device (3), a forced cooling spray system (4), a cyclone water removing device (5), the heat exchanger and an annealing furnace (11). The electronic gasification furnace is fixed with a temperature control system through a program controller. The forced cooling spray system is fixed in an air cooler.    USE - Annealing furnace biomass gas gasification device.    ADVANTAGE - The device ensures rapid gas cooling effect, reaches normal temperature state of a gas purification system quickly and avoids tar and water in gas. The device ensures better gas quality and heating rate of an annealing furnace, increases gas running efficiency of the gasification furnace, and reduces labor intensity.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic diagram of an annealing furnace biomass gas gasification device.    Spiral feeder (1)    Inner cylinder (2)    Outlet spraying device (3)    Forced cooling spray system (4)    Cyclone water removing device (5)    Annealing furnace (11)    Heat exchanger (14)    Electronic gasification furnace (17)
NOVELTY - The device has an air cooler (6) connected with a wood tar collection unit. A releasing valve (13) and a gas valve (14) are located between the air cooler and a gas-liquid separator (15), respectively. The gas-liquid separator is located with the wood tar collection unit. A burner (16) is fixed with an end of a boiler (17) and the wood tar collection unit by a coke-discharging pipe (23). A collection tank (7) is provided with a heater (8), a liquid level scale plate (9), a pointer (10) and a floating ball (11). The gas-liquid separator is connected with the wood tar collection unit.    USE - Biomass gasification cogeneration device.    ADVANTAGE - The device achieves better air cooler pneumatic pre-heating effect, improves heat efficiency of biomass gasification furnace with low water charcoal, reduces energy consumption for the drying process and improves wood tar yield with high economic value, and has better heat preservation and fluidity effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification cogeneration method.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional block view of a biomass gasification cogeneration device.'(Drawing includes non-English language text)'    Air cooler (6)    Collection tank (7)    Heater (8)    Liquid level scale plate (9)    Pointer (10)    Floating ball (11)    Releasing valve (13)    Gas valve (14)    Gas-liquid separator (15)    Burner (16)    Boiler (17)    Coke-discharging pipe (23)
NOVELTY - Extracting sugar involves subjecting lignocellulosic material, alkali, enzymes, and water to reactor, which operate continuously. The mass flow of lignocellulosic material, alkali, enzymes and water ratio, are regulated by maintaining pH in the reactor between 2-7. The enzymatic reaction in the reactor is performed at 20-80 degrees C for 8-120 hours, followed by continuous addition of sugar solution into reactor from the provided outlet. The hydrolyzed sugar extracted from the lignocellulosic material, is then collected as the product.    USE - Method for extracting sugar from lignocellulosic material (claimed).
NOVELTY - A biofuel is produced by extracting sap of a plant (100), making the sucrose contained in the sap react with a sucrase, and decomposing into glucose and fructose.    USE - Production of biofuel (claimed).    ADVANTAGE - Biofuel is produced easily and semipermanently depends on sunlight using photosynthetic reaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a biofuel production unit (1) comprising electrode in which enzyme exists in surface, collection needle (11) with which plant pierces in order to collect the sap of plant (100), and sampling container (13) which accommodates the sucrase that reacts with sucrose of sap extract and decomposes into glucose and fructose.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biofuel production unit. (Drawing includes non-English language text).    Biofuel production unit (1)    Collection needle (11)    Tube (12)    Sampling container (13)    Holder (14)    Plant (100)
NOVELTY - The method involves splitting olefin message. Hydrogenation and deoxygenation are performed on a catalyst. Metal of platinum group is applied on a mesoporous carbonic carrier sub-unit. Selective oxidation splitting of dual communication is controlled with dibasic drying carbonaceous acids with length of carbonaceous chain by micro-alga mono-unsaturated fatty acids, where source of fatty acids is a biomass of micro-alga, and composition of hydrocarbon biodiesel together with linear long-chain hydrocarbons is obtained.    USE - Method for obtaining diesel fuel from micro-alga.
NOVELTY - The apparatus (1) has a burner (2) that is installed in cylindrical combustion chamber (3) along cylindrical-axle core direction. Modification catalyst filled layer (4), conversion catalyst filled layer (5) and selective-oxidation catalyst filled layer (6) are installed in outer periphery of combustion chamber from lower-stage side. First adsorption agent filled layer (25) is positioned adjacent to gas flow path which leads to conversion catalyst layer from modification-catalyst filled layer. Second adsorption agent filled layer (27) is positioned in outer periphery of filled layer (5).    USE - Hydrogen generating apparatus installed in circumference of transformer.    ADVANTAGE - The first adsorption agent and second adsorption agent are maintained at appropriate temperature, so that adsorption capacity of the hydrogen sulfide by the hydrodesulfurization device is improved. The temperature of hydrogenation catalyst and adsorption agent is optimized, so that amount of hydrodesulfurization catalyst mounting is reduced. Thus, compactization of the hydrodesulfurization device is achieved. The manufacturing cost of the hydrogen generating apparatus is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a longitudinal cross-sectional view of the hydrogen generating apparatus. (Drawing includes non-English language text)    Hydrogen generating apparatus (1)    Burner (2)    Cylindrical combustion chamber (3)    Modification catalyst filled layer (4)    Conversion catalyst filled layer (5)    Selective-oxidation catalyst filled layer (6)    First adsorption agent filled layer (25)    Second adsorption agent filled layer (27)
NOVELTY - The method involves making the woody raw material (M) finer from extrusion hole (22) of first mold (24). The primary raw material (E) is supplied from second extrusion machine (38). The heating jacket (34) is operated based on temperature of raw material obtained by second temperature sensor (44), and the temperature of raw material is adjusted to predetermined 80-170 degrees centigrade. The raw material is extruded as a solid rod-shaped article (S) from many extrusion holes of second mold (46). The solid rod-shaped article on a pellet (P) is cut by a cutting device (42).    USE - Method for manufacturing wood pellet.    ADVANTAGE - The manufacturing method of the wood pellet does not require the drying process of a woody raw material in advance. A wood pellet can be manufactured by cutting a solid rod-shaped article on the pellet of desired length by a cutting device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side surface sectional view of first extrusion machine and second extrusion machine.    Extrusion hole (22)    First mold (24)    Heating jacket (34)    Second extrusion machine (38)    Cutting device (42)    Second temperature sensor (44)    Second mold (46)    Primary raw material (E)    Woody raw material (M)    Pellet (P)    Solid rod-shaped article (S)
NOVELTY - Manufacture of sulfonyl chloride compound (I) or (II) involves oxidizing thiol (III) and disulfide (IV) in the presence of oxidizing agent, and obtaining sulfonyl chloride compound. The oxidizing agent is sodium hypochlorite. The pH of the reaction system is controlled to 7 or less by reacting with an acid or a neutral substance.    USE - Manufacture of sulfonyl chloride compound used as functional material and intermediate material for pharmaceuticals and agrochemicals.    ADVANTAGE - The method enables efficient manufacture of sulfonyl chloride compound, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - Manufacture of sulfonyl chloride compound of formula: R1-SO2Cl (I) or R2-SO2Cl (II) involves oxidizing thiol of formula: R1-SH (III) and disulfide of formula: R1-S-S-R2 (IV) in the presence of oxidizing agent, and obtaining sulfonyl chloride compound. The oxidizing agent is sodium hypochlorite. The pH of the reaction system is controlled to 7 or less by reacting with an acid or a neutral substance.    R1,R2=organic group which does not react with sodium hypochlorite.
NOVELTY - This utility model claims a device for wood processing into a sterile biological granule, wood chips grain pressure device and sterilizing device, the housing inside a pressure material c, in a housing front part connected is provided wherein a pressure material feeding lumen, a housing lower side part is provided connected pressure material c. discharge wherein the housing has top hydraulic cylinder of the hydraulic pressure pole entering into a hole, has a ridge type pressing plate is in a stick pressing material c in front end part of the fluidization bed is circulation fluidization bed, sterilizing pneuma and supplying a source entrance connected, an air supply outlet and a circulation fluidization bed air flow under entrance connected. This a dust processing device into a sterile biological granule, using a wooden meal grain pressure device only has one of a jar, structure is simple, operation is easy, product manufacturing cost low, the weight is light, operation program, production efficiency without reducing the use of sterilizing device, can well removing bacteria is a biological granule, provide the one a sterile biological granule.
NOVELTY - This utility new type claims a biomass high then A l, composed of a feed comprising a furnace body and a furnace body, wherein the furnace body side wall provided with a wood coal outlet and a wood coal outlet under the bottom set with ash room, ash room provided with a reverse turning bed ash discharge furnace disk, the bottom ash room provided with rows of carbon wherein the lower furnace body is set with ash discharging motor mechanism, ash power mechanism has in a hollow rotating tube, rotating pipe lower end set with a inner box, the vertical upper end provided with multiple blade and set with a ash room, reverse turning bed ash discharge furnace disk by connecting rod set at upper end of blade side rotating pipe has a set with a plurality of through hole set at upper centre of inner furnace body, a centre oxygen inlet hose, a furnace body set with several outside wall oxygen inlet pipe. This utility new type can greatly increase wood coal conversion efficiency and burning speed, further through interaction mechanism, which not only is convenient to clean, but also for the furnace body inner air supply process, compact structure.
NOVELTY - This utility new type claims a biomass gasification, a furnace body comprises a high pressure air blower, the bottom furnace body set with water pool, water pool provided with inner chain plate, the side set with feeding pipe, feeding pipe end part provided with a feeding auger, a high pressure air blower has a cloth, cloth air tank by blowing radiating pipe connected to the feeding inner tube, a cloth wind box set with connecting to multi-blowing pipe of pool side is located on a secondary supplement blowing pipe chain furnace disk of the lower part, the furnace body side provided with fire, has a inner furnace burner. This utility new type comprises gasification and combustion efficiency is high and maintenance is convenient.
NOVELTY - This new utility model claims of one of biomass grain fuel production equipment, including feedstock screening device, air moving iron remove device, a cyclone separating device, a storage stirring device, spiral transport device, granulating device, discharge processing device and the transport air pipe; said feedstock filter device by the transporting air pipe connected with the cyclone separating device, of the transport air pipe mounted with the air moving iron remove device, the cyclone separating device and the material stirring device connected with, the material stirring device mounted with spiral transporting device; the spiral transporting device and the granulating device connected with, on the granulation device installed with the discharge processing device, the processing device and the discharge filter device connected with feedstock. This utility new type reasonable structure, production efficiency high, grain fuel forming is good, can consume low, production process of producing dust.
NOVELTY - The firewood has a single block (1) whose end is connected with a single incision longitudinal section (2). The single incision longitudinal section is fixed on a front panel of a shoe. A timber is divided into two sections (3,4). Another end of the single block is connected with a uniform section (7). Cross sections of the uniform section are connected by using a pile.    USE - Firewood.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional perspective view of a firewood.    Single block (1)    Single incision longitudinal section (2)    Sections (3,4)    Uniform section (7)
NOVELTY - The method involves supplying the oxidizing composition to a biomass fuel and heating over 290 degrees C to manufacture the synthetic gas. The oxidizing composition is comprised of steam of air of 1.24-1.5 Nm3 of per kg of biomass fuel.    USE - Method for manufacturing synthetic gas such as ethanol or methanol from biomass using the microorganism.    ADVANTAGE - The hydrogen concentration and calorific value of the synthetic gas are improved by using the biomass gasifier. The amount of tar generation is reduced. The efficiency of the gasifier is improved since the oxidizing composition is heated up using the sensible heat of the synthetic gas without need of external heat source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a gasifier of biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the feeding system of oxidizing agent, biomass and synthetic gas in gasifier. (Drawing includes non-English language text)    Biomass gasifier (1)    Heat exchanger (2)    Column switch (3)    Screw conveyor (4)    Coke weighing hopper (5)
NOVELTY - Recovering a volatile organic compound from a biomass material comprising: introducing a prepared biomass material comprising at least one volatile organic compound to a compartment of a recovery system; contacting the biomass material with a super-heated vapor stream to remove the volatile organic compound; recovering the removed volatile organic compound to provide the vapor component; retaining the vapor component as the superheated vapor stream; and releasing the prepared biomass material from the compartment after removal of volatile organic compound to provide the solid component.    USE - The method is useful for recovering volatile organic compound e.g., ethanol from a biomass material.    ADVANTAGE - The method is more economical in recovering volatile organic compounds from a biomass material.
NOVELTY - Method for fermenting sugars derived from plant material into a fermentation product using a fermenting organism, where lipoic acid, lipoate and/or lipoamide, or their blends are present or added before and/or during fermentation.    USE - The method is useful for fermenting sugars derived from plant material into a fermentation product, chosen from alcohol, preferably ethanol, fuel ethanol, potable ethanol and/or industrial ethanol (all claimed).    ADVANTAGE - The method boosts fermentation yield compared to fermentation where no lipoic acid/lipoate and lipoamide is present and/or added.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process for producing a fermentation product from starch-containing material; and    (2) composition.
NOVELTY - Methanol-based diesel fuel comprises at least 50 wt.% methanol, and 0.1-10 wt.% ignition improver that is a methanol soluble alkylene oxide adduct of glycerol.    USE - The fuel is useful for operating diesel engine (claimed).    ADVANTAGE - The fuel shortens the ignition delay time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use of a methanol soluble alkylene oxide adduct glycerol as an ignition improver for a methanol-based diesel fuel.
NOVELTY - The apparatus has a distribute load tub (10) for storing an organic waste of a processing object. An anaerobic digester (20) is provided with the organic waste to perform an anaerobic digestion process. An anaerobic digester effluent reservoir (30) stores effluent that is flowed out from the anaerobic digester. The distribute load tub is provided with a concentrate that is concentrated in a microorganism concentration device (40). Multiple nitrogen control tanks (60, 70, 80) supply nitrogen-free water among stabilization liquid that is flowed out from a stabilization bath (50).    USE - Anaerobic absorption apparatus for processing organic waste. Uses include but are not limited to food waste, masking number waste, livestock excretion waste and sewage sludge waste.    ADVANTAGE - The apparatus regularly maintains nitrogen concentration at the anaerobic digester so as to provide solid concentration in an effective manner. The apparatus supplies the nitrogen-free water to the anaerobic digester through the nitrogen control tanks so as to control nitrogen concentration and solid concentration in an efficient manner, so that operation of the digestion tank is steadily maintained and effectiveness of long-term operation process can be improved. The apparatus enhances operation efficiency by increasing bio gas production efficiency, so that stability of digested sludge effluent supernatant water quality is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an anaerobic absorption apparatus.    Distribute load tub (10)    Anaerobic digester (20)    Anaerobic digester effluent reservoir (30)    Microorganism concentration device (40)    Stabilization bath (50)    Nitrogen control tanks (60, 70, 80)    Organic carbon source reservoir (110)
NOVELTY - Solid lignocellulosic fuel composition comprises lignocellulosic syrup and at least one additional fuel component consisting of coal fines, where the lignocellulosic syrup is the product of a process for the production of ethanol from lignocellulosic biomass.    USE - Used as solid lignocellulosic fuel composition.    ADVANTAGE - The composition is in a form that is readily handled and transported, has much reduced dusting during handling, transport, and storage as compared to the additional fuel components alone, has reduced tendency to bridge and reduce flow out of a hopper, and is burned in any appropriate burning furnace such as a steam boiler, hot water boiler, process furnace, or other industrial or commercial combustion process with suitable emissions controls.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for production of solid lignocellulosic fuel composition comprising mixing lignocellulosic syrup composition with at least one additional fuel component consisting of coal fines.
NOVELTY - The method involves hydrophilically treating the tantalum substrate surface or the tantalum membrane surface on a substrate. A flux aqueous solution or a paste is coated to the substrate surface or the membrane surface. The substrate including the coated surface is heated in nitrogen source containing atmosphere. The Ta3N5 crystalline layer is subsequently formed on the substrate by cooling process. The tantalum membrane is formed by a sputtering method on a metal or the substrate of ceramics.    USE - Method of manufacturing tantalum nitride.    ADVANTAGE - The crystalline favorable tantalum-nitride crystalline layer is obtained efficiently in single step process.    DETAILED DESCRIPTION - The hydrophilization treatment is performed in ultraviolet irradiation or plasma exposure. The flux aqueous solution or paste is the aqueous solution or paste containing alkali carbonate. The nitrogen source containing atmosphere is formed with ammonia airflow. The nitrogen source containing atmosphere is heated at 600-1000 degrees C. The obtained tantalum nitride is formed in columnar shape or plate crystal. At least 80 % or more columnar crystal is oriented in the direction of 45 to 90 degree to the substrate. The tantalum-nitride crystalline layer is formed in the substrate surface. The visible light response photoelectrode is consisted of substrate/tantalum-nitride crystalline layer. Visible light is irradiated to the visible light response photo electrode, and hydrogen is obtained by performing photocatalytic degradation of water.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the scanning electron microscope image indicating the tantalum-nitride crystalline layer produced on the tantalum substrate. (Drawing includes non-English language text)
NOVELTY - Dielectric barrier discharge plasma reactor comprises a non-conductive material that is coated on outer side of a tank. A liquid is filled in the tank, where the amount of liquid is 10- 80% of the tank volume. An electrode is provided, where the top part of electrode touches the upper surface of the liquid.    USE - Dielectric barrier discharge plasma reactor used for pretreatment of biomass, surgical material and for wastewater treatment.    ADVANTAGE - The dielectric barrier discharge plasma reactor enables to increase the pH of the water for effluent treatment, removes lignin from biomass, enables the increase of the water temperature and allows the concentration of ionized species.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for deconstructing biomass, which involves putting the biomass to be treated in the reactor, covering the biomass with water, closing the reactor and generating electric current in the reactor through metal wires at constant temperature and constant pressure.
NOVELTY - The method involves removing and pre-pressing moisture. Binders or organic or inorganic products, flammable or inert products are routed in a mixer. Biomass is added with mud at a calorific value. Dosage of raw materials and mixtures varies between 0.1-99.9%. A resulting sludge of sanitary sewer is provided into a combustion chamber, where the sludge is burnt in dry form. Flammable gases are utilized for producing energy. A compressed product is produced with a certain calorific value. The compressed product is transported during burning or incineration process.    USE - Method for obtaining thermal and electrical energy from fuel briquette sludge of a sewage bowl for use in a power plant and a boiler (all claimed). Can also be used for a home, a commercial place and an industrial place.    ADVANTAGE - The method enables obtaining thermal and electrical energy in an environmentally friendly manner and utilizing renewable power sources and reutilizing organic and inorganic residues, so as to avoid pollutions in an effective manner.
NOVELTY - The invention relates to a multifunction equipment for bituminous briquetting consisting of several modules of a whole manufacturing chain controlled by a computerized control system so that the resulting briquettes satisfy the requirements for use, the starting material employed for briquetting consisting in wheat straws, wooden dust, maize stalks, vine shoots or other vegetable matters. The equipment, as claimed by the invention, consists of a shredder which grinds the starting material, some silos storing each kind of starting material from which the optimal briquette recipe is prepared using an automatic dosing system, a dryer, a steam mixer, a press feeding system provided with a worm conveyer for transporting the starting material, a pressing machine with a worm device, a briquette guiding and cooling line and an automatic briquette delivering module, the briquetting machine being provided with a precompression module with a conical worm device (1), a precompression chamber (2) which can move axially using a guiding support (3) ensuring the required precompression density, a gearmotor (4) for driving purposes, a worm device (6) pushing the precompressed biomass into a compression module (5) which is driven into rotation by a motor (7), using a belt transmission (8).
NOVELTY - The method involves utilizing a reactor (1) for decontaminating biological sludge, where the reactor is provided with a desiccant density solid and utilized for releasing water by reaction with organo-bioactive minerals. A system is utilized for washing water and removing a cake fertilizer. The system is utilized for drying the cake fertilizer. A raw sludge is produced between 1% and 5% of solids and 70% and 30% of organic solids. Biodigestion sludge is produced by production of biogas and liquid biofertilizer.    USE - Method for chemically recycling sludge of a treatment station of an urban sewage for use as biogas or fuel in an internal combustion engine.    ADVANTAGE - The method enables limiting growth of sludge of the treatment station of the urban sewage in an environment friendly manner. The method enables increasing efficiency of the dewatering system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a method for chemically recycling sludge of a treatment station.    Reactor (1)    Urban system (2)    Dosage system (3)    Fertilizer liquid reactor (4)    Flocculator (5)
NOVELTY - An ethanol is manufactured by fermenting paper manufacture waste material using fungi which belong to Zygomycota, Zygomycetes and Mucorales.    USE - Manufacture of ethanol used as biofuel.    ADVANTAGE - Enzyme addition amount required for fermentation process is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of the ethanol production from paper sludge by simultaneous saccharification fermentation system which combined Mucor circinelloides and cellulase cocktail agent pre-processed.
NOVELTY - Method for producing ethanol, involves contacting filamentous fungi chosen from Absidia, Backusella, and Gongronella with wood type biomass or its hydrolyzate.    USE - The method is useful for producing ethanol (claimed) which is used as biofuel.    ADVANTAGE - The method produces ethanol cost-effectively without additives.
NOVELTY - A solid fuel is obtained by baking wood-type biomass and has a chlorine content of 0.002% or less.    USE - Solid fuel is used for combustion facilities e.g. powdered coal boilers. Can also be used for power generation equipment and incineration systems.    ADVANTAGE - The solid fuel has low chlorine content, grindability equivalent to coal, and high calorific value and density (which enables easy mixing with coal), and can be manufactured efficiently with high yield, without requiring any special washing process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid fuel, involves baking wood-type biomass at a furnace temperature of 250-500 degrees C in an oxygen concentration of 10% or less.
NOVELTY - Manufacture of hydrocarbon from cellulose biomass involves hydrolyzing and saccharifying cellulose biomass, obtaining saccharides, and hydrocracking sugar alcohol obtained by hydrogenating saccharides. The preparation of saccharides and hydrocracking of sugar alcohol are carried out in presence of iridium-rhenium-type-catalyst.    USE - Manufacture of hydrocarbon e.g. hexane and pentane (claimed) used as fuel base material from cellulose biomass e.g. cellulose and wood powder.    ADVANTAGE - The method enables manufacture of hydrocarbon from cellulose biomass with high yield.
NOVELTY - The system has a unilateral external tank (1) provided with an electrolyte inlet and connected with an internal tank with sensors e.g. temperature sensors or pressure sensors. A reactor (4) is provided with a set of encapsulated cells. A filter and an oscillator (3) are arranged in a casing. Internal ducts in the internal tank are directly and vertically connected to the reactor. The external tank is provided with an automated pump and a valve. The reactor is connected with plates in parallel.    USE - Hydrogen and oxygen gas generation system for an internal combustion engine of a vehicle.    ADVANTAGE - The system reduces consumption of carbon monoxide emissions in internal combustion engines and avoids explosion of gases near a reactor. The inlet ducts are provided with an inlet air filter that can prevent entry of dust and water into the system. The oscillator allows power supply within certain voltages and currents for protecting an electrical system of a vehicle from being damaged.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a hydrogen and oxygen gas generation system. '(Drawing includes non-English language text)'    Unilateral external tank (1)    Battery (2)    Oscillator (3)    Reactor (4)    Motor (5)
NOVELTY - The method involves feeding biomass raw material to catalyst solution. Water content and catalyst are provided in oxygen limited atmosphere at 100-180 degrees Celsius. Temperature is maintained for 1-2 hours in oxygen atmosphere at 10-50 degrees Celsius/min. Residual solid substance is cooled to obtain biological carbon.    USE - High yield biological carbon preparation method.    ADVANTAGE - The method enables saving energy and providing high porosity.
NOVELTY - The device has a shell (10) provided with a condensing chamber that is connected with a condensing tube (4). The condensing pipe is provided with a spiral scraper (1). The shell is provided with a gas inlet (7) and a clean gas outlet (8). The condensing chamber is provided with a condensed water inlet pipe (2) and a return pipe (3). A driving device comprises a gear transmission device (5) and a motor (6). The motor drives the gear transmission device to drive the spiral scraper for rotating.    USE - Biomass combustible gas tar condensing separating device.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass combustible gas tar condensing separating device.    Spiral scraper (1)    Condensed water inlet pipe (2)    Return pipe (3)    Condensing tube (4)    Gear transmission device (5)    Motor (6)    Gas inlet (7)    Clean gas outlet (8)    Shell (10)
NOVELTY - The pool has a discharging vertical pipe connected with a fermentation pipeline along a fermenting pipe center axis. The fermenting pipeline is connected with a gas-guide tube. A feeding pipe is inserted into a biogas fermentation liquid face. A feeding pipe side wall is connected with a discharging pipe side wall at an interval. A guide pipe is connected with a valve body.    USE - Dual-cylinder binding straw marsh gas pool.    ADVANTAGE - The pool has reasonable structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a dual-cylinder binding straw marsh gas pool.
NOVELTY - The reactor has a liquid storage room arranged in a reactor main body. A lower part of a liquid storage chamber is connected with a triangular prism right-angle triangular structure. A solid liquid separating device is connected with a biogas outlet in the liquid storage chamber. A filler storage tank main body is connected with a fermentation room and a liquid storage room. A biogas slurry reflowing device is connected with a liquid exit, the fermentation room and the liquid storage room through a liquid entrance. An outside wall of the fermentation room is connected with a supporting plate.    USE - Box-type anaerobic dry fermentation reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a box-type Anaerobic dry fermentation reactor.
NOVELTY - Serratia marcescens A5, with the preservation number CGMCC No.9621, is new.    USE - The Serratia marcescens A5 is useful for preparing biodegradable agent for degrading degreased food waste or anaerobic fermentation of vegetable oil wastewater (all claimed).    ADVANTAGE - The strain improves anaerobic fermentation and hydrolysis of food waste, and biogas production efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) use of Serratia marcescens A5 for preparing biodegradable agent; and (2) use method of the biodegradable agent, comprising taking biodegradable agent containing 109 cell/ml Serratia marcescens A5, and inoculating into 5-20 vol.% biodegradable agent into food waste fermentation broth or wastewater.
NOVELTY - The device has a vibration plate (2) connected with a driving mechanism (3). Multiple electrode plate clamping slots (21) are formed with a lower side of the vibration plate. A side of an s Z-shaped multi-electrode plate is inserted in the plate clamping slot. An end part of permanent magnet (31) is fixed with a water electrolytic groove main body (1). The permanent magnet is fixed with an electromagnet. Each electrode plate is connected an inner part of the water electrolytic groove main body.    USE - Oxygen/hydrogen mixed gas generator plate vibration device.    ADVANTAGE - The device increases vibration effect of the electrode plate in a water electrolysis cell, and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a oxygen/hydrogen mixed gas generator plate vibration device.    Water electrolytic groove main body (1)    Vibration plate (2)    Driving mechanism (3)    Electrode plate clamping slots (21)    Permanent magnet (31)
NOVELTY - The structure has a water electrolytic groove main body (10) for containing electrolyte. An upper end surface of an electrode plate (20) is arranged with a connection part (201) and a bending part. An inner surface of the electrode plate is formed with a groove part (101). The electrode plate is mounted in an inner surface of the water electrolytic groove main body according to positive and negative polarities. The electrode plate is formed with multiple through-holes (203). A detachable cover plate (30) is fixed with a middle air outlet (301).    USE - Water electrolysis groove structure for an oxygen/hydrogen mixed gas generator.    ADVANTAGE - The structure can increase oxygen hydrogen mixing gas generating quantity.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of a water electrolysis groove structure.    Water electrolytic groove main body (10)    Electrode plate (20)    Detachable cover plate (30)    Groove part (101)    Connection part (201)    Through holes (203)    Middle air outlet (301)
NOVELTY - The device has a water electrolytic groove main body (11) connected to a power supply plate (12), a straight flow electric control unit (22), a direct current electric output unit (21) and a monitoring and feedback unit (23). A microprocessor (25) controls the direct current electric control unit, monitoring and feedback unit, and the ultrasonic wave control unit. An ultrasonic vibration mechanism (3) comprises an ultrasonic wave control unit (24). An ultrasonic wave generator (31) is mounted with the water electrolytic groove main body and an ultrasonic vibrator (32).    USE - Water electrolytic groove device.    ADVANTAGE - The device is more convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an water electrolytic groove device. '(Drawing includes non-English language text)'    Ultrasonic vibration mechanism (3)    Electrolytic groove main body (11)    Power supply plate (12)    Direct current electric output unit (21)    Straight flow electric control unit (22)    Monitoring and feedback unit (23)    Ultrasonic wave control unit (24)    Microprocessor (25)    Ultrasonic wave generator (31)    Ultrasonic vibrator (32)
NOVELTY - This utility new type provide the one a two level sludge drying system, comprising pre-processor pre-processor connection has conveying sludge inlet of sludge pump, pre-treating and Anaerobic fermentation tank outlet is connected, after Anaerobic fermentation tank gas outlet of biogas tank and a gas inlet connected, pneuma outlet and waste heat boiler of combustion engine connected, sludge outlet of Anaerobic fermentation tank through dewatering machine and a drying machine of sludge level connected with the inlet, a level drying machine of sludge outlet and second level drying machine of sludge inlet is connected, in a dryer set level used for crushing sludge, waste heat boiler through heat supply pipe a and a level, a level drying machine connected with a dryer heat supply source and reduces the sludge treatment plant for a power grid electric power requirement, outside row has peculiar smell gas, energy-saving safe; a two level for carrying out drying dewatered sludge, set in the first level crusher dryer inner, sludge group for carrying out in crushing, effective increase the drying speed, drying speed is fast, it saves space.
NOVELTY - This utility new type claims a biomass pressure conversion device A, two part this device comprises steam device happen reaction room and one, through a device, for each of a control component, a water vapour atmosphere under a pressure a biomass conversion process of experiment research, it can for heating rate, final temperature, heat preservation time, reaction pressure equal factor for biomass pyrolysis process of influence developing research work, accelerate research of a biomass conversion process, a large scale use of biomass energy establishes a certain.
NOVELTY - This new utility model claims of one of biomass heat conversion device, the device comprises oil bath sleeve, kettle body, stirrer, high pressure steam generator, tank cover, data collection mchine, vacuum pump, stirrer, may program controller and each valve series pipeline one, through the different valve open and closed, can realize biomass pressure, more pressure pyrolysis and vacuum pyrolysis equal of more complex process. This new utility model compared with the existing technology has the following advantages: the device full considering of different biomass heat conversion process of needed condition, can realize biomass pressure, more pressure pyrolysis and vacuum pyrolysis equal of more complex technique, the diversity of the biomass product, at the same time for searching the best biomass heat conversion process, increase use efficiency of the device.
NOVELTY - The microorganism carrier has a cage whose one end is opened with a network cover and is covered with a network cylinder. The cage is provided with a carrier material upper layer (4) made of resin, fiber and metal material, and a filter material lower layer (5) made of clay, lime, kaolin, diatomite and zeolite. The specific gravity of the filter material lower layer is larger than carrier material upper layer. The density of lower layer carrier material is less than the height of network cylinder.    USE - Microorganism carrier used for sewage treatment field.    ADVANTAGE - Since the carrier material affinity is small, the fall off of the microorganism carrier is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the microorganism carrier.    Carrier material upper layer (4)    Filter material lower layer (5)
NOVELTY - A system (10) for converting biomass to biocrude comprises a hydrothermal liquefaction (HTL) reactor configured for converting biomass slurry to biocrude; and a generator (17) configured for using a portion of thermal energy from combusted biogas for generating electrical energy, where the generated electrical energy and any remaining thermal energy from the biogas combustion are provided to the HTL reactor for heating the biomass slurry.    USE - The system and method are used for converting biomass to biocrude (claimed).    ADVANTAGE - The system allows for use of a variety of biomass and/or biowaste feedstocks in the process, including municipal biosolids, food waste, animal waste, grease waste, cellulosic waste, as well as microalgae. This facilitates recycling of waste materials that may have otherwise been subject to disposal in a land-fill. Advantages of the implementations of the systems and methods above include: (1) continuous flow, (2) comparatively high biomass-to-biocrude yields, (3) nearly free energy input capable of generating a positive energy return on investment (EROI) for the process, (4) recycling of organic waste materials to renewable biocrude, (4) energy self-sufficiency, (5) use of a reliable biowaste feedstock that is low cost and is likely to increase in amount over time with growing populations, (6) the ability to implement the system in developed and under-developed countries, (7) applicability to a wide variety of biomass feedstocks, and (8) easily scalable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process of converting biomass to biocrude.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of an HTL system.    System (10)    HTL system (12)    Solar thermal energy concentrating mechanism (14)    Electricity Generator (17)
NOVELTY - Primary fuel catalyst for combusting a secondary fuel, comprises gases produced by water electrolysis.    USE - The primary fuel catalyst is useful for combusting a secondary fuel (claimed).    ADVANTAGE - The primary fuel catalyst is capable of transmuting the radioactive elements of the secondary fuel into lighter elements having shorter half-lives and then to stable daughter products, thus reducing the long-term toxicity of secondary fuel (claimed) in an economic and effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for creating a fuel rod, comprising: drying and pulverizing a radioactive or bio-hazardous material; blending the dried pulverized radioactive or bio-hazardous material with aluminum and iron oxide (thermite blend) in 1:1 ratio; binding the dried pulverized radioactive or bio-hazardous material/thermite blend together using a small amount of water and a liquid binder, where the ratio of water and binder is 1:1; mixing 1 part water/binder with 4 parts of the dried pulverized radioactive or bio-hazardous material/thermite blend; and drying the mixture.
NOVELTY - Biofuel clumps or particles are prepared by grinding wheat straws, corn stalks, corn cobs, soybean straws, rice straws, reed sticks, wood dusts, wood blocks, branches, leaves, shells, pomace, bagasse, sunflower stalks, hay, bran, wheat bran and waste paper and heating the ground materials at high pressure.    USE - As biofuel clumps or particles.    ADVANTAGE - The biofuel clumps or particles are easy to store or transport, and has excellent standard coal combustion value of 7000 Kcal.
NOVELTY - This utility new type claims a biomass gas is a purification device, comprising mutually through pipeline connected between a dust sedimentation tank and gas fractionation tower, dust settling tank is rectangular box body, the one side set with the first air inlet, and the other side set with the first air outlet, the first air inlet is higher than the first air outlet between the inner wall and outside wall of dust sedimentation tank set with cooling layer, inner cooling layer set with continuous circulation of cooling water, gas fractionating tower is cylindrical and set with mutually connected a two layer, a first layer and a second layer, the first layer is set with second air inlet side, the side of second layer set with second air outlet, the second air inlet and the first air outlet wherein a, the first layer and second layer are set with chemical filler c, second layer of top part set with cooling water. This utility new type is a a biomass gas purification device of the biomass gas purification effect is good, and the structure is simple and easy to carry out and purification cost is low.
NOVELTY - A channel of this utility new type claims a biomass fuel delivery channel cleaning device, comprising machine frame and a transmission device set on a machine frame, and a inclined upper machine frame is set with a connection set at inclined upper wall of inner channel of a conveyor, the conveyor through a driving wheel and a driven wheel drives running in a machine frame, a driving wheel is set on upper part of a channel and the output end of a driving device connected and driven wheel is set at the bottom of the conveying channel, the conveyor set with a cleaning belt, a cleaning belt rear end connected at upper surface of a conveyor, the front end of cleaning with a free end, the cleaning with a length greater than conveyor belt lower side part to inner delivery channel bottom wall a distance, the end of said cleaning belt set has several cloth strips. Several cleaning with a cleaning setting b conveyor holding conveying channel at the bottom of a clean, effective to avoid the deposition of raw material and improves the device operation efficiency and increase the production rate.
NOVELTY - The hopper (10A) carries out sequential fall from an outlet opening (17). The granular material (P) is scraped out in an outside hopper (12) from an inside hopper (11) by rotation of a rake (16) in the bottom face (14) of outside hopper. The outlet opening and one or several bridging release portions (20) which blow off gas towards the one or both of the peripheral portions are provided. The bridging release portions are installed in rake rotation direction upstream of outlet opening. The peripheral portion of outlet opening is equipped with rotary bridging release portion.    USE - Constant-feeding hopper of granular material supply apparatus (claimed) for storing granular material such as biomass of grass and tree.    ADVANTAGE - The constant-feeding hopper is provided for taking measures against bridging and provided to ensure a stable supply of granular material. The formation of bridging in constant-feeding hopper is eliminated. The fluctuation of granular material supply-amount supplied from constant-feeding hopper is prevented, and the continuation of supply of stable granular material by granular material supply apparatus is attained.    DESCRIPTION OF DRAWING(S) - The drawing shows the longitudinal cross-sectional view and cross-sectional view of the constant-feeding hopper. (Drawing includes non-English language text)    Constant-feeding hopper (10A)    Inside hopper (11)    Outside hopper (12)    Bottom face of outside hopper (14)    Rake (16)    Outlet opening (17)    Bridging release portion (20)
NOVELTY - Breeding vegetable seed comprises selection, seedbed preparation, germination and sowing, where the seedbed preparation process adopts non-toxic nutritive soil (prepared by baking and fermentation) as matrix.    USE - The method is useful for breeding vegetable seed (claimed).    ADVANTAGE - The method is simple, economical, non-toxic, does not pollute the environment and enhances seedling growth.
NOVELTY - The greenhouse cultivation method involves constructing ecological greenhouse set with ventilation system and cultivation pool, and spraying a mist in the greenhouse. A mixture of straw and cow dung fermentation is cultivated, and the fermented feed is put into the cultivation pool bottom. A 10000 to 15000 earthworm seedling is put in the cultivation pool with cultivation soil humidity of 20 to 70 percent and temperature of 15 to 25 degrees centigrade. A fog cultivation device is set with the cultivation pool at 30 to 40 centimeters.    USE - Greenhouse cultivation method for butterfly.    ADVANTAGE - Prevents epidemic disease, and increases the cultivation benefit of farmers.
NOVELTY - This new utility model claims of one of crop straw comprehensive harvester, comprising tractor, picking crushing device, rotary air flow separation chamber, forming machine set, gear gearbox and harvesting machine chassis, picking crushing device hanging frame in harvesting machine is connected with front part of chassis, harvesting machine chassis front end, a traction frame and a hook connected with tractor, in turn fixed with gear gearbox after harvesting machine chassis top front to, forming material packaging device and molding material storage box, wherein the feedstock discharge port and rotating air flow separation chamber and crushing device in the crushing material lifting fan, is connected with gear of gear box equipped with the first power output shaft and the second power output shaft, power input shaft and power output shaft and the first forming unit connected with the power output shaft and the second picking and crushing device and power input shaft connected with. This new utility model set picking and collecting, crushing, dust separation, and press molding is integrated, increase of work efficiency and processing quality, reducing of the operator number and equipment operation cost.
NOVELTY - Biosolid fuel comprises at least one waste chosen from food waste, coffee bean pulp, slaughterhouse sludge, sludge from processing unit, slaughterhouse impurities, impurities from processing unit, waste of fish and shellfish, animal carcasses, and animal feces.    USE - The biosolid fuel is useful as alternative fuel (claimed).    ADVANTAGE - The biosolid fuel utilizes industrial waste, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing biosolid fuel, involves using the above-mentioned waste.
NOVELTY - The two stage fluidized bed biomass gasifier (1000) comprises a flowing layer (100), in which the spreader plate (50,60) is formed between the aqueous gas reactive portion (40) and the gas supply unit (20). The aqueous gas reactive portion has a lean layer mostly made of gas with a catalyst layer, in which the aqueous gas catalyst exists. The synthetic gas reactive portion (30) reacts with the aqueous gas catalyst to produce carbon monoxide in the steam and synthetic gas.    USE - Two stage fluidized bed biomass gasifier for hydrogen production.    ADVANTAGE - High concentration hydrogen is consecutively manufactured in an efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing hydrogen using a two stage fluidized bed biomass gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a two stage fluidized bed biomass gasifier.    Gas supply unit (20)    Synthetic gas reactive portion (30)    Aqueous gas reactive portion (40)    Spreader plate (50,60)    Flowing layer (100)    Two stage fluidized bed biomass gasifier (1000)
NOVELTY - The furnace has a furnace body filled with combustion-supporting gas. An air inlet hole is formed on a side wall of the furnace body. An air supply device is hinged on an upper part of the furnace body that is formed with a combustion layer. Biomass raw material is processed in a steam separating device and passed into the furnace body through an opening. Fuel gas is received from the furnace body. A steam conveying pipeline is connected with a steam supply device. Waste heat is passed to a heat source unit.    USE - Lower suction-type biomass gasification furnace.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a lower suction-type biomass gasification furnace.
NOVELTY - The furnace has a furnace body whose side wall is formed with an air inlet hole. An upper part of the furnace body is fixed with an air supply device and connected with an inner part of a biomass raw material supply unit. The biomass raw material supply unit is equipped with a steam input device. Biomass raw material is filled with gas fuel. The side wall of the furnace body is arranged with circumferential cloth. The steam input device is provided with a steam supply device, where an input end of the steam supply device is fixed with a steam input pipeline.    USE - Lower suction-type biomass gasification furnace.    ADVANTAGE - The furnace is filled with combustion-supporting gas so as to ensure nitrogen containing quantity and increase quality of fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a lower suction-type biomass gasification furnace.
NOVELTY - Biomass coal comprises microbial fermented biomass as raw material.    USE - Biomass coal.    ADVANTAGE - The biomass coal is cost-effective, has low ignition point, high burnout rate, good thermal stability, high strength, low levels of pollutant and good waterproof performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing biomass coal, which involves:    (A) utilizing 150-250 pts. wt. coal powder, 20-40 pts. wt. biomass, 4-6 pts. wt. desulfurization agent and 4-6 pts. wt. solid dust as raw materials;    (B) taking biomass and then crushing into strips of 2-5 centimeters;    (C) mixing biomass, water and leavening agent in mass ratio of 800-1200:400-600:1 and then fermenting for 7-10 days to obtain the fermented biomass;    (D) adding coal powder and sludge powder and then stirring the obtained material;    (E) adding the stirred material with desulfurization agent and solid dust and then stirring the obtained material;    (F) adding the stirred material with the fermented biomass and then stirring the obtained material for 10 minutes; and    (G) performing cold press molding and then keeping the molded material for 3 days to obtain the desired product.
NOVELTY - A solid fuel is obtained by drying cyanobacteria algae such that moisture content of dried product is 8-15%, adding denitration mildew-proof agent and performing extrusion molding of resultant material.    USE - Solid fuel (claimed).    ADVANTAGE - The solid fuel having high calorific value of 18-22 MJ/kg, is manufactured with high productivity and reduced energy consumption by simple, environmentally-friendly and economical process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of solid fuel.
NOVELTY - Large scale cultivation of microalgae using soybean waste water comprises (a) enlarging culture of microalgae, (b) preparing soybean product waste water into micro-algae culture medium, (c) inoculating microalgae into micro-algae culture medium and large-scale cultivation microalgae, (d) carrying out heterotropic cultivation to obtain micro-algae cell with large-scale lipid synthesis and accumulation, and (e) separating and recovering microalgae, and extracting micro-algae lipid.    USE - The method is useful for large scale cultivation of microalgae using soybean waste water (claimed).    ADVANTAGE - The method: saves lot of water resource and nutritional salt; reduces the cultivation cost; removes waste water chemical oxygen demand (COD), total nitrogen (TN) and total phosphorus (TP); regenerates energy; reduces emission; and is suitable for industrial application.
NOVELTY - Chlorella ellipsoidea glyceraldehyde-3-phosphate dehydrogenase (CemGPDH) protein comprising fully defined sequence of 618 amino acids (SEQ ID NO.2), as given in the specification, is new.    USE - The CemGPDH protein, gene and vector are useful in improving high palmitoleic acid and/or oleic acid content, or high total fatty acid content of yeast cell, plant cell or algae cell. The yeast cell, plant cell or algae cell are useful for producing biodiesel (all claimed).    ADVANTAGE - The gene: improves cellular fatty acid content; and transforms the yeast cell, plant cell and algae cell for significantly increasing total fatty acid content of cells. The GPDH: is suitable for catalytic synthesis of glycerol-3-phosphate (G3P) and triacylglycerol (TAG); involves in mitochondrial enzyme G3P shuttle; provides electronic respiratory chain; plays an important role in lipid synthesis and energy metabolism.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) gene encoding the cem glyceraldehyde-3-phosphate dehydrogenase (GPDH) protein; (2) vector, comprising the gene; (3) host cell, comprising cemGPDH protein, gene or vector; (4) preparing yeast cell, plant cell or algae cell containing high palmitoleic acid and/or oleic acid content, or high total fatty acid content, comprising transforming gene or vector into yeast cell, plant cell or algae cell, where the yeast is Saccharomyces cerevisiae, preferably uracil-deficient type S. cerevisiae INVSC1, the alga is Chlorella, preferably elliptical chlorella (C. ellipsoidea), and the plant is Arabidopsis thaliana, tobacco, rape, sunflower, soybean, Solanum lycopersicum, castor, cotton, sesame or peanut; and (5) use of the CemGPDH protein, gene and vector in improving high palmitoleic acid and/or oleic acid content, or high total fatty acid content of yeast cell, plant cell or algae cell.
NOVELTY - Complex enzyme comprises 4-10 pts. wt. cellulase, 3-8 pts. wt. xylanase, 2-8 pts. wt. beta -mannase, 3-10 pts. wt. glucoamylase, 1-5 pts. wt. protease, 1-3 pts. wt. phytase and 0.5-1 pts. wt. dextran.    USE - The complex enzyme is used for: cane molasses fermentation; and producing sugarcane molasses fuel ethanol (all claimed).    ADVANTAGE - The complex enzyme can increase the fermentation sugar content to more than 8%, reduces 20% of exogenous nutrients added, increases purity of the fermentation mash, increases raw material using rate, reduces waste liquid discharge and its influence, and is prepared by simple operation process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing complex enzyme comprising (i) sterilizing enzyme raw materials, and and then mixing according to ratio, and (ii) uniformly mixing, and vacuum packaging;    (2) use of complex enzyme in producing sugarcane molasses fuel ethanol; and    (3) molasses mash fermentation using complex enzyme comprising fermenting at 28-32 degrees C for 18-22 hours, then entering material into mash distillation and rectification process, at last, obtaining alcohol or fuel ethyl alcohol product.
NOVELTY - Producing lipid involves performing fermentation for lipid production with an alkaline oxygen-stage waste as a carbon source in presence of Rhodococcus opacus DSM 1069 strain. Transesterification reaction takes place, where the lignin fragments in alkaline oxygen-stage waste is degraded to obtain product.    USE - Method for producing lipid from Rhodococcus opacus DSM 1069 strain, where the produced lipid used in production of biodiesel or food additives (claimed).    ADVANTAGE - The method enables to produce lipid from Rhodococcus opacus DSM 1069 strain in a simple, and cost-effective manner. The method ensures effective reduced emission of pollutants arising from the degradation of lignin found in alkaline oxygen-stage waste, and thus prevents environmental pollution.
NOVELTY - The device has a liquid outlet (10) connected with an oil pump. A shell (6) is connected with an inner side of a top cover (1). An upper end of a spray pipe is connected with a condensing medium inlet. A guide plate is connected with a cooling pipe (5) that is connected with an outer spiral tube. A spray thrower (4) is connected with a gas-liquid mixer (2) that is connected with an air inlet pipe. The top cover is connected with another condensation medium inlet. The latter condensation medium inlet is provided with an inner spiral pipe and the outer spiral pipe through a spray hole.    USE - Vehicular biomass thermal cracking composite type condensing device.    ADVANTAGE - The device has compact and reasonable structure, convenient disassembling operation and convenient cleaning and maintaining operation, and ensures effective jet spray condensing process and vapor condensing process for thermal crack, reduces the condensation time, increases the liquid product yield, realizes valid recovery of condensing liquid with the bottom shell through first-stage condensed liquid separating area of liquid discharging outlet and occupies less floor area.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a/an vehicular biomass thermal cracking composite type condensing device.    Top cover (1)    Gas-liquid mixer (2)    Spray thrower (4)    Cooling pipe (5)    Shell (6)    Liquid outlet (10)
NOVELTY - The device has a feeding device (1) connected with a feeding pipeline (2). An anaerobic fermentation jar (3) is fixed with a methane pipeline (4) and a strip digestive liquid pipeline (5). A solid liquid separating machine (6) is integrated with a pan pipeline (7), where the anaerobic fermentation jar is connected with the solid liquid separating machine through the strip digestive liquid pipeline. A liquid storage jar (9) is fixed with a strip biogas pipeline (10). A strip biogas slurry reflow pipeline (12) is fixed on the feeding device.    USE - Biogas slurry reflow pipeline livestock anaerobic fermentation device for use in husbandry marsh gas preparation field.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a biogas slurry reflow pipeline livestock anaerobic fermentation device.    Feeding device (1)    Feeding pipeline (2)    Anaerobic fermentation jar (3)    Methane pipeline (4)    Strip digestive liquid pipeline (5)    Solid liquid separating machine (6)    Pan pipeline (7)    Liquid storage jar (9)    Strip biogas pipeline (10)    Strip biogas slurry reflow pipeline (12)
NOVELTY - The method involves adding biomass material with a dropping mixture, where the biomass material is selected from one of straw, saw dust and leaves. Solid-liquid separating process is performed on the dropping mixture by a centrifugal device. Distillation process is performed on the droppings mixture to remove dry solid waste. Activated carbon and livestock manure is passed to the droppings mixture to form gas, where mass ratio of the livestock manure is 1: 80 to 1: 120. Filtering process is performed to remove waste water by a filter i.e. multistage filtering element.    USE - Farm field waste treatment method.    ADVANTAGE - The method enables ensuring effective excrement treatment process in large cultivation field, improving farm nutrient environment to avoid soil pollution caused by unwanted waste and realizing quick and convenient waste treatment operation and large industrial scale usage effect.
NOVELTY - The device has a spiral conveyor connected with an outside cylinder (31) that is connected with a spiral shaft, where the spiral shaft is connected with a motor (33). An end part of a carbonization cylinder (2) is located in a rear end of a carbon room (4), where the carbonization cylinder is fixed with an inlet pipe (51) that is connected with a combustion furnace and the outside cylinder. The carbon room is connected with a smoke pneumatic pipe (52) and the combustion furnace, where a device base body is connected with the spiral conveyor and an activate cylinder (81).    USE - Continuous biomass carbonization device.    ADVANTAGE - The device has a carbonization product fixed with the smoke pneumatic pipe that is connected with the combustion furnace so as to improve heat energy circulation efficiency and avoid pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a continuous biomass carbonization device.    Carbonization cylinder (2)    Carbon room (4)    Outside cylinder (31)    Motor (33)    Inlet pipe (51)    Smoke pneumatic pipe (52)    Activate cylinder (81)
NOVELTY - The device has a reaction device connected with a control device. An end opening is formed on a steam device. An end cover is fixed on an upper part of the steam device through a seal bolt. A fire-resisting layer is formed on a ceramic heating plate. A heat preservation and heat insulation layer is arranged on the steam device. A water supplement pipeline is engaged with a steam pipeline. A steam pipe valve is fixed on the reaction device. An atmosphere gas control valve is fixed on the control device.    USE - Biomass pressure conversion device.    ADVANTAGE - The device effectively saves biomass energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass pressure conversion device utilization method.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic sectional diagram of a biomass pressure conversion device.
NOVELTY - The method involves performing dehydrating process on rubbish material to obtain drying material. Carburization process is performed on the rubbish material. Combustion process is performed at high temperature. Drying process is performed by a heat source through combustion gas, where temperature of the combustion gas is 1100 degrees Celsius. Decomposing and removing process is performed to obtain inorganic chemical component. The inorganic chemical component is burned at 800 degree Celsius. Evaporating process is performed to remove smoke and peculiar smell on the drying material.    USE - Rubbish carbon pneuma cogeneration processing method for a domestic rubbish and industrial waste processing field.    ADVANTAGE - The method enables ensuring zero discharge operation process so as to reach valid discharge standard without any additional external fuel at low processing cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a rubbish carbon pneuma production line device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a rubbish carbon pneuma production line device.
NOVELTY - This utility new type relates to a one for sludge in low temperature carbonization process of outside heat type heat de-carbonization furnace, comprising feeding device and tube, two end tube is respectively set with a front supporting wheel and a rear supporting wheel device, middle part set with tube in supporting wheel device, front supporting wheel device and a outer tube in supporting wheel set with a front heating room, in supporting wheel device and a tube between the rear supporting wheel device set with rear heating room, heating room after outside a wall is set with a smoke pneuma inlet, front heating room outside a wall is set with a smoke pneuma outlet, a smoke pneuma inlet through a wind channel and a smoke outlet pneuma. Using burning pyrolysis pneuma heating sludge so as to greatly reduce the energy cost, sludge carbonization product of sludge biological carbon, the retain the potassium and phosphorus element equal, and the copper equal heavy metal element into a stable state, can modified for sewage treatment plant sewage purification process, is used for absorbing a nitrogen in sewage, phosphorus and heavy metal, and a garden with biological carbon as base fertilizer or soil modifying agent.
NOVELTY - This utility new type claims a a biomass gasification furnace, comprising a biomass gasification furnace main body (1), wherein the gas output end of the biomass gasification furnace is set with several U-shaped by a pipeline unit (A) composed of a gas input pipeline, a U-shaped filter pipeline unit mutually detachably connected through a screw thread structure, the bottom of the U-shaped pipeline set with a inclined arrangement has a filtering mechanism (2), and the side wall of a U-shaped pipeline set with a mechanism of the through screw thread structure detachably mounted has a column-shaped impurity receiving unit (3), the impurity containing unit by transparent material. This biomass gasification furnace to produce a gas can be effective in filtering process, and a structure of the impurity can be sent to the collection device in, the whole structure and convenient maintenance.
NOVELTY - A biomass (a) is accommodated in a container (160). Spore-state microorganisms are germinated and adhered to biomass (a) by cooling or maintaining the biomass (a) still under predetermined conditions. The microorganisms is extincted by heating biomass (a) to which germinated microorganisms are adhered, and maintained still under predetermined conditions, to obtain biomass.    USE - Manufacture of biomass (claimed).    ADVANTAGE - The method enables manufacture of biomass, by suppressing spontaneous ignition of biomass fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for biomass accommodation apparatus (150), which has container which accommodates biomass by supplying steam to raw material of biomass, and steaming raw material, heating gas supply section (170) which makes biomass accommodated in container flow through gas adhering to biomass which heats biomass more than the extinction temperature of germinated microorganisms, and coolant gas supply portion (180) which makes biomass accommodated in container flow through the coolant gas which cools biomass to temperature which germination of microorganisms of spore state requires.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of biomass accommodation apparatus. (Drawing includes non-English language text)    Biomass accommodation apparatus (150)    Container (160)    Heating gas supply section (170)    Coolant gas supply portion (180)    Control portion (185)
NOVELTY - The reactor has anaerobic reaction pool (1) and feeding pipe (4) that are overlapped with each other. The height of reaction room (8) is set according to diameter of speed-regulating circulation pump (7) which is set with sludge reflux pipe (5). The low diameter and height ratios of pool are in range of 5:4 and 1:4 respectively. The reactor height is in range of 12-30. The backflow circulation device is set in feeding pipe with protective cover (2). The biogas slurry and residue overflow pipe (15) is connected to return pipe nozzle at feeding pipe with reverse flushing switch.    USE - STAIC efficient anaerobic reactor.    ADVANTAGE - The productivity of the anaerobic reactor can be improved. The fermentation rate of reactor can be improved. The reactor occupies less space. The investment of the reactor can be greatly reduced. The use efficiency of the reactor can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic reactor.    Anaerobic reaction pool (1)    Protective cover (2)    Feeding pipe (4)    Sludge reflux pipe (5)    Speed-regulating circulation pump (7)    Reaction room (8)    Biogas slurry and residue overflow pipe (15)
NOVELTY - Toilet flush system, where discharge is gravitationally fed through an inclined serrated pipe work to separate the solid wastes from the excess flush water volume, is claimed.    USE - The toilet flush system is useful to generate bio-gas from everyday household organic waste to reduce over-dependence on fossil fuel gas supply system.    ADVANTAGE - The toilet flush system: eliminates the use of separator tank(s); does not accumulate any waste that requires manual disposal, where all wastes are discharged into municipal sewage system; eliminates the need for many peripheral equipment, such as heaters, separator tanks, heat sources and dedicated pumps to achieve economic differentiation and hence early payback; is low profiled (claimed); and is compact.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for solids report to the reactor (in process, cycle) via a multi-level float switching arrangement, where the float switch detects both solid and water levels in the reactor to switch solid feed between the 2 reactors (reactor in cycle and standby), and also initiates and/or stop water intake to make up required wt/wt.% solids.
NOVELTY - A biodiesel composite additive comprises 9-14 pts. wt. barium petroleum sulfonate, 5-9 pts. wt. dialkyl dithiocarbamate, 3-5 pts. wt. isobutyl alcohol, 2-6 pts. wt. ethanol, 3-6 pts. wt. 2-ethyl hexanol, 6-10 pts. wt. glycol alkylphenyl ether, 5-11 pts. wt. polyoxyethylene cetyl phenolic ether, 3-8 pts. wt. tetraethylene pentamine, 5-10 pts. wt. long chain fatty acid ester. 3-6 pts. wt. p-phenylenediamine, 5-7 pts. wt. cyclopentane, 1-5 pts. wt. cyclopentanone, 4-9 pts. wt. aldol and 2-5 pts. wt. 1,3,5-triazine.    USE - Biodiesel composite additive used in fuel system.    ADVANTAGE - The biodiesel composite additive effectively cleans the carbon deposits in the fuel system, increases power and reduces environmental pollution.
NOVELTY - Preparing laminated biomass briquette, comprises (i) preparing inflatable thin layer of substrate by crushing debris of cellulose biomass, baking, adding quicklime and kaolin into biomass chips, mixing, and carrying out extrusion molding; (ii) carrying out surface treatment of inflatable thin layer of substrate, and carrying out surface roughening treatment of the inflatable thin layer of substrate, and coating an adhesive onto the surface of inflatable thin layer of substrate; and (iii) laminating the aligned coated thin layer of substrate which is inflated on the upper and lower surfaces.    USE - The method is useful for preparing laminated biomass briquette (claimed).    ADVANTAGE - The method has easy processing procedure, and high operation procedure; produces product with high density, and good molding thickness; and is suitable for easy large scale production.    DETAILED DESCRIPTION - Preparing laminated biomass briquette, comprises (i) preparing inflatable thin layer of substrate by crushing debris of cellulose biomass, baking, adding 3-8 wt.% quicklime and 2-5 wt.% kaolin into biomass chips in a equal dry weight of the raw materials, uniformly mixing, and carrying out extrusion molding to mold the product into regular shape; (ii) carrying out surface treatment of inflatable thin layer of substrate, and carrying out surface roughening treatment of the inflatable thin layer of substrate, and coating an adhesive onto the surface of inflatable thin layer of substrate; and (iii) aligning the coated thin layer of substrate which is inflated on the upper and lower surfaces, and laminating by passing through a laminated roller, to obtain the final product.
NOVELTY - This new utility model claims of one of rice hull decomposition separating system, wherein it comprises solid liquid separating chamber, gas discharge tube, cool water shower nozzle, solid liquid collecting slope, solid liquid out pipe arrange, solid liquid separation chamber, pump, carbon removal pipe; the gas solid liquid separating chamber is set with discharge pipe side, solid liquid collection inclined face to and gas solid liquid separating chamber is set with joint with cool water shower nozzle, solid liquid collection inclined face lower end set with solid liquid out pipe arrange; under the gas solid liquid separating chamber end formed with solid liquid separation chamber, solid liquid separation chamber side set with liquid discharging pipe, a liquid discharging pipe location of solid liquid out arrange pipe is higher than the bottom end face of solid liquid separation chamber is set with bottom with pump, pump connecting arrange coal pipe. This new utility model by designing one set can realize to heat decomposing to obtain the rice hull can fuel gas, a biomass extract liquid, solid coal rice hull of the third state object for separation.
NOVELTY - Upper part upper part the utility new model claims of one rice hull of the third state decomposing system, it comprises material transporting system, spray system catalyst, decomposing system, the material transport system the catalyst spray system, spray system the catalyst decomposing system. This new utility model by designing one set can realize system of heat decomposing rice hull, rice hull for decomposing is combustible gas, biomass extract liquid, solid coal rice hull of the third state and hot decomposing system.
NOVELTY - The system has a pressure tank (1) that is provided in the lower end portion of a segregation unit (21) in which the purified water in which the biogas is dissolved, is flowed. A separate purification tower (2) has a treated water drawing line that ejects the purified water in which the refinement object gas is mixed. A refinery gas outlet line ejects the methane gas sampled at the upper portion of segregation unit to outside. The refinery gas outlet line is connected to a desulfurization tower (10) in which hydrogen sulfide is removed.    USE - Separation and purification system for biogas.    ADVANTAGE - The refinery gas with high methane purity is obtained by providing the structure that performs separation using the difference of solubility of refinement object gas and vapor pressure including carbon dioxide and hydrogen sulfide.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the separation and purification system.    Pressure tank (1)    Separate purification tower (2)    Desulfurization tower (10)    Segregation unit (21)    Dehumidifier (23)
NOVELTY - The furnace has a sleeve cylinder whose bottom is connected to a gearbox, and a gearbox power input shaft connected with a power output device. A packing auger sleeve outside wall and an inner tube wall are integrated to form a heating room. A lower part of the heating room is arranged with a flue gas entrance tube. A smoke entrance and a smoke outlet are provided in a pneuma cylinder wall of the heating room. A carbonization furnace smoke outlet is connected to a flue gas entrance of a drying furnace.    USE - Single-tube grading biomass carbonizing furnace.    ADVANTAGE - The furnace enables the reaction temperature to be controlled easily, and has small volume, low failure rate and prolonged service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a single-tube grading biomass carbonizing furnace.
NOVELTY - The furnace has an inner housing sleeved in an outside shell. An air plate is arranged at bottom of a chamber. A cloth wind plate is provided at bottom of a burning room. A bottom part of the burning room is arranged with a shaft flow fan. An axial flow fan is arranged at an upper side wall of a smoke room. The axial flow fan is arranged in an upper part of an outside shell body. A guide flow plate is fixed in an inner shell. The air plate is provided with a strip-shaped hole. The guide flow plate is arranged with a driving motor, a gear mechanism and a rotating shaft connecting plate.    USE - Biomass granule making charcoal furnace.    ADVANTAGE - The furnace has uniform heating process and high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass granule making charcoal furnace.
NOVELTY - Biomass carbonization is carried out by drying biomass raw material by directly contacting with source gas; conveying biomass material to a carbonizing furnace and carrying out carbonization process; conveying carbonized biomass to a tar removing device, then conveying part of carbonized biomass product to a combustion furnace and other part to cold side of heat exchanger, and leading heating gas to bottom of carbonization furnace for heat exchange for pyrolysis of biomass; and sending produced pyrolysis gas to hot end of heat exchanger for heating carbonization furnace.    USE - Method for biomass carbonization (claimed).    ADVANTAGE - The method has low energy consumption and high production efficiency, is capable for continuous work, and allows easy control of carbonization temperature. The heating gas can uniformly dry biomass with high heat transfer rate.    DETAILED DESCRIPTION - Biomass carbonization comprises:    (A) drying biomass raw material by directly contacting with source gas;    (B) conveying biomass material to a carbonizing furnace and carrying out carbonization process;    (C) conveying carbonized biomass to a tar removing device, then conveying part of carbonized biomass product to a combustion furnace and other part to cold side of heat exchanger, and leading heating gas to bottom of carbonization furnace for heat exchange for pyrolysis of biomass;    (D) sending produced pyrolysis gas to hot end of heat exchanger for heating carbonization furnace; and    (E) sending flue gas of heat exchanger to drying chamber to be used as a source gas for biomass drying process.    An INDEPENDENT CLAIM is included for a biomass carbonization device comprising drying room,, tar removing device, heat exchanger, and combustion furnace.
NOVELTY - The device has a chamber (11) which is provided with a bucket (13). A spiral waste heat air inlet layer (7) and a carbon monoxide tester (9) are arranged in side portion of the chamber. An air inlet hole (14) is formed in bottom portion of the chamber. A feeding portion is composed of a hopper (1), a closeness feeder (2) and a distributor (5).    USE - Dry-sucking type biomass gasification device.    ADVANTAGE - Burning of the raw material can be prevented. The efficiency of the biomass gasification device can be improved. Biomass gasification can be performed stably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the dry-sucking type biomass gasification device. (Drawing includes non-English language text)    Hopper (1)    Closeness feeder (2)    Distributor (5)    Spiral waste heat air inlet layer (7)    Carbon monoxide tester (9)    Chamber (11)    Bucket (13)    Air inlet hole (14)
NOVELTY - The device has an air inlet pipe and a pressure pipe arranged in a kettle cover. An end of a pressure control valve is connected with a steam generator. Another end of the control valve is connected to a vacuum pump. One end of the pressure pipe extends to a top part of a kettle body. Another end of the pressure pipe is connected with a pressure tee. Two ends of the pressure tee are respectively connected with a vacuum pressure table valve and a steam pressure table valve. The vacuum pressure table valve is connected with a program controller.    USE - Biomass heat conversion device.    ADVANTAGE - The device can effectively perform biomass conversion process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass heat conversion device.
NOVELTY - Biodiesel is manufactured in one-step using alcoholysis by hydrolyzing raw material oil to yield water, fatty acid and glycerine, performing methanol gasification at 110-180 degrees C with methanol vapor pressure of 1-1.5 MPa, mixing evaporated methanol with stream of hydrolyzate, reacting at 1-1.5 MPa for 3-6 hours to obtain fatty acids, flash distilling to obtain primary product and balance methanol, and vacuum distilling primary product.    USE - One-step manufacture of biodiesel using alcoholysis (claimed).    ADVANTAGE - Process is simple, environment-friendly, cost-saving, does not require catalyst, and has high yield of stable and reliable products.    DETAILED DESCRIPTION - Biodiesel is manufactured in one-step using alcoholysis by hydrolyzing raw material oil to yield water, fatty acid and glycerine following reaction of R1COO-CH2-CH(R2COO)-CH2-OOCR3 + 3H2O=R1COOH + R2COOH + R3COOH + CH2OHCHOHCH2OH, performing methanol gasification at 110-180 degrees C with methanol vapor pressure of 1-1.5 MPa, mixing evaporated methanol with stream of hydrolyzate, reacting at 150-200 degrees C and 1-1.5 MPa for 3-6 hours to obtain fatty acids following reaction of R1COOH + CH3OH=R1COOCH3 + H2O, R2COOH + CH3OH=R2COOCH3 + H2O, and R3COOH + CH3OH=R3COOCH3 + H2O, flash distilling to obtain primary product and balance methanol, and vacuum distilling primary product.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of one-step manufacture of biodiesel using alcoholysis. (Drawing includes non-English language text).
NOVELTY - A solidifying point-lowering biodiesel composite additive comprises 0-5 wt.% OP-4 (RTM: Octyl phenol) alkylphenol ethoxylate, 5-10 wt.% OP-7 (RTM: Octyl phenol) alkylphenol ethoxylate, 35-60 wt.% coconut oil fatty acid diethanolamine, and 30-55 wt.% WD12-101 ethylene-vinyl acetate copolymer pour point depressant.    USE - Solidifying point-lowering biodiesel composite additive (claimed).    ADVANTAGE - Additive lowers cold filter plugging point and condensation point.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of solidifying point-lowering biodiesel composite additive which involves uniformly mixing raw materials at 65 degrees C, stirring at 200 r/minute in water bath at constant temperature for 15 minutes; and    (2) application of solidifying point-lowering biodiesel composite additive which involves mixing 0.5-1 wt.% additives to biodiesel.
NOVELTY - Organic waste treating agent comprises 50-85 wt.% organic acid, 1-25 wt.% activated carbon and 1-25 wt.% zeolite, where the organic acid is humic acid and fulvic acid.    USE - The treating agent is useful for producing organic waste fuel (claimed).    ADVANTAGE - The agent improves heating value of fuel, and produces fuel in short time, and is economical and environmentally friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) producing organic waste fuel, comprising (a) mixing organic waste and first organic waste treating agent, and separating first floating material, (b) processing for forming second floating material, (c) mixing the first and second floating materials with the second organic waste treating agent to form reaction product, and (d) drying the reaction product; and    (2) organic waste fuel produced by the above method.
NOVELTY - This utility new type relates to a biomass material, one in a dry distillation furnace in, for containing biomass material rod, comprising basket body, the bottom of the basket body is set with bottom net, the net is mesh aperture is less than the biomass material rod of the inner side section width, said basket body upper part is set with , the mesh aperture of the separting mesh large a width b of the biomass material rod, the top part of the charging basket are uniform distribute is set with upright post, the bottom of the charging basket and a location structure is set with a matching concave hole. This utility new type finish the regular biomass material of uniform bar code is put between the material rod, the charging basket, a basket and the gap between furnace wall uniformity, the heat conducting channel, so the electric heating is uniform, which greatly increase the heat efficiency, which can fully use heat flow, a period short, material is not easy to crushing, it reduces the waste of cost and material, at the same time the production of biomass charcoal high quality, integrity is good.
NOVELTY - This utility new type claims a one garbage biological tunnel type drying using a resource, this utility new type system using a method step as follows: pre-processing machinery sorting stage, biochemical filter leaching reaction stage, tunnel drying biological reaction stage, resource use separation stage. This utility new type system device a comprising the biological tunnel drying chamber, insulating layer, upender, air blower, waste pneuma biological filter, evaporator, waste gas absorber, a sieve, a magnetic separator, a spraying biological filter reactor, plate frame extrusion dewatering machine and wind power sorting machine, a sieve in turn a biological leaching filter reactor, plate frame extrusion dewatering machine, biological drying chamber and tunnel pneumatic separator. Has advantages as follows: the garbage resource sorting, separating magnetic substance, biochemical shower filter degradation, biological drying tunnel sealed environment-friendly and energy-saving, high heat value fuel use, waste discharge pneuma;
NOVELTY - A biomass fuel is manufactured by drying bark raw material until water content is less than or equal to 40%, cutting into greater than or equal to 1 mesh fragment, mixing with 8-20 meshes wood meal with water content of less than or equal to 5% in which weight ratio of bark fragment and wooden meal is 1:4.5-5.5, drying at 180-220 degrees C until moisture content is 10-13%, and molding.    USE - Manufacture of biomass fuel (claimed).    ADVANTAGE - Process is energy-saving and environment-friendly, and has high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow block diagram for manufacturing biomass fuel. (Drawing includes non-English language text).
NOVELTY - A biomass fuel manufacturing system comprises feeder (2), drying furnace (4), drying expansion cylinder (6), drying device (7), and briquetting machine (11) in which feeder is used for crushing bark, feeder discharging end is connected to drying expansion cylinder feeding end, drying expansion cylinder entrance receives crushed bark, drying expansion cylinder is connected to drying furnace, drying expansion cylinder is used for accepting dried bark, drying device feeding port receives dried material, and drying device is connected to briquetting machine in feeding auger (15).    USE - A biomass fuel manufacturing system (claimed).    ADVANTAGE - Biomass fuel manufacturing system is energy-saving and environment-friendly, has high efficiency, and uses waste.    DETAILED DESCRIPTION - A biomass fuel manufacturing system comprises feeder (2), drying furnace (4), drying expansion cylinder (6), drying device (7), and briquetting machine (11) in which feeder is used for crushing bark, feeder discharging end is connected to drying expansion cylinder feeding end, drying expansion cylinder entrance receives crushed bark, drying expansion cylinder is connected to drying furnace, drying expansion cylinder is used for accepting dried bark, drying device feeding port receives dried material, drying device is connected to briquetting machine in feeding auger (15), and briquetting machine receives material from drying device which is pressed into desired block.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of biomass fuel manufacturing system.    Feeder (2)    Drying furnace (4)    Drying expansion cylinder (6)    Drying device (7)    Briquetting machine (11)    Feeding auger (15)
NOVELTY - Electrolytic water-coal-slurry preparing hydrogen desulphurization device has an electrolyte pipe (2), which is connected to the bottom portion of a pipe network (7). A hydrogen discharge pipe (3) is located at the center of the upper portion of electrolytic groove electrode (4). A carbon dioxide discharge pipe (5) is arranged on the periphery of electrolyte pipe and has a microwave radiation device (1). The electrolytic groove electrode has two pieces of ultrasonic vibration rod (6) on both sides.    USE - Water coal desulfurizing electrolyte hydrogen producing device.    ADVANTAGE - Achieves a low cost device which has a simple structure, optional size, and works at normal temperature and normal pressure without additional condition. Chemical desulfurizing speed is fast and desulfurizing efficiency is high. Achieves simple process, and hydrogen cathode is made of high purity, without need further purification. Achieves time and resource-saving, mild reaction, and easy operation.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of a water coal desulfurizing electrolyte hydrogen producing device.    Microwave radiation device (1)    Electrolyte pipe (2)    Hydrogen discharge pipe (3)    Electrolytic groove electrode (4)    Carbon dioxide discharge pipe (5)    Ultrasonic vibration rod (6)    Pipe network (7)
NOVELTY - The device has a water conveying pump whose water inlet is connected with a water inlet regulating pool. A water outlet regulating pool is connected with a coagulation precipitation pool. A coagulating sedimentation pool is connected with the water conveying pump. A deposition pool is connected with a sludge discharge outlet. An aerobic pool inlet is connected with a bottom of an anaerobic pool. An aerobic pool outlet is connected with a water circulation pump. Discharge anaerobic pool mud is fixed with a sludge discharge inlet. An aeration disk is connected with an aerator.    USE - Dynamic film biogas slurry processing device.    ADVANTAGE - The water outlet of the aerobic pool is connected with a constant flow pump so as to realize discharging waste water of a film component. The aerobic pool is connected with the anaerobic pool so as to realize blocking waste water conveying direction in a film. The device is connected with the anaerobic pool and the aerobic pool so as to realize convenient distributing of water of a multi-of film component and single reverse flushing for a specific film component. The device maintains film component flux, regulates reverse flushing rate of flow, reduces film pollution and carries out reverse flushing for a total film module, and is convenient to adjust of water flow rate and reverse flushing time of the constant flow pump.    DETAILED DESCRIPTION - The device comprises industrial filter cloth that is selected from terylene short fiber, terylene fiber, vinylon, and polypropylene. An INDEPENDENT CLAIM is also included for a dynamic film biogas slurry processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a dynamic film biogas slurry processing device.
NOVELTY - The device has a feeder unit connected with an explosion-proof pressure relief seal device and a furnace wall heater. A grading rotary flow separator is connected with a high temperature fan and an exhaust port. A heating rod is connected with an end part of the feeder unit. A deoxidizer is connected with the feeder unit. A slag material is connected with the rotary flow separator. An air pressure valve is connected with the grading rotary flow separator. A splitting furnace is formed as a cylindrical-shaped structure. The high temperature fan is fixed to the heating rod.    USE - Domestic rubbish fluidization bed non-oxygen splitting device.    ADVANTAGE - The device is simple in structure and convenient to operate, and has high automatic degree, low energy consumption rate, high pneumatic tar product content performance and high activity product carbon structure, and realizes classification rubbish harmless treating process without caused by secondary pollutant generation system by utilizing a fluidization bed.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a domestic rubbish fluidization bed non-oxygen splitting device.
NOVELTY - The device has a multi-layer rotary dry distillation device body (2) connected with a multi-layer feeding system (1) and a carbon discharging system (4). The multi-layer rotary dry distillation device body is formed with an air outlet. The multi-layer feeding system is connected with the multi-layer rotary dry distillation device body. The carbon discharging system and a mounting rack (5) are connected with a remote control system (6). The feeding system is connected with a multi-layer spiral propeller (12). A multi-layer roller device body is provided with a driving device body.    USE - Domestic rubbish multi-layer rotary dry distillation device. Uses include but are not limited to domestic waste and kitchen waste, medical waste, sludge, agricultural waste biomass processing application.    ADVANTAGE - The device has high capacity, high efficiency and low material consumption, and wide range of application, and increases yield of dry distillation device, and can convert biomass into gas, oil and carbon from harmless resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a domestic rubbish multi-layer rotary dry distillation device.    Multi-layer feeding system (1)    Multi-layer rotary dry distillation device body (2)    Carbon discharging system (4)    Mounting rack (5)    Remote control system (6)    Multi-layer spiral propeller (12)
NOVELTY - The furnace has a furnace body whose upper end is fixed with a lower end of a side wall. An inner part of the furnace body is filled with combustion-supporting gas and formed with an air inlet structure. The side wall is formed with an interlayer. A lower part of the furnace body is fixed with an outer part of a gas fuel air supply device. The gas fuel air supply device is formed with the air inlet structure. An inner part of the furnace body is formed with an air inlet hole. A lower part of the furnace body is connected an output pipeline of a gas fuel pump.    USE - Lower suction type biomass gasification furnace.    ADVANTAGE - The furnace reduces side wall temperature and combustion fuel-gas consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a lower suction type biomass gasification furnace.
NOVELTY - A biodiesel is prepared by reacting Sorbifolia seed, ionic liquid, alkali as phase transfer catalyst, and short-chain alcohol as solvent into microwave reactor at 40-80 degrees C for 3-25 minutes, extracting Sorbifolia seed oil, synthesizing, standing, layering, and separating upper layer.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - Process is simple, energy-saving, and environment-friendly and has fast reaction speed, short reaction time, and low wastewater discharge, and product has high yield and good quality.
NOVELTY - A mulberry-branch-based biofuel is prepared by pruning mulberry branches, naturally drying, crushing into powder with particle size of less than or equal to 3 mm, drying until moisture content is 12-14%, uniformly mixing with auxiliary material, and pressing in molding machine to obtain pellet.    USE - Preparation of mulberry-branch-based biofuel (claimed).    ADVANTAGE - The method solves the problem of excessive trimming of mulberry branch. Resulting biofuel has high fuel combustion performance due to increased fuel density and reduced water content and burns without carbon dioxide and sulfur dioxide discharge, making the biofuel environment-friendly.
NOVELTY - 1-Cyclopropyl-6-fluoro-7-((R)-3-(3-nitrobenzylidene amino)-hexahydro-azepin-1-yl)-8-chloro-1,4-dihydro-4-oxo-quinolin-3-carboxylic acid boron diacetate chelate (IV) is new.    USE - 1-Cyclopropyl-6-fluoro-7-((R)-3-(3-nitrobenzylidene amino)-hexahydro-azepin-1-yl)-8-chloro-1,4-dihydro-4-oxo-quinolin-3-carboxylic acid boron diacetate chelate used as intermediate in preparing besifloxacin hydrochloride (claimed).    ADVANTAGE - The compound has simple preparation method with low reaction temperature and less energy consumption.    DETAILED DESCRIPTION - 1-Cyclopropyl-6-fluoro-7-((R)-3-(3-nitrobenzylidene amino)-hexahydro-azepin-1-yl)-8-chloro-1,4-dihydro-4-oxo-quinolin-3-carboxylic acid boron diacetate chelate of formula (IV) is new. INDEPENDENT CLAIMS are included for:    (1) preparation of compound (IV); and    (2) preparation of besifloxacin hydrochloride of formula (I), comprising reacting 8-chloro-1-cyclopropyl-6,7-difluoro-1,4-dihydro-4-oxo-quinolin-3--carboxylic acid boron diacetate compound of formula (II) with nitrobenzylidene amino-azepane compound of formula (III) or with mixture of (R)-3-amino-hexahydro-1H-azepane and nitrobenzaldehyde in presence of alkaline reagent in dichloromethane at 40-60 degrees C, and after reaction is finished, adding hydrochloric acid.
NOVELTY - This new type utility claims one biomass gasification furnace is a furnace structure, comprising a furnace body, a furnace body set with lengthways air inlet part with a circulation water cooling device air inlet, one side part of the furnace body is set with a gas nozzle device, a lengthways air, circulation water cooling air inlet device and between the combustible gas nozzle device is set with connected ventilation pipe component, the air outlet of the ventilating pipe and a air blower connected, circulation water cooling air inlet device and cooling device connected at the same time. Circulation water cooling air inlet device set with air inlet pipe, air inlet pipe sleeve set with cooling pipe, air inlet pipe and the cooling pipe flowing with circulation water for cooling heat dissipation, in in actual use, can obviously reduce the high temperature of the hearth is affect for air inlet pipe, which greatly prolongs the service life of air inlet device, at the same time is good for gasification furnace is long time continuous stable work, compared with the past technology air inlet device use life short (generally a number a number to months and so on) of the problem, this circulation water cooling air inlet device of life can be as long as use year number.
NOVELTY - This new utility model relates to one kind of small suction type biomass gasification furnace continuous closeness add material device, comprising upper furnace body cover plate, pouring cone cylinder, hopper, feedstock cavity, rotary blade, motor, motor bracket, a guide cylinder, rotating shaft, material rod and upper fan and lower fan, installed one top end connected coaxial end part of guide cylinder, the guide cylinder is connected installed motor bracket, motor bracket top end mounted motor, motor output shaft end coaxial fixed rotating shaft one end of furnace body in the feedstock cavity one side cover plate, rotating shaft the other end downward through guide cylinder coaxial to the following pouring cone cylinder bottom, internal pouring cone cylinder rotating shaft radial gap is fixed multi-edge of the material rod. The application of guide cylinder upper end fan when in rotation, wherein in forming stable negative pressure guide cylinder, and cone cylinder lower end fan pouring and forming micro-air flow rising common effect, low rotate speed information lower in the upper, lower two end fan, inner air entering into furnace to prevent the carry of the target material, the gasification furnace continuous work.
NOVELTY - This utility new type relates to one a biomass boiling bed, comprising feeding device, fluidized bed main body, a fire, a feeding device and fluidized bed main body, a fire boiling bed main body and a detachable connection, a fixed port with port of body entering into sprinkle fire mouth, the inner with air port of a shell further comprising a sprinkle fire entering into oral cavity body is a secondary supplement air port tube. This utility new type adopt modularization design, when assembling is convenient, maintain time can block, maintain progress up the port using two secondary air design, which ensures the biomass fuel gasification burning biomass fuel using rate is high. In addition adopt a new, effective for preventing biomass fuel plate, bridge and so on happen; at the same time, a modular according to claim a heat exchange assembly, a hot air in the heat exchange pipe in temperature gradually increased, dust removing effect is good, the heat exchange, after dust-removing, in the tail pneuma and ash discharge index reach the natural gas combustion discharge claim.
NOVELTY - A carbon powder processing incense carbon of this utility new type claims a one edible spice bag material made of waste, including ball mill (1), and ball mill through feeding cylinder (2) is a kneading machine (4), a kneading machine (4) inner is set with motor (6) and a connection without gravity slurry leaves double-shaft mixer; the kneading machine (4) is connected with a lower part (8), the hopper (8) through a transmission cylinder is provided with (9) a molding machine (10), molding machine (10) is a drying tower (11). This utility new type through the waste of edible spice waste bag material made of carbon powder carrying out ball-milling crushing, kneading, molding, and finally a final product by a drying, whole device a connecting character is good, and the operability is strong, the cost is low, the prepared carbon product incense combustion time is long, and fixed carbon value high, is non-toxic and tasteless, the waste of edible spice bag a waste changes waste into valuable, value a is a qualitative leap.
NOVELTY - The system has a system body provided with a hopper that is mounted with a splitting room. A collecting device is mounted with a lower part of the splitting room. An air blower group is provided with first, second and third air blowers, where the first and second blowers are placed with the splitting room. A multi-section adjusting switch is connected with the first, second and third air blowers. A lower part of an air purification room is connected with a blocking part through a pipeline. An injector is connected with the third air blower through the air purification room.    USE - Biomass combustion system.    ADVANTAGE - The system body is connected with the first, second and third air blowers so as to effectively adjust air control rate of the splitting room, and avoids corrosion effect of an inner wall of a cleaning device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass combustion system.
NOVELTY - This new utility model relates to one kind of biomass hopper pressure block machine, especially relates to a kind of one can add additive is uniform, high density compression processing livestock excrement, straw and ensilage feed equal production device of biomass compression block, category biological energy, livestock excrement treatment environmental protection area, feed area needed technique and device of it of the biomass hopper, the additive hopper, mixer, composed of machine, and system with feedstock controller, dehydrating device, all material plate, an infrared controller, storehouse, a flexible connector, an additive, a spiral extruder, hot steam disk pipe one, can provide dehydration, high temperature and high pressure, additive equal technology method produce biomass.
NOVELTY - A inner one a pressure roller, a ring module bi-directional interactive a molding machine, wherein pedestal (1) is mounted with a machine main machine box body (5), a semi through hole pressing roller motor (2) and the through hole ring mould motor (3), a machine main machine box body (5) through inner hollow shaft mounted with a hollow shaft (25), hollow shaft (25) connected through a ring mould hole (8) and through hole ring mould belt pulley (6), a hollow shaft (25) through a bearing mounted on a machine main shaft (18) and supporting shaft (10), a granulator (18) connect a semi through hole pressing roller belt wheel (4), a support shaft (10) mounted with a semi through hole pressing roller (9), a semi through hole pressing roller (9) is provided with an eccentric inner shaft (12), the through hole ring mould motor (3) and the through hole ring mould belt pulley (6) is connected, which is clockwise rotating, semi through hole pressing roller motor (2) and semi through hole pressing roller belt wheel (4) connected in anticlockwise rotating, is bi-directional rotary semi through hole between the pressure roller (9) and through hole ring mould (8). This molding machine has stable operation, electricity-saving, production efficiency is high.
NOVELTY - A catalyst comprises 1-10 %mass active metal and 90-99 %mass metal oxide. The active metal is elemental metal having hydrogenation activity. The metal oxide is chosen from oxide of iron, cobalt, nickel, copper, zinc, aluminum, magnesium, cerium, zirconium and gallium.    USE - Catalyst is used for hydrogenation of biodiesel byproduct glycerol to ethylene glycol.    ADVANTAGE - The catalyst has glycerol conversion rate of 100%, ethylene glycol selectivity of 60% or less, and excellent catalytic activity and stability, and is prepared by simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst, which involves dissolving metal element precursor dissolved in water, forming mixed solution of metal element precursor, adding precipitator, precipitating, adjusting pH to 8-12, aging, washing the resultant precipitate using water, drying and calcining the dried precipitate under mixed atmosphere of hydrogen and inert gas. The metal element precursor is nitrate, chloride or sulfate.
NOVELTY - Cultivating dragon fruit comprises choosing lowest temperature region with good ventilation, humus rich soil and loamy sand, drying, soaking healthy dragon fruit seeds in water, spreading soil, spraying water, covering with a plastic preservation film cover, maintaining and spraying clean water daily, transplanting seedling, planting a support, balancing the fertilization before flowering, where fertilizer includes manure, nitrogenous fertilizer, phosphate fertilizer and potassium fertilizer, irrigating, trimming branches, picking fruit, preventing and treating plant diseases and insect pests.    USE - The method is useful for cultivating dragon fruit (claimed).    ADVANTAGE - The method is pollution-free and economical.    DETAILED DESCRIPTION - Cultivating dragon fruit comprises (a) choosing lowest temperature region of 10 degrees C with good ventilation, soil rich in humus content and loamy sand with a pH of the soil of 6.5-8, (b) drying, taking healthy dragon fruit seeds, soaking in water for 1-2 days, spreading soil, spraying water, covering with a plastic preservation film cover, removing the film after more than 90% of the seed is germinated, maintaining and spraying clean water daily, transplanting seedling when the height is more than 5 cm, (c) planting a support having a height of 30-50 cm, planting 3-5 plants with a planting density of 300-350 plants/acre, (d) daily management by balancing the fertilization before flowering, where the fertilizer includes manure, nitrogenous fertilizer, phosphate fertilizer and potassium fertilizer, increasing potash fertilizer and magnesium fertilizer fertilization during flowering and fruiting period, irrigating once in every 3-7 days, maintaining moist soil, where 1 m surrounding the parts of the dragon fruit plant with hay, trimming branches, picking fruit after trimming branches and allowing to bud and (e) preventing and treating plant diseases and insect pests.
NOVELTY - Composite straw molding machine comprises sawtooth pressure roller (1), molding pressure roller (2), sawtooth pressure plate (3), cross-shaped connecting plate (4), power shaft (6) and extrusion mold (7).    USE - Composite straw molding machine.    ADVANTAGE - The machine increases adaptability of raw materials, reduces reactive power loss, reduces wearing of molded part, and improves molding effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of composite straw molding machine.    Sawtooth pressure roller (1)    Molding pressure roller (2)    Sawtooth pressure plate (3)    Cross-shaped connecting plate (4)    Power shaft (6)    Extrusion mold (8)
NOVELTY - The carbon set has a carbon kettle that is installed in a carbon kettle bracket (25) and mounted with a combustion disk. One side of a carbon kettle bracket is mounted with a base (19) used for fixing iron frame basket. A cross beam guide rail (22) is mounted between the carbon kettle bracket and base, and is mounted with an electric trolley (20). The electric trolley drives a roller (23) to move a hook (21) in up and down direction, so as to take carbon kettle arranged between carbon kettle bracket and base table.    USE - High-efficient environment-friendly energy-saving biomass charcoal unit.    ADVANTAGE - The biomass carbon is distilled effectively. The carbon kettle automatic loading and unloading process is realized. The upper end of charcoal unit is mounted with protective cover, so as to increase working safety and performance of carbon kettle.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the high-efficient environment-friendly energy-saving biomass charcoal unit.    Base (19)    Electric trolley (20)    Hook (21)    Cross beam guide rail (22)    Roller (23)    Carbon kettle bracket (25)
NOVELTY - The device has feeding device connected with a gas chamber (1) and a tank (2). The feeding device is provided with a feeding hopper (3) and the feeding belt (4). An inlet pipe (5) is provided in the lower portion of the gas chamber, and a dust discharge tube (6) is provided in the upper portion of the gas chamber. An ash outlet (7) is formed in the bottom of the gas chamber whose side portion is provided with a water spray port (8). A gas chamber outlet is connected with the tank through a spring switch valve (9).    USE - Device for processing rubbish for producing combustion gas.    ADVANTAGE - The rubbish is efficiently processed, thus the combustion gas is produced stably.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for processing rubbish for producing combustion gas.    Gas chamber (1)    Tank (2)    Feeding hopper (3)    Feeding belt (4)    Inlet pipe (5)    Dust discharge tube (6)    Ash outlet (7)    Water spray port (8)    Spring switch valve (9)
NOVELTY - Biomass granule fuel production device comprises a feeding-screening device, an iron removing device, a cyclone separating device, a material storage stirring device, a spiral conveying device, a granulating device, an exhaust gas treatment device and a wind conveying pipe. The feeding-screening device is connected with the cyclone separating device through the wind conveying pipe. The wind conveying pipe is mounted with the iron removing device. The cyclone separating device is connected with the material storage stirring device.    USE - Used as biomass granule fuel production device.    ADVANTAGE - The device has simple structure, reduces energy consumption and produces less dust.    DETAILED DESCRIPTION - Biomass granule fuel production device comprises a feeding-screening device, an iron removing device, a cyclone separating device, a material storage stirring device, a spiral conveying device, a granulating device, an exhaust gas treatment device and a wind conveying pipe. The feeding-screening device is connected with the cyclone separating device through the wind conveying pipe. The wind conveying pipe is mounted with the iron removing device. The cyclone separating device is connected with the material storage stirring device. The material storage stirring device is mounted with the spiral conveying device. The spiral conveying device is connected with the granulating device. The granulating device is mounted with the exhaust gas treatment device. The exhaust gas treatment device is connected with the material discharge screening device.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass granule fuel production device.
NOVELTY - Invention relates to agriculture, food processing industry, as well as to public municipal services. The invention is intended for disinfection and sequential phase, anaerobic decomposition of crushed biological wastes of products of farm animals, birds, human and production wastes of food processing industry with obtaining of biogas and disinfected (from pathogenic microflora, helminth, their eggs and seeds of plants) mineralised organic fertilisers, as well as bio-fodder additives. The device comprises a cylindrical shaped reservoir divided inside with partitions alternately not reaching the top and bottom of the reservoir into the flow chambers of fermentation to produce over each of their pair of separate gas sections, loading and discharge pipes, heaters of substrate and a gas pipeline connected to the gas sections. The cylindrical shaped reservoir has the height equal to its diameter and its volume is divided by coaxial partitions into five coaxial chambers, the volumes of which are respectively equal to 3, 3, 5, 74, 15% of the device volume, and the loading chamber is located in the centre of the device, and the discharge is at the periphery.    USE - Agriculture.    ADVANTAGE - Invention provides reduction in heat loss, deep temperature pasteurisation of raw material and its hydrolysis at the beginning of the process, the uniform supply of raw material from one chamber to another, minimising dead spots, elimination of the temperature gradients in the volume and, consequently, obtaining biogas and fertilisers of higher quality with identical periods of disposal of raw materials.5 cl, 2 dwg
NOVELTY - The integrated crop straw harvester has a picking and crushing device (1) that is suspended in a harvesting machine chassis (4) which is connected with a traction frame (5). The traction frame is connected with a tractor connecting hook. The harvesting machine chassis is connected with a fixing gear. A rotary gas flow separating chamber (2) is fixed in a molding machine set (3). A gearbox (6) is provided with a power output shaft and a power input shaft which is coupled with a crushing unit (1-2).    USE - Integrated crop straw harvester used in agricultural field.    ADVANTAGE - The picking and collecting, crushing, dust separating and pressing molding functions are integrated efficiently in the crop straw harvester. The working efficiency and processing quality of the crop straw harvester are improved. The operating cost and labor intensity for operating the integrated crop straw harvester are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the integrated crop straw harvester.    Picking and crushing device (1)    Crushing unit (1-2)    Rotary gas flow separating chamber (2)    Molding machine set (3)    Harvesting machine chassis (4)    Traction frame (5)    Gearbox (6)
NOVELTY - Preventing trichodiniasis in swamp eel breeding tank, involves filling 1/3 of the swamp eel breeding tank made up of stainless steel, with bamboo leaves, adding Eclipta prostrate, Acalypha australis, apple snails and Ipomoea aquatica in the tank, then introducing water, adding 0.1-0.5 g extract of traditional Chinese medicinal composition containing chinaberry bark, rhizoma calami, fructus quisqualis, Chinese torreya seed, Cyrtomium fortunei, pistachio nuts, radix rehmanniae and radix sophorae flavescentis, in breeding tank.    USE - The method is useful for preventing trichodiniasis in swamp eel breeding tank (claimed).    ADVANTAGE - The method enables to reduce trichodiniasis infection rate by 40-60% and promotes swamp eel growth, and is convenient and environmentally-friendly.    DETAILED DESCRIPTION - Method for preventing trichodiniasis in swamp eel breeding tank, involves (a) opening swamp eel breeding tank made up of stainless steel, filling 1/3 of the tank with bamboo leaves, adding Eclipta prostrate, Acalypha australis, apple snails and Ipomoea aquatica in the tank, then introducing water, seeding swamp eel and harvesting I.aquatica, and (b) adding 0.1-0.5 g extract of traditional Chinese medicinal composition prepared by extracting traditional Chinese medicinal composition using water, in breeding tank, where the traditional Chinese medicinal composition comprises 60-80 pts. wt. chinaberry bark, 10-30 pts. wt. rhizoma calami, 5-10 pts. wt. fructus quisqualis, 4-8 pts. wt. Chinese torreya seed, 10-16 pts. wt. radix stemonae, 20-28 pts. wt. Cyrtomium fortunei, 15-20 pts. wt. pistachio nuts, 8-15 pts. wt. radix stemonae, 15-22 pts. wt. radix rehmanniae and 12-18 pts. wt. radix sophorae flavescentis.
NOVELTY - Preventing ichthyophthiriasis in swamp eel breeding tank, involves filling 1/3 of the swamp eel breeding tank made up of stainless steel, with bamboo leaves, adding Eclipta prostrate, Acalypha australis, apple snails and Ipomoea aquatica in the tank, then introducing water, adding 0.1-0.5 g traditional Chinese medicinal composition comprising fructus quisqualis, radix stemonae, C.fortunei, pistachio nuts, radix rehmanniae, radix sophorae flavescentis, dried ginger, chili pepper and wheat bran, in breeding tank.    USE - The method is useful for preventing ichthyophthiriasis in swamp eel breeding tank (claimed).    ADVANTAGE - The method promotes swamp eel growth, and is convenient and environmentally-friendly.    DETAILED DESCRIPTION - Method for preventing ichthyophthiriasis in swamp eel breeding tank, involves (a) opening swamp eel breeding tank made up of stainless steel, filling 1/3 of the tank with bamboo leaves, adding Eclipta prostrate, Acalypha australis, apple snails and Ipomoea aquatica in the tank, then introducing water, seeding swamp eel and harvesting I.aquatica, and (b) adding 0.1-0.5 g traditional Chinese medicinal composition in breeding tank, where the traditional Chinese medicinal composition comprises 5-10 pts. wt. fructus quisqualis, 10-16 pts. wt. radix stemonae, 20-28 pts. wt. Cyrtomium fortunei, 15-20 pts. wt. pistachio nuts, 8-15 pts. wt. radix stemonae, 15-22 pts. wt. radix rehmanniae, 12-18 pts. wt. radix sophorae flavescentis, 3-5 pts. wt. dried ginger, 7-15 pts. wt. chili pepper and 80-90 pts. wt. wheat bran, and is prepared by crushing radix stemonae, C.fortunei, pistachio nuts, radix rehmanniae, radix sophorae flavescentis, dried ginger and chili pepper into powder, mixing fructus quisqualis and wheat bran, adding suitable amount of water and granulating mixture.
NOVELTY - This utility new type relates to a processing field, specifically relates to a straw granule molding machine one mould. A including a discharging mould disc, disc comprising upper mould and lower mould, upper mould and lower mould are is annular, one side upper mould is set with a multi-upper chute, each one corresponding to a discharging groove are set with a low groove in one side lower module is, the discharging mould passes through the upper groove and lower groove form a space from the inner ring and outside ring. This utility new type straw granule molding machine mould, the grinding disc is set with upper mould and lower mould two part, upper mould and lower mould are set with multi up a discharging groove, a discharging mould each extending through a chute, a discharging mould time is damaged, it is only need to removed the damage of the discharging mould for a single maintenance. A. Thus, a straw granule molding machine operation is simple, the maintenance is convenient and simple, cost is also a futher.
NOVELTY - The method involves analyzing sewage temperature, hydrogen content and sulfate reducing bacteria content. The bacteria screening is performed by synchronization of desulfurization and denitrification processes. The use of indoor simulation method field test parameters is determined, according to hydrogen sulfide content and polymer solution viscosity test, to determine the process parameters based on desulfurization and denitrification bacteria activator dosing process. The activating agent such as sodium nitrate, potassium nitrate, phosphate and ammonium di-hydrogen phosphate are used.    USE - Method for maintaining viscosity of polymer solution in sewage oil field.    ADVANTAGE - The requirement of hydrogen sulfide for maintaining polymer solution viscosity is reduced, and the stable viscosity is maintained for long time. The maintenance of the polymer solution viscosity is performed in safe and nvironment-friendly manner, and the processing cost is reduced.
NOVELTY - The method involves obtaining a solid content of rough fermentation liquid by spiral extruding device for marsh gas fermentation liquid preliminary separation. A flocculating agent is added to the rough fermentation liquid. The plant powder filter aid is added to fermentation liquid after flocculation, and the mixture is stirred. The biogas residue and biogas slurry are obtained with plate frame type filter press provided with pressure filter.    USE - Method for performing solid-liquid separation of marsh gas fermentation liquid used for processing organic fertilizer.    ADVANTAGE - The biogas slurry of solid content is separated directly, so as to process the organic fertilizer. The slag water content is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block flow diagram illustrating the marsh gas fermentation liquid solid-liquid separating process. (Drawing includes non-English language text)
NOVELTY - The equipment has a transport unit for transferring biomass to a lower part of a reactor along upper direction. An ignition unit is arranged with an ignition area. The ignition unit ignites the biomass in an inner side of the reactor. A supply unit supplies the biomass to the reactor. The transport unit is installed at the inner side of the reactor. An air flowing part flows air to the biomass. The supply unit is provided with a feed screw and installed at an inner side of a supply chamber. The supply chamber is connected with a storage chamber that stores the biomass.    USE - Upward screw-fixed bed bio-char producing equipment for a reactor.    ADVANTAGE - The transport unit transfers the biomass to the lower part of the reactor along the upper direction so as to regularly maintain constant height of the ignition area, so that surface area of the equipment can be increased and uniform airflow into the biomass can be maintained, thus improving bio-char producing efficiency of the equipment. The combustion of the biomass in the storage chamber can be prevented by supplying nitrogen to the storage chamber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an upward screw-fixed bed bio-char producing method.    DESCRIPTION OF DRAWING(S) - The drawing shows an exploded perspective view of an upward screw-fixed bed bio-char producing equipment.
NOVELTY - A desulfurization media is obtained by mixing 40-50 wt.% sludge containing cellulose, 35-45 wt.% iron(III) hydroxide, 2-7 wt.% dolomite with 3-8 wt.% slaked lime and 0.5-1 wt.% nutriment.    USE - Desulfurization medium for removal of sulfide from biogas (claimed). Can also be used as sulfur fertilizer.    ADVANTAGE - The medium has high desulfurization efficiency, recycled waste resources and enhanced resource utilization, high porous structure, and is environment-friendly,.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for removal of sulfide.
NOVELTY - Method for preparing antioxidation peptide, involves (a) obtaining canned liquid of Decapterus muroadsi as raw material, (b) performing ultrafiltration using hollow fiber membrane having molecular weight of 10 KDa, where the filtrate comprises 2.403 times of protein, and (c) adding 6500-7000 U/g alkaline protease to filtrate, and performing hydrolysis at 55-60 degrees C for 3-4 hours to obtain the product, where the pH of the filtrate is 8-9.    USE - The method is useful for preparing antioxidation peptide (claimed).    ADVANTAGE - The method is simple, convenient to perform, environmentally-friendly and cost-effective.
NOVELTY - This utility new type claims a one-section gas in sludge treatment device, comprising sludge dewatering unit, coal preparation unit and sludge combustion treatment unit, this utility new type after the dehydration of sludge and coal powder mix is made into high temperature pyrolysis coal-section inner gas in furnace, fully using sludge production reducing coal burning, at the same time reducing coal is high temperature a futher dehydrating drying and without oxygen for coal dry distillation, carbonization process is a dry distillation coal gas re-introduced into the furnace for burning, completely eliminate participate toxic and harmful substances in dry distillation of coal, at the same time, copper, zinc, lead, chromium, arsenic in exist of sludge and so on is not easy to decompose a harmful metal element also in entering into slag is melted and in cooling after curing satisfy a is safe.
NOVELTY - This utility new type claims a farm of one energy-saving marsh gas system, belonging to the technology field of marsh gas. This utility new type the row wherein a livestock and poultry manure to a temperature in Anaerobic fermentation jar, the flushing water wherein a to normal temperature Anaerobic fermentation jar, temperature in Anaerobic fermentation jar and normal temperature Anaerobic fermentation jar is air outlet are connected to storage jar in through pneuma and desulphurization system outlet of pneuma storing jar connected to stove a marsh gas pool and a generator, set with a collector in a marsh gas pool generator, one heat energy heat collector pipe is connected to livestock and poultry for heat preservation, heat energy tube through the other temperature in Anaerobic fermentation jar in form circulation pipeline is; in Anaerobic outlet temperature of the fermentation jar to a marsh liquid pool, pool through pump in the biogas slurry is discharged in a field, normal temperature outlet Anaerobic fermentation jar is connected to aerobic processor, is aerobic processor connected in a natural in. This utility new type effective to increase a yield of methane, the methane contamination and zero emission, furthest realize the resource.
NOVELTY - This utility model claims a biological aviation kerosene hydrogenation cracking reaction device, reactor tube top part of gas-liquid mixed liquid through inlet branch pipe is connected with spiral type nozzle, reactor inner tube set with at least two layer or more catalyst bed layer, lower catalyst bed layer upper part provided with combination type liquid collection distributor, catalyst bed layer part provided with supporting catalyst is hump type screen, cold hydrogen feed wherein is set between adjacent catalyst bed layer, each catalyst bed layer is of a wall in lower side provided with a temperature test wherein, side wall of catalyst bed layer and this test wherein the temperature corresponding to the lower part is set with catalyst discharge port, upper part is set with combined liquid collection distributor by insulating plate, the vent pipe and the liquid pipe composed of the through liquid pipe b is set baffle center, lower part has discharge pipe is connected. This utility new type is beneficial effect: this utility new type increase a hydro-cracking reaction efficiency and increase yield of biological aviation kerosene, b is suitable for continuous industrial production process.
NOVELTY - A combustion catalyst is prepared by preparing aid containing magnesium oxide supported on ( gamma )-aluminum oxide using ( gamma )-aluminum oxide as carrier, magnesium nitrate solution as precursor solution, impregnating resultant product with copper nitrate solution as impregnation solution, and supporting copper oxide as active component on ( gamma )-aluminum oxide-magnesium oxide composite. The impregnation process is carried out by ultrasonic biochemical treatment.    USE - Combustion catalyst is used in catalytic combustion of ultra-low concentration methane.    ADVANTAGE - The catalyst component has excellent activity and stability, and is prepared by quick and simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of combustion catalyst. The mass ratio of aluminum and magnesium in ( gamma )-aluminum oxide-magnesium oxide composite is 4:1. The magnesium nitrate solution is prepared by dissolving magnesium nitrate in deionized water. The concentration of magnesium nitrate solution is 0.3 mol/L. The copper nitrate solution is prepared by dissolving copper nitrate in deionized water. The concentration of magnesium nitrate solution is 0.3-0.4 mol/L.
NOVELTY - Dihydroxyanthraquinone green sulfuric acid waste treatment involves heating 30-55 wt.% dihydroxyanthraquinone sulfuric acid concentrated waste at 80-120 degrees C, and then adding activated carbon and an oxidant to the obtained material with stirring for 30-60 minutes. The obtained material is filtered to give activated carbon residue and a filtrate. The obtained filtrate is mixed with magnesium oxide with stirring for 1 hour at 3-7.5 pH, and then filtered them to give a solution of magnesium sulfate and magnesium boron silicon precipitates.    USE - Method for treating dihydroxyanthraquinone green sulfuric acid waste (claimed).    ADVANTAGE - The method enables to treat dihydroxyanthraquinone green sulfuric acid waste in a simple, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Dihydroxyanthraquinone green sulfuric acid waste treatment involves heating 30-55 wt.% dihydroxyanthraquinone sulfuric acid concentrated waste at 80-120 degrees C, and then adding activated carbon and an oxidant to the obtained material with stirring for 30-60 minutes. The obtained material is filtered to give activated carbon residue and a filtrate. The obtained filtrate is mixed with magnesium oxide with stirring for 1 hour at 3-7.5 pH, and then filtered them to give a solution of magnesium sulfate and magnesium boron silicon precipitates. The obtained material is crystallized, and then centrifuged. The obtained material is dried to obtain a magnesium sulfate heptahydrate. The obtained crystalline magnesium sulfate heptahydrate is dried at 200 degrees C to obtain anhydrous magnesium sulfate products. The obtained material is mixed with activated carbon residue at 400-1100 degrees C to obtain the finished product.
NOVELTY - A livestock and poultry biogas slurry liquid is used by mixing plant ash and livestock and poultry biogas slurry liquid in which mass-to-volume ratio of plant ash and livestock and poultry biogas slurry liquid is 1-10%, filtering, regulating pH to 7.5-9, measuring phosphate (PO43-) concentration, adding magnesium ion (Mg2+) chemical agent in which molar ratio of Mg2+ and PO43- is 1-2:1, mixing for 30-60 minutes, reacting Mg2+ and hydroxide ion (OH-) to obtain magnesium hydroxide (Mg(OH)2) precipitate, releasing PO43- to obtain struvite crystal, and recovering nitrogen.    USE - Use of livestock and poultry biogas slurry liquid (claimed).    ADVANTAGE - Process is safe, environment-friendly, and low cost.    DETAILED DESCRIPTION - A livestock and poultry biogas slurry liquid is used by mixing plant ash and livestock and poultry biogas slurry liquid in which mass-to-volume ratio of plant ash and livestock and poultry biogas slurry liquid is 1-10%, filtering, regulating pH to 7.5-9, measuring PO43- concentration, adding Mg2+ chemical agent in which molar ratio of Mg2+ and PO43- is 1-2:1, mixing for 30-60 minutes, reacting Mg2+ and OH- to obtain Mg(OH)2 precipitate, releasing PO43- to obtain struvite crystal, recovering nitrogen and phosphorus in livestock and poultry biogas slurry liquid, directly using 300-800 kg/acre livestock and poultry biogas slurry liquid as farmland fertilizer, adding plant ash with amount of 20-50 kg/acre, maintaining soil water content to greater than or equal to 20% for greater than or equal to 5 days, and releasing PO43- to obtain struvite crystal.
NOVELTY - High-ammonia nitrogen organic wastewater treatment involves providing wastewater with high-ammonia nitrogen concentration into anaerobic treatment unit, adding alkali solution to adjust pH, then providing the effluent into stripping unit through effluent pipe, and providing the resultant product into ammonia nitrogen stripping unit using biogas generated in anaerobic treatment unit. The high-ammonia nitrogen organic wastewater treatment is carried out using anaerobic unit, stripping unit, absorbing device, and gas treatment unit.    USE - High-ammonia nitrogen organic wastewater treatment (claimed).    ADVANTAGE - The method enables high-ammonia nitrogen organic wastewater treatment with reduced impurities and excellent recyclability of biogas.
NOVELTY - A large-scale cultivation sewage is treated by carrying out drainage engineering rebuilding to separate rainwater and sewage, separately dealing with manure and urine, automatically separating contaminated livestock drinking water to reduce waste of drinking water, constructing biogas digester, re-processing facilities, and aquaculture wastewater treatment for biogas treatment, carrying out planting combination which is large-scale cultivation and local farmland combination, or vegetable garden or garden planting combination, and increasing application of organic fertilizer.    USE - Treatment of large-scale cultivation sewage (claimed).    ADVANTAGE - Process is harmless, environment-friendly, and low cost.    DETAILED DESCRIPTION - A large-scale cultivation sewage is treated by carrying out drainage engineering rebuilding to separate rainwater and sewage, separately dealing with manure and urine, automatically separating contaminated livestock drinking water to reduce waste of drinking water, constructing biogas digester, re-processing facilities, and aquaculture wastewater treatment for biogas treatment, carrying out planting combination which is large-scale cultivation and local farmland combination, or vegetable garden or garden planting combination, increasing application of organic fertilizer, reducing use of pesticide, treating farmland breeding cycle, and releasing sewage.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram for treating large-scale cultivation sewage. (Drawing includes non-English language text).
NOVELTY - The furnace has an outside tube (3) whose upper part is arranged with a cover plate (4) and lower part is arranged with a water cooling jacket (9), a gas outlet (8), a middle tube (2) and a water cooling jacket (9). The middle tube is provided with a transfer piece (17). A fire grate (12) is located in a lower part of the water cooling jacket. An upper surface of the water cooling jacket is arranged with a combustion chamber (11). An upper part of the combustion chamber is arranged with a gasification room (10). A side surface of an ash bucket is arranged with an air inlet (18).    USE - Heating gas suction type biomass gasification furnace.    ADVANTAGE - The furnace reduces production dust, and has better filtering effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a heating gas suction type biomass gasification furnace.    Middle tube (2)    Outside tube (3)    Cover plate (4)    Gas outlet (8)    Water cooling jacket (9)    Gasification room (10)    Combustion chamber (11)    Fire grate (12)    Transfer piece (17)    Air inlet (18)
NOVELTY - Methanol gasoline complexing agent comprises 4-5 wt.% of triethanolamine, 30-35 wt.% of liquid paraffin, 3-5 wt.% of Tween-80 (RTM: Polysorbate 80), 3.5-6 wt.% of oleic acid, 25-28 wt.% of butyl alcohol, 12-14 wt.% of isoamyl alcohol, 5-8 wt.% of acetone, 1-5 wt.% of ethylene glycol monobutyl ether, 5-6 wt.% of coal oil and 6-10 wt.% of benzene.    USE - The methanol gasoline complexing agent is useful in vehicle (claimed).    ADVANTAGE - The agent can be prepared with easily available raw materials, in a simple, safe and eco-friendly manner, and can effectively solves the high low vehicle methanol gasoline product with a series of conventional technology.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the agent comprising mixing the liquid paraffin, butyl alcohol, triethanolamine and isoamyl alcohol according to a ratio of 6:5:1:2.4-8.75:7:1:3.5 to obtain a mixture A, mixing Tween-80 (RTM: Polysorbate 80), oleic acid and acetone according to a ratio of 1:0.7:1-1:2: 2.67 to obtain a mixture B, mixing ethylene glycol monobutyl ether, coal oil and benzene according to a ratio of 1:1:1.2-1:6:10 to obtain a mixture C and finally mixing the mixtures (A)-(C).
NOVELTY - Mixed fuel comprises 10-90 vol.% of isobutyl alcohol and balance amount of gasoline.    USE - The mixed fuel is useful in gasoline machine.    ADVANTAGE - The mixed fuel has good combustion performance, high energy density and high fuel economy.
NOVELTY - Producing fuel, comprises adding 80-85% of methyl alcohol or ethyl alcohol as raw material in 2% of catalytic additives and less than 18% of water and then stirring, performing transesterification reaction, standing for 4 hours and then checking.    USE - The method is useful for producing fuel (claimed), which is useful in hotel, restaurant, factory, school, and domestic.    ADVANTAGE - The method produces the fuel in an environmentally-friendly manner.
NOVELTY - Mixed fuel comprises 20-40 vol.% of positive amyl alcohol, 20-40 vol.% of biological diesel oil and 30-50 vol.% of petroleum diesel oil.    USE - The mixed fuel is useful in diesel engine (claimed).    ADVANTAGE - The mixed fuel: can effectively increase oxygen content; exhibits good synergistic effect; does not need to add other component or auxiliary agent to a sufficient combustion; and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the mixed fuel comprising mixing the raw materials as above per se under a normal temperature and normal pressure and uniformly stirring the mixture.
NOVELTY - Use of aluminum-iron ore for manufacturing hydrogen fuel, is claimed, where the application method comprises adding aluminum ore and iron ore to water.    USE - The aluminum-iron ore is useful for manufacturing hydrogen fuel (claimed).    ADVANTAGE - The aluminum-iron ore is capable of manufacturing the hydrogen fuel without pollution.
NOVELTY - The device comprises a sludge dryer, which is equipped with a feed port, a discharge port and a feed inlet and is provided with a sludge inlet, a feeding device and a sludge discharging device. The sludge discharging device is provided with a sieving machine, a discharging machine and a vibration machine. The sieving machine is provided with a sludge conveying device. The discharging machine and the vibration machine are provided with a sludge recovery device. The feeding device, the sludge conveying device and the sludge recovery device are provided with a belt conveyor.    USE - The device is useful for preparing fuel from sludge (claimed).    ADVANTAGE - The device is capable of simply and efficiently preparing the fuel from sludge with increased heat efficiency and reduced cost.    DETAILED DESCRIPTION - The device comprises a sludge dryer, which is equipped with a feed port, a discharge port and a feed inlet, and provided with a sludge inlet, a feeding device and a sludge discharging device. The sludge discharging device is provided with a sieving machine, a discharging machine and a vibration machine. The sieving machine is provided with a sludge conveying device. The discharging machine and the vibration machine are provided with a sludge recovery device. The feeding device, the sludge conveying device and the sludge recovery device are provided with a belt conveyor. The sludge discharging device is a spiral shaped conveying machine. The spiral shaped conveying machine is provided with the sludge dryer, the discharging machine and the vibration machine. The sieving machine and the vibration machine are connected with an eccentric shaft. The eccentric shaft is provided with a bearing base and a driving wheel. The driving wheel is connected with an electric machine.
NOVELTY - Preparing biodiesel oil, comprises adding monomer acid and macroporous styrenic strongly acidic cation exchange resin into an esterification reaction oil heating kettle by carbon dioxide replacement into the kettle, performing esterification, continuously adding dimethoxymethane, stopping the addition of dimethoxymethane when the acid value is less than 1 mg potassium hydroxide/g, cooling to obtain biodiesel semi-finished products, cooling the semi-finished product, and adding the composite catalyst comprising nitrate compounds, oleic acid, alcohols, and polylactic acids to obtain product.    USE - The method is useful for preparing biodiesel oil (claimed).    ADVANTAGE - The method is capable of economically preparing water immiscible biodiesel oil with good water resistance.    DETAILED DESCRIPTION - Preparing biodiesel oil, comprises adding monomer acid and macroporous styrenic strongly acidic cation exchange resin into an esterification reaction oil heating kettle by carbon dioxide replacement into the kettle, performing esterification at a temperature of 130-160 degrees C for 30 minutes, continuously adding dimethoxymethane, stopping the addition of dimethoxymethane when the acid value is less than 1 mg potassium hydroxide/g, cooling to a temperature of below 80 degrees C to obtain biodiesel semi-finished products, cooling the semi-finished product to 30 degrees C, and adding the composite catalyst comprising nitrate compounds, oleic acid, alcohols, and polylactic acids to obtain the product. An INDEPENDENT CLAIM is included for the biodiesel oil prepared by the above method.
NOVELTY - Preparing biodiesel using waste plant oil, comprises adding waste plant oil, methanol and solid base catalyst to a three-necked flask, heating, stirring the reaction mixture, taking out and cooling, removing methanol by liquid separation, separating catalyst, removing excess methanol and water by esterification reaction, adding catalyst mixture of methanol to the three-necked flask, heating and stirring, transferring the product to a separatory funnel, adding fatty acid methyl ester, soap, methanol, glycerin and solid base catalyst, water washing, and removing water to obtain biodiesel.    USE - The method is useful for preparing biodiesel using waste plant oil (claimed).    ADVANTAGE - The method is capable of simply and economically preparing the biodiesel with good catalytic activity and high purity and conversion rate of more than 96% under mild reaction condition.    DETAILED DESCRIPTION - Preparing biodiesel using waste plant oil, comprises adding waste plant oil, methanol and solid base catalyst to a three-necked flask, condensing and refluxing pipe, heating at 80-120 degrees C, stirring the reaction mixture for 2-5 hours, taking out and cooling, removing methanol by liquid separation, separating catalyst, removing excess methanol and water formed by esterification reaction using a rotary evaporator to obtain oil product, adding catalyst mixture of methanol to the three-necked flask, heating and stirring, removing the reaction flask and terminating by cooling, transferring the product to a separatory funnel, adding fatty acid methyl ester, soap, methanol, glycerin and solid base catalyst, water washing at 80-120 degrees C, and removing water to obtain biodiesel.
NOVELTY - The system has a biogas pool (2) whose bottom part is connected with a ground (3). A colony house (1) is connected with the biogas pool that is connected with a fermentation room (4). An upper part of the fermentation room is formed with a gas storage space. The fermentation room is connected with an upper part of a water pressure chamber (5) and a pool cover (7). The water pressure chamber is connected with a water pressure channel. The biogas pool is formed with an inlet (9) that is connected with a toilet of the colony house and an inner part of the fermentation room.    USE - Three-dimensional colony house pneumatic methane biogas pool ecological system.    ADVANTAGE - The system is energy-saving and environment-friendly, and reduces occupying space and land resource utilization rate, and protects the colony house from being affected by external pollution.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a three-dimensional colony house pneumatic methane biogas pool ecological system in partial section.    Colony house (1)    Biogas pool (2)    Ground (3)    Fermentation room (4)    Water pressure chamber (5)    Pool cover (7)    Inlet (9)
NOVELTY - Mutant protein CeDGATl1 comprises 713 amino acids (SEQ ID NO: 2), given in the specification.    USE - Mutant protein CeDGATl1 used for preparing fatty acids such as palmitic acid, palmitoleic acid, stearic acid and oleic acid for producing biodiesel (all claimed).    ADVANTAGE - The mutant protein CeDGATl1 effectively increases fatty acid content in yeast, plant or algal cells.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fatty acid, which involves transforming vector into yeast, plant or algal cells, where yeast is Saccharomyces cerevisiae, alga is Chlorella ellipsoidea and plant is selected from Arabidopsis, tobacco, rapeseed, sunflower, soybean, hemp, cotton, sesame or peanut.
NOVELTY - Biomass preparation involves selecting raw materials such as agricultural resource, poultry excrement, organic waste water, where agricultural resource is selected from wood, marsh gas, rice hull, tree bark, grass, rice corn, corn core, rice, wheat straw, peanut shell, sugarcane dreg and cotton seed hull. Organic waste water is selected from domestic waste water, alcohol waste water, sugar water, pharmaceutical waste water, paper making waste water, animal lipid and waste catering oil.    USE - Method for preparing biomass for biogas generation (claimed).    ADVANTAGE - The method enables to prepare biomass in an eco-friendly manner with wide applicability.    DETAILED DESCRIPTION - Biomass preparation involves selecting raw materials such as agricultural resource, poultry excrement, organic waste water, where agricultural resource is selected from wood, marsh gas, rice hull, tree bark, grass, rice corn, corn core, rice, wheat straw, peanut shell, sugarcane dreg and cotton seed hull. Organic waste water is selected from domestic waste water, alcohol waste water, sugar water, pharmaceutical waste water, paper making waste water, animal lipid and waste catering oil. The obtained raw materials are mixed in fermenting pool. The obtained mixture is kept for performing fermentation.
NOVELTY - Biodiesel production involves utilizing microbial oil.    USE - Method for producing biodiesel (claimed).    ADVANTAGE - The method enables to produce biodiesel in a simple and eco-friendly manner.
NOVELTY - The boiler has a gasification room and a gas phase combustion room that are connected with a water cooling fire grate. A secondary air inlet is connected with the gas phase combustion room. A middle part of the gasification room is formed with a feeding opening. A lower part of the secondary air inlet is formed with an observation hole. An air pre-heater is connected with a gasification agent entrance. The gasification room is connected with a peripheral throat part and a refractory furnace wall. A water cooling jacket is connected with the water cooling fire grate.    USE - Biomass gasification combustion boiler.    ADVANTAGE - The boiler is rational in design and convenient to use, economic, energy-saving and compact in structure, and has high working efficiency, and greatly reduces carbon content of inner residue and increases efficiency of combustion.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a biomass gasification combustion boiler.
NOVELTY - This utility new type relates to manufacture biomass energy using device, especially a one pneuma a biomass fuel, comprising a furnace body, a hopper, a furnace door structure, and air inlet pipe and air outlet pipe, wherein the top of the furnace body fixed with a quantitative feeder, set with a gas through the pneuma hole of a side wall of a part to the bottom of the furnace body under the furnace body, a upper furnace body side wall of the the pneuma hole fixed with a furnace body seal cover lower seal cover and a furnace body, a furnace body seal cover lower cover seal and mutually separated furnace body, the upper furnace body seal cover and the pneuma hole form the pneuma channel, this the pneuma channel and air outlet pipe connected; the furnace body under the seal cover and the pneuma hole form air inlet channel I, an air inlet of the air inlet channel I and this connected air inlet pipe, the air inlet of the air inlet pipe is also connected air inlet channel II and a form of lower part of furnace bridge, the bridge b positoin c is the furnace door structure in. This utility new type because the structure has the advantages of is: structure is simple, reduces the energy consumption and manufacturing into more important is a, the structure can be any biomass is pressed into block or rod can be directly gas.
NOVELTY - This new utility model claims of one of waste wood continuous furnace. It comprises a tower body, a closed upper end cover of the reaction gas outlet pipe provided with the nitrogen entrance pipe and waste wooden meal entrance pipe, upper part of the tower barrel body along axial direction is installed one of multi-angle steel bracket respectively in mutually fixed with big, small heating plate, wherein the lower part of tower body tube along multi-angle steel support shaft of the above each respectively in fixed with big, small cooling plate, flow channel and smoke distribution system of the whole multi-heating plate connected with the side stirrer is multi-shell of heating plate and of the whole cooling plate and multiple scraping stirring device respectively drive rotation, the lower part of upper, lower transmission shaft set with coal powder outlet pipe, upper, lower transmission shaft respectively connected with motor, tube along axial direction set with multi-number. Using waste wood chips as continuous fast preparing coal powder, at the same time can recovery using wood coal, wood tar and pyroligneous equal product, this utility model has new production period short, can consume low, carbonization uniform, elastic big operation, the adaptability is wide, can continue operating character equal.
NOVELTY - This new utility model belongs to energy and chemical industry technology area, and claims of one of solid heat carrier oil rock smelting preparing page integration system of dry distillation gas preparing methane. The solid heat carrier oil page rock refining system made of integrated dry distillation gas preparing alkyl includes in turn connected with the oil shale dry distillation unit, shale oil gas separation unit, CO2 unit, C1-C3 unit and separating CO methanation unit. This new utility model system for dry distillation gas methane by-product and olefin, the industry greatly increase economic income of oil shale processing, using this utility new type the solid heat carrier oil page rock making economic income of manufacture system of integrated dry distillation gas preparing alkyl compare the traditional solid hot carrier oil page rock smelting preparing process increase about 9%, then all production cost increase about 7%, using C1-C3 sequence separating technology, to obtain high value chemical products of olefin and ethane, using low temperature methanation technique, to obtain natural gas, reducing of pressure the gas shortage.
NOVELTY - This new utility model claims of one of RDF production system, applied in solid waste processing area and refuse derived harmless treatment and forming of fuel. The utility model is new technique process comprises: feeding, transport, and metal fuel waste separation, rough crushing, fine crushing, drying, RDF forming, and waste gas discharge. The production system, suitable operation, production efficiency high, and on RDF fuel rod production process without need to add binder, produce process meet environmental protection requirement, use and maintenance cost low.
NOVELTY - The utility model claims a new sludge treatment technology area, specifically is a kind of one fuel sludge preparing device, the structure is simple, using low cost, can increase heat efficiency of active sludge burning furnace; it comprises sludge drier, sludge drier is equipped with a feed port and a discharging port, the discharging port to the sludge drier feeding port position is set with sludge feeding device, a sludge drier is provided with sludge discharging device, wherein the discharge end of sludge discharge device to vibration sieving machine, a vibration sieving machine is set with discharge to the fuel is set with sludge transporting device.
NOVELTY - This new utility model claims of the new utility model claims of one without pre-mixing a kind of biological diesel oil gas-liquid spraying reaction device, solving of the traditional machine cantilever stirring method stirrer supporting difficult, slow rotating speed result in lipid and methanol contact not full, pre-produce low efficiency, production cost and for high acid value lipid condition requirement and high problem, wherein comprising: top exhaust port provided with the spray reaction room, lipid storage room, standing room product, methyl alcohol and concentrated vitriol mixed liquid storing chamber, floating, lipid atomizing nozzel, methyl alcohol and concentrated vitriol atomizing nozzel, the methyl alcohol and concentrated vitriol mixed liquid storing chamber and spray reaction room between connection with one end extended into the methyl alcohol in the spray reaction room and concentrated vitriol feedstock passage, said lipid storage chamber and reaction chamber between spray connected with one end extended into the lipid feedstock passage in the spray reaction room. By atomizing nozzel in installed in the spray reaction room, using lipid and methyl alcohol and acid catalyst are as state entering into spray atomizing reaction chamber, to increase contact area of liquid, and using circulation channel accelerate esterification reaction is proceeding. The utility model has no new, structure is simple, production efficiency high, production cost is low, and can be used for acid value compare high of lipid in biologic diesel oil.
NOVELTY - The multi-multistage meander stir the biogas digester is by transverse rows between the multi-square pool between one and a big gear with a one level, multistage longitudinal row with a set square of pool body, between each of the pool is a diagonal position are set with two wherein a liquid flow channel, the material liquid forming meander between a square pool of the pool and the pool level and level pool, at the same time each level pool is one in each pool are set with square by gear transmission power of independent rolling stir device, through add material of car front the first level first between the pool and the last one level at last one between the rear of the discharging car at the same time work together to make the whole digester form water level difference of water potential power, auxiliary stir, fermenting material liquid forming meander fermentation between one by one in each one between each first-stage pool of marsh gas pool.
NOVELTY - This new utility model provide a kind of one solar energy heat storage, marsh gas production, greenhouse planting integrated system, can full utilize the sun can maintain the temperature in marsh gas pool. Comprising several of greenhouse, greenhouse base provided with at least two lower part of marsh gas pool, greenhouse base one side equipped with feedstock wherein, one side provided with discharging port and marsh gas pool and solar energy heating device connect. This new utility model using solar heating device can absorb solar energy for heating, after taking heat transfer to marsh gas pool, at the same time full using heat preservation temperature on the greenhouse, make the temperature in the marsh gas pool distribution reasonable, even though in cold weather, too can ensure the high efficiency marsh gas fermentation.
NOVELTY - Producing fuel pellets using waste wood or waste medium after mushroom cultivation, comprises (a) adding lignin in crushed waste wood or waste medium to maintain greater than or equal to calorific value of pellets shape, (b) heat compressing the obtained waste wood or waste medium for molding in pellets, and (c) drying the molded pellets.    USE - The method is useful for producing fuel pellets using waste wood or waste medium after mushroom cultivation (claimed).    ADVANTAGE - The method secures high calorific value and adhesive strength of pellets.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the method for producing fuel pellets using waste wood or waste medium after mushroom cultivation (Drawing includes non-English language text).
NOVELTY - Solid fuel prepared by using high-quality fallen leaves into cylindrical shape having diameter of 50-200 mm and length of 50-400 mm under pressure of 100-500 kg/cm2, is claimed.    USE - Used as a solid fuel.    ADVANTAGE - The fuel is harmless to the human body and is environmentally friendly. The method provides fuel according to the application by varying characteristics and calorific value of flame during combustion of the mixed materials, and produces fuel in bulk amount.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing solid fuel, comprising mixing material including 100 pts. wt. fallen leaves, 10-20 pts. wt. charcoal powder and 1-5 pts. wt. natural binder; 100 pts. wt. fallen leaves, 15-30 pts. wt. straw and 3-5 pts. wt. natural binder; or 100 pts. wt. fallen leaves, 15-25 pts. wt. slack and 1-5 pts. wt. natural binder, and compressing under pressure of 100-500 kg/cm2. The total volume of the solid fuel is reduced to 5-10% due to the compression. The apparent specific gravity of the fuel is 0.45-0.65 ton/m3. The fuel is formed with at least one through-hole having inner diameter of 20-30 mm along the longitudinal direction. The fallen leaves comprise 100 pts. wt. broad-leaved tree fallen leaves and 5-30 pts. wt. needle-leaf tree fallen leaves.
NOVELTY - The apparatus comprises: a buffer tank; a first in-line mixer that is arranged within the buffer tank and comprises a first mixed gas, where the first mixed gas comprises biogas and the first external gas to be mixed; a second in-line mixer that is arranged within the buffer tank and comprises a second mixed gas, where the second mixed gas comprises biogas and the second external gas to be mixed; a first turbulence member that generates a turbulent flow in the first mixed gas located in first in-line mixer; and a second turbulence member that generates a turbulent flow in second mixed gas.    USE - The apparatus is useful for adjusting heating value of biogas (claimed).    ADVANTAGE - The apparatus uniformly adjusts the heating value of the biogas.    DETAILED DESCRIPTION - The apparatus comprises: a buffer tank; a first in-line mixer that is arranged within the buffer tank and comprises a first mixed gas, where the first mixed gas comprises biogas and the first external gas to be mixed; a second in-line mixer that is arranged within the buffer tank and comprises a second mixed gas, where the second mixed gas comprises biogas and the second external gas to be mixed; a first turbulence member that generates a turbulent flow in the first mixed gas located in the first in-line mixer; and a second turbulence member that generates a turbulent flow in the second mixed gas located in the second in-line mixer. The first and second turbulence members have funnel shape, and comprise multiple openings. Multiple helixes are formed on an inner surface of the turbulence member.
NOVELTY - The apparatus (100) has an inlet port (120) through which food waste plastic film is input. The food waste plastic film is passed through both side plates rotatably arranged along longitudinal direction of main portion (110). The upper portion of rotator (130) is equipped with multiple hammers. The bottom portion of rotator is equipped with cleansing water spray portion used for spraying washing water downward. A drain portion is used for draining emitted waste washing water, and the food waste plastic film is ejected. A partition wall is used for separating the two drain portions.    USE - Apparatus for cleaning vinyl bag of food garbage.    ADVANTAGE - The food waste contained in large amount is efficiently washed, and the fuel efficiency degradation of the solid fuel due to the food waste remaining after the food waste plastic film is manufactured is prevented. The environmental contamination is prevented, and improved economic effect is achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for cleaning vinyl bag of food garbage.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus for cleaning vinyl bag of food garbage. (Drawing includes non-English language text)    Apparatus for cleaning vinyl bag of food garbage (100)    Main portion (110)    Inlet port (120)    Rotator (130)    Hammer fixing plate (131)
NOVELTY - Separation and detection of ambrisentan and its analog involves performing isocratic high-performance liquid chromatography using long chain 8C or 18C alkyl group-bonded-column containing mixed solution comprising acetonitrile, water and glacial acetic acid as mobile phase with a flow rate of 0.5-1 ml/minute, and detecting using detector at detection wavelength of 190-230 nm. The detector is UV detector or diode array detector. The content of acetonitrile is 50-60%. The content of water is 40-50%. The content of glacial acetic acid is 0.1-0.5%.    USE - Separation and detection of ambrisentan and its analog (claimed).    ADVANTAGE - The method enables separation and detection of ambrisentan with excellent reproducibility, by simple, economical and environmentally-friendly process. The instrument used for separating ambrisentan has less noise. The separated ambrisentan has strong practicability.
NOVELTY - A biomass fuel caking preventing caking method involves performing chemical analysis of biomass ash and/or clinkering materials to determine content of non-combustible components in the form of oxides such as silicon dioxide, phosphorus pentoxide, potassium oxide, aluminum oxide, calcium oxide, magnesium oxide or iron oxide. The composition of biomass ash is plotted into a ternary phase diagram of potassium oxide, calcium oxide, silicon dioxide. The eutectic temperature of the biomass ash of the first melt formation is read out.    USE - Method of preventing caking of biomass fuel.    DETAILED DESCRIPTION - A biomass fuel caking preventing caking method involves performing chemical analysis of biomass ash and/or clinkering materials to determine content of non-combustible components in the form of oxides such as silicon dioxide, phosphorus pentoxide, potassium oxide, aluminum oxide, calcium oxide, magnesium oxide or iron oxide. The composition of biomass ash is plotted into a ternary phase diagram of potassium oxide, calcium oxide, silicon dioxide and/or a mixture of potassium oxide, sodium oxide, a mixture of calcium oxide, magnesium oxide, and a mixture of silicon dioxide and aluminum oxide. The eutectic temperature of the biomass ash of the first melt formation is read out.
NOVELTY - Producing pellet or block, comprises: mixing animal manure and coffee waste, and molding; mixing discarded starchy materials in coffee waste, and compressing at high temperature and high pressure; mixing wood chips and coffee waste, and molding to pellets; mixing at least one of coal, sewage sludge and house sludge with coffee waste, adding adhesive discarded starchy materials, and molding to pellets; mixing at least one of rice straw, rice husk and hay with coffee waste, and molding to pellet or block.    USE - The method is useful for producing pellet or block (claimed).    ADVANTAGE - The method produces high density pellet or block.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing coffee waste block, comprising mixing at least one of coal and sewage sludge with coffee waste, adding adhesive discarded starchy materials, and heating to greater than 80 degrees C to reduce moisture content to 20-70%.
NOVELTY - The ammonia nitrogen removal apparatus (100) has a re-cycling divider (150) that re-circulates anaerobic digester effluent to the acid fermenter (110) and hydrolysis tank (120). An alkali influx container (130) supplies strong base comprising sodium hydroxide or potassium hydroxide into hydrolysis tank in which strong base is stirred into effluent from the acid fermenter. The acid fermenter converts the oil and fat component of the organic wastewater into water-soluble components, generates methane and converts ammonia nitrogen into free ammonia.    USE - Apparatus for removal of ammonia nitrogen through re-cycling of anaerobic digester effluent.    ADVANTAGE - The recirculation of anaerobic digester effluent is optimally maintained, and the ammonia nitrogen is easily converted into free ammonia.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for removal of ammonia nitrogen through re-cycling of anaerobic digester effluent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view showing the arrangement of apparatus for removal of ammonia nitrogen through re-cycling of anaerobic digester effluent.    Apparatus for removal of ammonia nitrogen (100)    Acid fermenter (110)    Hydrolysis tub (120)    Alkali influx container (130)    Re-cycling divider (140)
NOVELTY - Preparation of solidified fuel involves drying water-containing natural acorn, compressing using compressor, drying obtained product, solidifying by compressing using compressor, and cutting the resultant product into predetermined size.    USE - Preparation of solidified fuel used as substitute for wood and charcoal for cooking meat.    ADVANTAGE - The method enables economical preparation of solidified fuel. The solidified fuel prevents discharge of harmful substances e.g. carbon monoxide during cooking.
NOVELTY - Chinese goosebeery foliar fertilizer having slow release function comprises 40-60 pts. wt. urea, 10-20 pts. wt. starch, 10-30 pts. wt. formaldehyde, 1-5 pts. wt. aspartic acid, 1-5 pts. wt. glycine, 1-5 pts. wt. methionine, 20-30 pts. wt. humic acid, 3-8 pts. wt. potassium dihydrogen phosphate, 20-50 pts. wt. potassium chloride, 1-5 pts. wt. borax, 5-10 pts. wt. ferrous sulfate, 10-15 pts. wt. zinc sulfate, 5-10 pts. wt. ammonium citrate, 2-15 pts. wt. calcium sulfate, 2-5 pts. wt. Trichoderma, 2-5 pts. wt. gibberellin, and 2-5 pts. wt. curing agent.    USE - Used as Chinese goosebeery foliar fertilizer having slow release function.    ADVANTAGE - The fertilizer realizes slow release of various element, thus supplying sufficient Chinese goosebeery growth nutrients; and increases Chinese goosebeery fruit rate to 89.78%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing Chinese goosebeery foliar fertilizer with slow release function comprising (i) mixing starch and water, pasting to obtain starch paste, adding urea and formaldehyde in the starch paste to obtain solution, (ii) preparing fertilizer granule: adding humic acid, potassium dihydrogen phosphate, potassium chloride, borax, ferrous sulfate, zinc sulfate, ammonium sulfate, and calcium sulfate into the solution, mixing to obtain slurry, adding curing agent and mixing to obtain fertilizer granule, placing the fertilizer granule in a fluidization bed, where the air inlet temperature is 40-50 degrees C, the air outlet temperature is 30-40 degrees C, and (iii) preparing special fertilizer: adding aspartic acid, glycine, methionine, Trichoderma and gibberellin in fluidization bed to obtain mixed fertilizer, i.e. fertilizer, where the fluidization bed nozzle pressure is 0.08-0.25pa, compressed air pressure is 0.5-0.75 pa, the rate of flow is 800-1200 ml/hour.
NOVELTY - The device has a biomass processing unit that is connected to a feeding unit. The housing is connected with a first collecting device and a second collecting device. The second collecting device is connected with a first condensing device. The first condensing device is connected with a filtering device. The filtering device is connected with a separating device. The separating device is connected with the second condensing device. A vacuum is formed in the inner portion of the housing.    USE - Biomass reaction device.    ADVANTAGE - Convection heat exchange of the biomass reaction device is ensured. The use range of the biomass reaction device is improved. The structure of the reaction device is simplified. The reaction efficiency of the reaction device is improved at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of the biomass reaction device.
NOVELTY - The device has a pre-processing system (1), a drying system (2), a whole pyrolysis furnace (4), an integrated combustion furnace (5), a combustion gas purification system (6), a carbon molding system (7) and a gas storage cabinet (8) that are mutually connected. A solar energy heat collector (9) is connected to a temperature adjusting system (3). The temperature adjusting system is used to control the heat flow in gas and other fluid, to control the temperature change, to control a fuzzy operation, and real-time control of each fluid flow.    USE - Multi-joint device of pyrolysis-gas combined circulation of biomass.    ADVANTAGE - The integral of the reaction process is controlled, and a continuous efficient production of high heat value gas and high temperature charcoal, wood tar and wood vinegar product is achieved. The full splitting of biomass and the valid target of product quality are achieved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a whole pyrolysis-gas combined circulation of biomass multi-joint method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-joint device of pyrolysis-gas combined circulation of biomass.    Pre-processing system (1)    Drying system (2)    Temperature adjusting system (3)    Whole pyrolysis furnace (4)    Integrated combustion furnace (5)    Combustion gas purification system (6)    Carbon molding system (7)    Gas storage cabinet (8)    Solar energy heat collector (9)
NOVELTY - A biomass oil is obtained by mixing dehydrated vegetable oil and dehydrated waste oil in mass ratio of 2-4:1 at 80 degrees C, and has carbon content and viscosity of 20% or more and 15 mm2/second or less, respectively.    USE - Biomass oil is used in non-ferrous smelting.    ADVANTAGE - The biomass oil is manufactured by simple and economical process, with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biomass oil.
NOVELTY - Preparation of rosuvastatin calcium (I) involves preparing chiral diol by microbial fermentation, preparing chiral side chain and condensing resultant product with calcium salt.    USE - Preparation of rosuvastatin calcium (claimed).    ADVANTAGE - The method enables efficient, environmentally-friendly and economical preparation of non-toxic atorvastatin calcium with reduced energy consumption.    DETAILED DESCRIPTION - Preparation of rosuvastatin calcium of formula (I) involves preparing chiral diol by microbial fermentation, preparing chiral side chain and condensing resultant product with calcium salt.
NOVELTY - This utility new type claims a one new biomass reaction device, comprising the biomass processing unit, a feeding unit and reaction device, a biomass between processing unit, a feeding unit and a react mutually connected, a new biomass reaction device further comprises a reaction device and a phase of a reaction device for discharge of the first collecting device and used for reaction device for feeding a second collecting device, said collecting device further and the first condensing device is connected, the condensing device and the filtering device are connected. Through a way, this utility new type is a one new biomass reaction device, by means of a condensing and collecting device and a device for rapid heating of biomass, and a convection heat exchange, so the use range is wider, and it can make the product in time, a good effect.
NOVELTY - This new utility model claims of one of sludge production can use fuel gas and pyrolysis gasification device, the device main body as one closeness straight shell, upper shell end connected with one bell jar structure and feedstock port, lower end shell of the slag plate, with water between the slag plate and sealing shell, inner shell wall is concave-convex shape, one solid is installed on shell internal centre guide column, guide column with shape of guide groove, shell bottom inner cavity forming section drying, distillation, carbonizing section, gasification section and combustion section, wherein the inner wall of the combustion section setting one water cold cavity, respectively installed with temperature measuring sensor in shell outside the distillation, carbonizing section, gasification section and combustion section, this utility new type single gasification device can daily processing 200 ton water-containing rate less than 60% of sludge, sludge treatment and realize reduction, harmless and energy, operation cost is low, the automatic operation and management can save a lot of manpower and cost of one ton water-containing rate less than 30% and average sludge can generate gasification 1600Nm3 fuel gas can.
NOVELTY - 5-Nitro-2-(propylsulfanyl)pyrimidine-4,6-diol (II) is reacted in presence of phase transfer agent, chlorinating agent or brominating agent to obtain 5-nitro-2-(propylsulfanyl)pyrimidine (I).    USE - Preparation of ticagrelor used as anticoagulant.    ADVANTAGE - The method provides 5-nitro-2-(propylsulfanyl)pyrimidine with high yield and high purity by economical and environmentally-friendly process. The method reduces the amount of halogenating agent and reduces the emission of toxic substances.    DETAILED DESCRIPTION - 5-Nitro-2-(propylsulfanyl)pyrimidine-4,6-diol of formula (II) is reacted in presence of phase transfer agent, chlorinating agent or brominating agent to obtain 5-nitro-2-(propylsulfanyl)pyrimidine of formula (I).    R=Cl or Br.    An INDEPENDENT CLAIM is included for intermediate of (1S,2S,3R,5S)-3-(5-amino-6-bromo-2-propylsulfanyl-pyrimidin-4-ylamino)-5-(2-hydroxy-ethoxy)-cyclopentane-1,2-diol and (1S,2S,3R,5S)-3-(7-bromo-5-propylsulfanyl-(1,2,3)triazolo(4,5-d)pyrimidin-3-yl)-5-(2-hydroxy-ethoxy)-cyclopentane-1,2-diol.
NOVELTY - The apparatus has a multi-division pass station (120) arranged in a central part of a main body (110). The main body is formed with a through hole (121). A cooling part (130) supplies cooling water to the main body using pumping of a feed pump (140) through a feed line (141). A biogas transfer line supplies biogas to a biogas required place. A desulfurizer removes sulfide in the biogas of the biogas transfer line for removes moisture in the biogas, and is arranged between the biogas transfer line and a dehumidifier. The dehumidifier dehumidifies the moisture removed biogas.    USE - Apparatus for removing moisture of biogas in a biogas utilization power generation plant.    ADVANTAGE - The apparatus rapidly removes the moisture of the biogas generated in a biogas utilization power generation plant even when structure is in simple. The apparatus reduces energy consumption during moisture removing operation and improves moisture elimination efficiency. The apparatus utilizes the biogas for power generation in a biogas marine boiler so as to improve service life of the biogas marine boiler. The apparatus reduces length of the biogas transfer line and construction cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for removing moisture of biogas.'(Drawing includes non-English language text)'    Main body (110)    Division pass station (120)    Through hole (121)    Cooling part (130)    Feed pump (140)    Feed line (141)
NOVELTY - Heavy-metal-containing sewage sludge is sterilized and deodorized by preprocessing sludge until water content is 90-95%, adding biogas liquid to sewage, extracting nicotine or solanesol tobacco residue, performing solvent method to extract lignin from plant raw material, using stir machinery under electromagnetic wave effect for 20-40 minutes to obtain mixed liquid, performing solid-liquid separation and washing with water to obtain dry sludge slag and filtrate, separating, recycling clear liquid to sewage processing system, and performing heavy metal slag refining.    USE - Sterilization and deodorization of heavy-metal-containing sewage sludge (claimed).    ADVANTAGE - Method has low energy consumption and short processing time and is low-cost and environment-friendly.    DETAILED DESCRIPTION - Heavy-metal-containing sewage sludge is sterilized and deodorized by preprocessing sludge until water content is 90-95%, adding biogas liquid to sewage, extracting nicotine or solanesol tobacco residue, performing solvent method to extract lignin from plant raw material, using stir machinery under electromagnetic wave effect for 20-40 minutes to obtain mixed liquid, performing solid-liquid separation and washing with water to obtain dry sludge slag and filtrate, processing stored dry sludge slag into organic fertilizer, building material, and/or fuel, controlling pH of filtrate to 6-8.5 using lime, adding 8-12 g calcium sulfide (CaS) per cubic meter and stirring for 25-35 minutes to separate heavy metal, separating by machinery filter to obtain clear liquid and heavy metal residue, recycling clear liquid to sewage processing system, and performing heavy metal slag refining to recover heavy metal in which mass ratio of biogas liquid, tobacco residue, lignin, and sewage is 100-1000:1-2:1-2:1000-10000.
NOVELTY - Preparing acetic acid involves inoculating anaerobic acetogenic bacteria in substrate and microelement nutrient solution in a reactor and then stirring to obtain mixture. Oxygen is removed from reactor and then mixture is fermented to obtain the product.    USE - Method for preparing acetic acid (claimed).    ADVANTAGE - The method enables to produce acetic acid in efficient manner with utilization of waste resources.
NOVELTY - The solid fuel comprises a main body having right and left sides, front and back surfaces and upper and lower surfaces facing each other. The solid fuel is made of wood, and is formed on a main alcoholic fermentation groove having a predetermined surface depth with a fermentation alcohol. A perforation part of the fermentation groove is provided with an angular side of the main body, so that two sides of the main body are connected with each other. An end of the perforation part is mounted on a central part of the main body.    USE - The solid fuel is useful for cooking or heating in camps.    ADVANTAGE - The solid fuel is simple to produce with high yield and compact size, and is cost-effective.    DETAILED DESCRIPTION - The solid fuel comprises a main body having right and left sides, front and back surfaces and upper and lower surfaces facing each other. The solid fuel is made of wood, and is formed on a main alcoholic fermentation groove having a predetermined surface depth with a fermentation alcohol. A perforation part of the fermentation groove is provided with an angular side of the main body, so that two sides of the main body are connected with each other. An end of the perforation part is mounted on a central part of the main body. The fermentation groove is equipped with top and bottom portions of the main body. An exposed elongated groove is provided with the front and back surfaces of the main body. The elongated groove has multiple sections that are separately arranged with each other so that the solid fuel is formed with different thickness. The fermentation groove is a cross shaped fermentation groove. A fermentation alcohol supplying unit is arranged on an upper side of the main body. An INDEPENDENT CLAIM is included for a method for preparing a solid fuel.
NOVELTY - Invention relates to agriculture. The method comprises recovering the useful product, primarily soluble biodigestible sugars, and the subsequent disposal of lignocellulosic wastes. Upon extraction of useful product the straw of grain crops is subjected to deep processing, namely dispersion and fermentation. Lignocellulosic wastes after extraction of useful product are subjected to additional crushing to a particle size less than five microns. Then they are mixed with the gaseous fuel and combusted in the combustion chamber of a gas turbine plant for generating electrical and heat energy. At that the electrical and heat energy obtained in the process of combustion is used directly in the process of deep processing of straw. The useful product in the form of nanostructured carbohydrate powder is used as raw material for production of biofuel.    USE - Agriculture.    ADVANTAGE - Invention enables to recycle by waste-free way the straw to obtain valuable nanostructured powder and simultaneous generation of heat and electrical energy.5 cl, 1 dwg
NOVELTY - Method of biological purification of sewage water with active silt is realised with application of biologically active substance, which is represented by powder-like substance UWDM-1, containing rotaxane molecules and binuclear copper complex, in amount, providing its concentration in bioreactor, equal 10-6-1.10-10 mg/dm3. Device for method realisation consists of hermetic case (1) with branch pipes of input (2) of sewage water, discharge (3) of purified water, discharge of biogas (4), coaxially located in case hollow central tube (5) with branch pipes of supply (6) and discharge (7) of heat-carrier, means for supply of biologically active substance. Means for supply of biologically active substance is made in form of mixer with drive (8), provided with dosing devices (9) in upper part, and in lower part connected by means of pipeline (1) with upper part of case (1). Central tube (5) is separated by not less than two transverse nets (11), covered with porous material (12). Holes (13) of nets (11) are located with displacement relative to each other.    USE - Chemistry.    ADVANTAGE - Increased efficiency of purification.2 cl, 1 dwg, 1 ex
NOVELTY - The gasifier has a preheated section for separating moisture included in fuel, and a reactor for gasifying the fuel, where the moisture separated from the preheated section is combustion-reacted in the reactor. Another reactor reforms synthetic gas generated in the former reactor. The fuel is selected from bio pyrolysis oil, disposable edible oil, lubricating oil waste or colloidal fuel. A delivery tube delivers the moisture separated from the fuel to the latter reactor while being connected between the preheated section and the latter reactor.    USE - Multi-stage gasifier.    ADVANTAGE - The gasifier increases the reaction time by supplying only the fuel element in which moisture is removed, thus improving gasification efficiency of the multi-stage gasifier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a multi-stage gasifying method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a multi-stage gasifier. '(Drawing includes non-English language text)'
NOVELTY - Decomposing lignin comprises culturing Asticcacaulis silvisoli CGM1-3EN strain.    USE - The method is useful for decomposing lignin (claimed), which is useful in the production of biofuel.
NOVELTY - Biogas plant includes vertical sealed cylindrical tank (1) equipped with dome (3) and bottom (4), which have a shape of a flattened cone. Bottom (4) is installed with its smaller base downwards, and with dome (3), vice versa, upwards. The external part of the tank and bottom (4) is wound with heating strip (5) connected to temperature control (6). Inside tank (1) there is a mixing device representing two-bladed agitators (8) installed perpendicular on horizontal shaft (7). Shaft (7) is offset downwards from the centre of tank (1). Blades (9) of agitator (8) have a meshed structure of a trapezoid shape, which converges towards the axis of shaft (7). Span of blades (9) located in the centre of the shaft is larger than that of the adjacent blades.    USE - Power industry.    ADVANTAGE - Enlarging the range of plants for processing of organic wastes of agricultural production; obtaining a disinfected biological fertiliser without any smell, which can be used as a fertiliser without any additional operations.2 dwg
NOVELTY - Producing biofuel oil for power generation, comprises reacting more than 5% of fatty acids and vegetable oils or animal oils in an alcohol in the presence of acid catalyst and converting into fatty acid alkyl esters, recovering the alcohol from the reaction product, and performing purification to remove the water and the catalyst from the reaction product.    USE - The method is useful for producing biofuel oil for power generation (claimed).    ADVANTAGE - The method ensures efficient and economical production of large amount of biofuel oil without emission of carbon dioxide.
NOVELTY - Pellets comprise 1-5 wt.% palm kernel expeller (PKE), and 95-99 wt.% palm byproduct chosen from palm kernel shell (PKS), palm empty fruit bunch (EFB), oil palm trunk (OPT) and oil palm frond (OPF), where the pellet is dehydrated at 70-100 degrees C, until the water content becomes less than 10 wt.%, and has initial deformation temperature (IDT) of greater than or equal to 1150 degrees C.    USE - The pellets are useful as renewable fuel (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation method of the above-mentioned pellets, which involves mixing raw materials, compressing mixture, preparing the mixture into pellets, and drying the pellets at 70-100 degrees C to obtain pellets having less than 10 wt.% water content.
NOVELTY - Solid fuel manufacturing device comprises a sludge storage tank (100) for accommodating the sludge, a first dryer (200) for lowering the moisture content of the sludge accommodated in the sludge storage tank, a molding machine containing at least one pair of drums spaced apart from each other for molding sludge dried from the first dryer into certain form, a releasing agent providing unit for providing the releasing agent to the pair of drums without sticking the sludge to the drums, and a second dryer for lowering moisture content of the molded sludge to less than or equal to 10%.    USE - Used as a solid fuel manufacturing device.    ADVANTAGE - The device is economical, continuously produces solid fuel, and avoids sticking of the sludge to the molding machine by utilizing the releasing agent.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) manufacturing solid fuel using sludge, comprising (a) primarily drying to reduce the moisture content of the sludge to less than or equal to 20-30%, (b) crushing the primarily dried sludge, (c) introducing the crushed sludge into the molding machine, and molding (solidifying) the sludge by mixing the release agent into the sludge such that the total weight is less than or equal to 5%, and (d) producing the solid fuel by the secondarily drying the molded sludge to reduce the moisture content to less than or equal to 10%; and    (2) solid fuel prepared by the above method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the solid fuel manufacturing device.    Sludge storage tank (100)    Hopper (110)    First dryer (200)    Conveyor (221)    Moisture discharging unit (230)
NOVELTY - Stabilizing anaerobic digestion system, comprises (i) introducing activated sludge containing anaerobic groups in an anaerobic digestion tank containing anaerobic digestion reaction mixtures, (ii) primary adding substrate mixtures containing monosaccharides, polysaccharides and oligosaccharides into the anaerobic digestion tank, and (iii) further adding the substrate mixtures.    USE - The method is useful for stabilizing anaerobic digestion system (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the method for stabilizing anaerobic digestion system (Drawing includes non-English language text).
NOVELTY - The apparatus has horizontal auger tube that is provided with inlet for a heat carrier and a second inlet for biomass. A first outlet is provided for pyrolysis gas and a second outlet is provided for heat carrier and transformed biomass. An inclined auger tube is arranged with an inlet at or below the second outlet of first auger tube, to receive the heat carrier and transformed biomass from the second outlet of first auger tube and an outlet communicating with the first inlet, so as to deliver heat carrier.    USE - Apparatus for pyrolysis of organic material biomass for producing solid, liquid and gas pyrolysis products.    ADVANTAGE - The horizontal reactor removes most of the volatile matter while the second, inclined auger reactor, allows for a longer contact time and removal of the remaining volatile matter under slow pyrolysis conditions.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the self contained fast pyrolysis system.    Pitch (1)    Reactor tube (2)    Inclined tube (3)    Cyclone (6)    Storage (8)
NOVELTY - A solid fuel composition comprises 34.8 vol.% or more coffee waste component, 34.8 vol.% or more wood dust component, and 26.1 vol.% or more adhesive for binding the coffee waste component and the wood dust component. The coffee waste component comprises 40 wt.% or less water.    USE - Solid fuel composition is used for formation of spherical pellets (claimed) used in stoves.    ADVANTAGE - The solid fuel composition enables formation of spherical pellets having excellent durability and fluidity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for formation of spherical pellets, which involves mixing coffee waste component, wood dust component, and the adhesive, to form a fuel composition mixture, extruding the fuel composition mixture to form one or more elongate units, receiving one or more elongate units of the fuel composition mixture, positioning one or more elongate units between a pair of grooved rollers, in which each grooved roller comprises grooves and each of grooves on each of the rollers is aligned respectively with another grooves on the other roller, and rotating the grooved rollers to cut and compress the one or more elongate units into spherical pellets.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of system for forming spherical pellets.    System (20)    Mixer (22)    Extruder (24)    Redirection device (28)    Forming device (30)
NOVELTY - Manufacture of non-shaped biofuel involves grinding coffee sludge, dehydrating coffee sludge powder to water content of less than 10 wt.%, separating water by passing through compression roller at a pressure of 500-5000 kgf/cm, storing pressed coffee sludge oil, accumulating coffee sludge powder to thickness of 30 mm, drying to water content of less than 7 wt.% by passing through portable hot-air dryer, cooling to 90-100 degrees C, coating coffee sludge pressed oil on surface of cooled coffee sludge by spraying and filling resultant product in moisture-proof packaging bag.    USE - Manufacture of non-shaped biofuel (claimed) used for power generation.    ADVANTAGE - The method enables manufacture of non-shaped biofuel having high efficiency, using environmentally-friendly coffee sludge.    DETAILED DESCRIPTION - Manufacture of non-shaped biofuel involves grinding coffee sludge, dehydrating coffee sludge powder to water content of less than 10 wt.%, separating water by passing through compression roller at a pressure of 500-5000 kgf/cm, storing pressed coffee sludge oil, accumulating coffee sludge powder to thickness of 30 mm, drying to water content of less than 7 wt.% by passing through portable hot-air dryer, cooling to 90-100 degrees C, coating coffee sludge pressed oil on surface of cooled coffee sludge by spraying, and filling resultant product in moisture-proof packaging bag. The amount of coffee sludge pressed oil is 0.01-0.3 pts. wt. with respect to 100 pts. wt. cooled coffee sludge powder.
NOVELTY - A solid fuel composition is prepared by crushing cow pats with width, length and height of 120 mm, injecting used cooking oil or disposable edible oil, and baking at 200-400 degrees C for 30-200 seconds.    USE - Solid fuel composition (claimed).
NOVELTY - The equipment has a gas exhaust port (106) that is formed in the bottom side of a reactor (100). A dry zone (101), a thermal area (102), an oxidative region (103) and a reducing zone (104) are formed in the reactor from the upper side of the internal space in which the biomass (108) is filled. The synthetic gas (105) ejected from the reducing zone and the water supplied from the outside are heat-exchanged in a heat exchange unit (400). The wood composite biomass is put into the reactor in the anoxic condition for producing the half carbonization fuel.    USE - Half carbonization fuel production equipment.    ADVANTAGE - The biomass including timber is produced easily with the half carbonization. The carrying of the biomass material is facilitated easily, if the biomass material is made the pellet form storage so that the generation efficiency is improved. The harmful insect flowing into the foreign country is blocked conveniently before supplying the imported wood material to each generating station.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the half carbonization fuel production equipment. (Drawing includes non-English language text)    Reactor (100)    Dry zone (101)    Thermal area (102)    Oxidative region (103)    Reducing zone (104)    Synthetic gas (105)    Gas exhaust port (106)    Biomass (108)    Heat exchange unit (400)
NOVELTY - Invention relates to pyrolysis of timber and its wastes and the other renewable organic stock. Proposed device comprises furnace connected with pyrolysis chamber, cylindrical retorts with gas collecting elements at the bottom connected via gas discharge pipes with said furnace. Said furnace is isolated from pyrolysis chamber by perforated wall. Said chamber is divided by perforated walls into compartments to house at least two retorts. Note here that wall lower part has at least one opening to receive refractory element with through holes wherein fitted are gas discharge pipes. Ends of gas discharge pipes are arranged at the refractory element centre. Plane of the latter wherein terminate through holes is located at the angle to furnace hearth. Pyrolysis chamber compartment adjacent to furnace can be connected via gas line with one of compartments at mid part of pyrolysis chamber. Furnace top part is shaped to curved arch. Hollow cylindrical element with cover of ID larger than retort OD can be fitted at top cover of every compartment of pyrolysis chamber. Note here that compartment top cover is composed of two parallel metal sheets with spacing communicated with atmosphere and inner chamber of the compartment.    USE - Process engineering.    ADVANTAGE - Accelerated pyrolysis, ruled out gas discharge pipe destruction, simplified design.4 cl, 6 dwg
NOVELTY - Invention is referred to remediation of oil-contaminated soils, in particular, to soil cleanup from oil pollution. The invention may be used for restoration of oil-contaminated soils in high north conditions. In order to restore soils from oil pollution poultry manure is introduced upon application of probiotics with strains of Bacillus subtilis TNP-3-DEP and Bacillus subtilis TNP-5-DEP to poultry.    USE - Oil and gas industry.    ADVANTAGE - Invention allows reducing oil concentration in soil during 3 months of summer period.
NOVELTY - Biogas unit contains heat insulated methane tank, consisting of an extruder mixer, electric biomass mixers, pumps, chambers of hydrolytic, acid and methane fermentation, each is fitted with a heat exchanger. To the outlet of the methane tank, to the methane fermentation chamber the gas-holder and the fermented mass separator are connected. The biogas unit is fitted with the unit of sources of renewable and other currently excessive energies in networks. The unit of sources of renewable and other excessive energies comprises the thermal accumulator fitted with heat exchangers, fire-bar elements and a generator; this thermal accumulator is connected to sources of renewable energy and mains. Meanwhile the heat accumulator inlet for make-up water is connected to the line, and hot water outlets of the heataccumulator are connected to an extruder mixer and fermentation chambers. Heat accumulator's fire-bar element by means of electric energy switches is connected to electric mixers, pumps and the extruder mixer or to the generator with a possibility of operation of the latter from the sources of renewable energy or in case of their absence - from the mains during the time period of low tariffs for payment of the electric power.    USE - Power engineering.    ADVANTAGE - Increase in biogas production due to providing the optimum modes of continuous fermentation of biomass in zones of cold climate with the long heating period.4 cl, 1 dwg
NOVELTY - The method involves sending multiple types of organic waste (1) to a mixer/homogenizer (2). The organic waste is carried out to an anaerobic bio-digester (3). The collected waste is sent to multiple acceleration devices (4). Final amount of methanogenic bacteria fraction leaving the acceleration devices are returned to the anaerobic bio-digester. The organic waste is mixed and distributed in entry sections of the anaerobic bio-digester. The organic waste is processed for successive cycles of duration.    USE - Method for producing biogas with high-methane content from organic waste to generate electricity.    ADVANTAGE - The method enables stabilizing microbiological activity in the organic waste, so that methane content in the organic waste is enhanced and accelerated, thus facilitating production of increased and stabilized quantity of the biogas with high methane content.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing biogas with high-methane content from organic waste to generate electricity.    Organic waste (1)    Mixer/homogenizer (2)    Anaerobic bio-digester (3)    Acceleration devices (4)    Expert system (5)
NOVELTY - Composition comprises 60% ethylhexyl nitrate, 20% naphtha, 10% fatty alcohol alkoxylates, 10% fatty acid condensate, solvent and descaling agent.    USE - Composition for formulation of liquid additive for biofuels (claimed).    ADVANTAGE - The composition minimizes issuance of pollutants such as hydrocarbons and carbon monoxide.
NOVELTY - Electroflotator contains case with branch pipes for supply of sewage and discharge of pure water and a branch pipe for discharge of foam, as well as anode and cathode placed in case. Case is divided into electroflotation chamber and chamber of after-purification with catalyst vertical partition and lower overflow, in upper part of electroflotation separate compartment is made for hydrogen accumulation, in upper part of after-purification chamber special compartment is made for accumulation of oxygen, which are provided with discharge pipelined of hydrogen and oxygen respectively. Cathode and anode are placed perpendicularly to each other in electroflotation chamber. Anode is cylinder-shaped, and is located on vertical axis of chamber, cathode is made in form of net and is located below anode horizontally. Gas-distributing grid with charge for catalyst located on it is rigidly fixed in lower part of after-purification chamber.    USE - Chemistry.    ADVANTAGE - Increased efficiency of sewage water purification from emulsified organic substances.1 dwg
NOVELTY - This new utility model relates to one of water electrolysis hydrogen device of comprehensive treatment device, belonging to hydrogen or oxygen the electrolytic water technology area. Bottom of the device tank body has gas import, supplement the water outlet overflow pipe extends to gas-liquid separator bottom, lower part of jar body equipped with external interconnect and the supplement water import, middle part of jar body equipped with relux component, upper part of tank body set with drop catching net. The water electrolysis hydrogen device of comprehensive processing device aiming at the existing technology for integration and, for water electrolysis hydrogen process in multi-steps collective, the invention provides one kind of water electrolysis hydrogen process at the same time in gas to carry out washing, cooling, system to supplement water and comprehensive treatment device, implement multifunction integrated, decrease electrolytic water hydrogen manufacture device the total floor area, saving cost and increase device whole space utilization rate.
NOVELTY - The method involves carrying-out dilution of a high viscosity output substrate with fermenter contents so as to reduce viscosity of the substrate by degradation processes in the fermenter. Fresh output substrate and the fermenter contents are mixed with one another by a hydraulic flow and by a gas injecting process. A blowing equipment (3) is arranged at an inlet (2) of the output substrate to blow the mixture of the output substrate and the fermenter contents. The blowing equipment is designed as a downwardly bent jacket tube (9) that is closed at a lower end.    USE - Method for depositing heavy components e.g. sand, splits and stones (all claimed), from a high viscosity output substrate of a biogas plant.    ADVANTAGE - The method enables carrying-out dilution of the high viscosity output substrate with the fermenter contents so as to reduce the viscosity of the substrate by the degradation processes in the fermenter such that the heavy components can be effectively deposited from the starting substrate without compromising efficiency of the degradation processes in the biogas plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for depositing heavy components from a high viscosity output substrate of a biogas plant for separating of components.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic side and plan views of a depositing device with a funnel-shaped equipment.    Inlet (2)    Blowing equipment (3)    Pipe (6)    Gate valve (7)    Downwardly bent jacket tube (9)
NOVELTY - The apparatus has a conveyor that moves in the specific direction. A slurry coating unit is placed in the upper portion of the conveyor, for coating the film with the slurry for electrode metallization. A heat treatment unit is placed in the upper portion of the conveyor, for heating the slurry coated on the film by rapid thermal annealing in hydrogen and argon environment.    USE - Apparatus for manufacturing solid oxide fuel cell.    ADVANTAGE - The electrode of solid oxide fuel cell is manufactured quickly by coating slurry on film and heating the coated slurry with the rapid thermal anneal processing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the method for producing solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid oxide fuel cell manufacturing apparatus.
NOVELTY - Double-stage continuous underground generator of biohydrogen includes a biogenerator installed in the ground, filled to a certain level with biomass, a gas discharge pipe and a pipe for removal of residual biopulp. The biogenerator comprises two bioreactors, arranged in the ground at the depth of up to 2000 m, connected in series by working medium. In the proposed device there are systems for self-flowing charging and discharging of bioreactors under action of gravity of a column of input biomass and gaslift effect of methane and hydrogen biopulps, a system of acidification of methane biopulp, a system of sowing microfauna supply and a system of supply of biostimulant at the initial section of the bioreactor core of the 2nd stage.    USE - Power engineering.    ADVANTAGE - Optimal temperature conditions of reactions of anaerobic transformation of biomass, makes it possible to produce high-pressure biohydrogen at the outlet of the plant, develops conditions for self-flowing charging of a bioreactor with biomass, gaslift discharging of biohydrogen and residual biopulp.
NOVELTY - A compost is prepared by taking rotten compost, kitchen garbage and straw, mixing, and carrying out aerobic fermentation.    USE - Method for preparing compost used for reducing greenhouse gas emission (claimed).    ADVANTAGE - The method is simple and low-cost. The compost has soft texture, strong absorbing ability, and rich in methane and nitrite.
NOVELTY - A functional bioorganic base fertilizer is prepared using chicken excrement by selecting chicken manure with stick length of 5 mm, crop straw as bottom fertilizer with stick length of 5-8 mm, drying, and absorbing.    USE - Method for preparing functional bioorganic base fertilizer using chicken excrement (claimed).    ADVANTAGE - The method establishes efficient decomposing technology and aerobic fermentation technology system, livestock and poultry excrement treatment time, increases production efficiency, fundamentally ensures fermentation effect through microorganism different temperature area growth, effectively removes excrement smell, and rapidly decomposes livestock and poultry excrement waste for 7-10 days.
NOVELTY - An organic fertilizer is prepared using dry branches and fallen leaves municipal waste by cutting and crushing green waste branches, measuring water content, adding composite microorganism microbial inoculum, additive, urea and monopotassium phosphate, mixing uniformly, adding water, and piling; and starting, raising temperature, composting, controlling temperature, maturing, determining 52-54.6% organic matter, 1.8-1.92% nitrogen, 1.05-1.7% phosphorus pentoxide, 1.3-1.5% potassium oxide, 30-35% water content and pH value of 7.5, and fermenting.    USE - Method for preparing organic fertilizer using dry branches and fallen leaves municipal waste (claimed).    ADVANTAGE - The method is simple, improves soil, and reduces waste and pollute.    DETAILED DESCRIPTION - An organic fertilizer is prepared using dry branches and fallen leaves municipal waste by cutting and crushing green waste branches into 3-5 cm, measuring water content, adding 0.1-0.2 wt.% composite microorganism microbial inoculum, 1-3 wt.% additive, urea and monopotassium phosphate, mixing uniformly, adding water, adjusting water content to 60-70%, and piling at 1.5-2 m high; and starting at 10 degrees C, raising temperature to 60 degrees C, composting, controlling temperature at not greater than 70 degrees C, maturing for 18-22 days, or starting at less than 10 degrees C, raising temperature to 65 degrees C, controlling temperature at not greater than 65 degrees C, maturing at 28-32 days, determining 52-54.6% organic matter, 1.8-1.92% nitrogen, 1.05-1.7% phosphorus pentoxide, 1.3-1.5% potassium oxide, 30-35% water content and pH value of 7.5, and fermenting. The composite microorganism microbial inoculum is Aspergillus niger, Saccharomyces cerevisiae yeast, Bacillus subtilis and Trichoderma reesei at mass ratio of 2:1:2:2. The additive is wheat bran, rice husk or peanut shell powder.
NOVELTY - Rubber tree special fertilizer comprises greater than or equal to 7.5 wt.% total of nitrogen (N), phosphorus (P) and potassium (K), greater than or equal to 45% organic material, and less than or equal to 30 wt.% water. The weight ratio of N, P and K is 2:4-5:0.8-1.2.    USE - Special fertilizer for rubber tree (claimed).    ADVANTAGE - The special fertilizer meets nutrient needs of seedlings after planting, improves survival rate of seedlings, and reduces dosage of chemical fertilizer and fertilization frequency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by mixing fresh chicken manure, fresh pig manure and calcium superphosphate, controlling water content at 50-60 wt.%, and uniformly spraying fermentation agent; controlling temperature at 65-75 degrees C, preferably 70 degrees C by turning and continuously fermenting for 15-20 days, preferably 18 days; and determining moisture index. If water content is less than or equal to 30 wt.%, fermentation is completed. If water content is more than 30 wt.%, drying is performed until water content is less than or equal to 30%.
NOVELTY - A 4,5-dihydroxy-2-methylbenzoic acid compound (I) is prepared by mixing 2-methylbenzoic acid derivative (II) and alcohol as solvent, performing catalytic hydrogenation, and reacting at 20-90 degrees C for 1-6 hours under 1-4 atmospheres.    USE - Method for preparing 4,5-dihydroxy-2-methylbenzoic acid compound (claimed).    ADVANTAGE - The method is safe, and environment-friendly. It has high yield, and low cost.    DETAILED DESCRIPTION - A 4,5-dihydroxy-2-methylbenzoic acid compound of formula (I) is prepared by mixing 2-methylbenzoic acid derivative of formula (II) and alcohol as solvent, performing catalytic hydrogenation, and reacting at 20-90 degrees C for 1-6 hours under 1-4 atmospheres.
NOVELTY - Preparation of ligustrazine from rhizoma ligustici wallichii using supercritical carbon dioxide comprises crushing rhizoma ligustici wallichii, supercritical carbon dioxide extracting at 40-70 degrees C, adding modifier, extracting for 1-2 hours, adding glycerin fatty acid ester, dissolving in methanol, performing chromatography, discarding eluate and performing solvent recovery.    USE - Method for preparing ligustrazine from rhizoma ligustici wallichii using supercritical carbon dioxide (claimed).    ADVANTAGE - The preparation method is simple, environment-friendly and suitable for industrial production.
NOVELTY - Brevibacillus brevis strain H3 with preservation number CCTCC No. M 2013481 is new.    USE - B. brevis strain H3 with preservation number CCTCC No. M 2013481 for preparation of decomposing microbial inoculant (claimed) used for efficient fermentation of animal waste and organic fertilizer.    ADVANTAGE - B. brevis is environment-friendly, grows rapidly, breaks down protein and fat, and has high lipase activity.
NOVELTY - Pesticide application for peas comprises foliar spraying first pesticide composition at jointing stage and foliar spraying second pesticide composition at heading stage. The first pesticide composition comprises hexaconazole aqueous dispersion, streptomycin, copper sulfate, triazolone, bismerthiazol, mepiquat chloride, and water. The second pesticide composition comprises bismerthiazol aqueous dispersion, carbendazim aqueous dispersion, streptomycin, 4-iodo-phenoxyacetic acid, ammonium molybdate, and water.    USE - Method for pesticide application for peas (claimed).    ADVANTAGE - The method saves pesticide, increases efficacy and reduces pesticide dosage, and reduces pesticide residues in crops and pollution.    DETAILED DESCRIPTION - Pesticide application for peas comprises foliar spraying first pesticide composition at jointing stage and foliar spraying second pesticide composition at heading stage. The first pesticide composition comprises, per mu, 9 g 30 wt.% hexaconazole aqueous dispersion, 10 g 20 wt.% streptomycin, 20 g copper sulfate, 18 g 25 wt.% triazolone, 12 g 50 wt.% bismerthiazol, 5 g 98 wt.% mepiquat chloride, and 50 kg water. The second pesticide composition comprises, per mu, 10 g 30 wt.% bismerthiazol aqueous dispersion, 30 g 50 wt.% carbendazim aqueous dispersion, 15 g 20 wt.% streptomycin, 8 g 98 wt.% 4-iodo-phenoxyacetic acid, 20 g 35 wt.% ammonium molybdate, and 50 kg water.
NOVELTY - The catalyst includes active carbon as carrier, cobalt, and nickel as active components, and zirconium, potassium and magnesium as co-catalyst components. The activated carbon is fruit shell active carbon, wood active carbon, straw active carbon, lignite active carbon or other active carbon.    USE - Catalyst for reforming methane and carbon dioxide gas.    ADVANTAGE - The catalyst has strong carbon dioxide absorbing ability, and enhanced catalytic property and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing catalyst, which involves:    (A) immersing particles of activated carbon in concentrated ammonia;    (B) washing with distilled water repeatedly;    (C) drying in an oven and microwave at room temperature to obtain a modified activated carbon;    (D) mixing the modified activated carbon with an organic binder uniformly;    (E) grounding the mixed material in a mortar uniformly;    (F) heating the mixture at 75 degrees C in a tube furnace under nitrogen atmosphere to obtain an electrode sheet;    (G) connecting the electrode sheet by using a good conductor to power supply to metal nitrate actives salt solution to obtain a catalyst precursor; and    (H) reducing catalyst precursor in hydrogen atmosphere at 55 degrees C to get catalyst.
NOVELTY - The method involves fermenting an organic waste for more than half a day at a temperature range of 50-80 degrees C. The organic waste processed by fermenting is degreased, by applying pressure on organic waste, so that the fat and oil are separated. The degreasing of organic waste is performed within the housing of a processing apparatus (A).    USE - Method for processing target object such as waste material and organic refuse.    ADVANTAGE - The quantity of fat and oil is reduced and the easily reusable organic substance is obtained from the organic waste. By forming opening in the upper portion of the partition wall, the process target object is introduced from upper direction to the degreasing tank, so that smoothing of introduction of process target object is attained. Since the big lump which cannot pass through the opening, and the process target object of fiber remain are stirred in the processing tank, the refinement is accelerated. The power-saving effect is attained by using the exhaust-gas used for heating deodorizing. The efficiency of degreasing is increased, as a result of fermenting processed material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a processing apparatus; and    (2) a treatment device.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view showing the internal structure of the processing apparatus.    Storage tank (10)    Processing tanks (11,12)    Drying/deodorizing unit (30)    Hopper (55)    Roller (60)
NOVELTY - An agricultural composition comprises a lignocellulosic syrup; and a soil conditioning material.    USE - The agricultural composition is used for conditioning soil (claimed).    ADVANTAGE - An agricultural composition that is easily handled and applied and additional materials that are readily available from renewable resources, which can be used as binders in soil conditioners, are provided.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a process for producing an agricultural composition by combining the lignocellulosic syrup with the soil conditioning material, where pellets or granules comprising the syrup and the conditioning material are produced; and    (2) a method for conditioning soil by applying the agricultural composition above to the soil.
NOVELTY - Method for production of agent for enhancing soil, involves subjecting a biomass feedstock to a treatment comprising sequential or concurrent ramps of temperature and pressure to produce at least one volatile component released from the biomass feedstock during the treatment and a nonvolatile component comprising biomass fractionator apparatus (BMF char), rendering a surface of the BMF char hydrophilic, and exposing the BMF char to microorganisms.    USE - The method is useful for production of agent for enhancing soil (claimed).    ADVANTAGE - The method is simple to perform.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of enhancing soil health, which involves providing a BMF biochar, and adding the BMF biochar to soil.
NOVELTY - The method involves moisturizing organic material to a latent moisture content entrained in organic material. The organic material is subjected to a vacuum below atmospheric pressure for a time period to bring latent moisture content to a vaporization point. The organic material is homogenized (S2) when material is subjected to vacuum below atmospheric pressure to rupture cell walls of material to provide treated organic material. The treated material is delivered to further processing.    USE - Method of treating organic material such as manure, carcasses, agricultural products and residues.    ADVANTAGE - The moisturized organic material is below the vaporization point and the heat is added to the organic material to reduce the vacuum subjected to the organic material. The organic material from which inorganic material is removed and/or from specific source to have relatively constant characteristics thus providing enhanced operational efficiency. The heat recapture device is utilized with moisture collectors, organic material treatment apparatus and/or with vacuum apparatus requiring moisture collection to protect the vacuum pump.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an apparatus for treating organic material;    (2) a moisture collector; and    (3) a heat recapture device.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart illustrating a method for treating organic material.    Step for loading organic material (S1)    Step for homogenizing organic material (S2)    Step for actuating vacuum pump (S3)    Step for destructing pathogens (S5A)    Step for processing discharged material (S5B)
NOVELTY - Invention relates to medicine, food industry and cosmetics, particularly, to natural dyes and biomarkers. This method comprises separation of red alga biomass from culture medium and its flushing. Cell walls are destructed and pigment is subjected to water extraction. Final product is conserved while biomass is extracted at the growth linear stage or under quasi continuous culture mode. Besides, is includes separation of said biomass from culture medium, flushing of cell biomembranes and water extraction.    USE - Biotechnologies.    ADVANTAGE - Simplified process, lower costs, high quality of finished products.
NOVELTY - The device comprises a tank (2) having lead angles at top and bottom, an internally coated sleeve (3), blades (4), and a metering device (5). The metering device is arranged in the tank with a light emitting device (6). Minerals dosing system (7) is connected to a reservoir (8) for mixing salts, which are sucked directed by a pump (9) to the tank. An iron or phosphate metering system (10) is also connected to the pump. The tank has an outlet pipe connected to another tank.    USE - Device for optimizing growth of algae for producing biofuel.    ADVANTAGE - The device provides exponentially more productive raw materials compared with soybean and alcohol in a simple and eco-friendly manner, and reduces greenhouse effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for optimizing growth of algae.    Tank (2)    Internally coated sleeve (3)    Metering device (5)    Light emitting device (6)    Minerals dosing system (7)    Reservoir (8)    Pump (9)    Iron or phosphate metering system (10)
NOVELTY - Preparing sugar involves preparing a slurry by adding an aqueous solution containing a sugar or a sugar solution to biomass, where the slurry has biomass content of 10-30 weight/volume%, and obtaining the sugar having glucose as a main component by adding a cellulose degrading enzyme and/or a hemicellulose degrading enzyme to the biomass-containing slurry to degrade the cellulose and/or hemicellulose contained in the biomass.    USE - The method is useful for preparing sugar, preferably glucose or sucrose (all claimed).    ADVANTAGE - The method prepares efficiently high concentration of saccharified liquid using less amount of enzyme.
NOVELTY - A hydrogen production method in underground involves pressingly injecting hydrocarbon-utilizing hydrogen-producing bacteria activator into underground.    USE - Production of hydrogen used in production of methane (claimed) used for electricity and gas.    ADVANTAGE - The method enables efficient production of hydrogen even if its is neither oil field nor abandoned mine.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for methane production method in underground, which involves producing hydrogen by hydrogen production method in underground.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of the methane production system.    Gas reservoir (2)    Oil layer (3)    Bearing stratum (4)    Activator press injection installation (10)    Methane production system (100)
NOVELTY - Utilization of intestinal bacteria from slaughtered animals in industrial processes and waste treatment, comprises adding mono or disaccharides or their polymers into the stomach manure of a slaughtered animal or manure produced by it or refinery sludge, to increase the productivity or production levels of wanted biotechnical products.    USE - Used as a method of utilizing intestinal bacteria from slaughtered animals in industrial processes and waste treatment.    ADVANTAGE - The biotechnical treatment of slaughter waste containing stomach manure, rapidly decreases waste problems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for performing the above method, where fructose, fructose-containing sugar, byproduct fraction or waste or glucose that is enzymatically converted into fructose, is added into stomach manure, after the adjustment of humidity percentage, in a separate reactor (A) from the bio-reaction.
NOVELTY - The extruder has material supply unit, a grinding unit, a heating unit, and a cooling unit that are arranged with each other. A seal ring is multiply arranged by the heating unit. Several elements are arranged with a kneading disk. Left-hand threads are arranged in the heating unit. Clearance with the seal ring and cylinder which are arranged by heating unit is 0.5-10.0% of a cylinder bore. An injection line is installed in the grinding unit. The water cooled jacket and/or the injection line are arranged at cooling unit. The material supply unit is equipped with a compactor.    USE - Twin screw extruder such as single-axis screw extruder and multi-axial screw extruder for hydrothermally treating cellulose containing biomass. Uses include but are not limited to cellulose containing biomass such as cryptomeria japonica and chamaecyparis obtusa, rice straw, straw, corn cob, cassava, bagasse, and sugarcane leaf.    ADVANTAGE - The lot of cellulose containing biomass is pre-processed continuously, and the cellulose containing composition is obtained with high saccharification property. The manufacturing process of industrially useful saccharide is performed with high efficiency and the hydrolysis process of biomass composition is constructed efficiently from a pretreatment process.    DETAILED DESCRIPTION - The ratio of length of the screw from cutting start of screw under the hopper of screw extruder to front-end with a diameter is 30-80 in a grinding unit, a heating unit, and the whole cooling unit, and is 10-40 in a grinding unit. Cellulose containing biomass is soft biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the seal ring used for the screw extruder.
NOVELTY - Pre-processing of biomass involves crushing a cellulose-containing biomass starting material in a crushing unit of the screw extruder such that the maximum particle diameter is 1000 mu m or less, adjusting the water content to 20-80%, hydrothermally-treating in a heating unit at 150-250 degrees C for 0.1-10 minutes while mixing and crushing, cooling the treated product in cooling unit to 100 degrees C or less, and recovering a cellulose-containing biomass treated product having average particle diameter of 100 mu m or less.    USE - Pre-processing of biomass used in manufacture of biomass composition used for manufacturing saccharide (all claimed).    ADVANTAGE - The method enables efficient pre-processing of biomass with high diastatic activity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacturing of biomass composition; and    (2) manufacture of saccharide.
NOVELTY - Cellulose-containing biomass feedstock is ground in a grinding portion of screw extruder to particle size of 1000 mu m or less, hydrothermal treatment is carried out, heated in a heating unit having an element comprising 1 or more sets of kneading disk and/or reverse-threaded screw provided immediately before a sealing ring, and hydrothermal treatment is carried out while mixing and crushing. The processed material is cooled, and collected to obtain biomass with few amount of furfural byproduct, which is a fermentation-inhibiting component from cellulose-containing biomass feedstock.    USE - Processing of biomass used for manufacturing saccharide (claimed).    ADVANTAGE - The method provides biomass having high saccharification property, and high quality with high productivity. Kneading, grinding and mashing process of biomass are carried out simultaneously.    DETAILED DESCRIPTION - Cellulose-containing biomass feedstock is ground in a grinding portion of screw extruder to particle size of 1000 mu m or less, and moisture content of 30-80%, hydrothermal treatment is carried out at 150-200 degrees C for 0.1-15 minutes, heated in a heating unit having an element comprising 1 or more sets of kneading disk and/or reverse-threaded screw provided immediately before a sealing ring, and hydrothermal treatment is carried out while mixing and crushing. The processed material is cooled by cooling unit provided after heating unit, and collected at 100 degrees C or less to obtain biomass with few amount of furfural byproduct, which is a fermentation-inhibiting component from cellulose-containing biomass feedstock. INDEPENDENT CLAIMS are included for the following:    (1) manufacture of biomass composition; and    (2) manufacture of saccharide, which involves hydrolyzing biomass composition.
NOVELTY - The electrolytic cell (1) has a cathode compartment (12), an anode compartment (4), a cover lid (5), and a diaphragm (11). The cover lid has a first line (6) for withdrawing hydrogen gas formed and a second line (7) for withdrawing halogen formed. The anode (8) is extending into the interior space of cell, and is connected to a current supply line (9). The diaphragm separates the cathode compartment and the anode compartment.    USE - Electrolytic cell for manufacture of hydrogen gas and halogens from molten electrolyte.    ADVANTAGE - Distance between cathode and anode is made shorter, thus more energy is effective, without danger that hydrogen gas formed enter the anode compartment. Cell voltage is lowered due to the shorter distance, and saves energy. Electrical short circuit is prevented by the diaphragm while allowing the transport of ionic charge carriers that are needed to close the circuit during the passage of current in an electrochemical cell.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for the manufacture of hydrogen gas and halogen; and    (2) a use of a membrane or a diaphragm in an electrolytic cell.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic diagram of an electrolytic cell.    Electrolytic cell (1)    Anode compartment (4)    Cover lid (5)    First line (6)    Second line (7)    Anode (8)    Current supply line (9)    Diaphragm (11)    Cathode compartment (12)
NOVELTY - An electrolytic cell (1) comprises one or more cathode and one or more anode. At least one of anode or cathode is gas diffusion electrode (8).    USE - Electrolytic cell is used in manufacture of hydrogen and halogen e.g. chlorine and fluorine (claimed) used as etching gas and chamber cleaning gas in manufacture of semiconductor, photovoltaic cell, thin-film transistor liquid crystal display and micro-electromechanical system.    ADVANTAGE - The electrolytic cell has improved current efficiency and energy efficiency, excellent electroconductivity, and low ohmic resistance. The gas diffusion electrode contained in the electrolytic cell provides excellent wetting characteristics for the molten electrolyte.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) usage of gas diffusion electrode as anode and/or cathode in electrolytic cell; and    (2) manufacture of hydrogen and halogen e.g. chlorine and fluorine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of electrolytic cell.    Electrolytic cell (1)    Cathode compartment (2)    Anode compartment (4)    Lid (5)    Gas diffusion electrode (8)
NOVELTY - Composition comprises ash produced by burning lignocellulosic filter cake and optionally lignocellulosic syrup, where the filter cake and syrup are co-products of a process for the production of alcohol from a lignocellulosic biomass.    USE - The composition in form of pellets, granules or briquettes is used for enhancing land surface. The land surface is chosen from a field, a road, a landfill, and a site needing at least one of fill material and stabilization. The surface is a field and the composition acts as a stabilizer or a fertilizer (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) process for producing energy and a land application composition, involves providing a lignocellulosic filter cake that is a co-product of a process for the production of alcohol from a lignocellulosic biomass, optionally providing a lignocellulosic syrup that is a co-product of a process for the production of alcohol from a lignocellulosic biomass, providing at least one combustion enhancement material, adding the filter cake of (a), optionally the syrup of (b), and the combustion enhancement material of (c) to a vessel, and combusting the contents of the vessel, where the lignocellulosic ash is a land application composition; and    (2) method for enhancing a land surface, involves applying the composition to a land surface.
NOVELTY - Topical composition comprises oil free foamable emulsion, propellant agent, ultraviolet A and B rays protecting agent, water, acceptable inactive excipients and perfume.    USE - Topical composition for sunscreen protector for skin (claimed).    ADVANTAGE - The topical composition is easy to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing topical composition, which involves mixing free foamable emulsion, propellant agent, ultraviolet A and B rays protecting agent, water, acceptable inactive excipients and perfume.
NOVELTY - Obtaining biofuel involves reducing particles of the lignocellulosic and amylaceous biomass and fermenting the obtained material by using one or multiple microorganisms capable of producing and modulating production of enzymes that degrade lignin, cellulose, and hemicelluloses at temperature between 10-80 degrees C, and pH 2-12. The obtained material is fermented by using one or multiple microorganisms such as Baccilus at 10-50 degrees C and at pH2-12 by one or multiple microorganisms such as Saccharomyces spp. at 10-60 degrees C at pH 2-12 for extracting alcohols.    USE - Method for obtaining biofuel from lignocellulosic and amylaceous biomass.    ADVANTAGE - The method enables to obtain biofuel from lignocellulosic and amylaceous biomass in a cost-effective and eco-friendly manner.
NOVELTY - Enzyme-catalyzed conversion of atrazine is performed by adding chlorine peroxidase to atrazine aqueous solution, mixing, adjusting pH to 2.5-4 using 0.1 mol/L phosphate buffer solution, adding 30 mass% hydrogen peroxide (H2O2) aqueous solution, and stirring at room temperature for 3-10 minutes in which molar ratio atrazine:chlorine peroxidase:H2O2 is 1:0.0019-0.0075:15-50.    USE - Enzyme-catalyzed conversion of atrazine (claimed).    ADVANTAGE - Enzyme-catalyzed conversion of atrazine is simple, low-cost, and environment-friendly and has mild conditions, high atrazine conversion rate, and short conversion time.
NOVELTY - The equipment (1) has a valve lock (10) provided with a centrifuge unit (12) that is formed on a screw-end part (13). The screw-end part directs biomass (15) towards a drier (14). The centrifuge unit comprises a duct outlet that is connected to a feed valve (16). A filter (17) is connected to a pump (19). A tank (3) is connected with an oil reservoir (23). A filtering valve (24) is connected with another filter (25) and attached to a pump (26) that is arranged between the latter filter. A recycling valve (27) is attached to an outlet valve (28) and the pump.    USE - Equipment for removing oil, biofuel, biomass and proteins of algae (all claimed).    ADVANTAGE - The equipment removes algae or microalgae and biofuel in an effective manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an equipment for removing oil, biofuel.    Equipment for removing oil (1)    Tank (3)    Valve lock (10)    Centrifuge unit (12)    Screw-end part (13)    Drier (14)    Biomass (15)    Feed valve (16)    Filters (17, 25)    Pump (19)    Oil reservoir (23)    Filtering valve (24)    Pump (26)    Recycling valve (27)    Outlet valve (28)
NOVELTY - A pharmaceutically acceptable polyolefin and aluminum foil packaging material heat sealing glue comprises 25-35 wt.% ethyl acetate, 25-35 wt.% cyclohexane, 15-20 wt.% chlorinated polypropylene, 8-12 wt.% methyl methacrylate, 4-8 wt.% butyl acrylate, 2-5 wt.% acrylic acid, and 0.5-1.5 wt.% benzoyl peroxide in which total of raw materials is 100%.    USE - Pharmaceutically acceptable polyolefin and aluminum foil packaging material heat sealing glue (claimed).    ADVANTAGE - Glue is non-toxic, environment-friendly, suitable for medical packaging, does not affect product appearance, and has improved graft ratio and peeling strength.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of pharmaceutically acceptable polyolefin and aluminum foil packaging material heat sealing glue which involves dissolving chlorinated polypropylene in mixed ethyl acetate and cyclohexane solvent at 60-70 degrees C under nitrogen gas atmosphere with stirring at 300 rpm, heating to 80 degrees C, dropping 15% benzoyl peroxide, reacting for 15 minutes, dropping 80% benzoyl peroxide for 1-1.5 hours, dropping methyl methacrylate, butyl acrylate, and acrylic acid solution at 85 degrees C, heat preserving, reacting for 2-3 hours, dropping remaining benzoyl peroxide, and cooling.
NOVELTY - Herbicide comprises cyclosulfamuron and imazamox as active ingredients.    USE - The herbicide is useful in rice (claimed) for controlling annual and perennial weeds.    ADVANTAGE - The herbicide has synergistic effect, high efficiency, long lasting effect, and is safe on rice.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the herbicide, comprising mixing cyclosulfamuron, imazamox, dispersing agent, wetting agent, disintegrator and filler, grinding in a superfine jet mill, kneading, then adding into fluid bed granulation dryer, granulating, drying, and screening.
NOVELTY - Purification of LED material high-purity methyl iodide comprises taking crude methyl iodide, soaking in Zeolite Socony Mobil-12 (ZSM-12) molecular sieve chelating adsorbent, filtering, adding filtrate into rectifying device, rectifying to obtain liquid and performing ultrafiltration.    USE - Method for purifying LED material high-purity methyl iodide (claimed).    ADVANTAGE - The method has more simple and environment-friendly operation, and low production cost. It ensures good-quality product.
NOVELTY - Production of isoborneol acetate ester comprises heating alpha -pinene, introducing into isomerization reactor, and contacting with catalyst; introducing into camphene tower to obtain refined camphene and dipentene; mixing refined camphene and acetic acid, heating, and esterifying with catalyst; and refining to obtain refined camphene and acetic acid mixture and isoborneol acetate ester, and removing acetic acid in refined camphene and acetic acid mixture to obtain refined camphene.    USE - Method of producing isoborneol acetate ester (claimed).    ADVANTAGE - The method solves problem such as difficult to continue production, high labor intensity, and low product yield.
NOVELTY - An infusion multi-layered co-extruding polyolefin inner layer pellet comprises styrene-ethylene-butylene-styrene (SEBS) copolymer, fill oil, polypropylene (PP), filler, and Antioxidant 1076 (RTM: 3,5-Bis(1,1,-dimethylethyl)-4-hydroxybenzenepropanoic acid octadecyl ester), and is prepared by mixing SEBS and fill oil, standing to fully swell SEBS and obtain SEBS-charged oil, mixing SEBS-charged oil with PP, filler, and Antioxidant 1076, placing mixed blend in roller mill, rolling and mixing, cooling, discharging, smashing, extruding, and granulating to uniform particle size.    USE - Infusion multi-layered co-extruding polyolefin inner layer pellet for transfusion apparatus or medical infusion product, such as disposable bag.    ADVANTAGE - The pellet has small drug absorption, high transparency, light weight, convenient use, is environment-friendly, and does not react with taxol and fat emulsion anti-cancer drug.    DETAILED DESCRIPTION - An infusion multi-layered co-extruding polyolefin inner layer pellet comprises 35-40 wt.% SEBS copolymer, 25-29 wt.% fill oil, 27-30 wt.% PP, 6-7 wt.% filler, and 0.4-0.6 wt.% Antioxidant 1076, and is prepared by mixing SEBS and fill oil in high speed mixer for 25-30 minutes, standing for greater than or equal to 1 day to fully swell SEBS and obtain SEBS-charged oil, mixing SEBS-charged oil with PP, filler, and Antioxidant 1076, placing mixed blend in roller mill at 210-220 degrees C, rolling and mixing at 170-175 degrees C for 30-40 minutes, cooling to normal temperature in Banburying chamber, discharging, smashing in crusher, extruding, and granulating with double-screw extruder to uniform particle size in which double-screw extruder comprises machine head divided to 5 sections having temperature control of 155-170 degrees C at 1st section, 170-180 degrees C at 2nd section, 180-195 degrees C at 3rd section, 170-185 degrees C at 4th section, 170-180 degrees C at 5th section, and 170 degrees C at machine head.
NOVELTY - This utility new type relates to the medicine preparation residue removing device, especially to an agricultural and forestry product medicine residue purifier without ozone discharging, comprising a shell, an ozone generator; the shell for starting with a closeness structure, a shell lower end form a number in a water container, the air outlet of ozone generator has ozone conveying pipe connecting the ozone conveying pipe extending to a water container of the internal inner shell, set with ozone remover at internal or external of shell, ozone remover comprises a water container and a second interior space of suction and shell of pump body, wherein pump body connected, the air outlet of pump body through air outlet tube connected to a second water container, the second a water container and the external connected, through removing the whole product of pesticide residue and a process d, using ozone to dissolve b characteristic of water, a neutralizing ozone for treatment of b agent is dissolved in water, a rapid effective removing overflowing of ozone, which ensures safety of household environment.
NOVELTY - The method involves converting solid biomass into synthetic gas. Gas is subjected to a cleaning and modifying system (5) for permanent pollution cracking process. Cooled synthetic gas is entered into a turbine (6), where excess heat energy produces electrical energy. Cooled gas is purified in a purification system (7) and passed to an electricity generator (8). The electricity generator is connected with a gas turbine combustion engine and a fuel cell. Heat or fume is fed to the turbine and converted into electricity. Biogas (2) i.e. fuel, is passed to the generator.    USE - Method for producing electricity from agricultural biomass power plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an agricultural biomass power plant. '(Drawing includes non-English language text)'    Biogas (2)    Cleaning and modifying system (5)    Turbine (6)    Purification system (7)    Electricity generator (8)
NOVELTY - The tank has an intermixing device referred as a heat exchange apparatus that works according to principle of a heat pipe or two-phase thermosiphon. A heating body is supplied with vanes whose internal cavities are connected to a shaft of the intermixing device. A heating portion is carried out beyond limits of a case of the tank and placed in a heating chamber. A half-coupling part of a drive part is provided on the chamber. An extinguisher is fixed at an upper end of the shaft, where a blade of the extinguisher is installed at a level window for discharging foam into a loading pocket.    USE - Methane-tank for generating biogas from agricultural and industrial organic waste.
NOVELTY - Ammonia is absorption-immobilized from a waste gas containing ammonia using a fixative. The absorption-immobilized ammonia is heated. The separated ammonia gas is passed to a combustion furnace or a cement kiln. The gas component recovered with ammonia is burnt while reducing nitrogen oxides in combustion exhaust gas. The waste gas is an exhaust gas from various production processes, or a gas having odor of poultry farming stock raising industry, excrement composting process, compost, wastewater treatment or industrial waste-treatment process.    USE - Processing of waste gas used for reducing nitrogen oxides in combustion exhaust gas during manufacture of cement (all claimed).    ADVANTAGE - The method enables environmentally-friendly processing of waste gas. The cement manufactured using the waste gas has excellent quality.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) utilization method of waste gas in reduction of nitrogen oxides in combustion exhaust gas; and    (2) manufacture of cement, which involves performing collection process of absorption-immobilizing ammonia from the waste gas containing ammonia using fixative, moving the fixative to separate facilities for separating ammonia from the fixative, heating the fixative and absorption-immobilizing and separating ammonia gas, burning the gas component recovered with ammonia while passing the separated ammonia gas to combustion furnace or cement kiln and reducing nitrogen oxides in the combustion exhaust gas, moving the fixative to a waste gas generation source which generates the waste gas, and repeating the collection process.
NOVELTY - Method for directly producing biodiesel from wet biomass involves pretreating wet biomass by adding alcohol, adding alcohol and catalyst to pretreated biomass, and heating to perform transesterification reaction.    USE - Method for directly producing biodiesel e.g. fatty acid alkyl ester from wet biomass e.g. wet microalgae, without extracting lipid (all claimed).    ADVANTAGE - The method enables economical and efficient production of biodiesel without separating lipid, by environmentally-friendly process. The waste generated during production of biodiesel is recyclable.
NOVELTY - Method for using chicken excrement for earthworm cultivation involves constructing an earthworm raising farm near chicken breeding field, using the bred earthworms for feeding chicken excrement and feeding the chicken with the earthworm.    USE - The method is useful for using chicken excrement for earthworm cultivation (claimed).    ADVANTAGE - The method easily processes chicken manure without polluting environment, and effectively saves chicken breeding cost by not less than 30-40%.
NOVELTY - Interconnected biorefinery process for microalgae or any biomass rich in proteins, lipids and carbohydrates, involves (a) harvesting or concentrating biomass, (b) producing biodiesel by wet direct transesterification (WDT) using remaining microalgal biomass after protein extraction, and (c) producing biogas from the liquid and remaining biomass from the previous step by anaerobic digestion process at neutral pH and 20-40 degrees C or 40-60 degrees C for 30 days.    USE - The interconnected biorefinery process for microalgae or any biomass rich in protein, lipids and carbohydrates is used for producing proteins, biodiesel, and biogas (claimed).    ADVANTAGE - The process improves overall downstream process.    DETAILED DESCRIPTION - Interconnected biorefinery process for microalgae or any biomass rich in protein, lipids and carbohydrates, involves (a) harvesting or concentrating biomass, where the harvesting is performed by natural sedimentation of extracellular polymeric substances, alkalinity-induced flocculation or adding coagulants to the culture protein and/or amino acids production by protein solubilization under alkaline conditions using harvested biomass, the protein and/or amino acid production are obtained from harvested or concentrated biomass of step (a) by a chemical process, and the protein solubilization is achieved by increasing pH to 8-12, maintaining at 20-60 degrees C and stirring during 10 minutes to 1 hour, (b) producing biodiesel by wet direct transesterification (WDT) using remaining microalgal biomass after protein extraction, and (c) producing biogas from the liquid and remaining biomass from the previous step by anaerobic digestion process at a neutral pH and 20-40 degrees C or 40-60 degrees C for 30 days.
NOVELTY - A mutagenized Desmodesmus sp. culture (ATCC PTA-120599) or (ATCC PTA- 120600), is new.    USE - The mutagenized Desmodesmus sp. culture is useful for reducing growth of fungus in liquid culture system (claimed), and producing fuel products e.g. oil, and petrochemicals.    ADVANTAGE - The mutagenized Desmodesmus sp. has increased biocide tolerance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method (M1) for producing algal biomass, involves (a) providing liquid culture system, and (b) inoculating the liquid culture system with at least one of Desmodesmus sp. (ATCC PTA-120599) or (ATCC PTA- 120600); and (2) method (M2) for reducing the growth of fungus in a liquid culture system, involves (a) providing a liquid culture system, (b) inoculating the liquid culture system with at least one of the above-mentioned mutagenized species, and (c) treating the liquid culture system either before or after step (b) or both before and after step (b) with an effective concentration of a fungicide composition to reduce the growth of fungus, where the fungicide composition contains FRAC 29 fungicide as an active ingredient.
NOVELTY - A high-temperature alkaline salt xylanase XynSL4, where its amino acid sequence is fully defined 380 amino acids (SEQ ID NO: 1), given in the specification, is new.    USE - The high-temperature alkaline salt xylanase XynSL4 is useful for industrial bleaching of pulp, for biomass degradation, and for seafood processing (claimed).    ADVANTAGE - The high-temperature alkaline salt xylanase XynSL4 has high enzymatic activity, and can be efficiently used in paper making, and in biological energy and equal food industry field.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a high-temperature alkaline salt xylanase gene which encodes the high temperature alkaline xylanase XynSL4;    (2) a recombinant vector which comprises the high-temperature alkaline salt xylanase gene;    (3) a recombinant strain which comprises the high temperature alkaline salt xylanase gene; and    (4) a method of preparing the high-temperature alkaline salt xylanase XynSL4.
NOVELTY - Compressed bed comprises composition obtained by mixing 60-90 vol.% peat, 5-20 vol.% vermiculite, 1-5 vol.% diatomite, 0.1-3 vol.% fertilizer, 0.1-3 vol.% surfactant, and 0.01-1 vol.% microorganism, where the composition is placed on a plate and compressed to obtain compressed bed having thickness of 3-5 mm.    USE - The compressed bed is useful for cultivating rice plant (claimed).    ADVANTAGE - The compressed bed promotes root growth in rice plant.
NOVELTY - An industrial waste mixture recycling method involves recycling industrial waste mixture obtained in the production of biodiesel comprising a mixture of the glycerol fraction, degumming product and other vegetable fats and biological compounds into food materials and/or feed material.    USE - Method for recycling industrial waste mixture.
NOVELTY - The method involves culturing yeast of lipolytica species on a growth medium. Aqueous solution is comprised of a carbon source and a mixture of after-containing glycerol and waste degumming vegetable fats. The growth medium is maintained at temperature of below 34 degree Celsius. PH value of an oxygenated medium is maintained between 2.5-7.5 by addition of concentrated ammonium. A nitrogen source is added with the concentrated ammonium. Broth mush is replaced in a fresh portion part.    USE - Method for treating industrial waste generated during production of biodiesel and vegetable fats.
NOVELTY - A substantially pure Candida host cell comprising (a) first genetic modification class that comprises one or more genetic modifications that collectively or individually disrupt an alcohol dehydrogenase gene in the substantially pure Candida host cell, or (b) the above-mentioned first genetic modification class, and second genetic modification class, where the second genetic modification class comprises an insertion of a first gene into Candida host cell genome, is new.    USE - The substantially pure Candida host cell is useful for biotransformation of substrate to product, and in oxidation of fatty acid into alpha -carboxyl- omega -hydroxyl fatty acid (all claimed), and in production of biofuels.    ADVANTAGE - The host cell cost-effectively produces biofuels, and eliminates use of toxic reagents.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for alpha -carboxyl- omega -hydroxyl fatty acid which is oxidized from substantially pure Candida host cell.
NOVELTY - An organic-semiconductor composition comprises 5,12-diazatetracyclo-hexadeca-1,3,5,8,10,12,15-heptaene derivative (I), and a migration inhibitor.    USE - Organic-semiconductor composition is used for forming organic thin-film transistor for electronic paper and display device (all claimed).    ADVANTAGE - The organic-semiconductor composition improves the insulation reliability of organic thin film transistor without decreasing the mobility of the organic thin film transistor.    DETAILED DESCRIPTION - An organic-semiconductor composition comprises 5,12-diazatetracyclo-hexadeca-1,3,5,8,10,12,15-heptaene derivative of formula (I), and a migration inhibitor.    A1,A2=S, Se or O;    R1-R6=H or substituent of formula: asterisk-L-R;    L=bivalent coupling group chosen from group of formulae (L-1)-(L-10);    R=H, optionally substituted alkyl, oligo oxyethylenyl having two or more oxyethylene units, oligosiloxane containing more than one silicon atom or optionally substituted trialkylsilyl;    m=4;    m1=2;and    R'=H or substituent.    (i) R' optionally bonds with R adjacent to L, to form condensed ring. An INDEPENDENT CLAIM is included for organic thin-film transistor (100), which comprises organic-semiconductor layer (50) produced using the organic-semiconductor composition.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of organic thin-film transistor. (Drawing includes non-English language text)    Substrate (10)    Gate electrode (20)    Source electrode (40)    Organic semiconductor layer (50)    Organic thin-film transistor (100)
NOVELTY - N-alkyl, N-cycloalkyl, N-alkenyl, N-aryl amine or imino propionic acid (III) or (IV) is new.    USE - The N-alkyl, N-cycloalkyl, N-alkenyl, N-aryl amine or imino propionic acid is useful in a corrosion inhibiting formulation to inhibit corrosion of ferrous metals (all claimed) in contact with hydrocarbon fuels and crude oil.    DETAILED DESCRIPTION - N-alkyl, N-cycloalkyl, N-alkenyl, N-aryl amine or imino propionic acid compounds of formula (III) or (IV) is new.    R = 1-30C linear or branched alkyl or alkenyl or 5-12C acylic alkyl or 5-12C aryl;    R1 = H or -CH3; and    R2 = H.    INDEPENDENT CLAIMS are also included for:    (1) a process for obtaining N-alkyl, N-alkenyl, N-cycloalkyl, N-aryl amino or imino propionic acids (III) and/or (IV);    (2) a corrosion inhibiting formulation comprising: N-alkyl or N-alkenyl or N-cycloalkyl or N-aryl amino or imino propionic acids; a polyether derived from propylene oxide or ethylene oxide or their copolymers; and a solvent comprising of aromatic compounds including toluene or xylene, and an alcohol including methanol, ethanol or isopropanol, gasoline and/or diesel; and    (3) a composition (C1) comprising: at least one component including crude oil, gasoline, jet fuel, methyl tert-butyl ether, diesel fuel or alcohol; and at least one of (III) or (IV) to inhibit corrosion of ferrous metals in contact with the composition.
NOVELTY - Graphite alkenyl composite material preparation involves dissolving chitosan in 3% acetic acid solution, and then performing ultrasonic treatment for 1-12 hours. The obtained material is mixed with 2-10 g/L sodium periodate for 10-60 minutes at 40-80 degrees C, and then the obtained material is centrifuged. The obtained material is washed with deionized water, and then dried them. The obtained material is mixed with certain amount of silver ammonia solution and graphene oxide mixed solution at 40-100 degrees C for 1-12 hours, and then heated them at 160-220 degrees C for 48 hours.    USE - Method for preparing graphene alkenyl composite material (claimed).    ADVANTAGE - The method enables to prepare graphene alkenyl composite material in simple and eco-friendly manner.    DETAILED DESCRIPTION - Graphite alkenyl composite material preparation involves dissolving chitosan in 3% acetic acid solution, and then performing ultrasonic treatment for 1-12 hours. The obtained material is mixed with 2-10 g/L sodium periodate for 10-60 minutes at 40-80 degrees C, and then the obtained material is centrifuged. The obtained material is washed with deionized water, and then dried them. The obtained material is mixed with certain amount of silver ammonia solution and graphene oxide mixed solution at 40-100 degrees C for 1-12 hours, and then heated them at 160-220 degrees C for 48 hours in a hydro-thermal reaction vessel. The obtained material is mixed with polytetrafluoroethylene, and then cooled the obtained material naturally. The obtained material is washed with ethyl alcohol and deionized water, and then centrifuged them. The obtained material is dried to obtain the finished product.
NOVELTY - Silicon fertilizer preparation involves taking 30-70% molybdenum ore, 10-15% dolomite or high magnesium limestone, 10-15% anthracite or white coal, 0.2-1% calcined alkali metal additive agent, 0.2-1% zinc sulfide, 0.2-1% potassium chloride, 0.2-1% aluminum powder and 0.2-1% iron powder. The raw materials are ground into fine powder of 80 meshes size, and then adding water. The obtained material sintered at 1250-1300 degrees C for 10-15 minutes to obtain silicon fertilizer. The obtained material is crushed to 90-100 meshes size to obtain the finished product.    USE - Method for preparing silicon fertilizer (claimed).    ADVANTAGE - The method enables to prepare silicon fertilizer in cost-effective and eco-friendly manner, and ensures improved yield with industrial application.
NOVELTY - Domestic garbage landfill leachate recycle involves filtering domestic garbage landfill leachate, and then decomposing them in anaerobic bioreactor. The obtained material is performed for ultra-filtration with 0.3-0.51% operation pressure difference, and then concentrated them. The obtained material is performed for ultra-filtration with 1-1.51% operation pressure difference. The obtained material is concentrated at greater than or equal to 750 degrees C to obtain the finished product.    USE - Method for recycling domestic garbage landfill leachate (claimed) used for producing organic liquid fertilizer.    ADVANTAGE - The method enables to recycle domestic garbage landfill leachate, ensures reduced reverse osmosis of concentrated liquid.
NOVELTY - Biological fertilizer composition comprises Azotobacter, phosphorus solubilizing bacteria, potassium solubilizing bacteria.    USE - Biological fertilizer composition used for activating soluble mineral element and improving crop nutrition and growth.    ADVANTAGE - The biological fertilizer composition ensures improved disease resistance ability.
NOVELTY - Fertilizer composition preparation involves taking 28-30 wt.% dried pig manure, 5-7 wt.% dry dairy manure, 15 wt.% corn straw, 8 wt.% leaf, 6 wt.% hay, 6 wt.% rapeseed cake, 20 wt.% dried pond sludge, 2 wt.% organic fertilizer fermenting agent, 6 wt.% potassium sulfate, 0.5 wt.% amino acid chelated iron, 0.4 wt.% amino acid chelated magnesium, 0.3 wt.% amino acid chelated zinc, 0.3 wt.% humic acid chelated manganese and 0.5 wt.% humic acid chelated copper. The dried pig manure, dry dairy manure, corn straw, rape seed cake and dried pond sludge are crushed.    USE - Method for preparing base fertilizer composition used for cultivating chestnut (claimed).    ADVANTAGE - The method enables to prepare fertilizer composition, which ensures improved yield of chestnut.    DETAILED DESCRIPTION - Fertilizer composition preparation involves taking 28-30 wt.% dried pig manure, 5-7 wt.% dry dairy manure, 15 wt.% corn straw, 8 wt.% leaf, 6 wt.% hay, 6 wt.% rapeseed cake, 20 wt.% dried pond sludge, 2 wt.% organic fertilizer fermenting agent, 6 wt.% potassium sulfate, 0.5 wt.% amino acid chelated iron, 0.4 wt.% amino acid chelated magnesium, 0.3 wt.% amino acid chelated zinc, 0.3 wt.% humic acid chelated manganese and 0.5 wt.% humic acid chelated copper. The dried pig manure, dry dairy manure, corn straw, rape seed cake and dried pond sludge are crushed, and then organic fertilizer fermenting agent and water are added to the obtained material. The obtained mixture is fermented in sealed container for 28-30 days, and then the obtained material is dried. The obtained material is mixed with remaining crushed raw material to obtain the finished product.
NOVELTY - Fertilizer comprises 40-60 pts. wt. chicken manure, 5-10 pts. wt. straw, corn powder, 5-10 pts. wt. urea, 10-20 pts. wt. metal ion solution, 1-2 pts. wt. citric acid, 5-10 pts. wt. potassium chloride, 5-10 pts. wt. tripolyphosphate, 5-10 pts. wt. sodium hexametaphosphate, 5-10 pts. wt. borax, 5-10 pts. wt. zinc sulfate, 3-8 pts. wt. gypsum powder, 0.5-2 pts. wt. fermentation microbial inoculum and balanced quantity of of water.    USE - Fertilizer used for rose (claimed).    ADVANTAGE - The fertilizer is rich in nutrients and increases yield of rose flowers.
NOVELTY - Preparation of multi-substituted olefin involves providing polyaniline-loaded nano-palladium as catalyst and ethyldiisopropylamine as base and catalytically coupling olefinic carbon-hydrogen bond and halogenated hydrocarbon in N,N-dimethylformamide solvent.    USE - Preparation of multi-substituted olefin used in pharmaceutical industry (claimed).    ADVANTAGE - The method enables preparation of multi-substituted olefin with high yield without using phosphine ligand, under mild reaction conditions, using reduced amount of catalyst. The catalyst is recyclable.
NOVELTY - A Vibrio, is new. The Vibrio is capable of assimilating alginic acid. The Vibrio comprises 16S ribosomal RNA gene, where the gene comprises a base pair sequence exhibiting at least 95% sequence identity to a base pair sequence of SEQ ID NO: 1. Sequence not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The Vibrio is useful for producing target substance. The Vibrio is V. alginolyticus (NITE BP01635). The target substance is amino acid, ethanol, isopropyl alcohol, acetone, propylene, 1,3- butanediol, 1,4-butanediol, 1-propanol, 1, 3-propanediol, 1,2-propanediol, ethylene glycol, or isobutanol. The amino acid is chosen from L-lysine, L-ornithine, L-arginine, L-histidine, L-citrulline, L-isoleucine, L-alanine, L-valine, L-leucine, glycine, L-threonine, L-serine, L-proline, L-phenylalanine, L-tyrosine, L-tryptophan, L-cysteine, L-cystine, L-methionine, L-glutamic acid, L-aspartic acid, L-glutamine, and L-asparagine (all claimed). The target substance is also used as foodstuffs, fuel, feed, and pharmaceutical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing target substance, which involves (a) obtaining Vibrio capable of assimilating alginic acid, and producing target substance, culturing Vibrio using culture medium containing carbon source (saccharide ) derived from seaweeds, and recovering accumulated target substance from the target substance.
NOVELTY - A sintering-resistant loading-type gold-platinum-palladium-type catalyst contains platinum, palladium and gold nanoparticles supported on a porous carrier composition. The weight ratio of platinum and palladium in platinum, palladium and gold nanoparticles is 1:4-2:1. The size of platinum, palladium and gold nanoparticles is 10m nm or less.    USE - Sintering-resistant loading-type gold-platinum-palladium-type catalyst is used in high-temperature catalytic applications e.g. methane activation, automobile exhaust treatment and alkane oxidation.    ADVANTAGE - The loading-type gold-platinum-palladium-type catalyst having excellent sintering resistance is prepared with high yield, by simple method. The gold-platinum-palladium-type catalyst is used at temperature of 700 degrees C or more.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sintering-resistant loading-type gold-platinum-palladium catalyst, which involves synthesizing porous support having three-dimensional pore structure, dispersing platinum, palladium and gold nanoparticles within pore of porous carrier to obtain catalyst precursor, and calcining catalyst precursor.
NOVELTY - Kitchen food waste processor comprises inner bucket (1) and outside bucket (2), where middle part of the outside bucket and outside bucket is provided with inner ring (3). Bottom of inner bucket is provided with inner ring. The upper part of inner is divided into upper layer storage layer (5), and the lower part is divided into lower layer and extrusion forming layer (6), where the upper storage layer is connected with bucket wall. The upper storage layer, the lower layer, and extrusion forming layer is provided with layered clapboard (30).    USE - Kitchen food waste processor used for processing waste for preparing fertilizer.    ADVANTAGE - The kitchen food waste processor is worked in eco-friendly manner, and ensures reduced food waste and use of resource.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a kitchen food waste processor.    Inner bucket (1)    Outside bucket (2)    Inner ring (3)    Storage layer (5)    Extrusion forming layer (6)    Layered clapboard (30)
NOVELTY - Remediation of soil comprises selecting different bred of earthworms capable for different degree of pollution and according to soil condition; building culture medium bed from livestock and poultry manure, and plant straw or sludge; covering with straw layer; putting earthworm into culture medium; maintaining culture medium at 6-35 degrees C and moisture content at 35-55%; allowing full fermentation of organic waste, livestock manure, straw and sludge; collecting earthworm manure from culture bed; and putting collected earthworm manure into soil that needs remediation.    USE - Remediation of soil.    ADVANTAGE - The method achieves artificial breeding of earthworms that produces earthworm manure during normal metabolism process. This earthworm manure provides rapid soil improvement that is economical, safe, and environment-friendly.    DETAILED DESCRIPTION - Remediation of soil comprises selecting different bred of earthworms capable for different degree of pollution and according to soil condition; building culture medium bed from livestock and poultry manure, and plant straw or sludge at 1-100 m long and 1-3 mm wide; covering with straw layer; putting selected earthworm into culture medium bed; maintaining temperature at 6-35 degrees C and moisture content at 35-55%; feeding earthworm with enough food once per month to allow full fermentation of organic waste, livestock manure, straw and sludge; collecting loose culture medium from bed surface to obtain earthworm manure; repeatedly scraping out loose bed material to obtain earthworm manure until earthworms settle at bottom layer; collecting earthworms; and putting collected earthworm manure into soil that needs remediation.
NOVELTY - Method for storing fresh-cut herbs of Orobanche, involves harvesting Orobanche herb, wetting the herb using water, drying the harvested Orobanche herb, and airing the dried Orobanche herb for 12-48 hours.    USE - The method is useful for storing fresh-cut herbs of Orobanche (claimed).    ADVANTAGE - The method reduces microorganism and insect eggs in soil, is environmentally-friendly, cost-effective and simple, and improves quality.
NOVELTY - Michelia alba fertilizer comprises 5-7 pts. wt. nitrogenous fertilizer, 2-4 pts. wt. phosphate fertilizer, 3-5 pts. wt. potash fertilizer, 40-50 pts. wt. coal residue, 20-30 pts. wt. water Liao, 30-40 pts. wt. wormwood, 20-40 pts. wt. hawthorn, 18-20 pts. wt. lees, 18-22 pts. wt. balsam pear, 30-50 pts. wt. Spatholobus stem, 20-24 pts. wt. licorice, 0.03-0.05 pts. wt. chitin and 50-60 pts. wt. water.    USE - Michelia alba fertilizer used as crop organic fertilizer.    ADVANTAGE - The fertilizer increases quality of soil, has low cost and simple process, and has no residue and pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of Michelia alba fertilizer comprising taking coal residue, water Liao, wormwood, hawthorn, lees, balsam pear, Spatholobus stem, and licorice, and ventilation drying; adding nitrogen fertilizer, phosphate fertilizer, potassium fertilizer and chitin, crushing after adding water, and fully stirring; and sealing the mixture, fermenting for 7 days, standing for 24 hours, and pelletizing.
NOVELTY - Processing anglerfish waste involves (a) cutting anglerfish, removing e.g. liver, taking fish skin, bones and internal waste, and cutting waste into blocks, (b) subjecting fish skin, and bones separated from the fish to enzyme hydrolysis by adding alkaline protease at a suitable temperature, (c) separating lower and upper layer of hydrolyzate, (d) centrifuging hydrolyzate to obtain precipitate and supernatant, and collecting precipitate and drying precipitate, and (e) separating oil phase and aqueous phase in supernatant, and drying aqueous phase.    USE - The method is useful for processing anglerfish waste (claimed).    ADVANTAGE - The method is effective, and has good operability.    DETAILED DESCRIPTION - Processing anglerfish waste involves (a) cutting anglerfish, removing liver, stomach, tailbone, and gallbladder, taking fish skin, bones and internal waste, and cutting the waste into blocks, (b) subjecting the fish skin, and bones separated from the fish to enzyme hydrolysis by adding alkaline protease to fish skin, and bones at a suitable temperature, (c) separating lower and upper layer of hydrolyzate, (d) centrifuging the hydrolyzate to obtain precipitate and supernatant, and collecting the precipitate and drying the precipitate, and (e) separating oil phase and aqueous phase in the supernatant, and drying the aqueous phase.
NOVELTY - This utility new type provide the biogas purifying use pressure drive water pump system, comprising water pump, turbine, water storage tank, analysis tower, tower and water washing tower, a water pump electric machine main shaft through a shaft joint and a connecting turbine, water pump outlet pipeline through a water washing tower inlet, water washing tower outlet pipeline through a turbine inlet and a turbine outlet through pipeline connecting the upper part tower inlet, flash tower lower part outlet pipeline through a parsing tower inlet, analysis tower outlet pipeline through a water storage tank inlet, water storage tank outlet through pipeline connecting water pump inlet. This utility new type is a beneficial effect, saving energy and reducing using electric load, production cost is reduced.
NOVELTY - A one carbon pneuma joint environment-friendly wood continuous carbonization and gasification of a device. The wood raw material according to a certain speed from the top continuously inject, gasification of solid carbon according to a certain speed from the bottom continuously discharging, At the same time, after a dispersed into one with a quantitative air, a inner bed layer is a high temperature gas by high temperature draught fan from the lower part continuous extraction and pressurizing in the top part into the burner. A water cold bottom plate in a furnace brackets (1), (2), the upper part in turn connect with multi-annular space gas is a gas derive segment (3), a furnace shell (4) and smoke-suppressant wherein furnace cover (5), a lower part a charcoal cooling pipe (6), the inner side of building refractory brick (7) and heat preservation layer (8), charcoal cooling pipe (6) lower part a multi point a balanced continuous a kick-out device (9), a low and in turn a spiral feeder (10) is a star-shaped discharging valve (11). The advantages: easy manufacturing, low investment, convenient operation, energy saving, there is no three-waste.
NOVELTY - This utility new type relates to a one biological diesel catalytic splitting device, comprising in turn of a splitting furnace, catalytic jar, heat exchanger and oil storage tank, first splitting furnace through the raw material vaporizing separating the heavy oil, and then the oil catalyzing splitting into gasoline and diesel oil is low molecule quantity through catalytic jar, then the oil gas cooling a liquid oil and non-condensable gas to remove impurities is wherein, finally collecting liquid oil through oil tank using density difference principle and separate the oil mixed in through a water heat exchanger, a product quality gasoline and diesel oil in accordance with a quality index of biological diesel oil. This utility new type provide a biological diesel oil catalytic splitting device, structure is simple, production cost is low, production efficiency is high, product quality is good.
NOVELTY - This utility new type provide a one to produce biogas fertilizer mainly is methane pool system, comprising acidifying, pool, concrete biogas pool, a soft marsh gas pool number and source liquid pool, a soft marsh gas pool in turn number, and the first soft marsh gas pool and a concrete marsh gas pool is connected with the last one soft marsh gas pool and a source liquid pool. This utility new type marsh gas pool system, one a concrete marsh gas pool and fully fermentation of a multi-soft marsh gas pool, produce a large amount of biogas slurry and biogas residue to for farm use, and produce little marsh gas for machinery operation, light and so on use.
NOVELTY - Preparing aerobic sludge compostable composite microbial agent, comprises taking Bacillus subtilis having a preservation number of CICC.NO. 10066, Bacillus licheniformis having a preservation number of CICC.NO. 10103, Lactobacillus acidophilus having a preservation number of CICC.NO. 6075, Candida utilis having a preservation number of CICC.NO. 31272, and Phanerochaete chrsosporium having a preservation number of CICC.NO. 40719, and mixing, and inoculating each culture into a fermentation culture medium, and culturing, to obtain the product.    USE - The composite microbial agent is useful in aerobic sludge composting process (claimed).    ADVANTAGE - The method produces composite agents which are inoculated into early aerobic sludge compost, so that the pile reaches high temperature phase as early as 4-6 days, where the compostable cycle required time is 11-14 days, stockyard moisture content is decreased by 18-25%, and the reactor total nitrogen content is increased by 15-20%, and thus it improves composting process.
NOVELTY - The microbial agent comprises nitrobacter strain or the culture fluid as the active ingredient and provides excellent digestive effect of the organic material and the growth capability. The microbial agent improves the physico-chemical property of the effluent in the livestock excretion disposal system. The microbial agent is provided to the lower part of the microbial agent medium layer through an input tube.    USE - Microbial agent, such as nitrobacter, for use in a livestock wastewater treatment system (Claimed).    ADVANTAGE - The microbial agent comprises nitrobacter strain or the culture fluid as the active ingredient and provides excellent digestive effect of the organic material and the growth capability, and hence ensures cost effective processing of effluent, and high efficiency and reduced cost of the microbial agent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a purifier for the purifying method of the livestock wastewater. (Drawing includes non-English language text).
NOVELTY - This utility new type relates to one a biomass gasification device. One a biomass gasification furnace, comprising a furnace body, a furnace body comprising the storage layer, burning layer and ash layer, a body layer is set with oxygen-increasing combustion wherein an air outlet, an ash layer and the bottom of the furnace body is set with a slag outlet, the storage layer upper part matching set with feeding device, an ash layer lower part set with a device with a spiral ash-stir, the bottom of the combustion layer set with activity fire grate, the fire grate activity set including a multi-row furnace grate of the furnace unit. This utility new type effectively carry out slag to ensure the normal use of biomass gasification furnace, provide sufficient pneuma source, which avoids the breaking, is the phenomenon, greatly increase the market competitive power of device.
NOVELTY - This utility new type relates to a biomass pneuma one machine for removing system. A biomass gasification machine one seal protecting dust removing device, comprising pedestal shell of biomass gasification machine, set with a shell body outlet of one side and the bottom is set with a shell body bottom of the discharging of the discharging mechanism comprising a shell body set at the bottom of driving rotating shaft centre, is set with driving motor, a speed reducer side under a driving rotating shaft and a shifting fork is set with driving rotating shaft upper part, the driving electric machine and speed reducer through a transmission, output end of speed reducer and driving the rotating shaft through the connecting shaft, the driving rotating shaft and shell bottom plate lower part and set with a base, the shell body upper part fixing plate set with shaft set, the shifting fork middle part through fixed bolt and shaft set with set clearance match shaft set is a driving rotating shaft top protecting hood, a shifting fork part rotate around the driving rotating shaft fixed. This utility new type structure is simple, design is reasonable, through concave-convex structure is a special bearing and an annular groove and an annular bulge mutually matching is, effective protection of the bearing, increase the use life of bearing.
NOVELTY - This utility new type relates to a biomass gasification machine set one decoking device. A biomass gasification machine set one multi-pipe condensing decoking device, comprising upper and lower two hollow tank body and a side by side in a multi-set of condensation pipeline between two tank body, two box body and condensing pipeline between a connected connection, two in a hollow box body upper opening set with a air inlet and air outlet, further set with supporting feet and cleaning wherein a hollow tank body of the bottom. This utility new type has simple structure, aiming at the existing technology exist, a new process is improved and innovation of structure, so the utility model is a new type can exert greater the more effective a function in a biomass gasification machine set, this utility new type for a gas characteristic in biomass gasification machine set a direction of distributing and design a decoking dust removing effect is improved greatly.
NOVELTY - This utility new type relates to a biological diesel oil one desolventizing device, comprising pump, an ejector, a cooler and storage tank, comprising pump, an ejector, a cooler and storage tank, a circulation operation of this device is to methyl alcohol is cooling medium, a storage tank for the liquid is methyl alcohol, and tank bottom of outlet connection is through a pump rear pipeline, and a nozzle connecting injector, the injector is at the bottom and cooler entrance of a, biological diesel oil production in a add excess methanol in the injector by evaporation after reaction is finished, after cooling in a methanol solution of a top outlet and the storage tank by a cooler. This utility new type in the conventional biological diesel oil production of said vapour-liquid cooling time of methanol into high efficiency of luminous liquid cooling can be a negative pressure, desolventizing time is shortened, and the methyl alcohol basically without loss, high removing efficiency, a heat exchanger area is reduced more than 50%, device investment and operation cost a has a important popularization value.
NOVELTY - One a biogas slurry pre-concentrate, orderly comprising a source of liquid tank, liquid pump source, multi-medium filter, cross-flow filter and micro-filter film component, a cross-flow filter and micro-filter film component in the concentrated water side are a source and liquid tank. Pre-processing device further comprising a backwashing pump, a cleaning for each of a component. This utility new type greatly reduces the biogas slurry concentrate type reverse osmosis film of load, slows down the happen of film pollution, reducing the reverse osmosis film of cleaning time, investment and operation cost is low, small occupied area, and using after backwashing segment disk-tube reverse osmosis film permeation side outlet, which saves the dosage of water.
NOVELTY - This utility new type claims a steam combustion-supporting one a time type biomass gasification furnace, comprising a biomass by one secondary gasification device, dust purifier, a secondary gasification heat exchanger a burning tube, a one time biomass gasification device by a splitting chamber, spiral feeder, an ignition device, a rotating shaft and reverse turning bed, one end exhaust pipe and a splitting chamber and side wall of splitting chamber and a connecting part, and the other end and entrance of smoke dust purifier connection, pneuma exit of smoke dust purifier through gas conveying pipe and gas inlet pipe of a secondary gasification heat exchanger connection, the gas pipe is a secondary gasification heat exchanger connecting with a combustion tube. Because the dust cleaner and a secondary gasification heat exchanger, a splitting of a smoke dust purifier dust removing after entering into a secondary gasification heat exchanger carry out a secondary gasification to make the gas in the containing a tar gasification again, so as to make the energy a futher use.
NOVELTY - This utility new type relates to a biomass granule one melting furnace, comprising a furnace body, a furnace body set with inner hearth, a furnace body set with a feeding device, the furnace body has a secondary one concreting of shell, the inner wall of a shell set with an asbestos insulating layer, an asbestos insulating layer inside a refractory brick by build into a hearth with a return air channel, the top part of the hearth set with furnace cover, a furnace body of furnace cover is hinged with a horizontal set of heat recovery chimney, one side of the hearth is provided with a feeding square wherein, a air inlet set on the adjusting plate. This utility new type of furnace shell by one time casting concreting, strong shock resistance, high temperature resistance, prolongs the service life of whole machine, melting and heat preservation is integrally semi-gasification combustion to swirl type air distribution design, a hearth inner heating surface and heat uniformity, so that the production efficiency of metal melting increase, satisfying requirement of the enterprise, without pollution.
NOVELTY - This new utility model belongs to user for biomass gasification furnace technology area, specifically claims a kind of one user for biomass heat de-coal gas combustion stove, connect one supply of pyrolysis and pyrolysis double for a kind of reaction product (gas and carbon residue) dividing time period dividing position for cooking the technology scheme, wherein, comprising rotary roller type pyrolysis reactor of present stator and the hollow cylinder structure is sleeved in to the central stator, stator comprises from outside to inside in turn is shell, heat preservation layer, an electric heating layer, an electric heating radiation in and pass through polymer sunlight irradiation in the said each layer, rotor comprises inner shell, in shell inner wall baffle plate, inside shell one end is cap cover and the other end is rotating connector, inner shell is exposed two end outer side stator outside is in turn fixed on insulating layer, shell, gear, gear and gear coupling of the motor shaft. The utility model is new type of smoke not containing tar, and no residual tar stove, ignition fire, add cooking heat, simple structure, wide use in agriculture herdsman home cooking and heating.
NOVELTY - This utility new type relates to a primary-secondary garbage straw stick one pneuma for furnace, comprising outside furnace and inner furnace containing a raw material containing moisture of drying raw material, inner lower part by a furnace to below set with hopper-shaped ash outlet wherein a hopper-shaped dust collecting pool, the hopper-shaped ash outlet wherein a hopper-shaped dust collecting pool is furnace side wall set with a hopper-shaped ash outlet is higher than lower wherein is air outlet, wherein inner furnace overhead support b outside furnace is hopper-shaped the upper part space, wherein the bottom of internal furnace set with inner ash outlet wherein, a connection set b furnace with hopper-shaped ash wherein the upper part space and set with inner furnace inner ash b the upper part space of stir device a furnace lower part set with along the axial direction set outside is connected with a speed reducer and a rotating of the ash outlet shaft, an ash shaft. This gasification furnace can satisfy different raw material gasification, in large scale production.
NOVELTY - This utility new type outside one relates to a straw gasifier, comprising a furnace body lower pushing feeding device, lower push device is set on feed wherein the feed, a feed a feed pipe connecting b the bottom of the furnace body, a furnace body upper part set with an air outlet, the lower pushing feeding device comprising a feeding pushing plate and the left and right sliding plate, left and right pushing plate set with a feeding b wherein outside along the feeding direction wherein the feed of the left and right two side is b feed wherein the feed direction vertical to a centre shrunk port shape section or a side expanding state, the feeding push plate corresponding to the feed direction wherein the feed is set with feed wherein the reciprocating feeding or exiting through a left, right pushing plate, a feeding wherein inner outer wall of a size smaller than a size of the inner or feeding tube. Efficient combustion and removal of gasification furnace, the structure is simple, the operation is convenient, time saving force, ash-discharge property and combustion gasification.
NOVELTY - This utility new type relates to one a pyrolysis gasification tar multistage circulation filtering collecting device, belonging to the biomass use technology field. This device comprising in series between the pyrolysis gasification device and water-cleaning and de-dusting device, cooling device and pneuma storage device, the cooling device and the pneuma device set with draught fan connected with a filter screen filtering device, carbon absorbing filtering device and a graphene film filter between the water-cleaning and de-dusting device and cooling device. After using this utility new type, through the pyrolysis gas circulation of cooling water due to the multiple filter and the very pure, storage used for heat generation or a centralized gas supply, a burn fully, without pollution of clean energy.
NOVELTY - This utility new type relates to a biomass pneuma one purification cabinet, comprising cabinet body, said cabinet body upper part set with an air outlet, the bottom of cabinet body set with the water wherein the inner cabinet body by inner upper to lower orderly set with water inlet tube, labyrinth water washing room and nozzle of the pneuma tube, air inlet pipe is lower than the lower part cabinet body. Using water through pre-removing tar, matching corresponding to subsequent labyrinth water washing efficiency of tar adjusting air inlet, a maximum, the best removal rate of quantitative biomass pneuma.
NOVELTY - This utility new type relates to a Anaerobic dry fermentation a continuous automatic feeding and discharging system, belongs to biomass using technology field. The bottom of this system include feeding the top part provided with a feeding end and a discharging end with a discharging wherein a fermentation library wherein the lower fermentation library is set with spraying pipe of spray head and a drain gate plate connected through a biogas collection pool, inner fermentation library is set with interval are arranged above, collection pool through a pipeline and a liquid circulation pump connected spraying pipe, a bottom inner fermentation library by the feeding end is equipped with a spiral conveyor to a discharge end, a feeding port is equipped with the bottom of the hopper is set with start-shaped discharging machine, a feed conveyor located at a lower part of a discharging wherein is equipped with a opening and closing a discharging baffle plate, wherein wherein material discharging baffle plate is at the low end of conveyor. This utility new type realize the automatic continuous feeding and discharging, which greatly saves the dry fermentation engineering construction and operation cost and increase the methane. feeding and discharging work efficiency.
NOVELTY - The modifying septic tank water-saving energy-saving system has sewage collection fermentation which uses marsh gas production system. A water inlet has one end connected to a fermentation jar or fermenting pool, and the other terminal is connected to a source tank. A slurry waste water resource collection is connected to the fermentation jar or fermenting pool water outlet, and the biogas liquid waste is connected to water resource collection (5) using source with septic tank through water pressure limiting pipe and fermentation jar or fermenting pool.    USE - Modifying septic tank water-saving energy-saving system.    ADVANTAGE - Provides septic tank water-saving energy-saving system which is economic, water-saving, energy-saving, and environment friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a modifying septic tank water-saving energy saving system.    Drain pipe (1)    Processing methane fermentation production (2)    Marsh gas energy collection (3)    Water pressure limiting tube (4)    Sewage water resource collection (5)
NOVELTY - Saccharomyces cerevisiae SC-spt1509 strain with the preservation number CCTCC NO: M2014316, is new.    USE - The strain is useful in fermentative production of ethanol fuel (claimed).    ADVANTAGE - The strain has high sugar alcohol conversion rate, xylose utilization rate of more than 65%, and increases ethyl alcohol production rate to 46.66%. The method is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use method of the Saccharomyces cerevisiae strain in fermentative production of ethanol fuel, comprising (i) inoculating Saccharomyces cerevisiae SC-spt1509 on culture plate containing basic culture medium and culturing at 35-40 degrees C for 2-3 days, (ii) inoculating resulting culture on slant culture medium and culturing at 35-40 degrees C for 1 days, (iii) inoculating resulting slant culture on seed culture medium and culturing at 35-40 degrees C for 8-12 hours, and (iv) inoculating resulting seed culture on fermentation culture medium, where the inoculating volume is 6-12% (vol./vol.) and fermenting at 35-40 degrees C for 30-50 hours.
NOVELTY - Bioorganic fertilizer is prepared by (a) heating, drying and crushing organic raw materials, sterilizing the crushed organic raw materials, adding fermentation agents comprising 300000000/g viable cells to the sterilized mixture, and fermenting the mixture to obtain organic fertilizer, and (b) mixing the organic and inorganic raw materials, heating, drying and crushing the mixture, granulating the crushed mixture, drying, cooling the mixture, adding fermentation agents comprising more than 200000000/g viable cells to the mixture, and fermenting the mixture.    USE - The bioorganic fertilizer is useful for promoting plant growth (claimed).    ADVANTAGE - The bioorganic fertilizer increases mortality of insect eggs to more than 95%, and is prepared cost-effectively.    DETAILED DESCRIPTION - Bioorganic fertilizer is prepared by (a) heating, drying and crushing organic raw materials, sterilizing the crushed organic raw materials, adding fermentation agents comprising 300000000/g viable cells to the sterilized mixture, and fermenting the mixture at 25-35 degrees C for 7-10 days to obtain organic fertilizer, where the fermentation agents comprises 20-30% Actinomyces, 10-20% Lactobacillus, and 50-70% yeast, and (b) mixing the organic and inorganic raw materials, heating, drying and crushing the mixture, granulating the crushed mixture, drying, cooling and screening the mixture, adding fermentation agents comprising more than 200000000/g viable cells to the mixture, and fermenting the mixture, where the fermentation agent comprises 30-50% Bacillus subtilis, 15-30% Azospirillum, 15-30% Rhizobium and 20-30% Streptomyces.
NOVELTY - This utility new type claims a one combined living waste packing device, comprising wet storage hopper, a stirrer, an additive adding device, adding quicklime device, a conveying device and a wolf tooth rod needle is filling type packaging machine, a conveying device with two a and discharging wherein wherein one conveying device between a setting material in a mixer wherein a wet storage hopper is the feeding port, and the other a conveying device setting in a mixer between the feeding port and a filling type packaging machine is provided with wolf tooth rod is needle, said additive adding device and quicklime add a setting in the feeding port of the stirrer. After using a technology plan, this utility new type one a combined living waste packing device, a rear crushing of the domestic garbage is convenient for storage, transportation and use of waste, household garbage derived fuel increase of production efficiency, structure is scientific and rational arrangement, convenient and practical production efficiency high.
NOVELTY - Organic fertilizer comprises 30-80 pts. wt. chicken manure, 1-30 pts. wt. dairy manure, 1-30 pts. wt. sheep manure, 1-10 pts. wt. potassium fulvate, 1-10 pts. wt. tea seed cake, 1-10 pts. wt. soybean cake, 1-10 pts. wt. tobacco stalk and 0.1-1 pt. wt. chitosan.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer enables to control root-knot nematodes, and provide pest and disease resistance to crops including banana.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic fertilizer, which involves (a) crushing and sieving tea seed cake, soybean cake and tobacco stalk using sieve of 60 meshes, (b) mix, drying, and pulverizing chicken manure, dairy manure, and sheep manure, and (c) adding products obtained in the steps (a) and (b), adding potassium fulvate and chitosan to obtained mixture, and packing obtained mixture.
NOVELTY - This utility new type relates to one used for a biomass without oxygen low temperature carbonization furnace is air guiding device, set with a dry distillation furnace, used for guidance inner dry distillation furnace is a pneuma, comprising a dry distillation furnace cover, the top centre of the dry distillation furnace cover is set with motor base, a electric machine base of the top fixed a motor, the motor shaft of the electric machine through a shaft joint rotating shaft, the rotating shaft passes through the downward a dry distillation furnace cover and fixing a fan, the fan is set with a plurality of uniform distribute a fan blade, a dry distillation furnace cover and fan is set with air guide body. This utility new type through the guide flow fan and dry distillation furnace cover combine to make a flow of dry distillation furnace form inner circulation, realize the uniform heating of material, reaction, heat energy use rate is high, increase the production efficiency.
NOVELTY - This utility new type claims a one garbage, comprising a household garbage organic matter and surface after crushing hole with hole of cylindrical packing film, a household garbage organic matter after crushing fill inner hole with hole of cylindrical packing film in surface and two end sealing is sausage. This utility new type one a garbage bowel is convenient for storage, transportation and use, a is a household garbage derived fuel supply is ready, so as to greatly save manufacturing into domestic garbage derived time of fuel, increase economic benefit.
NOVELTY - This utility new type claims a RDF domestic garbage pyrolysis gasification gas burning clean high efficiency power generation system, including garbage, trash crushing machine, domestic garbage drying device, making the additive adding device, a pyrolysis gasification furnace, a combustion chamber, a hot air device, a steam generator, a building a device, a temperature adjusting room and tail pneuma processing pool, the domestic garbage source through separating, crushing and drying, then RDF is made of solid fuel, the RDF solid fuel pyrolysis gasification process generate a combustion gas, combustible gas, burning the hot air heat exchange through a steam outlet, the steam generator steam generation process. This utility new type household garbage RDF a pyrolysis gasification gas burning clean high efficiency power generation system, RDF solid fuel source than organic high garbage, fly ash total quantity greatly reduce energy effective to weight d. high temperature combustion gas to make the dioxin completely decompose and eliminate pollution of at the same time brings many benefits.
NOVELTY - This utility new type claims a household garbage one RDF a pyrolysis gasification gas clean high efficiency power generation system, including garbage, trash crushing machine, domestic garbage drying device, making the additive adding device, a pyrolysis gasification furnace, a pneuma generator, an expansion screw electric generator, building material preparation device, a temperature adjusting room and tail pneuma treatment pool, a source household garbage into the RDF solid fuel gasification generate a combustion gas, a combustion pneuma generation, the generation of waste heat gas the pneuma to expansion screw futher is generation electric generator. This utility new type one a domestic garbage RDF a pyrolysis gasification gas clean high efficiency power generation system, RDF fuel than solid source garbage organic matter high, pyrolysis gasification obtained using a combustion gas generation process, which greatly reduces the dioxin is a, a level generation, power generation is large, clean without pollution and waste in processing process of each one-like product can be a reasonably and fully use of.
NOVELTY - An environmentally-friendly chlorofluorocarbon-free refrigerant comprises 20-40 parts mass propane, 30-40 parts mass propylene, 25-40 parts mass cyclobutane, 10-15 parts mass tetrafluoropropene, 10-18 parts mass trans-1,3,3,3-tetrafluoropropene, 5-15 parts mass trifluoroiodomethane, 5-10 parts mass fluorine methyl iodide, 8-12 parts mass difluoromethane, 3-8 parts mass tetrahydrothiophene, 15-40 parts mass liquid carbon dioxide and 5-10 parts mass low-temperature frozen lubricating oil.    USE - Environmentally-friendly chlorofluorocarbon-free refrigerant (claimed).    ADVANTAGE - The environmentally-friendly, safe and economical chlorofluorocarbon-free refrigerant has ozone depletion potential of 0, low global warming potential and flammability, suppressed fuel explosion, and excellent cooling property. The long-term use of chlorofluorocarbon-free refrigerant does not damage the ozone layer. The leakage of refrigerant can be sensed by user due to the presence of unpleasant-odor of tetrahydrothiophene.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of environmentally-friendly chlorofluorocarbon-free refrigerant, which involves uniformly mixing liquid carbon dioxide, low-temperature frozen lubricating oil, propane, propylene, cyclobutane, tetrafluoropropenes, trans-1,3,3,3-tetrafluoropropene, trifluoroiodomethane, fluorine methyl iodide, difluoromethane and tetrahydrothiophene at room temperature of 20-25 degrees C.
NOVELTY - The unit has a unit part provided with a hearth (2) connected with an air ring inlet channel (3) and formed with a groove (16). The air ring inlet channel is connected with an air inlet pipe (9). A side part of the hearth is equipped with a gas pipe (8). A top part of the hearth is arranged with a seal cover (12). An upper part of an upper hearth (6) is connected with a guide air anti-blocking ring (7). An inner wall of the guide air anti-blocking ring is mounted with a poly air ring channel (14). An inner wall of the poly air ring channel is connected with an outlet end of the gas pipe.    USE - Flue-cured tobacco biomass gasification unit.    ADVANTAGE - The unit has stable operation, strong blockage effect and convenient biomass fuel and coal fuel usage effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a flue-cured tobacco biomass gasification unit.    Hearth (2)    Air ring inlet channel (3)    Upper hearth (6)    Guide air anti-blocking ring (7)    Gas pipe (8)    Air inlet pipe (9)    Seal cover (12)    Poly air ring channel (14)    Groove (16)
NOVELTY - Preparation of molded biomass fuel particles involves pre-processing biomass raw material, providing resultant product into closed vessel-type dryer, vacuuming, quenching the resultant product by uniformly mixing raw material with different density and moisture content, maintaining the resultant product for 10 hours or more, crushing, screening, providing the resultant product into centrifugal separator, providing resultant product into molding machine, and extrusion molding the resultant product.    USE - Preparation of molded biomass fuel particles (claimed).    ADVANTAGE - The method economically provides molded biomass fuel particles by environmentally-friendly process.    DETAILED DESCRIPTION - Preparation of molded biomass fuel particles involves pre-processing biomass raw material by slicing, segmenting and tableting the raw material to length of 50 mm or less, providing the resultant product into closed vessel-type dryer at 60-150 degrees C, vacuuming the resultant product at 133 Pa or less, then quenching the resultant product by uniformly mixing raw material with different density and moisture content until the moisture content becomes 15-22%, maintaining the resultant product for 10 hours or more, crushing the resultant product using crusher, screening the resultant product using sieve which is oval-shaped sieve with short shaft of 8 mm, long shaft of 20 mm, separating length of less than 20 mm and width of less than 8 mm, providing the resultant product into centrifugal separator to air-separation process of the resultant product, providing resultant product into molding machine, and extrusion molding the resultant product.
NOVELTY - A solid bamboo carbon rods are obtained by providing pure bamboo processing residue as raw material, crushing, sieving the resultant product, drying, pressing the resultant product into rod blank, and providing the resultant product into high-temperature anaerobic charcoal carbonization kiln. The solid bamboo carbon rods have diameter of 4-6 cm and length of 40-50 cm.    USE - Solid bamboo carbon rods (claimed).    ADVANTAGE - The solid bamboo carbon rods have excellent processability, and are manufactured by economical and environmentally-friendly process with high quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of solid bamboo carbon rods, which involves selecting bamboo floor, bamboo plywood, bamboo chopsticks, bamboo, bamboo chips and other waste bamboo as raw material, crushing raw materials, sieving the resultant product using 50 mesh steel sieve, drying the resultant product having particle size of less than 50 mesh, then re-crushing the sieved product having particle size of more than 50 mesh, then sieving, drying the resultant product to moisture content of 10%, pressing the resultant product, cutting the resultant product into blank, and providing the resultant product into carbonization kiln. The raw material is 100% pure bamboo components, and does not contain other wood chips or debris. The bamboo processing residue is obtained by aging the bamboo for more than 4 years.
NOVELTY - The drying system has a sieve (16) provided with a biological leaching filter reactor (18). A biological tunnel drying chamber (3) is arranged with an insulating layer (6) and a perforated pipe (7). The top portion of biological tunnel drying chamber is provided with a waste gas outlet (11) passing through a waste pneuma bio-filter (12), an evaporator (14) and a waste pneuma absorber (15). The biological tunnel drying chamber is arranged with a tripper (8).    USE - Tunnel-type biological garbage drying system.    ADVANTAGE - The biological drying tunnel is environment-friendly and energy-saving.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the tunnel-type biological garbage drying system.    Biological tunnel drying chamber (3)    Insulating layer (6)    Perforated pipe (7)    Tripper (8)    Waste gas outlet (11)    Waste pneuma bio-filter (12)    Evaporator (14)    Waste pneuma absorber (15)    Sieve (16)    Biological leaching filter reactor (18)
NOVELTY - A biomass-derived fuel comprises 10-30 pts. wt. pine sawdust, 20-50 pts. wt. hardwood sawdust, 5-10 pts. wt. organic solid waste, 20-30 pts. wt. straw powder, 5-10 pts. wt. pulverized coal, and 0.2 pt. wt. desulfurizing agent. The organic solid waste is obtained by drying and crushing municipal solid waste.    USE - Biomass-derived fuel (claimed).    ADVANTAGE - The biomass-derived fuel is environmentally friendly.
NOVELTY - An alcohol ether gasoline comprises 20-40 pts. wt. gasoline, 20-30 pts. wt. methanol, 10-20 pts. wt. ethanol, 10-25 pts. wt. hydrocarbon, 1-7 pts. wt. ethyl acetate, 2-8 pts. wt. methyl benzoate, 3-10 pts. wt. acetone, 5-15 pts. wt. methyl tert-butyl ether, 1-8 pts. wt. isopropyl ether, 1-5 pts. wt. polytetrafluoroethylene and 2-6 pts. wt. isopropanol.    USE - Alcohol ether gasoline is used for vehicle.    ADVANTAGE - The alcohol ether gasoline is safe and environmentally-friendly, and has excellent fuel economy and combustion performance, and reduces emission.
NOVELTY - An alcohol-based fuel comprises 50-75 wt.% methanol, 10-30 wt.% ethanol, 4-10 wt.% butanol, 3-11 wt.% additive, 2-7 wt.% corrosion inhibitor and 5-10 wt.% octane-number enhancing agent. The additive is a mixture of iron and acetone. The corrosion inhibitor is a mixture of ethyl acetate and methyl benzoate. The octane-number enhancing agent is a mixture of t-butyl acetate, crotonamide, methyl cyclopentadiene and methyl tert-butyl ether.    USE - Alcohol-based fuel is used for vehicle.    ADVANTAGE - The alcohol-based fuel is safe and environmentally-friendly, and has high octane number and fuel value, and reduces discharge emission.
NOVELTY - This utility new type claims a one organic solid waste splitting furnace is a blockage, comprising a mesh barrier plate (1), the arc-shaped blocking cover (2), an air outlet cylinder (6), a cylinder (4) and fixed bracket (5), wherein this flame retardant material cylinder (4) is larger than the air outlet cylinder (6), and sleeved on the air outlet cylinder (6), cylinder (4), one fixed terminal b inner furnace wall of furnace A, resistance, splitting cylinder (4), and the other end and hole blocking plate (1) is connected, this mesh blocking plate (1) of cylinder wall and close of one end are distribute a small multi-hole (11), arc-shaped blocking cover (2) setting a mesh barrier plate (1), arc-shaped blocking cover (2) of the cylinder part (22) of outside wall and a flame cylinder (4) between the inner wall set with fix bracket (5), the arc-shaped blocking cover (2) is fixed b a resistance cylinder (4) up. This utility new type to reduce or avoid a splitting is not solid granule with gas out or blocking door, the splitting process proceeding smoothly.
NOVELTY - A grease composition comprises 30-35 wt.% base oil, 0.1-0.5 wt.% zinc dialkyl phosphorodithioate, 0.5-1 wt.% sulfurized fats and oils, 3-5 wt.% modified calcium sulfonate, 3-5 wt.% polyisobutylene, 3-5 wt.% castor potassium acetate, 25-30 wt.% thickener (soap), 5-10 wt.% polyethylene terephthalate and 10-15 wt.% liquefied petroleum gas propellant.    USE - Grease composition is used for automobile component.    ADVANTAGE - The grease composition has excellent water resistance, acid resistance, alkali resistance, moisture resistance, lubricating effect, wear resistance and abrasion resistance, and can quickly permeate into the automobile component.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of grease composition, which involves uniformly mixing base oil, zinc dialkyl phosphorodithioate, sulfurized fats and oils, modified calcium sulfonate, polyisobutylene, castor ester potassium, thickener (soap), polyethylene terephthalate and liquefied petroleum gas propellant.
NOVELTY - Method for treating sewage sludge, involves (a) subjecting the sewage to activated sludge treatment, passing treated sewage to secondary sedimentation tank, storing the sludge in storage tank, and passing the sludge from the storage tank to anaerobic fermentation tank, (b) performing anaerobic fermentation of the sludge to produce biogas, biogas residue and biogas slurry, and (c) subjecting the biogas to wet desulfurization and dry desulfurization for purification of biogas, storing purified biogas, and directly discharging the biogas slurry to a conditioning tank.    USE - The method is useful for treating sewage sludge to produce biogas, biogas residue and biogas slurry. The biogas and biogas residue are used as auxiliary fuel for power plant (all claimed).    ADVANTAGE - The method consumes less energy.    DETAILED DESCRIPTION - Method for treating sewage sludge, involves (a) subjecting the sewage to activated sludge treatment, passing treated sewage to secondary sedimentation tank, adjusting moisture content of sludge at 95.5-97%, storing the sludge in storage tank, and passing the sludge from the storage tank to anaerobic fermentation tank through screw conveyor, (b) performing anaerobic fermentation of the sludge by pumping pressure and stirring the sludge during anaerobic fermentation to produce biogas, biogas residue and biogas slurry, where the anaerobic fermentation is performed without using mechanical power, and (c) subjecting the biogas to wet desulfurization and dry desulfurization for purification of biogas, storing purified biogas in a storage tank, directly discharging the biogas slurry to a conditioning tank provided with nutrients, water and microorganism, and promoting microbial activity in the conditioning tank.
NOVELTY - Preparation of biochar comprises mixing sludge biostraw with compressed molding; compression molding of biochar into the tube furnace carbonization; and chemically modifying the carbonized particles to produce biochar having a porous structure.    USE - Method for preparing biochar used for purifying heavy metal containing wastewater (claimed).    ADVANTAGE - The method solves the low moisture content of raw cotton stalks problems, improves adhesion of compression molding materials, and helps solve the environmental problems of sludge.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the method for preparing biochar (Drawing includes non-English language text).
NOVELTY - High-concentrated waste is added to pretreatment tank, pre-treated, pre-treated liquid waste is added to primary anaerobic reactor, stirred and fermented to obtain biogas. The biogas is entered into secondary anaerobic reactor through outlet pipe. The biogas is entered into three-phase separator, purified, and the processed effluent is passed to sedimentation tank for subsequent processing after discharged from the separator.    USE - Processing of high-concentrated waste e.g. livestock and poultry wastewater.    ADVANTAGE - The method enables processing of high-concentrated waste with reduced energy consumption by an economical and reliable process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for processing high-concentrated waste, which consists of primary anaerobic reactor, feeding tank, secondary anaerobic reactor, feeding tank effluent pump and sedimentation tank.
NOVELTY - The method involves pumping active sludge to high-speed aeration tower after pre-processing a sewage pump. The microorganism is contained in active sludge of a high speed aeration tower (2). The active sludge is entered into a buffer pool (6) from high speed aeration tower. The active sludge is pumped to a low-speed aeration tower (8) by sewage pump. The active sludge is entered into a precipitation pool (11) from low-speed aeration tower. A reflux pump (13) is pumped back to high and low-speed aeration towers, after depositing sludge in buffer and precipitation pools.    USE - Biogas liquid discharging sewage type aeration-biodegradable treatment method for production of livestock manure organic waste material fermentation for farmland.    ADVANTAGE - The aeration-biodegradable treatment process is simplified, and the oxygenation efficiency is improved. The aeration-biodegradable treatment process is popularized easily, and the energy consumption and processing cost are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the biogas liquid discharging sewage type aeration-biodegradable treatment process.    High speed aeration tower (2)    Buffer pool (6)    Low-speed aeration tower (8)    Precipitation pool (11)    Reflux pump (13)
NOVELTY - The method involves obtaining high concentration poultry waste water from a pool. Livestock waste water is entered into an anaerobic reactor. Continuous stirring process is performed. Marsh gas is produced. Air three phase separating process is performed. Marsh gas purification process is performed. Solid-liquid separating process is performed in a separating pool. Water is entered into a biochemical processing system. Water is fed into a SBR pool. Aerating process is performed. Sedimentation separating process is performed. Water is discharged from a discharging pool.    USE - High concentration standard discharge livestock and poultry waste water processing method.    ADVANTAGE - The method enables efficiently performing waste water processing operation and anaerobic fermentation process so as to realize renewable energy and marsh gas production in an energy-saving and environment-friendly manner. The method enables increasing processing quality and reliability in a cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a high-concentration two level anaerobic livestock and poultry waste water and biogas producing air processing system.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a high-concentration two level Anaerobic livestock and poultry waste water and biogas producing air processing system.'(Drawing includes non-English language text)'
NOVELTY - The method involves entering papermaking sludge into a regulating pool. The regulating pool is set with an inner stirrer. The material in the regulating pool is entered into a first-stage reactor and anaerobic treatment is performed. The water is entered into second stage reactor after first stage reactor. Liquid, solid and gas are phase-separated. Anaerobic reactor is arranged to produce sludge in sludge storage tank. The settled sludge is entered into a filter system with an organic fertilizer.    USE - Papermaking sludge biogas production and utilization method.    ADVANTAGE - The efficiency of the biogas production is high. Energy-saving and environment-friendly can be achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the papermaking sludge biogas production and utilization method. (Drawing includes non-English language text)
NOVELTY - The method involves moving a cutting machine through double-track of a main machine. The floor is mounted with a clamp holder which is mounted with a circumferential clamp. The circumferential clamp is configured for mounting a circular saw which is configured for cutting the log predetermined length. A burning gasification furnace is configured for purifying the wastes from the furnace, and the high temperature gas is introduced into the injection entrance.    USE - Method for manufacturing biomass granule.    ADVANTAGE - Improved energy saving effect and reduced cost is achieved.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the method for manufacturing biomass granule. (Drawing includes non-English language text)
NOVELTY - Recycling of kitchen garbage involves mechanically sorting non-combustible inorganic solids from kitchen garbage, removing impurities, then mechanically crushing the resultant product into particles, adding drying agent, subjecting resultant product into molding process, continuously circulating desiccant, drying, adding auxiliary fuel, uniformly mixing the resultant product, pressing and molding the resultant product to obtain solid fuel having calorific value of 4000 kcal/kg or more.    USE - Recycling of kitchen garbage (claimed).    ADVANTAGE - The method enables recycling of kitchen garbage by economical, environmentally-friendly and simple process with reduced energy consumption, without generation of sewage and odor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for system for recycling kitchen garbage.
NOVELTY - The structure is provided with feeding tubes (2,3), a discharging pipe (4) and red mud plastic film (1) that are drawn under water pressure and designed by cut heat seal bonding process using inflatable support tube (7).    USE - Marsh gas pool structure for household garbage.    ADVANTAGE - The ellipsoid red mud plastic film achieves the full advantage of the structure of production of biogas and user-friendly so that with the gas production rate, handling and installation is simple.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating biogas pool structure.    Red mud plastic film (1)    Feeding tubes (2,3)    Discharge pipe (4)    Bath pipe (5)    Inflation tube (7)
NOVELTY - Processing lignocellulosic biomass involves (a) performing steam explosion of the lignocellulosic biomass, and adding dilute acid to the processed material, (b) detoxifying blasting material, and (c) performing fermentation of the material using cellulase enzyme complex.    USE - The method is useful for processing lignocellulosic biomass (claimed).    ADVANTAGE - The method increases ethanol yield by 83.191%.    DETAILED DESCRIPTION - Processing lignocellulosic biomass involves (a) performing steam explosion of the lignocellulosic biomass, and adding dilute acid to the processed material, (b) detoxifying blasting material, and (c) performing fermentation of the material using cellulase enzyme complex. The complex is prepared by mixing Aspergillus niger strain C112 (CCTCC NO: M 2012129) capable of producing beta -glucosidase and Trichoderma reesei strain RUT C30 (ATCC 56765) capable of producing cellulase, concentrating and purifying the mixture, where the ratio of beta -glucosidase activity to filter paper activity is 1.048-2.685. The A.niger strain C112 (CCTCC NO: M 2012129) capable of producing beta -glucosidase is obtained using a culture medium comprising 25-30 g/l corncob, 20-30 g/l straw powder, 5-6 g/l peptone, 10-13 g/l ammonium sulfate, 6-8 g/l potassium dihydrogen phosphate, 0.5-1 g/l calcium chloride dihydrate, 0.5-1 g/l magnesium sulfate heptahydrate, 1-2 ml/l Tween 80 (RTM: Polysorbate 80), 0.5-1 ml/l Mandels trace element, 100-150 ml/l citric acid buffer solution at a concentration of 1 mol/l, where water is added to the medium to make it 1 l.
NOVELTY - Method for quantitatively determining enzymatic activity of exonuclease, involves providing single-stranded DNA complementary to template primer, adding exonuclease I, performing exonuclease I enzymatic reaction, annealing single-stranded DNA templates, forming single-stranded DNA template/primer complex, adding polymerase to form double-stranded DNA, and measuring relative amount of single-stranded or double-stranded DNA in the reaction system by measuring exonuclease I activity degree.    USE - The method is useful for quantitatively determining enzymatic activity of exonuclease (claimed).    ADVANTAGE - The method is simple and convenient to perform, and environmentally-friendly, and prevents radioactive contamination.    DETAILED DESCRIPTION - Method for quantitatively determining enzymatic activity of exonuclease, involves providing single-stranded DNA complementary to template primer, adding exonuclease I, performing exonuclease I enzymatic reaction, annealing single-stranded DNA templates, forming single-stranded DNA template/primer complex, adding polymerase to form double-stranded DNA, and measuring relative amount of single-stranded or double-stranded DNA in the reaction system by measuring exonuclease I activity degree, where the exonuclease I activity and the extent of the reaction system are inversely proportional to amount of double-stranded DNA.
NOVELTY - This utility new type provide a one application biomass gasification technology of food oven, comprising a furnace cover, wherein, the bottom of the furnace body set with mortar, bottom ash tank set with wheels, mortar one side set with ash removing door, mortar wall middle part set with mortar and c is connected air inlet pipe, the top centre set with mortar pneuma distribution plate; the top of the furnace body set with seal water tank, furnace cover buckling seal in a water tank, gas pipe one side connected in upper part of the furnace body, a gas pipe is set with discharging furnace cover, gas pipe the other end vertical to downward extends to collecting jar inner bottom sewage collecting jar set with a bracket, a gas pipe lower part a and a secondary air, roasting bottom connected. The device is a one braising and baking, integrated device, the labour intensity is greatly reduced user.
NOVELTY - This utility new type claims a biomass granule machine with one ring mould, comprising circular mould main body, the ring die hole and mould. A ring mould main body comprising inner layer ring mould and the ring mould outer layer; the ring between inner layer and outside layer annular die with one channel set with groove, the groove surface is set with key groove, the ring mould inner layer set with a opening groove wherein, the ring mould inner surface layer set with several layer ring mould hole, the ring hole centers include outside hole, hole and inner hole, a ring mould main body is one whole structure. This utility new type granulator with ring die has structure design is reasonable, the discharge effect is good and use life is long and so on.
NOVELTY - This utility new type claims a biological fuel granule is made of one machine, it comprising a machine made, pressing, pressing, pressing bed and limiting plate. The machine is made of one end of one side and a crusher through a pipeline, the upper machine is made in lower part mounting die bed, the machine is made in two side wall each mounted with a one, a press mounted into the top of a machine, a low pressure machine mounted with a pressure shaft two, the lower two pressure shaft mounted with a mould. This utility new type has simple structure, biological straw by crusher, conveying the prepared machine inside the press pressing into granular fuel combustion use rate is high after crushing, the cost is low.
NOVELTY - A one-liquid-solid three phase separator pneuma, upper part and lower part two block clapboard (8) according to an included angle of 45 degrees and a vertical side wall (9) form marsh gas collecting room (3), a block plate (8) is a pneuma-liquid separating area (1), a second baffle plate upper part is sludge settling zone (2), the lower clapboard in pneuma-liquid separating area is set with lower flow guide plate, inclined plate set with a sludge zone. Sewage by Anaerobic reactor entering into the bottom, with sludge to move upwards, at the same time, microorganism effect under a methane bacteria produce marsh gas, forming solid-liquid-pneuma mutually contained a mixed fluid, entering into three phase separator to move upwards. This utility new type device structure is compact, flow guide plate design is especially, collecting the help of marsh gas, at the same time reduce the rising gas for disturbance of the return sludge, the sludge.
NOVELTY - This new utility model claims of one process of coalbed methane produced water outlet of device, belonging to sewage processing technology area. The device comprises: for the coalbed methane produced out water for uniformly stirring and homogenizing tank, and the homogenizing tank connected and used for reducing CODCr and catalyze oxidation, and the catalyze oxidation interconnect is used for removing fluorin ion, iron remover of sulfur ion, and the ion remover connected and used for separating precipitated flocculation sediment tank, set with an electrochemical oxidation device and filler catalyze oxidation device and wherein said catalyze oxidation, of the iron remover is set with with electrochemical device, the electrochemical device comprising two individual electrode, wherein one electrode of two or three of electrode with catalyst layer, said catalyst is Shanghai environmental engineering limited company production sales and IR-CF catalyst. The device can effective remove out of coalbed methane produced water sulphide, organic matter equal reducing substance, fluoride and suspended substance, can be to China standard one level discharge standard GB8978-1996 of the.
NOVELTY - This utility new type relates to one used for a biogas liquid of a device, comprising a first sedimentation pool, the first purification pool and the first sedimentation pool is connected, and the first purification pool connected a second purification pool and the second purification pool and a flocculation connected the first purification pool and the second purification pool set with a for the first purification pool and the second purification pool intermittent aerator for aerating and charging oxygen of air blower and a air blower and the air inlet pipeline of the aerator, the air blower for the aeration process, a flocculation tank set with a water inlet pipe, medicine preparation and the tank inlet pipeline is connected and the medicament pipeline connected and a medicine preparation system, through intermittent aeration and oxygen is in a aerobic-facultative-Anaerobic biological process is a, inner control period different... stage, operation mode is flexible, so as to achieve better removing nitrogen and phosphorus removal effect, and intermittent aeration mode can prevent sludge expansion problem, and combine flocculating pool adding flocculating agent in the water quality is better and reaches the requirement of the exhaust standard.
NOVELTY - This utility new type claims a household garbage one fluidization bed without oxygen splitting device, a splitting feeder on one end splitting device is, the oxidization and splitting a feeder, the upper anti-explosion pressure relief seal device is placed in the top of the deoxygenator. splitting the oxidization furnace of lower side, a splitting furnace side mounted with a furnace wall heater, and splitting furnace end is placed a reformer following splitting furnace side set with heating rod, the slag material and splitting furnace wherein a, a classifying cyclone separator and a reformer, the air pressure valve and a classifying cyclone separator connected, a high temperature fan and heating rod connect. This utility new type is a one new-type fluidization bed splitting system, not a classification garbage harmless treatment, a continuous treatment, operation is simple, the automatic degree high, system optimization, low unit energy consumption, without a secondary pollutant generation. b, product splitting pneuma hot a high tar content is low, product structure are carbon, active high.
NOVELTY - This utility new type relates to one type of a biomass continuous pyrolysis furnace, a furnace body structure from upper to lower in turn is divided into a feeding section, a decoding section, cooling section, cooling section water inlet of middle jar install a first knife gate valve, a first knife gate valve mounted one a start-shaped feeder outlet of middle jar install a second knife gate valve, upper part of a feeding section set with air outlet, a furnace body upper part of feeding section and a second knife gate valve connecting the bottom of a furnace body mounted one a start-shaped bar material machine, star bar material machine through a knife gate valve and third spiral conveying machine, a multi-pyrolysis furnace tube mounted in a hot solution of inner furnace body section, heating jacket is covered a section of pyrolysis furnace, one a stirring mechanism mounted in the feeding of inner furnace body section and the other one a stirring mechanism mounted in inner of water cooling section furnace body. This utility new type can realize biomass a material fluidization continuous pyrolysis gasification, a load continuous adjustable.
NOVELTY - This utility new type relates to biomass continuous pyrolysis furnace anti-clogging material shifting mechanism, structure is frequency modulation motor, a speed reducer mounted in a substrate, welding a foundation bed in shell of furnace body, adjusting frequency electric machine and direct-connected speed reducer, a speed reducer output shaft neck a driving chain wheel, a tank mounted in a furnace body, a tank mounting one inner shaft and one end extends into the inner body shaft, a small gear, a driven chain wheel mounted in a tank of a same shaft a, and the small gear in inner furnace body, a chain set in the driving chain wheel, a driven chain wheel, the small gear and big gear ring mutually mesh, big gear ring and lower steel body is mounted a ring inner clamping welding rod in a big gear ring. This utility new type mounted in a biomass material pyrolysis furnace in, a outside through a forced driving power, the biomass a material normal a normal add material in a pyrolysis furnace and product carbon and pyrolysis furnace normal continuous operation.
NOVELTY - This utility new type belongs to the garbage processing device, especially relates to a new-type pyrolysis gasification furnace one. The gasification furnace comprising a furnace body, a furnace body set with inner furnace gate, the bottom of the furnace body and a blast pipeline connected, the top of the furnace body set with coal feeding pipeline, the top of the furnace body is further connected and feeding pipeline, the pipeline one end pushing and pushing a connection, and the other end and the furnace body a, radial and the a connected pipeline, pipeline and a furnace body of a is one cambered surface and inclined plate compose a irregular shape, inclined plate and the horizontal line is 5 degrees to-10 degrees, a furnace body is further connected a section coal discharging tube and a lower section coal discharging pipe. This utility new type structure is simple, the design is reasonable, the garbage pyrolysis gasification process, which avoids the large amount of garbage landfill, saves land, garbage by the high temperature can kill each a harmful a completely removing smell, after gasification of ash can as a paving material of the whole process without waste water, waste a pneuma, would not affect environment.
NOVELTY - This utility new type claims a one biomass, municipal domestic waste integrated splitting the pneuma furnace, wherein a vertical parallel of two furnace and two furnace top furnace cover opening up with one connected U-shaped pipe is connected a splitting furnace, structure of two completely same furnace, each furnace inner table set with the one material grate, furnace grate downwards set with high temperature combustion pneuma inlet, high temperature combustion pneuma downwards set with one catalyst inlet grate, a is the tar splitting catalyst, lower part set with furnace gas exit, set with a two heat stress compensator in a connected U-shaped pipe, a U-shaped pipe connected the top end set with one raw material adding device, set with one addition and subtraction is used for cold coal inner regulating furnace temperature of cold shock gas tube between a grate and catalyst raw material grate. Would not produce dioxin poisonous gas time The production splitting gas furnace, a tar in gas furnace inner production of completely splitting, so as to prevent the happen of second pollution.
NOVELTY - A new one is zinc alloy two hole pneuma in furnace, it relates to gasification furnace technology field, lower end of main body mounted with a lower cover body, a lower cover mounted with a regulating pole, regulating pole upper end is mounted with a regulating ball, and ball set in the pneuma regulating inner hole, lower end of regulating pole mounted with regulating handle, main body is set with a furnace core inner hole, a furnace body is outside a wall main body are symmetrically set with oxygen inlet hole, it can burn fully, the oxygen amount high, increase utilization rate, the raw material is saved, operation is simple and convenient.
NOVELTY - This utility new type claims a one ecological farmhouse, this ecological farmhouse comprising marsh gas pool, a distribution cabinet, a wind driven generator, a photovoltaic array, solar energy water heater, pigsty, and toilet, pigsty, , a field of a centralized waste discharging marsh gas pool, marsh gas generated by the marsh gas pool used for house heating, gas, biogas residue as organic fertilizer with a b, wind driven generator and photovoltaic array is composed of wind-solar hybrid generation system of power distribution to a distribution cabinet, a power distribution cabinet used for lighting, heating such as a domestic house. This utility new type energy-saving and environment-friendly, changes waste into valuable, the multi-a is a comprehensive using technology of renewable energy application b production and life of rural peasant household family a, increase the comprehensive use rate of a renewable energy source, solves the problem that the farmers with problem and reduces rural pollution, increase the income of farmer and reduces farmer production cost.
NOVELTY - One for a straw gasification and grain drying of integrated device, comprising straw gasification furnace device, a hot air furnace and grain drying device, the straw gasification furnace through a gas steel pipe and hot air furnace is connected with the hot air furnace through gas steel pipe and grain drying device is connected. This utility new type is beneficial effect is: through fully using straw gasification after combustion of the heat for drying, not only a grain structure is simple, but also reduces the pollution for environment is saved.
NOVELTY - This utility new type relates to one a marsh gas pool, specifically is a resin base composite material one multifunctional marsh gas pool. This marsh gas pool comprising marsh gas pool main body, marsh gas pool upper cover, shell, heater, a water inlet pipe, a water outlet pipe, a heater pedestal, cracking pipe, sewage pump, a feeding pipe, a discharging pipe, an air outlet pipe and marsh gas boiler, the heater pedestal set in inner bottom of marsh gas pool main body centre position, heater a heater set with a pedestal, a heater one end connecting with a water inlet pipe, and the other end connecting with the hot water pipe, water inlet and outlet of the boiler heat the water inlet tube and the hot water tube and the gas connection, the storage shell set with a marsh gas pool upper cover, is set with an air outlet pipe, an air outlet pipe in marsh gas pool upper cover upper centre position of two side are set with a feeding pipe and a discharging pipe, the breaking pipe one end through the feeding pipe or the discharging pipe entering into marsh gas pool main body inside, the other end set with a 500 mm high from a liquid level, a breaking pipe fixed in biogas pool upper cover up and a set with a sewage pump. This utility new type marsh gas pool structure is simple and reasonable, the use life is long, the heat preservation effect is good, and it has breaking function, high, b fit in use.
NOVELTY - This new type utility claims one three-dimensional type house a pneuma biogas pool system, comprising barn (1) and marsh gas pool (2), a methane pool (2) built under a ground (3), barn (1) is located in the marsh gas pool (2) is, in the fermentation room (4) is set with upper water pressure chamber (5) and water pressure chamber cover (6), a fermenting room (4) is provided with a pool cover (7), cover (6) and outlet of pool cover (7) is located in the barn (1) inner, water pressure chamber (5) through water pressure channel (8) and the fermentation room (4) connected, marsh gas pool (2) is feeding wherein (9) is located in the barn (1) of toilet (10) and inner and fermentation room (4) connected. This utility new type methane pool and a colony house, furthest using the space, saves the land resource, and form three-dimensional ecological system between a marsh gas pool and colony house, reduces the colony house of the external pollution, energy-saving and environment-friendly.
NOVELTY - The method involves purging a reactor (12) of oxygen, and supplying a feed stream containing methane into the reactor, while maintaining oxygen-free conditions in the reactor. The methane is disassociated into carbon and hydrogen in the reactor at temperature ranging from 700 degrees Celsius to 1400 degrees Celsius and under oxygen-free conditions in the reactor by supplying a catalyst e.g. particulate carbon. The hydrogen is discharged from the reactor. A particle support is supplied into the reactor for absorbing carbon produced in the reactor and forming a carbon-loaded particle support.    USE - Method for producing hydrogen from methane for power generation application and for use as a feed material for a chemical process e.g. gas-to-liquid (GTL) process or gas-to-olefin (GTO) process, to produce long-chained hydrocarbons e.g. diesel fuel and petrol, and short-chain hydrocarbons e.g. olefins ethylene and propylene, for powering vehicles and manufacture of plastic household goods.    ADVANTAGE - The method enables controlling oxidation of carbon for producing hydrogen and carbon monoxide with minimized generation of carbon dioxide. The method enables carbon monoxide formed in the reactor to flow upwardly along axial direction of another reactor and exit through a carbon monoxide outlet for downstream processing with minimal purification in a cost-effective manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for producing separate streams of hydrogen and carbon monoxide from methane    (2) a reactor for producing hydrogen and carbon by paralyzing methane    (3) a reactor system for producing separate streams of hydrogen and carbon monoxide from methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a reaction system.    Reactors (12, 14)    Conduits (20, 34)    Ignition sources (22, 24)    Feed stream inlet part (28)    Ash outlets (36, 38)
NOVELTY - A M30 methanol-gasoline fuel additive comprises 16-24 pts. wt. metal corrosion inhibitor, 10-20 pts. wt. anti-swelling agent, 22-33 pts. wt. solubilizing aid and 48-60 pts. wt. combustion improver.    USE - Additive is used for M30 methanol-gasoline fuel for automotives.    ADVANTAGE - The additive can be prepared by environmentally-friendly process. The M30 methanol-gasoline fuel containing the additive has high combustion efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of M30 methanol-gasoline fuel additive, which involves adding tert-butanol, 5-methyl-2-hepten-4-one, 4-trifluoromethoxy benzyl alcohol and ethylene glycol monobutyl ether into a reactor, reacting at 53-58 degrees C for 40-50 minutes, adding dimethyl carbonate and O,O-dibutyl zinc dithiophosphate, stirring at 41-48 degrees C for 15-25 minutes, then adding polyisobutylene amine and methylisothiazolinone, stirring at 33-35 degrees C for 20-25 minutes, adding pyrazolone and methyl benzotriazole and stirring for 10-15 minutes.
NOVELTY - A solid fuel comprises biomass, coal slime, binder, desulfurization agent, oxidizing agent and waterproofing agent. The weight ratio of biomass, coal slime, binder, desulfurization agent, oxidizing agent and water is 70-90:10-30:10-20:3-5:3-5:2-4. The biomass is made from cotton stalk and sawdust, in weight ratio of 1-3:1.    USE - Solid fuel (claimed).    ADVANTAGE - The solid fuel having high calorific value and excellent storage stability, moisture-proof property and water resistance, is manufactured efficiently with high productivity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of solid fuel.
NOVELTY - Producing wood fuel involves selecting sawdust, wood shavings, branches and wood pieces as raw material and then cutting or crushing the raw material to obtain wood powder. The obtained wood powder is sieved to remove the impurities having diameter more than 4 centimeter. The sieved material is dried through hot air drying process to reduce the water content to 8-10%. The qualified material is separated and then the separated material is kept in a granulating molding machine to obtain the granule size of 10-12 millimeter. The granulated material is cooled to normal temperature.    USE - Method for producing wood fuel (claimed).    ADVANTAGE - The method enables to produce wood fuel in environment friendly manner, and has reduced air pollution and utilized waste.    DETAILED DESCRIPTION - Producing wood fuel involves selecting sawdust, wood shavings, branches and wood pieces as raw material and then cutting or crushing the raw material to obtain wood powder. The obtained wood powder is sieved to remove the impurities having diameter more than 4 centimeter. The sieved material is dried through hot air drying process to reduce the water content to 8-10%. The qualified material is separated and then the separated material is kept in a granulating molding machine to obtain the granule size of 10-12 millimeter. The granulated material is cooled to normal temperature. The qualified material is separated and then the separated material is kept in a granulating molding machine. The obtained material is cooled and then the debris material is filter out. The obtained material is re-conveyed to the scrap granulator and then to granulated molding machine to obtain the finished product.
NOVELTY - Producing biomass fuel, comprises (a) selecting plant fiber as raw material and then crushing, adding the crushed powder into a container and then enzymolyzing at temperature of 50-80 degrees C, where the water content of the plant fiber is 50-60%, adding a catalyst in a reaction container and then reacting, (b) fermenting raw material using solid fermentation method at temperature of 50-55 degrees C for 30-45 minutes, and (c) separating and purifying the fermentation material using film separating technology.    USE - The method is useful for producing biomass fuel (claimed).    ADVANTAGE - The method rapidly produces the biomass fuel with high quality.
NOVELTY - The furnace has an electric air blower (300) fixed with a cuboid housing unit (100) that is fixed with a gas stove (400). A furnace body is fixed in an inner cuboid housing unit through a supporting base (203). A furnace wall interlayer is formed with a heat insulating layer (201). A gas connected pipe (205) is connected with a control valve (209). A ventilation branched pipe (204) is connected with an inner furnace body. A gas branch pipe is connected with a gas stove air inlet. The ventilation branched pipe is fixed with control valve (210).    USE - High efficient biological carbon gasification furnace for rural area.    ADVANTAGE - The furnace has better environment-protecting and energy-saving effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front sectional view of a high efficient biological carbon gasification furnace.    Cuboid housing unit (100)    Heat insulating layer (201)    Supporting base (203)    Ventilation branched pipe (204)    Gas connected pipe (205)    Control valve (209)    Control valve (210)    Electric air blower (300)    Gas stove (400)
NOVELTY - The apparatus (100) has a cleaning bath section (170) which is connected to a lower portion of a cold trap (150), to filter the condensed water within the cold trap. An oil mist dust collector (185) is connected to the vacuum pump (180), to removes the oil included in the air. A secondary gate valve (122) is arranged in the rear end of the drying furnace (120). The sewage sludge is pulverized by a pulverizing device (191) connected to the back-end of drying furnace. A pellet molder (192) is connected to the pulverizing device, for molding the sewage sludge to the pellet-form.    USE - Apparatus for drying sewage sludge.    ADVANTAGE - The sewage sludge is sucked with the vacuum pump and is heat-exchanged with the oil heated within the drying furnace, thus the sewage sludge is dried efficiently and quickly. The dumping of sewage sludge in ocean is prohibited, and the cost for the sewage sludge drying process is effectively reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sewage sludge drying apparatus.    Sewage sludge drying apparatus (100)    Drying furnace (120)    Secondary gate valve (122)    Cold trap (150)    Cleaning bath section (170)    Vacuum pump (180)    Oil mist dust collector (185)    Pulverizing device (191)    Pellet molder (192)
NOVELTY - Method of thermocatalytic processing of industrial and solid household wastes includes milling wastes and their thermal processing in air medium at 550-750 degrees C and pressure 1.2-2.0 atm, catalytic thermodestruction of gaseous products in presence of transition metals of iron subgroup, characterised by the fact, that catalytic thermodestruction is realised at temperature 500-550 degrees C, weight ratio of catalyst and wastes 0.01-0.05, air consumption 1.5-4.0 m3 per 1 kg of solid raw material, as catalyst transition metals of iron subgroup, applied on artificial zeolite ZSM-5 in quantity 1-15 wt %, are applied.    USE - Chemistry.    ADVANTAGE - Reduced content of resins, method is characterised by degree of conversion, percent of gasification.5 tbl, 6 ex
NOVELTY - Preparation of Sorghum shell cultivation culture includes taking Sorghum shell, sawdust, rice bran, bran, peanut, calcium carbonate, superphosphate, urea, ammonium sulfate, nutritive soil and water an crushing into 0.2-0.9 cm powder, controlling pH value to 6-7, bottling, performing sterilization for 1-2 hours, cooling to 38-62 degrees C, cultivating for 26-31 days at 18-23 degrees C with 70-80% humidity, and harvesting.    USE - Method for preparing Sorghum shell cultivation culture used for mushroom cultivation.    ADVANTAGE - The method is environmental-friendly, time-saving, and has high yield.
NOVELTY - Propane catalytic combustion catalyst preparation involves adding 2 mol/liter sodium carbonate or potassium carbonate solution dropwise in 0.2 mol/liter ethanol solution precursor in a water bath at 25-60 degrees C to form a precipitate. The sodium or potassium carbonate solution is mixed with precursor solution in a volume ratio of 2:5, where a precipitating agent and hydrogen peroxide are added dropwise to form a precipitate. The formed precipitate is filtered and dried at 250-450 degrees C to obtain a catalyst.    USE - Method for preparing propane catalytic combustion catalyst (claimed).    ADVANTAGE - The method prepares propane catalytic combustion catalyst in a simple and cost-effective manner.
NOVELTY - Performing static solid state fermentation (SSF) comprises mixing a bulking agent with a biomass to form a mixture; adding the mixture to a static solid state bioreactor; irrigating the mixture with an aqueous solution; flowing a gas through the mixture; and maintaining a microorganism supporting environment within the mixture by calculating a specific heat of an aqueous solution flow, calculating a specific heat of a gas flow, and balancing the aqueous solution flow with the gas flow.    USE - The method is used for performing static SSF (claimed).    ADVANTAGE - Provided is an improved static solid state bioreactor that may be used for SSF of biomass. The SSF bioreactor and process provide advantages over existing submerged liquid fermentation technologies, including high product yield, low cost, ease of use, and scalability.
NOVELTY - The plate has micropore groups comprising a first micropore (11) and a second micropore (12) and a round, square or rectangular gas diffusion channel used for communication between the first micropore and the second micropore. The gas diffusion channel is provided with a micro-pore wall (1112) between the first micropore and the second micropore and filled with high flux biochemical reaction product gas. The high flux biochemical reaction product gas is selected from one of hydrogen sulfide, nitrogen oxide, carbon monoxide, carbon-di-oxide, acetylene, methane, hydrogen or ammonia.    USE - Micropore plate for a high-flux filter enzymatic activity regulator (claimed), for high-throughput detection of gas generated by biochemical reaction.    ADVANTAGE - The micropore plate realizes high-throughput detection of a gas generated by biochemical reaction without interfering biological and/or chemical reaction and target substance with each other.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a micropore plate.    Micropores (11, 12)    Micropore reaction hole (110)    Micro-pore wall (1112)
NOVELTY - An adhesive sheet (100) comprises a substrate (110) and an adhesive layer (120) on surface(s) of the substrate. The pressure-sensitive adhesive layer(s) partially or completely lose(s) adhesiveness upon an external stimulus.    USE - Adhesive sheet is used for conveying electrolytic membrane during manufacturing fuel cell membrane/electrode complex and laminate (all claimed).    ADVANTAGE - The adhesive sheet has excellent adhesiveness with respect to electrolytic membrane. The deformation and generation of wrinkles of electrolytic membrane is prevented while peeling.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of fuel cell membrane/electrode complex; and    (2) laminate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the adhesive sheet.    Adhesive sheet (100)    Substrate (110)    Adhesive layer (120)
NOVELTY - Aerobic composting odorless organic waste comprises taking organic garbage, weathering for 30-40 days, crushing, adding water, mixing, adjusting pH to 3-4 using dilute sulfuric acid, standing for 24 hours, discharging, adding 10 wt.% sawdust, 3-6 wt.% cellulase and 5-10 wt.% pectinase, stirring, standing for 6-8 hours, adjusting pH to 5-6, adding 2.5 wt.% mixed bacteria, fermenting at 32-38 degrees C for 6-8 days and mixing. Mixed bacteria comprises 10 wt.% Bacillus subtilis, 5 wt.% yeast, 3 wt.% Lactobacillus, 10 wt.% nitrifying bacteria and 5 wt.% Aspergillus niger.    USE - Method for aerobic composting odorless organic waste (claimed).    ADVANTAGE - The method is inexpensive.
NOVELTY - An organic material is treated by forming acidified paste of dewatered organic material and first acids; adding acidified paste to pressure vessel such that the vessel maintains predetermined head space pressure by injection of steam; adding second acids and bases to the vessel to combine with the acidified paste forming an exothermic mixture; subjecting the mixture to temperature and pressure for a retention time, in which the moisture content of the mixture is determined by the predetermined head space pressure; removing the mixture from the pressure vessel; and drying the mixture.    USE - Method for organic material treatment used in manufacture of bio-organically augmented fertilizer (claimed).    ADVANTAGE - The method is capable of processing biosolids into safe and commercially viable natural slow-release fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block view showing sections of Biosolid fertilizer Plant Flow Chart.    Insulated biosolids storage bin (105)    Steam generator (115)
NOVELTY - The detector (X) has a gas detection element (10) provided with a gas sensitization part. A double housing accommodates the gas detection element. An outer side double housing (51) is equipped with an adsorption part (31), which absorbs organic gas. A gas introduction port (20) introduces to-be-detected gas. An inner side double housing (52) is equipped with another adsorption part (32). Opening area of a restriction vent hole (40) is smaller than that of the gas introduction port. The restriction vent hole is formed between the adsorption parts.    USE - Heat wire semiconductor-type gas detector for use in a house.    ADVANTAGE - The detector easily suppresses influence of organic gas easily. The detector has improved to-be-detected gas responsiveness and productivity efficiency.    DETAILED DESCRIPTION - The gas detection element is a heat wire semiconductor-type gas detection element, a contact combustion-type gas detection element, a board semiconductor-type gas detection element and a solid electrolyte-type gas detection element. The organic gas is alcohol. The to-be-detected gas is combustible gas and carbon monoxide such LPG, methane and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic sectional views of a heat wire semiconductor-type gas detector.'(Drawing includes non-English language text)'    Heat wire semiconductor-type gas detector (X)    Gas detection element (10)    Gas introduction port (20)    Adsorption parts (31, 32)    Restriction vent hole (40)    Outer side double housing (51)    Inner side double housing (52)
NOVELTY - The fertilizer has an air supply pipe that injects the air flowed in organic fermentation product which is arranged in drain formed in back up fermentation room (11). A main portion fermenting device (20) includes the mixing transport unit which is gradually moved with escalator type organic fermentation product. A ventilation hole is formed in cover. An indentation clip is pressed in air supply pipe which is arranged in drain. The cover is arranged in drain through indentation clip and is arranged at ventilation structure to close upper portion of drain.    USE - Fertilizer for organic matter manufacturing system.    ADVANTAGE - The air supply in drain of backup fermenting device is stabilized. The cover is fixed to predetermined position of drain, such that the convenient elastic press is achieved according to detachment of cover. The accuracy of fertilizer is improved reliably. The filling drum is arranged to conveyer belt of main portion fermenting device to rotary structure. The damage of bucket wing with rubbing or collision is prevented effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the backup fermenting device.    Organic matter manufacturing system (1)    Backup fermenting device (10)    Backup fermentation room (11)    Main portion fermenting device (20)    Main portion fermentation room (21)
NOVELTY - The package is made of biodegradable polymer and composition of natural materials.    USE - Environmental-friendly biodegradable polymer package for use in form of a pot-shaped cup for conditioning creams, bottles, tubes, kits packaging, shampoo bottle and liquid soap packaging for storing cosmetics such as lipstick, mask, eyelashes, perfume, perfume spray, sprinkler and environment aromatizer and medicinal product or pharmaceutical product (all claimed).    ADVANTAGE - The package has high resistance, different thicknesses, better hardness and flexibility, and avoids environment pollution and energy sources utilization.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a pot-shaped cup for conditioning creams.    Pot-shaped cup (1)    Lid of pot-shaped cup (2)    Conditioning cream (3)
NOVELTY - Method for preparing organic fertilizer and organic feed, involves (a) grinding soft portion of scallop containing cadmium using water, and autolyzing the ground product, (b) adding chelate fiber to the autolyzed product to remove cadmium, and (c) heat-processing obtained product.    USE - The method is useful for preparing organic fertilizer and organic feed (claimed).    ADVANTAGE - The method enables environmentally-friendly and cost-effective preparation of additive-free organic fertilizer and organic feed.
NOVELTY - A freezing apparatus (R) consists of refrigerant circuit containing compressor (1,2), condenser (13,22), reduced pressure device and evaporator (3,9), which are cyclically connected in order. The freezing devices uses refrigerant composition comprising refrigerant (r1) having low boiling point of -89 degrees C to -78.1 degrees C, carbon dioxide, and refrigerant (r2) which is soluble with carbon dioxide at temperatures lower than the boiling point of carbon dioxide. The carbon dioxide is used as refrigerant in the refrigerant circuit.    USE - Freezing apparatus (claimed).    ADVANTAGE - The refrigerating device provides stable refrigerating capacity, and is capable of effectively eliminating problems due to the formation of dry ice from carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a refrigerant circuit of the freezing apparatus.    Compressor (1,2)    Evaporator (3,19)    High temperature side refrigerant circuit (4)    Low temperature side refrigerant circuit (6)    Condenser (13,22)    Capillary tube (16,28)    Cascade heat exchanger (17)    Freezing apparatus (R)
NOVELTY - Storing electrical energy, comprises (a) generating methane from carbon black and water using electrical energy, (b) storing the generated methane, (c) splitting stored methane into carbon black and hydrogen which is used for power generation, (d) collecting generated carbon black, and (e) re-using collected carbon black in step (a) such that a closed carbon cycle is formed.    USE - The method is useful for storing electrical energy (claimed).    ADVANTAGE - The method recycles carbon in simple manner, and avoids carbon dioxide emissions and so is environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a system comprising a power-methane conversion plant (90) to convert electrical power with carbon black and water into methane, and a methane-electricity conversion plant (92) to convert methane into hydrogen and electrical power with elimination of carbon black, where means is provided to re-supply carbon black from the methane-electricity conversion plant to the power-methane conversion plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the method for storing electrical energy.    Wind power (12)    Solar system (14)    Gas network (24)    Power-methane conversion plant (90)    Methane-electricity conversion plant (92)
NOVELTY - Fermentation liquid composition comprises silicate bacteria, Aspergillus niger, Bacillus amyloliquefaciens and Pediococcus acidilactici in a mass ratio 2:2:1:1.5. The fermentation liquid composition is prepared by crushing Enteromorpha prolifera to obtain 80 meshes size sea weed powder. The obtained material is mixed with plant oil, corn flour and water, and then the obtained material is stirred for 2-3 days. The obtained material is fermented for 10-15 days. The obtained material is performed for sedimentation.    USE - Fermentation liquid composition.    ADVANTAGE - The fermentation liquid composition is multifunctional in nature.    DETAILED DESCRIPTION - Fermentation liquid composition comprises silicate bacteria, Aspergillus niger, Bacillus amyloliquefaciens and Pediococcus acidilactici in a mass ratio 2:2:1:1.5. The fermentation liquid composition is prepared by crushing Enteromorpha prolifera to obtain 80 meshes size sea weed powder. The obtained material is mixed with plant oil, corn flour and water, and then the obtained material is stirred for 2-3 days. The obtained material is fermented for 10-15 days. The obtained material is performed for sedimentation, and then filtered them by using plate-frame filter press to obtain the finished product.
NOVELTY - Fertilizer composition preparation involves fermenting rapeseed shell, whole grass, tea seed shell, Camellia, plant ash, human and animal manures, and lime in presence of methane gas and moisture for 15-20 days. The obtained material is mixed with urea, and then granulated them. The obtained material is dried, and packed to obtain the finished product.    USE - Method for preparing fertilizer composition for cultivating crop and green plant and preventing and treating diseases and insect.    ADVANTAGE - The method enables to prepare fertilizer composition, which ensures improved yield of plant.
NOVELTY - Biological fermentation agent comprises beneficial microorganisms, that activate insoluble mineral elements, and then fermenting manure.    USE - Biological fermentation agent used for preparing organic fertilizer from crop straw, vine, manure, leaves, weeds, bran vinegar residue, sawdust, rosacea, vinegar slag, slag soy sauce, soybean, mushroom residue, pink slag, tofu, bone meal, bagasse, slaughterhouse residue and rural garbage, used for planting (all claimed).
NOVELTY - Fertilizer composition preparation involves taking 30-32 wt.% dried pig manure, 8-10 wt.% dry dairy manure, 15 wt.% peanut straw stick, 4 wt.% bean cake, 4 wt.% rapeseed cake, 25 wt.% dried pond sludge, 2 wt.% organic fertilizer fermenting agent, 4 wt.% diammonium phosphate, 5 wt.% potassium sulfate, 0.2 wt.% amino acid chelated iron, 0.3 wt.% amino acid chelated calcium, 0.1 wt.% amino acid chelated magnesium, 0.1 wt.% humic acid chelated manganese and 0.3 wt.% humic acid chelated copper. The dried pig manure, dry dairy manure, peanut straw stick, bean cake and rape seed cake are crushed.    USE - Method for preparing fertilizer composition used for cultivating Ginkgo tree (claimed).    ADVANTAGE - The method enables to prepare fertilizer composition, which ensures improved disease resistance ability and yield of fruit of Ginkgo tree.    DETAILED DESCRIPTION - Fertilizer composition preparation involves taking 30-32 wt.% dried pig manure, 8-10 wt.% dry dairy manure, 15 wt.% peanut straw stick, 4 wt.% bean cake, 4 wt.% rapeseed cake, 25 wt.% dried pond sludge, 2 wt.% organic fertilizer fermenting agent, 4 wt.% diammonium phosphate, 5 wt.% potassium sulfate, 0.2 wt.% amino acid chelated iron, 0.3 wt.% amino acid chelated calcium, 0.1 wt.% amino acid chelated magnesium, 0.1 wt.% humic acid chelated manganese and 0.3 wt.% humic acid chelated copper. The dried pig manure, dry dairy manure, peanut straw stick, bean cake, rape seed cake and dried pond sludge are crushed, and then organic fertilizer fermenting agent and water are added to the obtained material. The obtained mixture is fermented in sealed container for 26-28 days, and then the obtained material is dried. The obtained material is mixed with remaining crushed raw material to obtain the finished product.
NOVELTY - Preparation of urea involves carrying out high-temperature treatment of waste in reactor provided with oxygen, obtaining synthesis gas comprising carbon monoxide, carbon dioxide and hydrogen, converting carbon monoxide of synthesis gas into carbon dioxide and hydrogen using water, separating carbon dioxide, converting nitrogen into ammonia using separated hydrogen, and reacting carbon dioxide and produced ammonia. Oxygen for high-temperature treating of urea, and nitrogen are obtained by air-separation process.    USE - Preparation of urea used as synthetic fertilizer.    ADVANTAGE - The method enables environmentally-friendly preparation of urea.
NOVELTY - 3-hydroxy-5-androstene-17 beta carboxylic acid methyl ester is prepared by dissolving 3-hydroxy-5-androstene-17 beta carboxylic acid in alkali water, adding dimethyl carbonate, heating to reflux, performing esterification reaction while adding alkali solution dropwise every 20-40 minutes to adjusting pH to 8-10, cooling reaction mixture to 65-75 degrees C, adjusting pH with acid to 6-8, concentrating under reduced pressure to remove excess dimethyl carbonate, cooling with circulating water to less than or equal to 40 degrees C, directly filtering, washing with water until neutral, and drying.    USE - Preparation of 3-hydroxy-5-androstene-17 beta carboxylic acid methyl ester (claimed).    ADVANTAGE - 3-hydroxy-5-androstene-17 beta carboxylic acid methyl ester is low-cost and environment-friendly and has good quality, high yield, simple post-treating.    DETAILED DESCRIPTION - 3-hydroxy-5-androstene-17 beta carboxylic acid methyl ester of formula (I) is prepared by dissolving 3-hydroxy-5-androstene-17 beta carboxylic acid of formula (II) in alkali water, adding dimethyl carbonate, heating to reflux, performing esterification reaction while adding alkali solution dropwise every 20-40 minutes to adjusting pH to 8-10, cooling reaction mixture to 65-75 degrees C, adjusting pH with acid to 6-8, concentrating under reduced pressure to remove excess dimethyl carbonate, cooling with circulating water to less than or equal to 40 degrees C, directly filtering, washing with water until neutral, and drying in which alkali solution is sodium hydroxide solution, potassium hydroxide solution, sodium carbonate solution, potassium carbonate solution, sodium bicarbonate solution, and/or potassium bicarbonate solution..
NOVELTY - Method for producing antibacterial fermenting agent, involves adjusting moisture content of coffee bean pulp to 50-60%, inoculating microorganism in the coffee bean pulp and fermenting the pulp.    USE - The method is used for producing antibacterial fermenting agent which is used in fermented compost for controlling plant pathogens chosen from Colletotrichum acutatum, Alternaria alternata, Botrytis cinerea, Penicillium italicum, P.expansum, Fusarium oxysporum, Rhizoctonia solani and Sclerotinia sclerotiorum (all claimed).    ADVANTAGE - The fermented compost is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fermented compost, which comprises the antibacterial fermenting agent, and at least one composting raw material chosen from fallen leaves and food waste.
NOVELTY - Preparing fertilizer involves heating phosphoric acid in reactor at 100-130 degrees C with urea for 190-210 minutes. The reaction mixture is cooled to 15-25 degrees C to obtain crystal that is centrifuged to obtain intermediate. The obtained intermediate is reacted with ammonia gas for 50-70 minutes at 20-30 degrees C at pH 8.5-9.5. The obtained slurry is cooled to obtain crystal. The slurry is filtered and filtrate is crystallized. The filtered cake is dried to obtain ammonium dihydrogen phosphate products. Ammonium dihydrogen phosphate and a potassium compound is added to filtrate to adjust nitrogen, phosphorus and potassium content.    USE - Method for preparing fertilizer used for cultivating Celosia cristata (claimed).    ADVANTAGE - The method enables to prepare fertilizer in cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing fertilizer involves heating phosphoric acid in reactor at 100-130 degrees C with carboxamide for 190-210 minutes. The reaction mixture is cooled to 15-25 degrees C to obtain crystal that is centrifuged to obtain intermediate. The obtained intermediate is reacted with ammonia gas for 50-70 minutes at 20-30 degrees C at pH 8.5-9.5. The obtained slurry is cooled to obtain crystals. The slurry is filtered and filtrate is crystallized. The filtered cake is dried to obtain ammonium dihydrogen phosphate products. Ammonium dihydrogen phosphate and a potassium compound is added to filtrate to adjust nitrogen, phosphorus and potassium content. The trace elements are also added in filtrate to obtain mixture that is dried at 25-35 degrees C to obtain fertilizer.
NOVELTY - An oily sludge-treating agent comprises 2.5-10 wt.% surfactant, 0.25-2 wt.% bioenzyme, 0.05-0.2 wt.% calcium chloride, 5-10 wt.% propylene glycol and remainder of water.    USE - Agent is used for treating oily sludge (claimed).    ADVANTAGE - The agent enables efficient treatment of oily sludge with reduced oil-water interface tension of 10-2 mN/m at room temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating oily sludge using oily sludge-treating agent.
NOVELTY - The apparatus has a casing part equipped with an outer tube. A process bath performs fermentation of food waste. A deodorization chamber removes bad smell of air. The deodorization chamber is equipped with an ozone degradation chamber. A side of the ozone degradation chamber is formed with multiple vent holes. The vent holes inhale air into the ozone degradation chamber.    USE - Food waste treating apparatus.    ADVANTAGE - The apparatus prevents generation of bad smell.
NOVELTY - The apparatus has a casing part equipped with an outer tube. A process bath performs fermentation of food waste. A deodorization chamber is equipped with an ozone degradation chamber. A side of the ozone degradation chamber is formed with multiple vent holes. The vent holes inhale air into the ozone degradation chamber. An ozone decomposition catalyst is in contact with an inner circumference of each vent hole. The ozone degradation chamber is equipped with multiple guide boss parts that prevent ejection of the ozone decomposition catalyst into an outer side of the ozone degradation chamber.    USE - Food waste treating apparatus.    ADVANTAGE - The apparatus prevents generation of bad smell.
NOVELTY - Preparing Anoectochilus vinegar, by (a) cleaning bagasse and sugarcane leaves, crushing, adding water, adding complex enzyme comprising cellulase and hemicellulase, fermenting, adding glucoamylase, fermenting, adding active dry yeast, fermenting, adding acetic acid bacteria, fermenting, and filtering, (b) cleaning Anoectochilus, drying and grinding, and (c) mixing fermented vinegar obtained in step (a) and powder obtained in step (b), stirring, incubating, storing, filtering, packaging and sterilizing the packaged product.    USE - The method is useful for preparing Anoectochilus vinegar (claimed).    ADVANTAGE - The method is simple, environmentally-friendly and suitable for large scale production. The prepared Anoectochilus vinegar has gentle flavor, mellow taste and elegant fragrance.    DETAILED DESCRIPTION - Method for preparing Anoectochilus vinegar, involves (a) cleaning bagasse and sugarcane leaves, crushing, adding 3 times water to the crushed product, adding 2-5% complex enzyme comprising cellulase and hemicellulase, fermenting at 50-60 degrees C and 5 plus minus 0.2 pH for 10-12 hours, adding 0.5-1% glucoamylase to the fermented product, fermenting at 60-65 degrees C and 4.2 plus minus 0.2 pH for 5-10 hours, adding 0.5-1% active dry yeast to the fermented product, fermenting at 30-35 degrees C and 3.8 plus minus 0.2 for 3-5 days, adding 5-10% acetic acid bacteria to the fermented product, fermenting at 35-38 degrees C for 3-5 days, and filtering the fermented product, (b) cleaning Anoectochilus, drying the cleaned Anoectochilus and grinding using high-speed grinder, and (c) mixing fermented vinegar obtained in step (a) and powder obtained in step (b) in mass ratio of 100:0.1-1, stirring the mixture uniformly, incubating at 85-90 degrees C for 10-12 hours, storing for 3 months, filtering, packaging the filtrate and sterilizing the packaged product.
NOVELTY - A zinc oxide ceramic film preparing method involves taking magnesium alloy for removing oxide film, preparing electrolyte by utilizing 3-10 g/l zinc gluconate, 5-12 g/l sodium hydroxide, 4-8 g/l sodium phosphate, 1-3 g/l disodium edetate, 1-3 g/l sodium citrate, solvent and deionized water, taking magnesium alloy as an anode, immersing in electrolyte in stainless steel electrolyte tank as cathode, setting electric parameter with pulse voltage of 180-430 V and pulse frequency of 300-600 HZ for 5-30 minutes to obtain the finished product.    USE - Method for preparing zinc oxide ceramic film.    ADVANTAGE - The method enables preparing zinc oxide ceramic film with high bonding force and high corrosion resistant property, in simple and eco-friendly manner.
NOVELTY - Method for preparing special durian fertilizer using tricalcium phosphate byproduct, involves reacting phosphoric acid with carboxamide to generate urea phosphate, forming intermediate, adding calcium ions to the intermediate, cooling tricalcium phosphate slurry, centrifuging, filtering mixture, performing crystallization, detecting e.g. calcium content, drying tricalcium phosphate product, adding potassium component into the product, concentrating, adding concentrate into granulator, granulating, drying granules, sterilizing and packaging product.    USE - The method is useful for preparing special durian fertilizer (claimed).    ADVANTAGE - The method is cost-effective and environmentally-friendly, and avoids discharge of waste liquid.    DETAILED DESCRIPTION - Method for preparing special durian fertilizer using tricalcium phosphate byproduct, involves reacting phosphoric acid with carboxamide to generate urea phosphate, adjusting temperature to 100-125 degrees C, separating urea phosphate ion, forming intermediate, adding calcium ions to the intermediate to produce tricalcium phosphate slurry, cooling tricalcium phosphate slurry, centrifuging cooled slurry, filtering mixture, performing crystallization of the filtrate, detecting calcium, nitrogen and phosphorus content to obtain tricalcium phosphate product, drying tricalcium phosphate product at 75-85 degrees C until the moisture content reaches 2-3%, adding potassium component into the product, where the content of potassium component comprises nitrogen, potassium and phosphorus in a ratio of 1-3:1.9-2.5:1.1-1.7, concentrating mixture at 105-115 degrees C until the moisture content reaches 13-15%, adding concentrate into granulator, granulating concentrate, drying granules at 90 degrees C until the moisture content reaches 1-2%, sterilizing and packaging product.
NOVELTY - Compound fertilizer comprises 6-11 pts. wt. bone powder, 3-9 pts. wt. clay, 6-10 pts. wt. urea, 4-7 pts. wt. sodium molybdate dihydrate, 2-6 pts. wt. potassium chloride, 5-9 pts. wt. monoammonium phosphate, 4-6 pts. wt. dry silkworm, 3-7 pts. wt. ammonium sulfate, 2-4 pts. wt. phosphate, 7-11 pts. wt. royal jelly, 4-9 pts. wt. disodium hydrogen phosphate, 2-8 pts. wt. Bacillus megaterium, 3-5 pts. wt. growth regulator and 2-9 pts. wt. rare earth element.    USE - Compound fertilizer.    ADVANTAGE - The compound fertilizer is efficient, and increases economic benefit and provides balanced nutrition to meet needs of plant growth by reducing soil compaction.
NOVELTY - Method for preparing foliar fertilizer involves weighing 80-90 pts. wt. sisal wastewater, 5-10 pts. wt. inorganic fertilizer, 1-2 pts. wt. trace element, 3-5 pts. wt. organic acid, and 0.1-0.5 pts. wt. surfactant, mixing uniformly, fermenting in a closed container at 30-50 degrees C for 10-15 days, filtering fermented broth and collecting filtrate to obtain the product, where the inorganic fertilizer comprises more than 9 %mass nitrogen, more than 4 %mass phosphorus, preferably phosphorus pentoxide and more than 12 %mass potassium, preferably potassium oxide.    USE - The method is useful for preparing foliar fertilizer, which is useful for promoting growth of vegetable (claimed).    ADVANTAGE - The method enables to reduce environmental pollution and prepare nutritious foliar fertilizer, which significantly improves vegetable yield, and is cost-effective.    DETAILED DESCRIPTION - Method for preparing foliar fertilizer involves weighing 80-90 pts. wt. sisal wastewater, 5-10 pts. wt. inorganic fertilizer, 1-2 pts. wt. trace element, 3-5 pts. wt. organic acid, and 0.1-0.5 pts. wt. surfactant, mixing uniformly, fermenting in a closed container at 30-50 degrees C for 10-15 days, filtering fermented broth and collecting filtrate to obtain the product, where the inorganic fertilizer comprises more than 9 %mass nitrogen, more than 4 %mass phosphorus, preferably phosphorus pentoxide and more than 12 %mass potassium, preferably potassium oxide, and the sisal wastewater is obtained by extruding water from sisal leaf and filtering extruded water, which is used on the same day, and the sisal residue is used in feed.
NOVELTY - Extraction and purification of calcium lactate involves centrifuging calcium lactate solution, removing impurities, adding phase-separation solvent, mixing, leaving-still, phase-separating, and crystallizing. The phase separation solvent comprises acetonitrile, or acetonitrile, ethyl formate, methyl formate, methyl acetate, ethyl acetate, tetrahydrofuran and/or methyl ethyl ketone mixed with 1-3C alcohol or 3-5C alcohol.    USE - Extraction and purification of calcium lactate used in preparation of high-purity lactic acid and fermentation liquid.    ADVANTAGE - The method enables simple, safe and environmentally-friendly extraction and purification of calcium lactate by eliminating back-extraction, using recyclable and nontoxic phase-separation solvent having low boiling point, with pigment removal rate of 97%, protein removal rate of 98% and total sugar removal rate of 98%.
NOVELTY - A high-entropy hydrogen storage alloy is lithium-doped titanium-vanadium-nickel composite (I) obtained by adding lithium metal to void of titanium-vanadium-nickel composite.    USE - High-entropy hydrogen storage alloy (claimed).    ADVANTAGE - The high-entropy hydrogen storage alloy has excellent electrochemical hydrogen absorption and desorption property and cycle stability, and high discharge rate.    DETAILED DESCRIPTION - A high-entropy hydrogen storage alloy is lithium-doped titanium-vanadium-nickel composite of formula: Ti55V10Ni35:Li (I), obtained by adding lithium metal to void of titanium-vanadium-nickel composite. An INDEPENDENT CLAIM is included for preparation of high-entropy hydrogen storage alloy.
NOVELTY - A garbage processing system is a fuel-based system having classifier which classifies garbage into organic waste and combustible waste. The system is reusable, so as to reduce energy consumption.    USE - Garbage processing system (claimed).    ADVANTAGE - The system processes garbage efficiently with reduced energy consumption.
NOVELTY - Usage method of biodiesel byproduct crude glycerin involves acidifying glycerin soap, separating crude glycerin byproduct, neutralizing crude glycerin, flash-evaporating under vacuum and distilling glycerin.    USE - Usage method of biodiesel byproduct crude glycerin (claimed).    ADVANTAGE - The method enables efficient and economical usage of biodiesel byproduct crude glycerin with high purity and productivity.
NOVELTY - Waste carbonization reaction system comprises a reactor (3), steam generator (6) and a control device; the control device is connected to the reactor, the steam generator is connected to the reactor for providing the steam, and the reactor carries out waste reaction so as to generate carbonization mixture; and the control device is used for controlling the reactor pressure, temperature changes, and reaction time.    USE - Used as a waste carbonization reaction system.    ADVANTAGE - The reaction system: is an advanced device; has high automation degree, low device investment costs; require small area; has high value for biomass fuel combustion; and produces low emissions.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the waste carbonization reaction system.    Multiple reaction tanks (2)    Reactor (3)    Steam generator (6)    Drying means (9)    First screening means (10)
NOVELTY - This utility new type provide the one a kitchen garbage biochemical processing machine, comprising rotary cylinder and stir shaft, a combustion heating device, the left and right fixing seat, rotary cylinder set on the left and right fixing base, a stir shaft average distribute set with several stirrer, directly set a containing space on the rotary cylinder in, set on the lower part of centre shaft of the revolving drum and left and right fixing seat is fixed by the side wall of the rotary cylinder is provided with one opening, and the opening is provided with one movable cover, combustion heating device and a hot air connecting, exit of air through one end opening of the rotary cylinder extends into the containing space inner, further comprising: shutter pa with the combustion heating device of table and a gasification device, a fuel inlet of the combustion heating. exit of gasification device connected. This utility new type provide use of kitchen garbage biochemical processing machine can be a resource recycling, and provide the best of environment protection; really realizes the kitchen waste, harmless and recycling standard.
NOVELTY - The fuel cell stack distributor (100) includes a fuel anode inlet and outlet (120) which is penetratedly located in a main case (110). The fuel anode inlet and outlet is crossly located corresponding to the fuel cell stack in order to supply and discharge of the fuel. An air electrode inlet and outlet (130) is penetratedly located corresponding to the fuel cell stack in order to supply and discharge of air. A first O-ring (122) is mounted in a fuel anode gasket groove (121) formed in the side of the fuel anode inlet and outlet.    USE - Distributor for fuel cell stack for generating electricity.    ADVANTAGE - The supplying and discharging of the fuel and air is improved, since the fuel anode inlet and outlet and the air electrode inlet and outlet are penetratedly formed in the main case. The manufacturing of the fuel cell stack distributor is facilitated.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the fuel cell stack distributor.    Fuel cell stack distributor (100)    Main case (110)    Fuel anode inlet and outlet (120)    Fuel anode gasket groove (121)    First O-ring (122)    Air electrode inlet and outlet (130)
NOVELTY - The module (10) has gas separation elements (12) comprising two membrane sheets (18) and a permeate carrier (20) that is sandwiched between the membrane sheets. The permeate carrier comprises macroporous layers and gas-impermeable sheet that is located between the macroporous layers, where the membrane sheets and the permeate carrier comprise a surface profile that comprises surface projections. The macroporous layers are provided by macroporous sheets. The permeate carrier comprises macroporous sheet that is folded around a gas impermeable sheet.    USE - Spiral wound gas separation module for separating gases e.g. carbon dioxide, nitrogen, methane, hydrogen and hydrogen sulfide. Can also be used for reducing gas for direct reduction of iron ore in steel production industry application, dehydration application of organic solvents i.e. ethanol dehydration application, pervaporation application, oxygen enrichment application, solvent resistant nanofiltration application and vapor separation application.    ADVANTAGE - The module allows a gas-impermeable sheet to improve selectivity and gas flux and to reduce compaction of the gas separation element arising from high pressures experienced by the module in an efficient manner. The module prevents the feed gas from entering permeate carrier without being filtered.    DETAILED DESCRIPTION - The macroporous layers comprise a knitted fabric. An INDEPENDENT CLAIM is also included for a process for separating gases and purifying feed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a partially exploded perspective view of spiral wound gas separation module.    Spiral wound gas separation module (10)    Gas separation elements (12)    Optional feed spacer screens (14)    Permeate collection tubes (16, 24)    Membrane sheets (18)    Permeate carrier (20)    Perforations (22)
NOVELTY - The membrane has a gutter layer activated by corona treatment, plasma treatment, flame treatment and ozone treatment, where discriminating layer, protective layer and gutter layer remain in place when a peeling force of 2.5 Newton/1.5 cm is applied to the outermost of the discriminating layer, the protective layer and the gutter layer. The discriminating layer is obtained from a composition, which is free from silane compounds that comprise acetoxy-groups, where thickness of the gutter layer on the support is influenced by controlling amount of curable composition.    USE - Composite gas membrane for use in a gas separation cartridge i.e. spiral-wound cartridge, of a gas separation module (all claimed) for separating feed gases e.g. carbon dioxide, nitrogen, hydrogen and hydrogen sulfide. Can also be used for reducing gas for direct reduction of iron ore in steel production industry application, dehydration application of organic solvents i.e. ethanol dehydration application, pervaporation application, oxygen enrichment application, solvent resistant nanofiltration application and vapor separation application.    ADVANTAGE - The membrane allows a porous support to provide mechanical strength to membrane without materially reducing gas flux. The membrane is designed with good combination of high selectivity and good robustness while improving wettability and adhesiveness.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for separating a feed gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of adhesive tape which is used to determine whether layers of composite membranes remain in place when peeling force is applied.    Adhesive tapes (1, 2)    Lighter area (3)
NOVELTY - The fuel cell (80) has an electrochemically active assembly located within the cavity capable of absorbing microwave radiation. A microwave applicator has a source of microwave radiation and a waveguide to transmit microwave radiation into the cavity. The cavity is configured such that desired microwave field configuration is produced within the cavity when a portion of the electrochemically active assembly is selectively heated. The fuel cell is tuneable so that desired microwave field configuration can be controlled and/or modified and/or optimized during operation.    USE - Fuel cell used to generate power, produce hydrogen, to produce industrially useful chemical, for carbon dioxide separation e.g. from a flue gas stream, to generate combined heat and power and/or to generate combined heat, hydrogen and power (all claimed). Uses include but are not limited to solid oxide fuel cell, polymer electrolyte membrane fuel cell, a direct methanol fuel cell, an alkaline fuel cell, phosphoric acid fuel cell, and molten carbonate fuel cell or regenerative fuel cell.    ADVANTAGE - The microwave field configuration in fuel cell enables a user to significantly influence or control the rate of catalytic reactions and/or electrochemical transport processes which occur within the interior or across interfacial regions of the electrochemically active assembly. The impedance of the cavity can be tuneable, in order to obtain and/or maintain effective coupling of the microwave field with the fuel cell, while improving safety of the fuel cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a fuel cell.    Fuel cell (80)    Cathode (87)    Electrolyte (88)    Upper wall (90)    Lower wall (91)
NOVELTY - The material comprising yttrium, neodymium, praseodymium, samarium, gadolinium, europium and terbium. A main body is formed with a bi-layer perovskite structure.    USE - Anode material for a solid oxide fuel cell during manufacturing process of an anode electrode (all claimed).    ADVANTAGE - The material is heated at high temperature and formed with the bi-layer perovskite structure so as to improve thermal chemical stability and conductivity. The material is simple to manufacture and inexpensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for manufacturing an anode material of a solid oxide fuel cell    (2) a solid oxide fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a solid oxide fuel cell.    Solid oxide fuel cell (100)    Anode (110)    Cathode (120)    Electrolyte (130)
NOVELTY - The method involves distributing (130) a mixture of hydrogen gas and natural gas through a natural gas network. A part of the hydrogen gas is removed (150) from the mixture according to the distribution of the mixture through the natural gas network and prior to distribution to a final consumer. The part of the hydrogen gas is removed from the mixture using a membrane filter.    USE - Method for distributing hydrogen gas to final consumers.    ADVANTAGE - The part of the hydrogen gas is removed from the mixture according to the distribution of the mixture through the natural gas network and prior to distribution to a final consumer, and hence ensures distributing the hydrogen gas to final consumers in an effective and simple manner to make it available to the final consumers in an easy manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a removal unit for removing a portion of a hydrogen gas from a mixture of hydrogen gas and natural gas from a natural gas network; and    (2) an apparatus for distribution of hydrogen gas to final consumers.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of a hydrogen gas distributing method.    Mixing hydrogen gas with natural gas (110)    Introducing mixture of hydrogen gas and natural gas into a natural gas network (120)    Distributing a mixture of hydrogen gas and natural gas through a natural gas network (130)    Redirecting the mixture to a removal unit prior to the arrival of the gas system at the final consumer (140)    Removing a part of the hydrogen gas from the mixture (150)
NOVELTY - A sugar is manufactured by wet-grinding herbal biomass using medium stirring-type grinder and acquiring ground process biomass, making ground process biomass contact with basic compound and acquiring alkali treated biomass and carrying out saccharification process of alkali treated biomass with enzyme.    USE - Manufacture of sugar used for manufacturing ethanol.    ADVANTAGE - Productivity is excellent.
NOVELTY - Alcohol production involves heating banana trunk in water with starter, and then performing distillation of the formed mixture. The heating process is accomplished through a coil, where the heated mixture is cooled with running water for transforming steam into liquid as alcohol.    USE - Method for producing alcohol.    ADVANTAGE - The method produces alcohol in a simple and cost-effective manner.
NOVELTY - A self-service multi-tube a ENT (ear-nose-throat), comprising piston rod, piston cavity, attraction pipe and delivery pipe, the inner piston rod is the piston cavity, the piston cavity outside side set with medicine absorbing pipe and delivery pipe, end of the administration tube set has, through dividing into multi-partition a cavity body of the piston inner cavity, a inner cavity body set with a root and a cavity body with a piston rod, the delivery tube and the piston cavity through activity connection connector, the connector and at the same time the connected connection of each cavity body and a delivery pipe, a connector and a piston cavity set with one-way valve. This utility new type of design of a multi-cavity body, a liquid between each of cavity body would not with each other, while at the same time adding in a multi-liquid of traditional Chinese medicine, satisfying conveniently and quickly is a, and a is the cross pollute of the sanitary and environment-friendly.
NOVELTY - Allyl alcohol production involves using glycerin from castor oil biodiesel production waste. The glycerin is reacted with formic acid at 260 degrees C to obtain a colorless and volatile product i.e. allyl alcohol.    USE - Method for producing allyl alcohol used as diluent in plastics industry, lubricants, cosmetics, pharmaceuticals and petrochemicals.    ADVANTAGE - The method enables to produce allyl alcohol in a simple, cost-effective and eco-friendly manner by using glycerin in large amount from biodiesel waste.
NOVELTY - An environment-friendly solvent comprises 80-90 wt.% camphene, 2-3 wt.% antioxidant, 2-4 wt.% surfactant, 5-8 wt.% catalyst, and 2-3 wt.% cosolvent.    USE - Environment-friendly solvent.    ADVANTAGE - The environment-friendly solvent has mild reaction condition, easy operation, good compatibility in pesticide products, good solubility.
NOVELTY - Biofungicide (I), is new.    USE - Biofungicide.    ADVANTAGE - The biofungicide ensures increased proportions of dodecyl groups, and prevents contamination and spread of fungus i.e. Aspergillus, preferably Aspergillus flavus, and can be prepared in a simple and cost-effective manner by using natural, abundant, and biodegradable raw material.    DETAILED DESCRIPTION - Biofungicide of formula (I), is new.    R1=represents diethylaminoethylamine;    R2=represents alkyl groups of hydrophobic nature, aromatic or aliphatic group selected from group of formulae (II-III);    n=4-11; and    m=1-5.    An INDEPENDENT CLAIM is included for a method for preparing biofungicide, which involves:    (A) performing deacetylation of chitosan;    (B) obtaining chitosan derivatives; and    (C) purifying alkylated derivatives.
NOVELTY - The apparatus (300) has a catalyst ink dryer part (100) provided with a spray dryer (120) according to spray-dries catalyst ink containing catalyst and electrolyte and forms catalyst powder. A catalyst application part (200) deposits catalyst powder on a gas-permeable base material (204). A pressure regulation part (206) i.e. suction blower, adjusts pressure of the catalyst application part. A grinding device grinds the catalyst powder provided between the catalyst ink dryer part and the catalyst application part.    USE - Catalyst layer manufacturing apparatus for fuel cells in a fuel cell power generation system.    ADVANTAGE - The apparatus can form the catalyst layer without improve coating rate of the catalyst powder.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a catalyst layer manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a catalyst layer manufacturing apparatus.    Catalyst ink dryer part (100)    Spray dryer (120)    Catalyst application part (200)    Gas-permeable base material (204)    Pressure regulation part (206)    Catalyst layer manufacturing apparatus (300)
NOVELTY - The composition comprises a mixture of components in a proportion of 68% ester of vegetable oils and 30% base ingredients ethylhexyl nitrate, and 2% fatty alcohol alkoxylate, and anti-scaling solvents.    USE - Composition for liquid additive formulation for mixtures of mineral diesel oil.    ADVANTAGE - The composition reduces emissions causing greenhouse effect, preferably particulate emissions and residual sulfur mineral diesel oil and consequent increase in agribusiness activities to reduce oil import costs.
NOVELTY - Carrying out aerobic composting involves feeding organic material on top of a compost column (10) and removing compound from a bottom (23). The compost column is divided by a grid (22) which supports fed organic material and allows passage of natural material which is already decomposed.    USE - Process for carrying out aerobic composting (claimed).    ADVANTAGE - The process enables to carry out aerobic composting in a continuous manner, equipment maintains suitable temperature due to thermal insulation, and prevents overheating of aerating system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of aerating system.    Compost column (10)    Composting stack (21)    Grid (22)    Bottom (23)    Diffusion of oxygen (24)
NOVELTY - The method involves collecting sewage treatment plant actual water quality parameter data, and selecting the water ammonia nitrogen concentration, total phosphorus TP quantity, anaerobic oxidation-reduction potential ORP, an aerobic section dissolved oxygen quantity, an aerobic total solid suspension and discharged water quantity, designing a recursive forecast for water ammonia nitrogen concentration from tissue neural network topology structure.    USE - Water ammonia nitrogen concentration forecast method.    ADVANTAGE - The method enables accurately forecasting sewage treatment concentration of water ammonia nitrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a water ammonia nitrogen concentration forecast method. '(Drawing includes non-English language text)'
NOVELTY - Granular rodenticide comprises 2-4 pts. wt. bromadiolone, 20-40 pts. wt. diclofenac sodium, 2-4 pts. wt. metronidazole, 0.6-3 pts. wt. saccharin, 0.4-0.6 pts. wt. salt, 20-35 pts. wt. peanut powder and 0.5-2 pts. wt. phenobarbital.    USE - Used as granular rodenticide.    ADVANTAGE - The rodenticide has simple preparation, and is economical and environmentally friendly.
NOVELTY - A plant straw treatment process comprises taking straw, removing impurities, pulverizing, adding 0.1-2.0 wt.% sodium carboxymethyl cellulose, stirring, putting into expanding machine, and carrying out hydrolysis reaction at 100-200 degrees C for 40-80 seconds.    USE - Plant straw treatment process used as papermaking material (claimed).
NOVELTY - The pool has a pool main body (1) arranged with a hole layer (2) and a porous liner layer (3). An upper end of the pool main body is provided with a supporting beam (4) and a water discharging pipe (5). An inner side of the pool main body is filled with fermentation liquid.    USE - Garden rubbish treatment pool.    ADVANTAGE - The pool has reasonable design, low processing cost, easy processing operation, convenient maintenance operation, high popularization value and wide application range.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a garden rubbish treatment pool.    Pool main body (1)    Hole layer (2)    Porous liner layer (3)    Supporting beam (4)    Water discharging pipe (5)
NOVELTY - Extracting hyodeoxycholic acid involves saponifying pig bile paste and then oxidizing the saponified material into calcium salt. The oxidized material is extracted and then the extracted material is subjected to decalcification. The decalcified material is subjected for crystallization and then the crystallized material is dried to obtain hyodeoxycholic acid.    USE - Method for extracting hyodeoxycholic acid (claimed).    ADVANTAGE - The method enables to extract hyodeoxycholic acid in simple, environment friendly and cost-effective manner, and with high yield and purity.
NOVELTY - This utility new type relates to greenhouse cultivation technology field, specifically claims a carbon dioxide generator and the a carbon dioxide generator is a plant growing lamp. A the inner plant growing lamp, comprising LED lamp body (1) and a shell, the LED lamp body (1) is provided with a carbon dioxide generator (2), a carbon dioxide generator (2) comprises a vessel (4), this vessel (4) has a generating fungi of carbon dioxide (5), the vessel (4) has set with a vessel (4) for inner temperature of temperature control unit (3). The LED lamp body (1) and a carbon dioxide (2) is located in the inner shell. This utility new type it is, the growing of fungus product using carbon dioxide, adding epiphyte for generating carbon dioxide, avoiding continuously adding fuel cause manpower and material resources cost high a problem, at the same time, this carbon dioxide generator does not release harmful gas, energy-saving and environment-friendly.
NOVELTY - This utility new type claims a a multi-layer digestion aerobic compost bed system, including a multi-layer multi-digestion bed, at least one of the composting room, at least one of an oxygen supply system. This utility new type process for sludge mixture in aerobic compost process in without need of turning or stirring, and without need for sludge mixture a forced ventilation of the aerobic microorganism in the sludge mixture can obtain enough oxygen finish aerobic compost, in process of aerobic compost can fully use the aerobic microorganism is self-heat energy, so the utility model is new type of technology solution item small floor area, but also can obviously reduce device investment and operation cost of aerobic compost, sludge stabilization of high aerobic compost time short, it can obviously increase effect and efficiency of aerobic compost, furthest reduce in sludge compost process of energy loss and reduces pollute environment.
NOVELTY - This utility new type is a organic fertilizer concentrated liquid a manufacturing device, the organic fertilizer concentrated liquid manufacturing device comprises fermentation pool, distillation device and vacuum processing device, a fermentation pool, the distillation device and vacuum processing device has pipe set is connected with the fermentation pool comprises pool body and filter screen, a filter screen set at the bottom of pool body, the pool body has set with pool cover, the filter screen inside has set with water pump, water pump and conduit is connected with the distillation device in turn has set with steam water tank, distillation chamber, distillation machine, concentrated liquid outlet and machine frame A, one side of said steam water tank has the water pipe set, said vacuum processing device comprises vacuum machine, cavity body, liquid fertilizer outlet and machine frame B, the vacuum machine set in middle part of vacuum processing device, the liquid fertilizer outlet set at the bottom of cavity body, this organic fertilizer concentrated liquid manufacturing device comprises simple structure, use concentrated liquid fertilizer efficiency high, without pollute of environment-friendly.
NOVELTY - This utility new type claims a device for recovering melamine tail pneuma using urea device, referring to melamine tail pneuma recovery processing technology field, comprising tail pneuma and a compressor set provided with one section decomposing tower of urea device, wherein said one section decomposing tower side wall and a section of decomposing tower is the following part separating a section corresponding to the bottom of the is provided with a tail pneuma entrance; the tail pneuma compressor through tail pneuma entrance and one section decomposing tower connected. This utility new type not only can better use of melamine tail pneuma heat, and urea production control process steady and convenient a urea production process, increase urea device without energy consumption.
NOVELTY - A silt cleaning device system of marsh gas fermentation pool and a cleaning construction process, a separate sewage dewatering machine, sewage pump, hand push suction sewage truck, a slope track frame of a flat track. Separating sewage dewatering machine comprises a machine frame, a machine frame set with memory slurry tank, a slurry dispenser. Slurry storing tank the upper part provided with a sieving machine, a sieving machine is divided into upper and lower two layer surfaces, for wherein water distributor set with clapboard, water outlet is for upper sieve and lower sieve for a hopper, and a lower sieve and a vibration sieving machine upper. Slurry storing tank provided with slag guide chute, an overflow pipe, a drain pump, seriflux stir device and sedimentation the dung dirt, diluting device. Slurry storing tank the upper part welding has distributor fixing frame. By a device and construction technique, can large fermenting pool to sedimentation dung dirt efficient cleaning process and a dewatering process.
NOVELTY - The utility model claims a high temperature anaerobic fermentation device, belongs to biological ferment field. Solves the problem of high temperature Anaerobic fermentation device for precision is low, the fermentation tank material inner body non-visible and biogas generated after can not liquefied by removing converying, a inconvenient problem is. This utility new type further comprises liquefying device, a marsh gas entrance window is electric heating piece, the liquefying device and marsh gas output pipe connected the side wall of the fermentation tank is provided with a through hole, the perspective window is fixed in a through hole of a fermentation tank side wall, electric heating piece fixed at a transmission shaft of stirrer, the electric heating piece through lead and external power supply connection. It is a b for biological fermentation.
NOVELTY - A toilet device comprises feces compartment with toilet seat (6) in connection with feces inlet and liquid tank below the feces compartment, liquid passage allowing liquid to be drained from the feces compartment into the liquid compartment, and vent passage to the composting compartment for exposing the feces bed inside the composting compartment to air to allow the feces to compost, thus forming compost product. The toilet seat comprises movable seat part (6A) connected to cover mechanism (100) having transmission unit to remove inner cover (101, 102) when activated.    USE - Toilet device for composting feces and/or for treating urine (claimed).    ADVANTAGE - The device prevents a person using it to see into the feces compartment under the seat of the toilet.    DESCRIPTION OF DRAWING(S) - The drawings are side views of toilet seat.    Toilet base surface (4)    Toilet seat (6)    Movable seat part (6A)    Cover mechanism (100)    Inner cover (101, 102)
NOVELTY - Method of production of active organic fertiliser from waste products consists in that the mechanical impurities are removed, supply, movement and also simultaneous mixing and homogenisation is carried out, and the waste products flow is fed for mixing and homogenisation tangentially creating a rotating vortex medium, the homogenised suspension is obtained, having the density of 1.26-1.3 g/cm3, affecting it with energy-saturated, electromagnetic rotating field from the magnetic domains, which carry out waste product dispergation with destruction of chemical and biological structures at the molecular level, thereby obtaining sterile emulsion which is then separated into fractions. The organic fraction with humidity of 85-87% is extracted into independent nutrient medium and additives are added to it in the form of strains of soil-forming microorganisms. The complex for production of active organic fertiliser from waste products comprises a unit of waste product treatment, the unit of simultaneous mixing and homogenisation, the means of feeding and movement of masses, and it is additionally provided with a unit of process activation with the magnetic domains, a unit of fraction separation, a mixer, and a dispenser of additives.    USE - Agriculture.    ADVANTAGE - Inventions enable to convert nitrogen, phosphorus and other elements in the biogenic forms of microelements and amino acids, which enables to obtain active organic fertiliser.2 cl, 1 dwg
NOVELTY - The apparatus has a rotary tank connected with a corrosion-resistance piping. An inner side of the rotary tank circulates flame-retardant gas at a low boiling point. A resistance part is connected to a tank inner wall. A tank part is driven by an adjustable speed motor. Low boiling-point flame-resistant liquid is high-pressure-steamed within the tank. A gas turbine is rotated for electric power generation. A stirring tank (6) is provided with a binary electric power generating apparatus. A control panel controls a continuous-type processing apparatus.    USE - Low temperature-type carbonization apparatus for carbonizing microorganisms in excretion of animal and plant residue.    ADVANTAGE - The gas turbine is rotated for electric power generation, so that removal of offensive odor and purification of drain are simplified and economization cost is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows front, top and right views of a microbial fermentation tank apparatus.    Material injection receptacle transfer apparatus (4)    Upper-tank fixed support frame (5)    Stirring tank (6)    Work-handling pipe (7)    Intermediate support frame (8)
NOVELTY - The method involves selecting (101) the edible functional material among pulses, cereals, green tea leaves, mulberry leaves, ginseng, garlic, broccoli, Hovenia dulcis fruit, Schizandra, Japanese apricot, which contain health functionality component, such as vitamin, calcium, chitosan or caffeine. The type of beverage to be manufactured is selected (102). The selected functional material is washed and dried (103). The dried functional material is pulverized into nano particles. The surface area of the functional material is expanded for mixing (105) the material with liquid.    USE - Method for manufacturing functional beverage.    ADVANTAGE - Efficient utilization of functional component is enabled. Easy and economical manufacturing of functional beverage is ensured with low energy consumption and with minimized waste generation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for manufacturing functional beverage.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart of a functional beverage manufacturing method. (Drawing includes non-English language text).    Selecting edible functional material containing health functionality component (101)    Selecting type of beverage to be manufactured (102)    Washing and drying selected functional material (103)    Mixing functional material with liquid (105)    Molecular bonding between nano particles of the functional material (106)
NOVELTY - Lignin thermoplastic material is prepared by enzymolyzing biomass feedstock to obtain lignin-containing slag, drying, crushing to obtain lignin material, mixing with polyethylene (PE) resin, and performing plastic extrusion.    USE - Preparation of lignin thermoplastic material (claimed).    ADVANTAGE - Lignin thermoplastic material has good waterproofing performance and high tensile strength.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram for the preparation of lignin thermoplastic material. (Drawing includes non-English language text).
NOVELTY - The method involves tape casting an anode support. The layers such as an anode functional layer, an electrolyte layer and a cathode functional layer are sprayed onto the anode support. The process comprises preparing anode slurry. The anode slurry is degassed. The anode slurry is casted onto a support to form a ceramic tape. The ceramic tape is dried to produce the anode support. The spraying layers comprise preparing ceramic slurry. The slurry is delivered to a spray nozzle. The slurry is sprayed and atomized onto an anode support to form a sprayed layer.    USE - Method for producing solid oxide fuel cell (SOFC) for use in transportation, residential and distributed-power application.    ADVANTAGE - The direct utilization of hydrocarbon fuels will increase the operating efficiency and reduce system costs, which accelerates the use of SOFCs in transportation, residential and distributed-power application. The SOFC that directly run on natural gas highly reduce the operating cost and accelerate the commercialization of SOFC system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating the solid oxide fuel cell.
NOVELTY - The fertilizer has a screen machine feeding device (140) that includes a feeding conveying mechanism that is provided with belts, tightening rollers and transmission rollers. A screening machine is set with filter rack (151), filter motor (152), rotating shaft (153), and filter screen rotating cylinder (154). A transfer device is set with motor, conveyer belt, transmission roller, and pedestal. A conveying belt is in turn set with head transmission roller, rear multi-rotating roller group and end transmission roller through transmission pedestal form circulation.    USE - Organic fertilizer in stacking fermentation after treatment device.    ADVANTAGE - The fertilizer operation is simple, use is convenient. The device is used for each of mechanism and material carrying out transmission, so as to realize automatic production, to reduce cost and increase production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of screen machine.    Screen machine feeding device (140)    Filter rack (151)    Filter motor (152)    Rotating shaft (153)    Filter screen rotating cylinder (154)
NOVELTY - The device has an oil return pipe (1342) whose one end is set with a heating cavity (1344) while other end is set with a guide heat oil return oil tank (1341). A stir mechanism is provided with a stir rotation axis along a circumferential direction. A stir element is set with a transverse pole (1323). A rotating shaft (1321) is connected with a stir motor. A horizontal end of the transverse pole is connected with rotating shaft. A bottom pole (1324) is formed parallel to the transverse pole. An end of transverse pole is set at a distance from a fermentation tank (133).    USE - Organic fertilizer production device for stirring fermentation system.    ADVANTAGE - The simple and convenient use of the device is ensured for fermenting, heating, sterilizing and stir multifunctional integration, so as to realize automatic production, reduce cost and increase production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic fertilizer production device.    Fermentation tank (133)    Rotating shaft (1321)    Transverse pole (1323)    Bottom pole (1324)    Guide heat oil return oil tank (1341)    Oil return pipe (1342)    Heating cavity (1344)
NOVELTY - The system has a stir mechanism which is set at an inner portion of a fermentation tank (133). A top portion of the fermentation tank is set with an entrance while bottom is set with a fermentation outlet. A heating mechanism (134) is provided with a guide oil return oil tank (1341), an oil pipe (1342), and four heating cavities (1344). An inner heating chamber is set with a heating coil pipe, an oil inlet pipe and an oil return pipe.    USE - Organic fertilizer production stirred fermentation system.    ADVANTAGE - The simple and convenient use for fermenting, heating, sterilizing and stir multifunctional integration is ensured so as to realize automatic production, reduction in cost and increase in production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic fertilizer production stirred fermentation system.    Fermentation tank (133)    Heating mechanism (134)    Oil return oil tank (1341)    Oil pipe (1342)    Heating cavities (1344)
NOVELTY - The fertilizer has a separating tank (124) that is integrally molded with conveying tank (125), and is inclined set with separating pedestal (121). The separating tank is respectively set with mixture entrance and plastic bag exit. A conveyor belt (127) is set with isolation network and transmission wheel. An oil inlet pipe and oil return pipe are set with one end of four heating cavity whose other end is respectively guide with heat oil return oil tank. The return oil tank return oil pipe of inner height is higher than the oil pipe.    USE - Organic fertilizer in piling and fermenting front processing device.    ADVANTAGE - The automatic production is realized, so as to reduce cost and increase production efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the organic fertilizer.    Separating pedestal (121)    Separating motor (122)    Separating tank (124)    Conveying tank (125)    Conveyor belt (127)
NOVELTY - This utility new type relates to a improved is organic fertilizer fermenting pool. The purpose is provide a temperature uniformity of a organic fertilizer fermenting pool, comprising fermenting pool, temperature control system and temperature control system and electric connection of temperature sensor and heating device, a fermentation pool is one a side wall, a heating device comprising a uniform distribute b multi-heating rod of fermentation pool inside of all heating rod vertical to b. bottom of the fermentation pool, a minimum gap between the heating rod is 20 to 40 cm, the heating rod is a fixed end mounted in a pool cover of fermentation pool top part, a pool cover for a fermentation pool top form seal, driving pool cover at the outside of the fermentation pool along the b direction is vertical to bottom of the fermentation pool is slide back and forth lifting mechanism. This utility new type ensures the whole fermentation process in the raw material stack is outside inner layer maintain uniform temperature, so as to ensure the homogeneity of raw material ferment, the production of organic fertilizer product a uniform high degree.
NOVELTY - The apparatus has an initial feedstock preparation unit sequentially connected with container for acidogenic processing of a substrate. A fermenter is connected with a source of a gas bubble system in a form of set of pipes. A biogas concentration unit is installed in a vertical inside of a case and placed in hollow cases of porous material. A bubble system comprises a set of pipes that is installed with exception condition for bringing gas from an atomizer directly to a provided unit for measuring concentration of the biogas.    USE - Direct-flow biogas installation apparatus.
NOVELTY - The reactor (1) has an entry portion (6) for supplying fuel, and an oxidization portion (11) oxidizing oxygen mixture under fuel supply. A discharge portion (31) comprises an exhaust opening (32) for removal of smoke combustible gas mixture. A stout/detour plate (26) is arranged in a detour portion under a reduction portion. A flowing against element (27) is arranged into the reduction portion, where position of the reduction portion is adjusted by the stout/detour plate and/or the flowing against element, and an idle passage area is influenced.    USE - Gasification reactor for recovering combustible gas from carbonaceous fuel i.e. timber, in form of hogged wood (all claimed).    ADVANTAGE - The reactor adjusts position of the reduction portion by the stout/detour plate, thus enhancing efficiency of the gasification reactor and performing large extent complete reaction of fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for recovering a combustible gas from carbonaceous fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a gasification reactor.    Gasification reactor (1)    Entry portion (6)    Oxidization portion (11)    Stout/detour plate (26)    Flowing against element (27)    Discharge portion (31)    Exhaust opening (32)
NOVELTY - The co-generation apparatus has fuel cell (11) which generates electric power by first generation amount at the time of power failure of electric power grid (3). A heater (16) consumes surplus electric power while supplying electric power to waste heat recovery unit (14) and self-sustaining outlet sockets (35a,35b). A fuel cell control unit (15) reduces generation amount of fuel cell to second generation amount which can continue exhaust-heat recovery operation, when electric current value of sum total output from sockets is continuously below judgment value for predetermined time.    USE - Co-generation apparatus with self-sustaining function for continuing electric power generation during power failure of electric power grid.    ADVANTAGE - Heat generated by electric heater can be utilized to produce warm water when using electric heater as electric load which consumes surplus electric power. Reduces useless power consumption by reducing surplus electric power in self-sustaining state.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic block diagram of the co-generation apparatus. (Drawing includes non-English language text).    Electric power grid (3)    Fuel cell (11)    Waste heat recovery unit (14)    Fuel cell control unit (15)    Heater (16)    Self-sustaining outlet sockets (35a,35b)
NOVELTY - The processing unit has a liquefied natural gas (LNG) storage tank arranged in a liquefied gas carrier. A mist separator separates mixing gas of mixed air-liquid condition of the LNG storage tank. A drain pot receives separated LNG from the mist separator. A boil off gas (BOG) compressor supplies BOG of high pressure to the drain pot and screw pipe of the liquefied gas carrier to return the separated LNG to the LNG storage tank. A cooling part cools the BOG by using LNG. An inert gas generator supplies inert gas of high pressure to the drain pot.    USE - BOG processing unit for a liquefied gas carrier.    ADVANTAGE - The processing unit avoids usage of a separate equipment for the inert gas generator and supplies the BOG to the LNG so as to prevent contamination of the LNG by inert gas. The processing unit selectively supplies BOG and inert gas to the LNG of the drain pot so as to improve operation efficiency of the processing unit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing BOG of a liquefied gas carrier.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a boil off gas processing unit.'(Drawing includes non-English language text)'
NOVELTY - Organic fertilizer in an aerosol container comprises solution containing an organic fertilizer and 0.5-2.5 %mass surfactant, where the organic fertilizer and surfactant are compressed together with propellant and the fertilizer is ball shape fertilizer.    USE - The organic fertilizer in an aerosol container is useful as horticultural fertilizer.    ADVANTAGE - The organic fertilizer in an aerosol container is convenient to use, and suitable for long-term storage and enables to visually confirm the amount of fertilizing.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preserving the fertilizer, which involves introducing the above-mentioned solution with propellant into an aerosol container and sealing the container.
NOVELTY - The gas sensor (4) has an electrode (3) that is contacted, and provided in a gas detection layer (2). The gas detection layer is included with a transparent conductive zinc oxide polycrystal thin film, and formed on a substrate (1). The carrier density of transparent conductive zinc oxide polycrystal thin film is 3.0asterisk1020/cm3 or less. The thickness of the polycrystal thin film is 50 nm or less, while element which consists of gallium and/or aluminum is added to the thin film.    USE - Gas sensor used for detecting various combustible gases such as acrylonitrile, acrolein, acetylene, acetaldehyde, arsine, ammonia, carbon monoxide, ethane, ethylamine, ethylbenzene, ethylene, ethyl chloride, vinyl chloride, chloromethyl, ethylene oxide, propylene oxide, hydrogen cyanide, cyclopropane, disilane, diborane, dimethylamine, hydrogen, hydrogen selenide, trimethylamine, carbon disulfide, butadiene, butane, butylene, propane, propylene, bromomethyl etc.    ADVANTAGE - The gas sensor using the zinc oxide polycrystal thin film is capable of attaining the high sensitivity, without using the amplifier circuit. The gas detection is performed by measuring the reduction of the electric current, while reducing the electric current flowing into gas detection layer. As the sensor sensitivity by gas detection mechanism has low temperature dependence, the sensor attaining favorable sensitivity at low temperature is provided. As the heating of gas sensor in very high temperature is made unnecessary, the power consumption is minimized. The fall of the precision of sensor sensitivity is prevented, as the change of the voltage by temperature rise is avoided.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the gas sensor.    Substrate (1)    Gas detection layer (2)    Electrode (3)    Gas sensor (4)
NOVELTY - The bioreactor system has a containment vessel (2) having a wall having inner and outer sides forming an interior having an inner diameter, lower end (6) and upper end, and a medial area. A vertically oriented flow tube is positioned in interior of containment vessel, with flow tube forming a longitudinal passage having a bottom, a top, and a medial area. The containment vessel and the flow tube are collectively structured to facilitate the circulation of fluid biomass between interior of containment vessel and longitudinal passage of flow tube.    USE - Bioreactor system for growing commercial volumes of biomass such as algae.    ADVANTAGE - A cost-effective and controlled bioreactor system is provided for small and large scale production of energy-rich algae or other forms of biological biomass utilizing magnetic fields to stimulate microbial growth and metabolism. The airlift design greatly adds to the efficiency of system by allowing for circulation of the biomass without the necessity of utilizing accessory pumps.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method of cultivating one or more organism in a biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a side exterior view of the bioreactor system.    Core bioreactor (1)    Containment vessel (2)    Lip (5)    Lower end (6)    Observation panel (63)
NOVELTY - The fermentor has a transition connecting pipe (9) fixed with a solid-liquid separating machine (12) through a slurry pump or spiral extruder (14), where solid content of the spiral extruder or the slurry pump is about 20%. The solid-liquid separating machine is fixed with a water-gas separator that is connected with the solid-liquid separating machine. The extruder is connected with a slurry return pump (15). A multistage biogas fermentation pool is located in a pneumatic room (5). A shell (1) is fixed in an inner end of a fermentation shell (4).    USE - Multi-stage biogas fermentation technology based continuity anaerobic dry fermentor.    ADVANTAGE - The fermentor has better standardization effect and high working efficiency, and avoids sewage mixing problem of the solid-liquid separating machine so as to increase production rate of biogas, thus improving energy-saving efficiency of the multistage biogas fermentation technology based continuity anaerobic dry fermentor.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a multi-stage biogas fermentation technology based continuity anaerobic dry fermentor.    Shell (1)    Fermentation shell (4)    Pneumatic room (5)    Transition connecting pipe (9)    Solid-liquid separating machine (12)    Slurry pump or spiral extruder (14)    Slurry return pump (15)
NOVELTY - The device has a middle pipe connected with a drain valve. A liquid phase air outlet is located in a liquid phase fermentation area. A drain pipe is fixed in a fermentation tank body. A three-way pipeline is connected with a liquid phase funnel. The drain valve is fixed with the liquid phase air outlet. A biogas slurry reflowing pipe is fixed with a biogas liquid circulation pump through a nozzle. A biogas backflow pipe is equipped with a biogas slurry backflow valve. An upper end of the fermentation tank body is connected with a pneumatic storage cabinet.    USE - Automatic pre-processing straw-two-phase ferment breaking shell integrated device.    ADVANTAGE - The device has better straw feeding efficiency and better water sealing effect, realizes continuous straw running efficiency and automatic breaking efficiency, and saves stirring power during solid-liquid phase fermenting process.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic diagram of an automatic pre-processing straw-two-phase ferment breaking shell integrated device.
NOVELTY - The device has a gas collecting tube (11) connected with a fermentation tank (19) that is connected with a storage tank (2). A gas flow meter (8) is connected with a pipeline valve (6). A sampling pipe (7) is connected with a sampling valve. A gas storage tank is connected with an upper part of an air outlet pipe (36) that is connected with a pneuma valve (1). A waste discharging pipe (14) is connected with a reverse turning bed valve (17) that is connected with the fermentation tank. A biogas storage tank (16) is connected with a bottom part of a waste liquid taking port (15).    USE - Continuous biogas anaerobic fermentation device for use in a laboratory.    ADVANTAGE - The fermentation tank is contained with ferment raw material so as to realize continuous biogas anaerobic fermentation process under laboratory platform.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a continuous biogas anaerobic fermentation device.    Pneuma valve (1)    Storage tank (2)    Pipeline valve (6)    Sampling pipe (7)    Gas flow meter (8)    Gas collecting tube (11)    Waste discharging pipe (14)    Waste liquid taking port (15)    Biogas storage tank (16)    Reverse turning bed valve (17)    Fermentation tank (19)    Air outlet pipe (36)
NOVELTY - Aspergillus niger JH-2 strain is preserved in China center for type culture collection center under accession number (CCTCC NO: M2014398), and is new.    USE - Aspergillus niger JH-2 strain used for synthesizing asiatic acid (claimed).    ADVANTAGE - The Aspergillus niger JH-2 strain is non-toxic and harmless, and also ensures effective biotransformation of asiaticoside to asiatic acid in a cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for synthesizing asiatic acid, which involves:    (A) performing fermentation by inoculating Aspergillus niger JH-2 strain into a fermentation medium; and    (B) incubating the inoculated fermentation medium at 28-32 degrees C for certain duration, where biotransformation takes place in presence of Aspergillus niger JH-2 strain to produce asiatic acid in the fermentation broth as desired product.
NOVELTY - Producing glycyrrhetinic acid involves inoculating fungal strain on to potato dextrose agar plate and then incubating for 3 days to obtain activated fungal strain. The loop full mycelium of activated strain is inoculated into the seed culture medium comprising liquorice, and then incubated at certain conditions to obtain seed broth. The inoculum of seed broth is inoculated into the fermentation medium to obtain fermentation broth. The resulting fermentation broth is evaporated at 50 degrees C to extract glycyrrhetinic acid from the liquorice.    USE - Method for producing glycyrrhetinic acid through microbial fermentation process (claimed).    ADVANTAGE - The method enables to produce glycyrrhetinic acid in a simple, cost-effective and environmental-friendly manner.    DETAILED DESCRIPTION - Producing glycyrrhetinic acid involves inoculating fungal strain on to potato dextrose agar plate and then incubating for 3 days to obtain activated fungal strain. The loop full mycelium of activated strain is inoculated into the seed culture medium comprising liquorice, and then incubated at certain conditions to obtain seed broth. The inoculum of seed broth is inoculated into the fermentation medium to obtain fermentation broth. The resulting fermentation broth is evaporated at 50 degrees C, where the obtained liquid phase solution is extracted thrice with ether, and then with ethyl acetate thrice to obtain extract. The obtained extract is evaporated at 50 degrees C to obtain liquid phase solution, which is then centrifuged at high-speed. The pellet is discarded to collect upper solution, which is then passed through silica gel column chromatography in the presence of solvent to collect eluate. The collected eluate is evaporated to dryness to obtain glycyrrhetinic acid as finished product.
NOVELTY - The device has a multi-parameter water quality tester (5.9) connected with an emptying tube reactor (5.13). A seal cover is connected with a gas collection pipe (9.5) through a U-type tube (9.7). A gas collection box (9.8) is connected with a portable gas analyzer (9.9). A pH meter (9.4) is connected with an electrode of a reactor wall part. A sludge fermentation reactor (9) is connected with a mud valve (9.1) through a discharging pump (7). A nitrogen reactor (5) is connected with the sludge fermentation reactor through a sludge reflux pump (8) and fixed with a sludge reflux valve (5.2).    USE - Anaerobic fermentation strengthening biological de-nitrogen and sludge reducing device.    ADVANTAGE - The device reduces residual sludge, collects anaerobic fermentation product efficiently and increases production capacity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an anaerobic fermentation strengthening biological de-nitrogen and sludge reducing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an anaerobic fermentation strengthening biological de-nitrogen and sludge reducing device.    Nitrogen reactor (5)    Multi-parameter water quality tester (5.9)    Emptying tube reactor (5.13)    Sludge reflux valve (5.2)    Discharging pump (7)    Sludge reflux pump (8)    Sludge fermentation reactor (9)    Mud valve (9.1)    PH meter (9.4)    Gas collection pipe (9.5)    U-type tube (9.7)    Gas collection box (9.8)    Portable gas analyzer (9.9)
NOVELTY - The device has a fermentation tank (11) that is set close to external insulating layer with a square space. The solar energy solar panels (10) of fermentation tank are set on top of the solar panels. A solar energy charging controller is connected with discharge circuit, and charge discharge circuit is connected with storage battery (3) and heater (5). The heat exchanger (2) is connected with fan (1). The fermentation tank upper portion air inlet pipe and air distribute pipe is connected. The fermentation tank is used for fermenting the fermenting tank inner cage bracket (12).    USE - Portable solid fermentation device.    ADVANTAGE - The fermentation product quality is stable, the energy consumption is low, and does not need external power supply, fit small scale and dispersion of solid waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the portable solid fermentation device.    Fan (1)    Heat exchanger (2)    Storage battery (3)    Heater (5)    Solar energy solar panel (10)    Fermentation tank (11)    Bracket (12)
NOVELTY - The device has a fan (1), a heat exchanger (2), a heater (3), a solar energy solar panel (11), a charging and discharge circuit (6), a storage battery (5), a fermenting tunnel (12), rolling doors (15), an air inlet (8) and an air outlet pipe (13). The rolling doors are arranged at ends of tunnel. The heat exchanger and the fan are connected with air outlet pipe. The heater and heat exchanger are connected with air inlet. The charging and discharge circuit is connected with solar energy solar panel. The battery is connected with heater, the air inlet and the air outlet pipe.    USE - Energy-saving type solid continuous fermenting device.    ADVANTAGE - The uniform and stable product quality is ensured, energy consumption is reduced, the operation cost is reduced and large-scale continuous processing mode is formed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy-saving type solid continuous fermenting device.    Fan (1)    Heat exchanger (2)    Heater (3)    Storage battery (5)    Charging and discharge circuit (6)    Air inlet (8)    Solar energy solar panel (11)    Fermenting tunnel (12)    Air outlet pipe (13)    Rolling doors (15)
NOVELTY - 1-benzhydryl-3-hydroxy azetidine hydrochloride is prepared by mixing dimethylanilide with epichlorohydrin, adding solvent to obtain reaction solution I, 1st reacting at 0-60 degrees C to obtain reaction solution II, pumping to microreactor with flowrate of 1-200 ml/minute, 2nd reacting at 60-250 degrees C with pressure of 0-2 MPa, separating, and purifying to obtain white crystal.    USE - Preparation of 1-benzhydryl-3-hydroxy azetidine hydrochloride (claimed).    ADVANTAGE - Preparation of 1-benzhydryl-3-hydroxy azetidine hydrochloride is simple, low-cost, and easy to control and has low energy consumption, high yield, product purity, and safety, short reaction time, and strong heat or reaction.
NOVELTY - Hydrocortisone is purified from fermentation broth by adsorbing fermentation broth to fillers to adhere hydrocortisone to filler material in which filler material surface is bonded with silicone functional groups which is alkyl, phenyl, amino, or nitrile group, and eluting adhered hydrocortisone with solvent which is alcohol.    USE - Purification of hydrocortisone from fermentation broth (claimed).    ADVANTAGE - Process is environment-friendly, uses reusable filler, and has better operational security and lower cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow chart of purification of hydrocortisone from fermentation broth. (Drawing includes non-English language text).
NOVELTY - Of the new utility model belongs to one of said domestic garbage for fermentation device, specifically by anti-seepage pit, air layer and fermentation bucket composed of filler, wherein anti-seepage pit bottom is compacted clay layer, compacted clay layer of laying anti-water layer, inner pit is paved with anti-seepage permeable filler layer, inner air filler layer is set with perforation drainage guide air pipe, air filler layer provided with a bottomless cover with fermentation bucket, fermentation bucket bottom buried air filler layer. Wherein, air layer lower part of filler is gravel layer, middle part is geotextile layer, the upper part is, anti-seepage pit outside provided with brick wall and anchoring. This new utility model solves of present technology and bottom product liquid bucket, inner bucket air effect is bad, fermentation reaction for compare the slow problem, providing the user with domestic garbage ferment device investment is low, operation is simple, process efficiency high.
NOVELTY - This utility new type claims a sludge aerobic compost fermentation is a bottom oxygen increasing device, wherein it comprise a has distributing pipeline (1), a gas pipeline (1) is a mounting has a multi-aeration pipe (2), an aeration pipe (2) of the top close, set with multi-side of a small hole at the periphery side wall (3). This utility new type structure is simple and practical, the use of special structure, solves the problem that the sludge aerobic is not uniform, easy to be blocked, difficult maintenance problem of the largest extent up the increasing process of aerobic sludge method, a sludge aerobic reaction, and because of a sufficient oxygen and a sludge treatment process in odour can be eliminate.
NOVELTY - Wherein this utility new type claims a one organic cultivation matrix aerobic fermentation device, the fermentation tank body is hollow cylindrical bottom welding cone composed of the cylinder tube in a fixed mounted ventilation plate, ventilation plate is provided with ventilation hole of uniform distribute, ventilation plate main body is divided into the fermentation 2 part, the upper part is material fermentation room, the lower part a pneuma room, collection room bottom end is mounted a liquid outlet ball valve, material fermentation room is equipped with inner temperature sensor, pneuma room side wall is provided with an air inlet and outlet, gas-guide tube distribute a uniform across the ventilation plate center of a circle, gas-guide tube top end close the bottom opening, an air pipe of vent hole, an air pump through air pipe and pneuma room side wall air inlet a, reflux pump and leachate collection room side wall wherein liquid outlet connected, reflux pump through liquid guide tube and mounting a spray nozzle of the fermenting jar body top part. This utility new type ventilation oxygen supply effect is good, a collection and a reflux of penetrating fluid, a stack for a moisture condition.
NOVELTY - The utility model claims a novel biological fermentation device, comprising a tank body, a spiral conveying motor, a vertical spiral shaft, stirrer, inflow valve, an air inlet, a water steam spraying device, a base, a discharge wherein, reflowing and wherein, for a, spiral conveying pipe, a sieve and pressurizing pump, the utility model uses separate circulation structure form, a finished product and impurity or not fully reaction of substance, impurity or a reaction is not completely through circulation can again use, which avoids the waste and is environment-friendly.
NOVELTY - Removal of hydrogen sulfide from a gas stream involves contacting the gas stream with a mixture of an ionic liquid and a physical absorption solvent or a non-aqueous solvent.    USE - The process is useful for removing hydrogen sulfide from a gas stream (claimed).    ADVANTAGE - The process provides an efficient way of removing hydrogen sulfide from a gas stream by adding ionic liquids to absorption solvents in a variety of weight percents to alleviate the viscosity issue, and achieve results that are better than the use of a solvent without the ionic liquid.
NOVELTY - Gasifier (1) comprises a reaction tube (2), a heating unit (7) associated with the reaction tube for pyrolysis of biomass in the reaction tube, a first continuous conveyor (3) arranged in the reaction tube to transport the biomass to be gasified through the reaction tube, and a return conveying unit (10) provided at the end of the reaction tube to re-transport the remaining biomass to be gasified to start of the reaction tube such that a circuit operation is formed through the reaction tube and the return conveying unit for at least portion of the biomass.    USE - The gasifier is useful for gasifying biomass (claimed).    ADVANTAGE - The gasifier gasifies biomass in complete manner, and controls humidity of the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the gasifier.    Gasifier (1)    Reaction tube (2)    First continuous conveyor (3)    Heating unit (7)    Return conveying unit (10)
NOVELTY - The machine has a traction arm (1) that is hinged at front end of a machine frame. A steering oil cylinder (5) is hingedly connected with inner side of the traction arm. The front and rear universal connecting shafts (2,4) are connected at front and rear sides of a drive shaft (3) attached to the traction arm. A speed reducer is connected to the universal connecting shafts. A connecting rod (7) is connected with a bracket (11) rotatably connected with a walking wheel (9). A lifting cylinder is hinged at upper end of machine frame and connected with the bracket.    USE - Agricultural fertilizer turning machine.    ADVANTAGE - The assorted connection of the agricultural fertilizer turning machine is increased while reducing the purchase cost for the user.    DESCRIPTION OF DRAWING(S) - The drawing shows a Side view of the agricultural fertilizer turning machine.    Traction arm (1)    Front and rear universal connecting shafts (2,4)    Drive shaft (3)    Steering oil cylinder (5)    Connecting rod (7)    Walking wheel (9)    Bracket (11)
NOVELTY - The organic fertilizer production device has a separating unit, a stir fermentation unit, a screen machine feeding unit (140), a screen machine and a granulating machine that are orderly connected in a machine frame. An electric machine screen (152) is fixed at a screen frame (151) and is connected with a driving screen rotating shaft (153). Two ends of the driving screen rotating shaft are provided with a powder material inlet and an impurity outlet and are connected with a screen rotating cylinder (154).    USE - Organic fertilizer production device.    ADVANTAGE - The organic fertilizer production device is simple in structure, low in cost and convenient to use. The production efficiency of the organic fertilizer production device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the screen machine.    Screen machine feeding unit (140)    Screen frame (151)    Electric machine screen (152)    Driving screen rotating shaft (153)    Screen rotating cylinder (154)
NOVELTY - The device comprises a transfer unit (110) having two rotating roller groups and a V-type bracket. The V-type bracket is fixed at upper side of a pedestal. The two rotating roller groups are sleeved in the V-type bracket. A fermentation unit (130) is provided with an electric machine, a driving end transmission roller, a conveying belt and a rear multi-rotating roller group connected in turn with each other. A rotary drum screening machine (150) is provided with a driving screen rotating shaft that is connected with an oil inlet pipe and an oil return pipe of an oil tank.    USE - Organic fertilizer production device.    ADVANTAGE - The organic fertilizer production device is simple in structure, low in cost and convenient to use. The production efficiency of the organic fertilizer production device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic fertilizer production device.    Transfer unit (110)    Separating unit (120)    Fermentation unit (130)    Screen machine feeding unit (140)    Rotary drum screening machine (150)
NOVELTY - This new utility model provide a kind of one liquid flow device, it comprises mixed flow pipe (1), wherein set with sleeve of mixed flow pipe at (1), (2), and sleeve and between flow tube forming with injection space (3) connected with the transfusion mouth of sleeve in (2) (2a), provided with one group injection hole on pipe wall of the mixed-flow pipe (1a), injection hole (1a) by using injection space is mixed-flow pipe and internal communicated, wherein the liquid outlet (1b) of mixed-flow pipe and inside of wall is set with one spiral distribution is composed of mixed-flow fin (4). When using this utility model new process for decontamination or anti-pesticide spray operation, solution is needed in sealed transport pipe in self-mixing, no need to manual mix deploy in advance, which avoids of many problem in current technology is, make solution mixing process is more safe, high efficient, environmental protection.
NOVELTY - Manufacture of bio-mesitylene from biomass involves treating biomass with aqueous solution, and acid catalyst to produce mixture of hemi-cellulosic and cellulosic sugars, fermenting the sugars mixture using bio-organism to fermentation broth containing n-butanol, acetone and ethanol, stripping acetone from fermentation broth, contacting acetone with heat-treated solid supported dehydration-cyclotrimerization catalyst treated with arylsilanes, arylsiloxanes, alkylsilanes, and/or alkylsiloxanes, collecting the bio-mesitylene and purifying bio-mesitylene by fractionation.    USE - Manufacture of bio-mesitylene used as intermediate for manufacturing high-performance polymers, bio-explosive, bio-composite and/or bio-adhesive.    ADVANTAGE - The method enables manufacture of bio-mesitylene with high selectivity and high yield.    DETAILED DESCRIPTION - Manufacture of bio-mesitylene from biomass involves treating a biomass with aqueous solution or extraction medium, and an acid catalyst to produce a mixture of hemi-cellulosic and cellulosic sugars, fermenting the mixture of sugars utilizing at least one bio-organism to a fermentation broth containing n-butanol, acetone, and ethanol, stripping acetone from the fermentation broth by sparging with a gas and condensing to form a liquid containing acetone, contacting acetone with a heat-treated solid supported dehydration-cyclotrimerization catalyst treated with arylsilanes, arylsiloxanes, alkylsilanes, and/or alkylsiloxanes for 1-500 seconds under pressure of 0.02 psig (1 torr to 1000 psig), collecting the bio-mesitylene and purifying bio-mesitylene by fractionation. The supported catalyst is prepared from treated aluminum and/or silicon oxide support, and contains 0.1-5 wt.% of group 5 metal oxide dispersed on aluminum and/or silicon oxide support.
NOVELTY - A plastic filter comprises biofilter, and bio-scrubber.    USE - Plastic filter for biological purification of biogas from sulfur compounds e.g. hydrogen sulfide.
NOVELTY - A town gas is continuously passed through a layer (A) containing a transition metal oxide and a layer (B) of normal activated carbon on the downstream of the layer (A), to remove the mercaptans in town gas by absorption. When removing the mercaptans in town gas by absorption, mercaptans are dimerized with the transition metal oxide using transition metal oxide containing manganese-iron system and chromium-iron system as a transition metal oxide of layer (A), and dimerized mercaptans are removed by absorption with activated carbon layer. Thus, desulfurization is enabled.    USE - Desulfurization of town gas used for gas e.g. liquefied petroleum gas, gasoline and kerosene for hydrogen production used for fuels for industrial application and household application, and manufacturing fuel hydrogen for fuel cells e.g. polymer electrolyte fuel cell and solid oxide fuel cell.    ADVANTAGE - The method enables economical desulfurization of town gas without converting tetrahydrothiophene to thiophene even when mercaptans can be dimerized and tetrahydrothiophene exists in town gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for desulfurization system, which comprises layer (A), and activated carbon layer (B).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining desulfurization and desulfurization system. (Drawing includes non-English language text)
NOVELTY - The apparatus (100) has piping portions (L1-L3), and a separator (2) that is provided to reduce a flow rate of hydrogen gas rather than the piping portion (L1) in which hydrogen gas is introduced into the separator. The hydrogen gas introduced from piping portion (L1) is equipped with an element by which hydrogen gas collides. A drain trap (3) is connected with the separator by piping portion (L2) so a movement of the water from separator turns into natural movement. The piping portion (L3) different from piping portion (L2) is connected with separator/piping portion (L1).    USE - Apparatus for generating hydrogen and oxygen.    ADVANTAGE - The size of the hydrogen and the oxygen generation apparatus is reduced. The leakage of hydrogen gas from the drain trap is suppressed by performing predetermined adjustment with respect to inflow and the drain from the drain trap of the gas from the separator to the drain trap. The load in condenser or adsorption tower is reduced, and product gas is formed efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen and the oxygen generation apparatus. (Drawing includes non-English language text)    Water-electrolysis apparatus (1)    Separator (2)    Drain trap (3)    Hydrogen and oxygen generation apparatus (100)    Piping portions (L1-L3)
NOVELTY - The method involves feeding flue gas or gas mixture into a reactor. The carbon dioxide alone or in admixture with water vapor and/or methane is subjected to pulsed and/or acoustic treatment. The carbon dioxide is then passed through the reactor (1) through thermally activated zones with temperature 800 to 1000 degrees C to the formation of carbon monoxide. The thermally activated zone comprises thermally activated solid carbon-containing fuel. The carbon dioxide passes through thermally activated zone which is a chemical electro-plasma zone.    USE - Method for capturing carbon dioxide and transforming into gaseous fuel by high temperature treatment used in heat and thermal power plant and industrial plant.    ADVANTAGE - The environmental issues resulting from the increase of carbon dioxide in the atmosphere is reduced. The need for looking for right places to store the captured carbon dioxide with other technologies is avoided. The gaseous fuel has less calorific than natural gas used for various heating purposes. The problem of increasing its caloric value is relatively easy to solve with the simultaneous carrying out the partial recovery of carbon dioxide to carbon oxide and the chemical recovery of hydrogen from water vapor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for implementing the method for capturing carbon dioxide and transforming into gaseous fuel by high temperature treatment.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for implementing the method for capturing carbon dioxide and transforming into gaseous fuel by high temperature treatment.    Reactor (1)    High voltage system (2)    Needle cathode (3)    Inlet pipe (4)    Rotating plate (5)
NOVELTY - An isolated cellulase polypeptide comprising an amino acid sequence about 90% identical to any of fully defined 451 amino acids (SEQ ID NO: 58-281) given in the specification, is new.    USE - The isolated polypeptide and recombinant microorganism are useful for cellulose processing; and for producing cellulosic ethanol (all claimed) for biofuels.    ADVANTAGE - Highly stable and active cellulases are provided that can withstand harsh conditions in ethanol production and processing, such as high temperature, low pH, and/or substrate pretreatment.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a nucleic acid encoding the polypeptide;    (2) a recombinant microorganism, where the microorganism expresses the nucleic acid, or where the microorganism expresses a nucleic acid encoding the polypeptide above;    (3) a method for producing cellulosic ethanol comprising adding the isolated polypeptide or the recombinant microorganism to a source material of cellulose for cellulose processing; and    (4) a method for cellulose processing comprising adding the polypeptide or the recombinant microorganism to a source material of cellulose.
NOVELTY - A composition comprises 1,2,3,3,3-pentafluoropropene and compound(s) chosen from 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 1,2,3,3-tetrafluoropropene, 3,3,3-trifluoropropylene, difluoromethane, pentafluoroethane, 1,1,1,2-tetrafluoroethane, ethyl fluoride, 1,1,1,2,3,3-hexafluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,3,3-pentafluoropropane, 1,1,1,3,3-pentafluorobutane, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, bis(trifluoromethyl)sulfide, carbon dioxide, ammonia, and trifluoroiodomethane.    USE - Composition is used as heat transfer fluids, foam blowing agents, aerosol propellants, and fire suppression and fire extinguishing agents in refrigeration, air-conditioning, and heat pump systems.    DETAILED DESCRIPTION - A composition comprises 1,2,3,3,3-pentafluoropropene, and compound(s) chosen from 1,3,3,3-tetrafluoropropene, 2,3,3,3-tetrafluoropropene, 1,2,3,3-tetrafluoropropene, 3,3,3-trifluoropropylene, difluoromethane, pentafluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,1,2-tetrafluoroethane, 1,1,1-trifluoroethane, 1,1-difluoroethane, ethyl fluoride, 1,1,1,2,3,3,3-heptafluoropropane, 1,1,1,2,3,3-hexafluoropropane, 1,1,1,3,3,3-hexafluoropropane, 1,1,1,3,3-pentafluoropropane, 1,1,1,3,3-pentafluorobutane, propane, n-butane, isobutane, 2-methylbutane, n-pentane, cyclopentane, dimethylether, bis(trifluoromethyl)sulfide, carbon dioxide, ammonia, and trifluoroiodomethane.
NOVELTY - An apparatus comprises cylindrical drum (20) with mesh surface (22) for rotating when partially disposed in water in which material to be extracted from body of water adheres to mesh surface, actuator for rotating drum, catch trough within cylindrical drum extending over a length of cylinder between 1st and 2nd ends of cylinder, and source of pressurized water outside of cylindrical drum for directing stream of water through mesh surface and into catch trough in which stream of water removes material from mesh surface and deposits material into catch trough.    USE - An apparatus for extracting material from a body of water (claimed). Can also be used for removal of contaminants, e.g. oil, trash, etc., and harvesting of materials, e.g. specific algae, for subsequent bio-fuel processing.    ADVANTAGE - Increasing the spacing of the mesh surface results in increased collection of strand material. The drum is physically coupled to the actuator, which may reduce or prevent slippage of the drum, during heavy loading.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for extraction of material from a body of water which involves rotating partially submerged drum with a mesh surface in a body of water having a material to be extracted from the body of water, applying pressurized stream of water to outside surface of drum on a portion of the drum above the water line, and catching the stream of water and material removed from the mesh surface by the stream of water in a receptacle disposed within the drum in which the receptacle is above a water line of the body of water.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of a collecting drum.    Collecting drum (20)    Mesh surface (22)
NOVELTY - Dried biomass production involves transporting conveyor belt continuously through wet wastes containing mostly crushed and sieved organic waste. The obtained organic waste is poured into inlet located at one end of a rotary cylinder dryer provided inside ribs, where the drier is heated at 250-300 degrees C. The waste drying pre-treatment is performed for 20-30 minutes. The predried waste is transferred at room temperature, and then cooled-down for 20-30 minutes.    USE - Method for producing dried biomass by treating organic wastes.    ADVANTAGE - The method produces dried biomass continuously by a two-step organic waste drying process, and provides utilization of wet organic waste in household waste with dry or almost dry organic waste such as paper, cardboard, sticks or dried leaves.    DETAILED DESCRIPTION - Dried biomass production involves transporting conveyor belt continuously through wet wastes containing mostly crushed and sieved organic waste. The obtained organic waste is poured into inlet located at one end of a rotary cylinder dryer provided inside ribs, where the drier is heated at 250-300 degrees C. The waste drying pre-treatment is performed for 20-30 minutes. The predried waste is transferred at room temperature, and then cooled-down for 20-30 minutes. The predried waste is moved through another dryer residence, where the dried biomass is transported from the previous storage silo.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic flowchart of the dried biomass production method.    Conveyor (1)    Ripper bag (2)    Heat-producing furnace (3)    Dryer (4)    Power extractor (5)
NOVELTY - Biodiesel production involves charging reactor with a fat and alcohol in a weight ratio of 1:1-20:1, and then adding 1.0-20.0% enzyme to perform enzymatic reaction. The formed mass is deposited in a reactor, where the enzyme is separated to obtain biodiesel. The obtained biodiesel is separated and purified.    USE - Method for producing biodiesel by using ultrasound in a batch or continuous mode.    ADVANTAGE - The method produces biodiesel in a simple, cost-effective and eco-friendly manner without leaving residues in final products.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an equipment for enzymatic production of biodiesel.    Reactor (10)    Pressurized fluid reservoir (20)    Sample jars (30)    Pump or compressor (31)    Thermostatic baths units (401,402,403)
NOVELTY - The hybrid biofuel is obtained from biomass impregnation with liquid biofuel.    USE - Hybrid biofuel for use in wood stoves, fireplaces, steel industry or ceramic industry (claimed).    ADVANTAGE - The hybrid biofuel can be provided in grains or powder form, and enables to recycle waste vegetable oil and biodiesel production process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for compressing hybrid biofuel into granulate state, which involves compacting hybrid biofuel within brackets obtained from biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the hybrid biofuel compression.    Hybrid biofuel (1)    Holder (2)    Manual instrument (3)
NOVELTY - Recovering phosphorus products from organic waste material, comprises mixing biological waste materials with a bulk material (12) from an alkaline material or bulk material mixed with alkaline material, placing produced mixture in a furnace, converting the total carbon- and hydrogen-containing compounds of the waste materials to synthesis gas under reductive conditions, withdrawing the synthesis gas at the upper end of the furnace, cooling the bulk material with oxygen-containing gas, separating into at least two fractions, and removing fine-grained fraction as phosphorus recyclable material.    USE - The method is useful for recovering phosphorus products from organic waste material.    DETAILED DESCRIPTION - Recovering phosphorus products from organic waste material, comprises mixing biological waste materials with a bulk material (12) from an alkaline material or bulk material mixed with alkaline material, placing produced mixture in a furnace, converting the total carbon- and hydrogen-containing compounds of the waste materials to synthesis gas under reductive conditions, withdrawing the synthesis gas at the upper end of the furnace, cooling the bulk material with oxygen-containing gas to a temperature of less than 500 degrees C at the lower end of the furnace, separating into at least two fractions, and removing the fine-grained fraction as phosphorus recyclable material.    DESCRIPTION OF DRAWING(S) - The figure shows schematic representation of a plant for carrying out the above mentioned (Drawing includes non-English language text).    Vertical shaft furnace (10)    Bulk material (12)    Mixing device (14)    Sewage sludge (16)    Metering device (18)
NOVELTY - The method involves cooling synthesis gas in a contactless multi-stage heat exchanger, and materially utilizing the synthesis gas according to exit from the heat exchanger. A working medium of a gas turbine is heated in the heat exchanger. The working medium is supplied to a waste heat boiler after exit from the gas turbine, where the waste heat boiler delivers residual heat utilized for vapor generation such that the vapor is utilized for generation of the synthesis gas. The working medium is utilized during an open gas turbine process.    USE - Method for energetically producing optimized synthesis gas to control charcoal and/or biomass in a chemical industry.    ADVANTAGE - The method enables supplying the working medium to the waste heat boiler that delivers the residual heat, which is utilized for vapor generation such that the vapor is utilized for generation of the synthesis gas, thus improving overall energy efficiency in the process control of coal/biomass material.    DETAILED DESCRIPTION - The working medium is selected from air, water vapor, argon and nitrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram illustrating a process for recovering heat and converting to electric power.    Charcoal or biomass (01)    Combustible raw gas (12)    Turbine exhaust air (45)    Pressurized air (124)    Saturated steam (501)
NOVELTY - The anaerobic-treatment installation (100) has an acid generation tank (2) that transduces the fat and oil containing waste water. A methane fermentation tank (3) transduces and methane-ferments the acid fermentation liquid. A fats-and-oils collection unit collects the fats and oils oil/water-separated by the acid generation tank. A saponification processing tank (4) performs saponification process of the fats and oils collected by fats-and-oils collection unit. A first line supplies saponification process liquid which arose in the saponification processing tank to acid generation tank.    USE - Anaerobic-treatment installation.    ADVANTAGE - The adherence of fats and oils to the acid generation tank and the methane fermentation tank can be prevented. The collected amount of biogas which arises in the methane fermentation tank can be raised, while preventing the accumulation of scum in the methane fermentation tank.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the anaerobic-treatment installation. (Drawing includes non-English language text)    Acid generation tank (2)    Methane fermentation tank (3)    Anaerobic-treatment installation (4)    Gasholder (5)    Anaerobic-treatment installation (100)
NOVELTY - The anaerobic-treatment installation (100) has an emulsion decomposition tank (2) that transduces the fat and oil containing waste water, and disassembles the emulsion in fat and oil containing waste water. An acid generation tank (3) accommodates an acid production microbe, and introduces and performs the souring of the supernatant liquid. A methane fermentation tank (4) introduces and methane-ferments the acid fermentation liquid which arose in the acid generation tank.    USE - Anaerobic-treatment installation for performing anaerobic treatment of organic waste water containing fats and oils.    ADVANTAGE - The adherence of fats and oils to the methane fermentation tank and the acid generation tank can be prevented. Since the saponification process liquid is supplied to the methane fermentation tank through acid generation tank, the collected amount of the biogas which arises in the methane fermentation tank can be raised. Since a saponification process is carried out by the saponification processing tank, the decomposition ratio of fats and oils can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anaerobic-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the anaerobic-treatment installation. (Drawing includes non-English language text)    Natural water tank (1)    Emulsion decomposition tank (2)    Acid generation tank (3)    Methane fermentation tank (4)    Anaerobic-treatment installation (100)
NOVELTY - A composite three-layer network cloth comprises surface layer (1), bottom layer (3) and support layer (2).    USE - Composite three-layer network cloth used for footwear and luggage (all claimed) for promoting blood circulation, activating human immune cells, preventing human body aging and premature senility, and killing harmful body germ.    ADVANTAGE - The cloth has strong biological wave function, excellent active interface and good deodorizing performance, does not damage human body, removes peculiar smell, maintains good living space, adjusting air quality surrounding environment, saves detergent dosage, and is helpful for purifying environment and environment-friendly.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of composite three-layer network cloth.    Surface layer (1)    Support layer (2)    Bottom layer (3)
NOVELTY - Preparation of pine mushroom culture matrix comprises peeling pine, slitting into sections, drying, crushing into 2-5 mm diameter, soaking in water at 1:1.5-5 mass ratio; mixing 25-35 pts. wt. pine bark granule, 10-18 pts. wt. wooden meal, 15-20 pts. wt. corn core, 10-15 pts. wt. bran, 1-2 pts. wt. gypsum and 1-2 pts. wt. lime; and filling material into culture bag, sterilizing and high pressure steaming for 3-5 hours.    USE - Method for preparing pine mushroom culture matrix (claimed).    ADVANTAGE - The method reduces mushroom production cost, reduces environment pollution, and increases yield.
NOVELTY - Leaf solution fertilizer comprises 30-40 pts. wt. composite amino acid (amino acid of soybean fermentation extracting powder), 8-15 pts. wt. calcium nitrate, 22-30 pts. wt. magnesium sulfate, 5-10 pts. wt. borax decahydrate, 2-8 pts. wt. zinc sulfate heptahydrate, 1-4 pts. wt. manganese sulfate, 1-3 pts. wt. ammonium citrate, and 3-8 pts. wt. additive.    USE - Leaf solution fertilizer for apple (claimed).    ADVANTAGE - The fertilizer combines the amino acid as chelating agent and chelated trace elements (chelated trace elements of plant cell walls which cannot easily be fixed), is easily accessible to location of plants, does not pollute the water quality and the environment, and has natural shape and appropriate stability. The amino acid can provide nitrogen for plants and is long-acting. The amino acid can be used as ligand, in the case without the need for photosynthesis directly involved in protein synthesis of the body, and compared with other chelating agents, there is more significant crop yield. The plant root, growth, reproduction and enlargement, and other growth stages are significantly promoted, hence promoting pollination and improving crop (especially fruit) product quality.
NOVELTY - Wheat fertilizer comprises 10-12 pts. wt. nitrogenous fertilizer, 8-10 pts. wt. phosphate fertilizer, 12-14 pts. wt. potash fertilizer, 20-30 pts. wt. protein mud, 10-12 pts. wt. furfural slag, 7-9 pts. wt. amino acid, 3-5 pts. wt. humic acid, 0.6-0.8 pts. wt. Effective Microorganism bacilli, 20-30 pts. wt. cordate houttuynia, 30-40 pts. wt. common andrographis herb, 80-100 pts. wt. chicken manure, and 8-10 pts. wt. fungus powder.    USE - Wheat fertilizer.    ADVANTAGE - The fertilizer has simple preparation, adds insecticidal and fungicidal component, reduces soil plant diseases and insect pests, reduces fertilizer loss, and is safe.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of wheat fertilizer comprising placing all the materials in a crusher, crushing and fermenting in a close jar; pre-heating at 75 degrees C in a screw mixer, holding at this temperature; adding reciprocating single-screw pin, opening screw mixer and maintaining mold head pressure at 1.0-1.2 MPa; and injection forming the granular fertilizer to obtain wheat fertilizer in screw die.
NOVELTY - Fructus ligustri lucidi fertilizer comprises 80-100 pts. wt. chicken manure, 50-60 pts. wt. herba houttuyniae, 30-50 pts. wt. bauxite, 40-50 pts. wt. mica powder, 20-30 pts. wt. banana peel, 15-17 pts. wt. chicken skin, 20-30 pts. wt. Phellodendron, 40-50 pts. wt. medical stone, 20-30 pts. wt. pomegranate rind, 40-50 pts. wt. kaolin, 15-17 pts. wt. wintergreen oil, and 150-170 pts. wt. water.    USE - Fructus ligustri lucidi fertilizer.    ADVANTAGE - The fertilizer contains rich nutrition elements, has adsorptivity, and can purify pollutant in soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer comprising taking chicken manure, herba houttuyniae, bauxite, mica powder, banana peel, chicken skin, Phellodendron, medical stone, pomegranate rind, kaolin, and wintergreen oil into a crusher, and crushing; adding water, fully stirring, and seal fermenting for 6-8 days; standing for 10 hours, and pelletizing.
NOVELTY - Preparation of a catechin gallate-containing compound (I) or (II) comprises dissolving catechin in acetonitrile, reacting with an acid chloride and tertiary amine, stirring, and processing.    USE - Method for the preparation of a catechin gallate-containing compound (I) or (II) (claimed).    ADVANTAGE - The method is simple, avoids toxic and irritating organic solvents, and is environment-friendly.    DETAILED DESCRIPTION - Preparation of a catechin gallate-containing compound of formula (I) or (II) comprises dissolving catechin in acetonitrile, reacting with an acid chloride and tertiary amine, stirring, and processing.    R=alkyl.
NOVELTY - Antibiotic residue is enzymatically treated by mixing enzyme composition comprising xylanase, mannanase, protease, alpha -amylase, pectinase, beta -glucanase, fatty alcohol polyoxyethylene ether, polyacrylamide, and polymerization Aluminum chloride in water with volume ratio of 1:50 to obtain enzyme composition solution, uniformly spraying on 1-5 L solution/ton antibiotic bagasse, uniformly stirring mechanically for 0.5-1 hour, transferring into hopper, reacting at 30-50 degrees C under natural pH for 1-4 hours, subjecting to solid-liquid separation, and applying supernatant in methane fermentation.    USE - Enzymatic treatment of antibiotic residue for solid organic fertilizer (claimed) and biogas fermentation.    ADVANTAGE - Process is environment-friendly, avoids discharge of waste to rivers and farmlands, recycles waste, and achieves comprehensive environmental management.    DETAILED DESCRIPTION - Antibiotic residue is enzymatically treated by mixing enzyme composition comprising 10-30 wt.% xylanase, 5-10 wt.% mannanase, 5-20 wt.% protease, 20-30 wt.% alpha -amylase, 5-10 wt.% pectinase, 5-10 wt.% beta -glucanase, 1-5 wt.% fatty alcohol polyoxyethylene ether, 3-8 wt.% polyacrylamide, and 2-10 wt.% polymerization Aluminum chloride in water with volume ratio of 1:50 to obtain enzyme composition solution, uniformly spraying on 1-5 L solution/ton antibiotic bagasse, uniformly stirring mechanically for 0.5-1 hour, transferring into hopper, reacting at 30-50 degrees C under natural pH for 1-4 hours, subjecting to solid-liquid separation, and applying supernatant in methane fermentation.
NOVELTY - The apparatus has a separation bioreactor separating solid from liquid to supply sludge to a sludge oxidation bath. The sludge oxidation bath is disassembled to dismantle sludge under an aerobic condition through action of a specific microorganism. A microorganism contact tub ferments sludge by contacting with the specific microorganism. A microorganism mixture tank mixes the microorganism supplied from multiple microorganism supply tanks. A sewage sludge processing unit includes specific microorganism for processing.    USE - Apparatus for treating sludge using mixed micro-organisms.    ADVANTAGE - The apparatus improves sludge disassembly efficiency and efficiently collecting sludge during treatment process and filtering through the bio-filter to effectively remove the odor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a sewage sludge processing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for treating sludge using mixed micro-organisms. '(Drawing includes non-English language text)'
NOVELTY - Preparing mushroom cultivation substrate using elm bark, comprises (i) peeling elm root bark, cutting to sections, drying, crushing by adding into a crushing machine, and mixing elm bark particles with water in mass ratio of 1:1-1.5, and soaking elm bark particles; and (ii) mixing 20-30 pts. wt. elm bark particles, 15-20 pts. wt. wooden meal, 15-20 pts. wt. corn stalk, 10-15 pts. wt. wheat bran, 1-2 pts. wt. gypsum and 1-2 pts. wt. lime, and simultaneously adding water in an amount of 1.3-1.5 times; and (iii) filling culture material to a culture bag, and sterilizing under high pressure steam.    USE - The method is useful for preparing mushroom cultivation substrate using elm bark (claimed).    ADVANTAGE - The method replaces cotton seed hulls with elm; is economical, and environmental friendly; completely utilizes active components of cellulose and lignin in elm bark; and increase the yield of mushrooms by producing mycelium.    DETAILED DESCRIPTION - Preparing mushroom cultivation substrate using elm bark, comprises (i) peeling elm root bark, and cutting into sections, drying, crushing by adding into a crushing machine into a diameter of 2-5 mm, and mixing elm bark particles by adding water in a mass ratio of 1:1-1.5, and soaking elm bark particles under moisture condition; and (ii) mixing 20-30 pts. wt. elm bark particles, 15-20 pts. wt. wooden meal, 15-20 pts. wt. corn stalk, 10-15 pts. wt. wheat bran, 1-2 pts. wt. gypsum and 1-2 pts. wt. lime, and simultaneously adding water in an amount of 1.3-1.5 times; and (iii) filling the culture material prepared into a culture bag, and sterilizing by using high pressure steam for 3-5 hours, to obtain the product.
NOVELTY - A sludge drying apparatus (100) comprises heat exchanger (41) which heats dry gas and supplies dry gas to drying apparatus (10) after heating, temperature detection unit (51) to detect temperature of exit (11) of drying apparatus, and control unit (52) which is controlled to increase heating temperature of dry gas of heat exchanger and to increase supply amount of dry gas to drying apparatus when detected temperature is below predetermined threshold value. The sludge drying apparatus generates solid fuel by drying granulated sludge made of dried sludge and dewatered sludge using dry gas.    USE - A sludge drying apparatus for production of solid fuel (claimed).    ADVANTAGE - The sludge drying apparatus can appropriately control moisture content of solid fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the sludge drying apparatus. (Drawing includes non-English language text).    Drying apparatus (10)    Exit (11)    Heat exchanger (41)    Temperature detection unit (51)    Control unit (52)    Sludge drying apparatus (100)
NOVELTY - A soil conditioner is prepared which involves mixing liquid-containing waste with a plaster to form a mixture.    USE - The process is useful for preparing soil conditioner (claimed) used for preparing slow-release fertilizer.    ADVANTAGE - Simple process for preparing soil conditioners is provided, in which various kinds of wet waste can be recycled in whole in a short period of time and processed into a soil conditioner, preferably a solid soil conditioner (coherent piece of solid soil conditioner). The soil conditioner prepared from the process may be further processed into a slow-release fertilizer which has further advantages such as slow-release of nutrients thus improving nutrient use efficiency (NUE) and reducing nutrient leaching and run-off. The process is able to prepare soil conditioners from nutrient-rich waste streams and sludge using a fast process while mitigating emission of foul odors. In particular, the process is a simple and low-cost process, as well as environment-friendly since the process consumes low-energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a soil conditioner prepared from the process.
NOVELTY - The gasifier has a thermal decomposition furnace (9) for generating pyrolysis gas (19, 19') and char (20) by supplying and thermally decomposing hydrocarbon resources solid fuels (11) to a fluidized-bed (18, 30). A thermal decomposition apparatus (5) is provided with a tar absorption furnace (10). Two tar absorbers (25, 25') absorb tar of the pyrolysis gas. A char gasifier (27) supplies char residue (20') to a char residue combustion furnace (7) with flow medium (15). A coke gasifier (28) supplies coke, which is not gasified to an absorber regenerative furnace (8).    USE - Gasifier for gasifying hydrocarbon resources solid fuels by circulating fluidized bed. Uses include but are not limited to coal, biomass, rubbish, and sewage sludge.    ADVANTAGE - The gasifier suppresses diffusion of heat, improves thermal efficiency and increases amount of extraction of gasifying gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a circulating fluidized bed gasifier.'(Drawing includes non-English language text)'    Thermal decomposition apparatus (5)    Char residue combustion furnace (7)    Absorber regenerative furnace (8)    Thermal decomposition furnace (9)    Tar absorption furnace (10)    Hydrocarbon resources solid fuels (11)    Flow medium (15)    Fluidized-bed (18, 30)    Prolysis gas (19, 19')    Char (20)    Char residue (20')    Tar absorbers (25, 25')    Char gasifier (27)    Coke gasifier (28)
NOVELTY - Enzyme composition comprises lipid-functionalized graphene or lipid-functionalized fullerenes, and at least one enzyme entrapped by, but not linked to, the lipid-functionalized graphene or the lipid-functionalized fullerenes, where the entrapped enzyme in the composition has an enhanced activity as compared to a control enzyme.    USE - The enzyme composition is useful for preparing e.g. detergents, pharmaceuticals, and cosmetic, and producing biofuel.    ADVANTAGE - The enzyme composition is cost-effective, and has excellent thermophilic and psychrophilic stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for entrapping an enzyme; and    (2) method for treating a substrate.
NOVELTY - Biomass feedstock comprising cellulose and water, is contacted with hydrogen in presence of catalyst capable of activating molecular hydrogen, to form hydrocatalytically treated mixture. Biomass material is partially oxidized to produce gas mixture comprising carbon monoxide and hydrogen. The biomass material does not include the hydrocatalytically treated mixture. The gas mixture is supplied to water gas shift reaction zone external to where the biomass feedstock is contacted with hydrogen, to generate hydrogen and carbon dioxide.    USE - Supplying hydrogen to hydrocatalytic reaction (claimed).    ADVANTAGE - The method enables efficient supply of hydrogen to hydrocatalytic reaction.
NOVELTY - Preparing tablet involves utilizing 291 g rhubarb, 103 g Hemerocallis, 92 g groundsel, 92 g peach fruit, 92 g rhizoma smilacis glabrae, 62 g wild rose, 62 g swertiamarine, 62 g apricot leaf and 62 g Kadsura longipedunculata. Wild rose, apricot leaf and Kadsura longipedunculata are crushed to obtain powder that extracted with ethanol using carbon dioxide supercritical extractor at pressure of 20-30 megapascals and temperature of 30-50 degrees C for 130-170 minutes. The carbon dioxide flow rate is 1-3 ml/g of crude drug. Remaining raw materials are extracted using microwave.    USE - Method for preparing tablet used for restraining mouse myeloma cell (P3X63Ag8) proliferation (claimed).    DETAILED DESCRIPTION - Preparing tablet involves utilizing 291 g rhubarb, 103 g Hemerocallis, 92 g groundsel, 92 g peach fruit, 92 g rhizoma smilacis glabrae, 62 g wild rose, 62 g swertiamarine, 62 g apricot leaf and 62 g Kadsura longipedunculata. Wild rose, apricot leaf and Kadsura longipedunculata are crushed to obtain powder that extracted with ethanol (4-6 vol.%) using carbon dioxide supercritical extractor at pressure of 20-30 megapascals and temperature of 30-50 degrees C for 130-170 minutes. The carbon dioxide flow rate is 1-3 ml/g of crude drug. Remaining traditional Chinese medicinal raw materials are crushed to obtain powder that is extracted with 60 % ethanol using microwave at 600-800 Watt for 2 times, each time for 5-10 minutes to obtain extract. The obtained extracts are combined and concentrated. The concentrate is purified using D101 macroporous resin column with 60% ethanol to obtain eluate. Ethanol is recovered from eluate at reduced pressure. The obtained eluate is concentrated and dried to obtain microwave extract. The microwave extract and supercritical extract are mixed to obtain mixture that is further mixed with starch and 60% ethanol to obtain pellet. The pellet is dried and tableted to obtain 200 pieces of tablet, each tablet of 0.5g.
NOVELTY - Preparing potassium dihydrogen phosphate fertilizer involves mixing phosphoric acid and carboxamide in mol ratio of 1.2-1.5:1 at 80-160 degrees C for 4-5 hours and then stirred at speed of 6 degrees C per minute by using a container to obtain intermediate product. Intermediate product is mixed with alkaline potassium and crystallized by using a crystallizer and then nitrogen (20-25%), phosphorus (3-6%) and potassium (10-14%) are mixed to obtain fermented filter cake of potassium dihydrogen phosphate product and filter liquid. Formaldehyde solution is mixed with the filter in mole ratio of (0.3-0.5):1.    USE - Method for preparing potassium dihydrogen phosphate fertilizer used for Chrysanthemum, and used in controlled-release fertilizer (all claimed).    ADVANTAGE - The method enables to prepare fertilizer that increases yield of Chrysanthemum, and has improved absorption.    DETAILED DESCRIPTION - Preparing potassium dihydrogen phosphate fertilizer involves mixing phosphoric acid and carboxamide in mol ratio of 1.2-1.5:1 at 80-160 degrees C for 4-5 hours and then stirred at speed of 6 degrees C per minute by using a container to obtain intermediate product. Intermediate product is mixed with alkaline potassium and crystallized by using a crystallizer and then nitrogen (20-25%), phosphorus (3-6%) and potassium (10-14%) are mixed to obtain fermented filter cake of potassium dihydrogen phosphate product and filter liquid. Formaldehyde solution is mixed with the filter in mole ratio of (0.3-0.5):1, and then potassium hydroxide solution, phosphoric acid solution and sulfuric acid solution are added and heated at 55-75 degrees C for 1-1.5 hours to maintain pH 3.5-4.0 and obtain a product. The product is granulated and dried to obtain fertilizer.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carboxamide in a reaction kettle in mol ratio of 1.2-1.4:1 at 120-150 degrees C with speed of 4 degrees C per minute for 130-150 minutes to obtain a mixture. The mixture is cooled to 30-40 degrees C and centrifuged to obtain intermediate product. Intermediate product is mixed with alkaline sodium in mol ratio of 1:0.9-1 and stirred at 60-80 degrees C with speed of 220-260 revolutions per minute for 50-70 minutes to maintain pH value to 8-9 to obtain a product. The product is cooled and crystallized by using a crystallizer to obtain filter liquid.    USE - Method for preparing fertilizer used for growing cotton (claimed).    ADVANTAGE - The method enables to prepare fertilizer in a cost-effective and eco-friendly manner, and does not discharge waste liquid during production process.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and urea in a reaction kettle in mol ratio of 1.2-1.4:1 at 120-150 degrees C with speed of 4 degrees C per minute for 130-150 minutes to obtain a mixture. The mixture is cooled to 30-40 degrees C and centrifuged to obtain intermediate product. Intermediate product is mixed with alkaline sodium in mol ratio of 1:0.9-1 and stirred at 60-80 degrees C with speed of 220-260 revolutions per minute for 50-70 minutes to maintain pH value to 8-9 to obtain a product. The product is cooled and crystallized by using a crystallizer to obtain filter liquid, and then nitrogen (9-11%) and phosphorus (2.8-3.5%) are mixed to obtain a filter cake. Ammonium dihydrogen phosphate is mixed with the filter cake and then alkaline sodium salt and trace elements are added to obtain a product. The product is heated in a drier at 26-32 degrees C with speed of 5 degrees C per minute for 40-60 minutes to obtain suspension liquid.
NOVELTY - Processing cow dung involves collecting cow dung, crushing cow dung and transporting into anaerobic reactor. The cow dung is fermented in an anaerobic reactor to covert nitrogen-containing organic matter into ammonia and methane. The cow dung is treated in aerobic reactor to obtain solid waste. The solid waste is sterilized to obtain the product.    USE - Method for processing cow dung used as fertilizer (claimed).    ADVANTAGE - The method enables to process cow dung in a simple and cost-effective manner.
NOVELTY - Organic fertilizer comprises 50-60 pts. wt. dairy manure, 30-40 pts. wt. sheep manure, 40-60 pts. wt. pig manure, 10-12 pts. wt. cottonseed, 20-30 pts. wt. ryegrass, 5-7 pts. wt. water, 1-3 pts. wt. yeast, 2-4 pts. wt. sodium humate, 8-10 pts. wt. oyster shell powder, 20-30 pts. wt. plant ash, 2-4 pts. wt. charcoal powder, 1-3 pts. wt. nitrogen, 1-3 pts. wt. phosphorus and 5-7 pts. wt. potassium.    USE - Organic fertilizer used for promoting growth of apple (claimed).    ADVANTAGE - The organic fertilizer relieves soil compaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) mixing dairy manure, sheep manure, pig manure, cottonseed, ryegrass, water, yeast, sodium humate, oyster shell powder, plant ash, charcoal powder, nitrogen, phosphorus and potassium to obtain mixture; and    (B) heating mixture and then granulating using granulation machine to obtain the product.
NOVELTY - Fertilizer comprises 8-15 pts. wt. plant ash, 3-7 pts. wt. composite microorganism inoculants, 4-6 pts. wt. nitrate, 8-14 pts. wt. zinc sulfate heptahydrate, 5-9 pts. wt. organic acid, 4-11 pts. wt. monopotassium phosphate, 3-5 pts. wt. tea seed shell charcoal, 5-9 pts. wt. calcium superphosphate, 3-8 pts. wt. ammonium bicarbonate, 2-5 pts. wt. amino acid, 1-4 pts. wt. potassium sulfate, 5-7 pts. wt. Bacillus subtilis and 6-10 pts. wt. bactericide.    USE - Fertilizer.    ADVANTAGE - The fertilizer has bactericidal effect, and improves soil and prevents soil compaction.
NOVELTY - The facility (100) has aeration tanks (110,120,130,140) that are installed at the lower portion of a convection derived type air jet apparatus (150). A microorganism activity frame (160) is set up in the gap in which the filter media activates the microorganism in the inside of each tank. The acid group branch of each aeration tank connects in outside of each tank to a diffuser in which an air pump is equipped. A bored air injector is set up in the upper side in the lower portion of each aeration tank and in which an air jet hole is provided at constant interval.    USE - Sewage disposal facility installed at non-discharge cyclization field room, for purifying wastewater in bathroom using microorganism.    ADVANTAGE - The decomposition of waste water is performed efficiently. The microorganism is activated effectively and the resolving power is improved. Hence the purification ability of the waste water by the microorganism is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the non-discharge cyclization field room.    Sewage disposal facility (100)    Flow control bath (101)    Aeration tanks (110,120,130,140)    Convection derived type air jet apparatus (150)    Microorganism activity frame (160)
NOVELTY - The apparatus has a screw conveyor (24) fixed with an upper end portion furnace for transferring organic waste of a cone shaped lower part (16) of a fermenter along upper direction. Multiple air supply ports (19) inject external air into the fermenter. A vent (18) is formed in a lower end portion of the fermenter for ejecting the organic waste of an agitation circle cask (22) to an outer side. A lower end portion of a stirrer is extended to the lower part of the fermenter to close the vent. The screw conveyor is installed in an inner side of the agitation circle cask.    USE - Fermenting organic waste decrement apparatus.    ADVANTAGE - The stirrer is installed in the fermenter along top and bottom directions so as to smoothly mix the organic waste in the fermenter along upper and lower directions, thus improving mixing process efficiency. The screw conveyor is installed in the inner side of the agitation circle cask and a screw blade in streamlined form so as to reduce load received during agitation process, prevent the apparatus from being damaged due to abrasion and improve durability of the apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a fermenting organic waste decrement apparatus.    Fermenter lower part (16)    Vent (18)    Air supply ports (19)    Agitation circle cask (22)    Screw conveyor (24)
NOVELTY - Decontamination of radioactive contaminated soil involves grinding the radioactive contaminated soil by adding aqueous solution of microorganisms group that stimulates fermentation-decomposition process to obtain a product. Waste material obtained from cutting-down of trees containing bark ( greater than or equal to 50%) and organic fertilizer are mixed with the product and pulverized to obtain granules. The granules are packed into water permeable and air permeable bag formed by using scarce material and then base material is mixed and stirred to obtain a mixed product.    USE - Method for decontaminating radioactive contaminated soil (claimed).    ADVANTAGE - The method is recycled, and decontaminates cesium radioactive metal contaminated soil in limited ventilation area.    DETAILED DESCRIPTION - Decontamination of radioactive contaminated soil involves grinding the radioactive contaminated soil by adding aqueous solution of microorganisms group that stimulates fermentation-decomposition process to obtain a product. Waste matSerial obtained from cutting-down of trees containing bark ( greater than or equal to 50%) and organic fertilizer are mixed with the product and pulverized to obtain granules. The granules are packed into water permeable and air permeable bag formed by using scarce material and then base material is mixed and stirred to obtain a mixed product. Fermentation promoter is added in the mixed product and then carrying out fermentation.
NOVELTY - The apparatus comprises a disposal of food partition element (1) that is equipped in a main body (2). A mixer (3) is provided for stirring the food waste at multiple disposal of food partition elements. A motor (4) is equipped in a lower side of the main body. An opening or closing plate (5,5a,5b) is rotatably arranged in the upper portion of the main body. The opening or closing plate opens and closes a food insert hole bruise (5aa). A switching board is installed in the upper portion of the main body. A locking apparatus (6) is provided for locking the switching board.    USE - Apparatus for disposing food waste.    ADVANTAGE - The apparatus comprises a disposal of food partition element that is equipped in a main body, and thus ensures easily ejecting the food waste. The maintenance of the food waste is convenient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for controlling food waste disposing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic cross-sectional view of a food waste disposing apparatus.    Disposal of food partition element (1)    Main body (2)    Mixer (3)    Motor (4)    Opening or closing plates (5,5a,5b)    Food insert hole bruise (5aa)    Locking apparatus (6)
NOVELTY - Method for producing ethanol, involves culturing transformed yeast having enzyme on its surface layer, in a culture medium comprising lignocellulosic-based biomass, where the enzyme hydrolyzes the lignocellulosic-based biomass.    USE - The method is useful for producing ethanol (claimed).    ADVANTAGE - The method restrains addition of cellulose, does not require addition of chemical substance, and suppresses production of waste material.
NOVELTY - Production of hydrocarbon product involves providing 4C hydrocarbon stream (C4) comprising 80% or more branched and unbranched hydrocarbons each comprising four carbon atoms, and recovering n-4C sub-stream (n-C4) comprising 80% or more unbranched hydrocarbons comprising four carbon atoms and an iso-4C sub-stream (i-C4) comprising predominantly branched hydrocarbons comprising four carbon atoms from 4C hydrocarbon stream. At least a portion of n-C4 sub-stream comprises 50-92% n-butane.    USE - Production of hydrocarbon product (claimed).    ADVANTAGE - The method provides hydrocarbon product having excellent usability, under mild reaction conditions, by economical process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the manufacturing process of hydrocarbon product.    Fission furnaces (11,12,13)    Treatment process (20)    Separation process (30)    Separation units (31,32)    Hydrotreatment process (41)
NOVELTY - Comprehensive utilization of furfural residue comprises: (1) washing furfural residue with water, extracting soluble component of residue using sulfuric acid and then pressure filtering; (2) adding a plant ash to the first clear liquid and uniformly mixing, then extracting water soluble component and pressure filtering; (3) adding water and cellulase to the first solid residue, then incubating to 30-65 degrees C for 1-100 hours, pressure filtering; and (4) mixing the second solid residue and the solid residue obtained in step (3) and fermenting to obtain organic fertilizer.    USE - The method is useful for the comprehensive utilization of furfural residue to prepare organic fertilizer and utilization of xylose residue (all claimed).    ADVANTAGE - The method completely uses furfural residue with zero exhaust and zero pollution, and provides a high value product such as organic fertilizer.    DETAILED DESCRIPTION - Comprehensive utilization of furfural residue comprises: (1) washing furfural residue with water, extracting soluble component of residue using sulfuric acid and then pressure filtering to obtain a first solid residue and a first clear liquid; (2) adding a plant ash to the first clear liquid and uniformly mixing, then extracting water soluble component and pressure filtering to obtain a second solid residue and a second clear liquid as plant nutrition liquid or liquid fertilizer; (3) adding water and cellulase to the first solid residue, then incubating at 30-65 degrees C for 1-100 hours, pressure filtering to give solid residue and clear liquid for producing a glucose; and (4) mixing the second solid residue and the solid residue obtained in step (3) and fermenting to obtain organic fertilizer.
NOVELTY - This utility new type relates to a one for a straw liquefied oil is capable of a rapid splitting reaction is a splitting tank, this a splitting tank by a vacuum of one box body, the upper part of this box body set with straw powder inlet and bed material inlet, lower part box body screw device used for output and a solid residual material after splitting reaction is connected, in the inner cavity of this box body set with the straw powder inlet and a bed material inlet connected a cylindrical mixed cavity, in this mixed cavity is set with several stir leaves, fixing the pivot shaft and one rotating motor b is connected is up, and this mixed at the bottom of cylindrical cavity is connected is one spiral pipeline, a spiral pipeline set with this there are several discharge hole. This utility new type the material in a short time the inner fully mixed, splitting, produce gaseous product and solid residual, following a match of reaction temperature, additive and catalyst, a heat value of the straw oil production is increased, and the straw conversion is conversion rate of straw oil increase.
NOVELTY - This utility new type relates to one a biomass gasification device. A lower one-sucking type biomass gasification machine set, comprising biomass gasification furnace, and biomass gasification furnace through the gas pipeline orderly connected air outlet of cyclone dust collector, cooling device, dust remover, oil liquid separator, air blower and coal purification device, the biomass gasification furnace comprising storage layer, burning layer and ash layer, a body layer is set with oxygen-increasing combustion wherein an air outlet, an ash layer and the bottom of the furnace body is set with a slag outlet, the storage layer upper part matching set with feeding device, an ash layer lower part set with a device with a spiral ash discharge stir the bottom of the combustion layer set with activity grate. This utility new type structure is simple, design is reasonable, through concave-convex structure is a special bearing and an annular groove and an annular bulge mutually matching is, effective protection of the bearing, increase the use life of bearing.
NOVELTY - This utility new type relates to one a biomass gasification furnace grate. A biomass gasification furnace one reciprocating pneuma bed activity grate, gasification furnace comprising furnace body, set with a multi-row furnace grate of the furnace unit, the single-row furnace grate unit including at least one of a two terminal with a semicircular shaft groove, the middle part is provided with a connecting rod driving ear is furnace grate assemble block, connecting rod driving ear all in a single-row furnace grate unit are set with a connecting pole is one, the bottom furnace grate unit further set and connected with one vertical pole is set with a connecting rod, a connecting pole and connecting pole one, a corresponding position inside a furnace body set with side by side used for supporting furnace grate assemble is a short shaft, the furnace grate assemble a two terminal is setting in a short shaft, one end a connecting rod passes through the furnace wall of the furnace body is set with a furnace body outside and a drive connecting pole mechanism connection. This utility new type for preventing dust agglomeration is a furnace grate at the same time effectively carry out slag to ensure the normal use of biomass gasification furnace, provide sufficient pneuma source, which avoids the breaking, is the phenomenon, greatly increase the market competitive power of device.
NOVELTY - This utility new type claims a biomass gasification unit one for water cyclone decoking protecting blocking device, which overcomes the existing technology in the biomass gasification machine set type problem for water and a discharge device is easy to coke tar dust blockage of mixture. This utility new type cyclone dust collector, a water removing protecting block decoking device, a water removing decoking protecting blocking device is rectangular, the external set with, a material unloading plate and material plate in inclined is set with a multi-V type gradually. A material unloading plate and the horizontal plane is not less than 10 degrees and less than 60 degrees. The V-type slot is gradually deep at most lower than the most shallow, V type slot is gradually opening angle is not less than 30 degrees and beta is not more than 120 degrees. And the existing technology, this utility new type can be the biomass gasification machine set purification device end the produce of water, dust and impurities such as tar collecting process, accumulation of tar and dust discharging plate in a lower effect gradually deep in a V type a, a slide, a completely.
NOVELTY - This utility new type claims a one organic solid waste process of pyrolysis device, comprising a feeding device, a combustion device, a pyrolysis device, gas purification device and discharging device, comprising a device, a feeding seal device, outside cylinder, a transfer room, a ball scraping plate device from circulation device, rolling, discharging seal device, driving device, wherein a discharging pyrolysis pneuma discharge port; a set in inside of outside cylinder, a feeding seal device set with feeding end b of expansion cylinder, a discharging seal device set with a discharging end of a b; a is a gap between outside cylinder and forming a transfer room, the heat energy of combustion room is transmitted to the expansion cylinder as pyrolysis heat source. The device using indirect heating rotary furnace, a flue gas heating and pyrolysis material does not directly contact, the material can not be polluted, increase quality of a pyrolysis pneuma, and a pyrolysis increase quality and yield of solid product. A is a fuel gas combustion heating rotary furnace directly, circulation use, so a reducing pyrolysis of the energy and reduces operation cost.
NOVELTY - This utility model claims a geothermal water heated biogas digester feed liquid device, comprising a water inlet valve and a water outlet valve, further comprising a heat exchanger, the heat exchanger in the marsh gas pool is used for marsh gas pool heating process, the heat exchanger one end connecting the water inlet water valve, one end connecting the water inlet outlet water valve, a multi-temperature sensor, the temperature sensor is at least one of connecting the marsh gas pool, at least one of a heat exchanger and a water outlet water valve, a temperature controller, a temperature sensor connection. This device can be geothermal into circulation heating inner spiral pipe, and a water flow amount in the spiral pipe through exchanging heat for methane pneuma pool inner material liquid carry out heating, and a temperature controller for carrying out the temperature control, this device using a water pressure controller a spiral pipe, and temperature sensor arrangement in a material liquid, material liquid temperature control.
NOVELTY - Controlling particle size of 2,4-dichlorophenoxyacetic acid, comprises adding 2,4-dichlorophenoxyacetic acid with saturated hydrochloric acid solution to obtain a mixture, placing the obtained mixture product into a crystallizer, continuously adding 2,4-dichlorophenoxyacetic acid with saturated hydrochloric acid solution and then discharging and processing.    USE - The method is useful for controlling particle size of 2,4-dichlorophenoxyacetic acid (claimed).    ADVANTAGE - The method is capable of simply controlling the particle size of 2,4-dichlorophenoxyacetic acid with high purity, granularity and yield, and less energy consumption.
NOVELTY - Producing ethanol fuel involves pulverizing food waste to obtain ground material rich in protein and fat. The obtained ground material is then mixed with water to prepare slurry, which is set for fermentation to obtain fermented mash. The obtained fermented mash is heated at certain condition to obtain certain product. Protein and fat are separated and then extracted from the obtained product, where the leftover product is further processed to obtain ethanol fuel as finished product.    USE - Method for producing ethanol fuel from food waste (claimed).    ADVANTAGE - The method enables to produce ethanol fuel by effectively utilizing food waste in an environmentally friendly.
NOVELTY - A white lees and corn straw mixed silage feed is prepared by crushing dry corn straw by using cutter into fine powder, mixing the crushed corn straw fresh lees by adding compound probiotic liquid and water to make mixed storage material moisture content of 60-75%, transferring the material into a fermentation tanks or barrels, filling fermenting pit with raw material, covering surface with a layer of plastic cloth, fermenting, sealing the bucket after filling, filling and pressing with soft rope, using sealing machine, determining whether quality of silage material is good or bad.    USE - White lees and corn straw mixed silage feed.    ADVANTAGE - The silage feed has improved palatability, improved nutritional value, improved digestibility, improved beef cattle weight gain, and low cost.    DETAILED DESCRIPTION - A white lees and corn straw mixed silage feed is prepared by crushing dry corn straw by using cutter into fine powder with length of 3-5 cm, mixing the crushed corn straw with fresh lees at a ratio of 2:3 by adding 5% compound probiotic liquid and water to make mixed storage material moisture content of 60-75%, transferring the material into a fermentation tanks or barrels with woven bag to form oxygen-free environment, filling fermenting pit with raw material, covering surface with a layer of plastic cloth, fermenting for 15 days, sealing the bucket after filling, where the bucket is covered a layer of plastic cloth, upper bucket cover and screw cover, followed by filling and pressing with soft rope, using sealing machine, determining whether quality of silage material is good or bad, if the material has green or yellow green, acid flavor, soft texture, slightly wet, and stem, the material is good quality to feed.
NOVELTY - Potassium dihydrogen phosphate fertilizer composition preparation involves mixing phosphoric acid and carboxamide in molar ratio 2.3-2.5:1 with stirring at 110-130 degrees C for 2-3 hours. The obtained material is mixed with alkaline salt and potassium dihydrogen phosphate with stirring at 70-100 rotations per minute for 45-55 minutes. The obtained material is crystallized at 15 degrees C, and then 1.2-3.5% nitrogen, 2.1-3.3% phosphorus pentoxide and 2.6-4.1% potassium oxide components are added to the obtained material. The obtained material is filtered and trace element containing compound are added.    USE - Method for preparing potassium dihydrogen phosphate fertilizer composition used for medlar (claimed).    ADVANTAGE - The method enables to prepare potassium dihydrogen phosphate fertilizer composition in cost-effective and eco-friendly manner, ensures reduced wastage.    DETAILED DESCRIPTION - Potassium dihydrogen phosphate fertilizer composition preparation involves mixing phosphoric acid and carboxamide in molar ratio 2.3-2.5:1 with stirring at 110-130 degrees C for 2-3 hours. The obtained material is mixed with alkaline salt and potassium dihydrogen phosphate with stirring at 70-100 rotations per minute for 45-55 minutes. The obtained material is crystallized at 15 degrees C, and then 1.2-3.5% nitrogen, 2.1-3.3% phosphorus pentoxide and 2.6-4.1% potassium oxide components are added to the obtained material. The obtained material is filtered, and then trace element containing compound is added to the obtained material. The obtained material is dried at 60-73 degrees C with 7 degrees C/minute for 0.5-0.8 hour to obtain the finished product.
NOVELTY - Preparing bio-fertilizer involves filtering fermented glutamic acid solution using micro-filter film to obtain filtrate that is sterilized. The sterile filtrate is mixed with active carbon in jar at 45-50 degrees C for 30 minutes to obtain decolored filtrate that is concentrated and crystallized to obtain glutamic acid crystal and mother liquid. The mother liquid is dried and crushed into powder that is hydrolysed with hydrochloric acid in reaction kettle at 60 degrees C for 12-15 hours. Potassium hydroxide is added to maintain pH of 7. Aqueous amino acid solution and metal ion are mixed at 40 degrees C.    USE - Method for preparing bio-fertilizer (claimed).    ADVANTAGE - The method enables to prepare bio-fertilizer in cost-effective manner.    DETAILED DESCRIPTION - Preparing bio-fertilizer involves filtering fermented glutamic acid solution using micro-filter film to obtain filtrate that is sterilized. The sterile filtrate is mixed with active carbon in jar at 45-50 degrees C for 30 minutes to obtain decolored filtrate that is concentrated and crystallized to obtain glutamic acid crystal and mother liquid. The mother liquid is dried and crushed into powder that is hydrolysed with hydrochloric acid in reaction kettle at 60 degrees C for 12-15 hours. Potassium hydroxide is added to maintain pH of 7. Aqueous amino acid solution and metal ion are mixed at 40 degrees C for 30 minutes to obtain chelated product that is dried and crushed to obtain amino acid chelate powder. The amino acid chelate, corn straw, stick powder, diatomite and mother liquid are stirred for 10 minutes to obtain mixture that is heated at 100 degrees C for 15-30 minutes. The obtained mixture is cooled to obtain another mixture. The mixtures, mother liquids, monoammonium phosphate, urea and water are mixed to obtain another mixture granulated and dried to obtain product.
NOVELTY - Organic fertilizer comprises 50-60 pts. wt. traditional Chinese medicinal extract, 10-20 pts. wt. livestock manure, 10-20 pts. wt. solid waste, 0.5-1 pts. wt. Bacillus subtilis and 0.5-1 pts. wt. effective microorganism bacteria.    USE - Organic fertilizer used for preventing crop plant diseases and insect pests.    ADVANTAGE - The organic fertilizer is safe, effective, economic and eco-friendly, and increases quality and yield of crops and reduces traditional Chinese medicinal waste of pharmaceutical factory.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves fermenting traditional Chinese medicinal extract, livestock manure and solid waste with water, Bacillus subtilis and effective microorganism bacteria solution for 7-10 days at 50 degrees C to obtain fermented mixture that is cooled to 35-40 degrees C to obtain organic fertilizer.
NOVELTY - L-tryptophan fermentation liquid is fed to an ultrafiltration membrane (m1) and filtered, to obtain permeate (p1). The permeate (p1) is provided into solution and filtered through ultrafiltration membrane (m2), to obtain ultrafiltration concentrate and permeate (p2). The permeate (p2) is concentrated, and crystallized, to obtain L-tryptophan.    USE - Extraction of L-tryptophan (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly extraction of L-tryptophan with high purity by simple method, without production of waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for L-tryptophan extracting device, which has ultrafiltration membrane (m1), ultrafiltration membrane (m2), concentrated crystallization unit, drying unit and solid-liquid separation unit.
NOVELTY - An acetylenic ketone compound (I) is new.    USE - New acetylenic ketone compound is used as intermediate for preparing pharmaceutical and functional material.    ADVANTAGE - The acetylenic ketone compound is manufactured by economical, safe, environmentally-friendly and simple process with excellent production efficiency.    DETAILED DESCRIPTION - An acetylenic ketone compound of formula (I) is new.    R1,R2=1-20C alkyl, 1-20C heteroalkyl, 3-20C cycloalkyl, 3-20C heterocycloalkyl, 2-20C alkenyl, 2-20C heteroalkenyl, 3-20C cycloalkenyl, 3-20C heterocycloalkenyl, 2-20C alkynyl, 2-20C heteroalkynyl, 3-20C cycloalkynyl, 3-20C heterocyclyl alkynyl, 1-20C alkoxy, cyano, nitro, optionally substituted aryl, optionally substituted heteroaryl, aryloxy, heteroaryl, aryl-1-20C alkyl, heteroaryl-1-20C alkyl, 2-20C alkenyl-1-20C alkyl or alkylcarbonyl.    An INDEPENDENT CLAIM is included for preparation of acetylenic ketone compound (I).
NOVELTY - Method for controlling Athetis lepigone, involves contacting crystal (Cry) 2Ab protein with night moth pests.    USE - The method is useful for controlling A.lepigone (claimed).    ADVANTAGE - The method is simple to perform and environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method of controlling plant producing A.lepigone, involves introducing polynucleotide encoding Cry2Ab protein sequence into genome of plant; (2) plant seed, obtained by crossing first plant with second plant to obtain seed; and (3) method culturing plant seed, involves planting at least one seed comprising genome containing polynucleotide encoding Cry2Ab protein sequence, allowing seeds to grow, artificially inoculating pest into grown plant, and producing plant with pest resistance.
NOVELTY - Production of biodiesel involves deprotecting palm oil, adding potassium hydroxide, performing deacidification, removing the leached layer, mixing with activated carbon, decoloring, carrying out catalytic transesterification, ultrasonically treating, subjecting to ester exchange reaction for 2-4 hours, separating oil layer, glycerol layer and alcohol layer, and obtaining biodiesel from oil layer. The catalyst is potassium carbonate. The content of potassium carbonate is 0.8-1.2 wt.%.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method enables production of biodiesel with palm oil conversion rate of 89-93%.
NOVELTY - A methanol-gasoline composite comprises 65-85 pts. wt. methanol, 5-12 pts. wt. gasoline, 0.8-1.5 pts. wt. paraffin oil, 2-6 pts. wt. glycerin, 1-5 pts. wt. acetone, 1-5 pts. wt. acyl amide, 0.8-3 pts. wt. t-butyl acetate, 1-4 pts. wt. dibutyl phthalate, 0.5-1.5 pts. wt. glycerol monostearate, 1-5 pts. wt. ethylbenzene, 1-4 pts. wt. tert-butanol and 0.2-0.5 pt. wt. iron chloride.    USE - Methanol-gasoline composite is used as fuel for vehicle.    ADVANTAGE - The methanol-gasoline composite has high oxygen content and calorific value, and produces low exhaust emissions after combustion, does not produce smoke, coke and residue during combustion and does not blacken the combustion system bottom, and is environmentally friendly, economical and safe to use.
NOVELTY - A pyrolytic liquefied-biomass fuel comprises 11-13 pts. wt. bagasse, 15-25 pts. wt. rice straw powder, 20-30 pts. wt. corn straw powder, 10-25 pts. wt. soybean straw powder, 10-20 pts. wt. potato straw powder, 10-20 pts. wt. barley straw powder, 5-15 pts. wt. broad bean stalk powder, 40-55 pts. wt. wheat straw powder, 5-9 pts. wt. rice cake, 5-10 pts. wt. chicken manure, 15-20 pts. wt. rice bran, 10-15 pts. wt. wheat bran, 5-8 pts. wt. potato, 15-20 pts. wt. grain slag, 10-16 pts. wt. Cassava residue, 5-12 pts. wt. grass straw, and 5-8 pts. wt. corncob.    USE - Pyrolytic liquefied-biomass fuel is used as substitute for fuel oil.
NOVELTY - The furnace has a feeding system (3) connected with a furnace body (1). A discharging system (4) is connected with a cylindrical steel pipe (44), a transverse pipe (43), a carbon discharging pipe (41) and a carbon discharging control valve (42), where the control valve is connected with a connecting end of a water tank (5). An upper end of the transverse pipe is connected with a frequency heating system (2). A heat preservation device (6) is connected with a refractory mortar (62). An outside layer of the furnace body is connected with a coil (22) and the heat preservation device.    USE - Continuous closed-type frequency-biomass destructive distillation domestic rubbish heating furnace for use in municipal area.    ADVANTAGE - The furnace has a piston connected with a pushing head so as to improve feeding speed, municipal domestic rubbish treatment effect and domestic rubbish cleaning efficiency and reduce energy consumption. The furnace can improve heating efficiency and economical benefit and avoid waste biomass carbon resources. The furnace has user friendly environment.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a continuous closed-type frequency-biomass destructive distillation rubbish heating furnace.    Furnace body (1)    Frequency heating system (2)    Feeding system (3)    Discharging system (4)    Water tank (5)    Heat preservation device (6)    Coil (22)    Carbon discharging pipe (41)    Carbon discharging control valve (42)    Transverse pipe (43)    Cylindrical steel pipe (44)    Refractory mortar (62)
NOVELTY - A methanol-gasoline composite comprises 35-55 wt.% methanol, 5-10 wt.% ether, 3-15 wt.% aromatic hydrocarbon, 5-8 wt.% surfactant and 20-50 wt.% solvent oil. The ether is ethylene glycol butyl ether, methyl tert-butyl ether or diisopropyl ether. The surfactant is MOA-3, MOA-9, MOA-3B or OS-15 type surfactant. The aromatic hydrocarbon is a mixture of toluene and xylene.    USE - Methanol-gasoline composite (claimed).    ADVANTAGE - The methanol-gasoline composite has excellent water resistance and storage stability for more than one year.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of methanol-gasoline composite, which involves mixing raw material components in a mixer.
NOVELTY - An exhaust gas purification tower distilling method involves separating liquid carbon dioxide from the tower before distilling process, adding 93-100% oxygen into the tower, followed by subjecting to decarburization process and steam time coal gasification process with red hit coke as catalyst for heat quantity absorption to produce carbon dioxide, hydrogen, methane and nitrogen gas, where the coal producing gas furnace would not adding distilled gas.    USE - Method for distilling exhaust gas purification tower.    ADVANTAGE - The method enables distilling exhaust gas purification tower with reduced gas intensity and considerable economic value.
NOVELTY - Honeysuckle fertilizer comprises 80-100 pts. wt. duck manure, 50-60 pts. wt. corn straw, 30-40 pts. wt. plant ash, 40-50 pts. wt. shell powder, 10-12 pts. wt. nitrogen fertilizer, 12-14 pts. wt. phosphate fertilizer, 5-7 pts. wt. potassium fertilizer, 10-12 pts. wt. oil residue, 0.2-0.4 pts. wt. EN source liquid, 20-30 pts. wt. pomegranate rind, 10-20 pts. wt. cabbage caterpillar powder, and 20-30 pts. wt. distillers' grains.    USE - Used as honeysuckle fertilizer.    ADVANTAGE - The honeysuckle fertilizer: is rich in nutrients; provides good environment for the growth of crops; improves the quality of soil fertility; and improves soil properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the honeysuckle fertilizer, comprising crushing the duck manure, corn straw, plant ash, shell powder, nitrogen fertilizer, phosphate fertilizer, potassium fertilizer, oil residue, EN source liquid, pomegranate rind, cabbage caterpillar powder and distillers' grains through a crusher, and fermenting in a sealed tank; and (ii) pre-heating a screw mixer to 80-100 degrees C, maintaining constant temperature, then adding the material obtained in the step (i) to a reciprocating single-screw pin mixer, opening the screw mixer and maintaining mold head pressure to 1-1.2 Mpa, injecting through screw die opening, and forming granular fertilizer to obtain the honeysuckle fertilizer.
NOVELTY - Sequencing batch activated sludge comprises adding pre-treated sewage into sequencing batch reactor (SBR), refluxing the digested sludge in the sludge digester and passing into the SBR reaction pool, mixing the wastewater and sludge in the SBR reactor to form a mixture, aerating, precipitating, draining, and purifying; adding the concentrated sludge from sludge thickener into the sludge digestion tank, carrying out digestion treatment; discharging the sludge in the sludge digester, passing part of the digested sludge back into SBR reactor, and discharging another part outside the tank.    USE - The method is useful for sequencing batch activated sludge (claimed).    ADVANTAGE - The method produces low sludge yield and consumes less energy (claimed).    DETAILED DESCRIPTION - Sequencing batch activated sludge comprises (i) adding pre-treated sewage into SBR reactor, refluxing the digested sludge in the sludge digester and passing into the SBR reaction pool, mixing the wastewater and sludge in the SBR reactor to form a mixture, passing water into the mixture, aerating, precipitating, draining and allowing to stand; then passing into the drainage phase, purifying, and using the supernatant as effluent, discharging in the SBR reactor, and discharging the remaining sludge into the sludge thickener; (ii) adding the concentrated sludge from sludge thickener into the sludge digestion tank, carrying out digestion treatment, and using the supernatant for pre-treatment of sewage; (iii) passing the concentrated sludge into the sludge digestion tank, digesting the sludge under anaerobic condition, discharging the sludge in the sludge digester, passing part of the digested sludge back into the SBR reactor, and discharging another part of the digested sludge outside the tank for sludge dehydrating and disposal.
NOVELTY - Synthesizing halometasone dissolving the corresponding dichlorobeclomethasone propionate compound in the presence of an inert gas, and reacting the mixture by adding aqueous alkaline solution at 0-30 degrees C for 3-5 hours to obtain halometasone.    USE - The method is useful for synthesizing halometasone (claimed).    ADVANTAGE - The method is simple, synthesizes high yield of halometasone, and does not make use of harmful solvents.
NOVELTY - A mixed refrigerant comprises fluoroethane, propylene and propane.    USE - Mixed refrigerant is used as substituent for R502-type refrigerant (claimed).    ADVANTAGE - The environmentally-friendly mixed refrigerant having global-warming potential of less than 12, ozone-depletion potential of 0 and slip temperature of less than 2 K, is manufactured with reduced energy consumption. The mixed refrigerant has cycle performance coefficient, volume refrigeration unit volume and cooling capacity per unit mass which is higher than cycle performance coefficient, volume refrigeration unit volume and cooling capacity per unit mass of R502-type refrigerant. The mixed refrigerant has standard volumetric capacity which is lesser than that of R502-type refrigerant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mixed refrigerant, which involves mixing raw materials in liquid phase.
NOVELTY - A mixed refrigerant comprises fluoroethane, propylene and propane.    USE - Mixed refrigerant is used as substituent for chlorodifluoromethane refrigerant (claimed).    ADVANTAGE - The mixed refrigerant having excellent durability, ozone depletion potential of 0, global warming potential of less than 12 and slip temperature of less than 3 K, is manufactured with reduced energy consumption. The mixed refrigerant has cycle performance coefficient, cooling capacity per unit mass and cooling capacity per unit volume which is more than cycle performance coefficient, cooling capacity per unit mass and cooling capacity per unit volume of chlorodifluoromethane refrigerant, respectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of mixed refrigerant, which involves mixing raw materials in liquid state.
NOVELTY - Biomass fuel pyrolysis reactor comprises a first rotating shaft (1), a second rotating shaft (2) and many rotating cones (3). The second rotating shaft is connected to the first rotating shaft, and co-rotates with the first rotating shaft. The rotating cone is located on the second rotating shaft. The rotating cone is fixedly connected to the second rotating shaft. The rotating cone and the second rotating shaft are made of stainless steel material.    USE - Used as biomass fuel pyrolysis reactor.    ADVANTAGE - The reactor has simple structure, easy operation procedure, and improved reaction efficiency; and is economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biomass fuel pyrolysis reactor.    First rotating shaft (1)    Second rotating shaft (2)    Rotating cones (3)    Outer heat insulation layer (4)    Inner heat insulating layer (5)
NOVELTY - The reaction furnace comprises a feeder, a chemical reaction device, a reduction reaction device, a combustion chamber, an annular water tank, a dust filter, a downstream channel, a discharge channel, a gas distribution pipe, an ignition device, a blasting device, and an ash outlet. The reduction reaction device is connected with the combustion device. The feeder is located in a feeding port. The feeding port is connected with a seal cover plate. The feeder is provided with a discharging groove. The cover plate is provided with a plug, and connected with a ring shaped pressing plate.    USE - The reaction furnace is useful for gasification of biomass (claimed).    DETAILED DESCRIPTION - The reaction furnace comprises a feeder, a chemical reaction device, a reduction reaction device, a combustion chamber, an annular water tank, a dust filter, a downstream channel, a discharge channel, a gas distribution pipe, an ignition device, a blasting device, and an ash outlet. The reduction reaction device is connected with the combustion device. The feeder is located in a feeding port. The feeding port is connected with a seal cover plate. The feeder is provided with a discharging groove. The cover plate is provided with a plug, and connected with a ring shaped pressing plate. The reaction device is connected with the annular water tank. A bottom part of the chemical reaction device is mounted with an ignition device.
NOVELTY - Producing bio-oil gas, comprises (a) collecting algae and invasive alien plants in a ratio of 1-3:1 and then drying, crushing and sieving into granule, placing the granule into a microwave pyrolysis device and then stirring into water to 100 degrees C for 1-2 hours, (b) carrying microwave pyrolysis treatment of the stirred material to 450-600 degrees C for 10-20 minutes and microwave radiation frequency of 2450 MHz to produce a mixed gas, and (c) heating the mixed gas into the furnace and then cooling to 0-10 degrees C, separating the biological oil, gas and coke in the mixed gas using a separating device.    USE - The method is useful for producing bio-oil gas (claimed).    ADVANTAGE - The method improves the recovery rate and yield of the bio-oil gas to 10-20% and 30-60%, respectively.
NOVELTY - The device has a circulation fluidization bed gasification furnace (1) whose upper part is connected with a first cyclone separator (2). The circulation fluidization bed gasification furnace is equipped with a circulation fluidization bed boiler (9) through a slag (8). A lower part of the circulation fluidization bed boiler is connected with the first cyclone separator through a feeding pipe (4). The circulation fluidization bed boiler is arranged with a second cyclone separator (10) that is connected with a flue part (12).    USE - Biomass, solid waste and fuel charging device.    ADVANTAGE - The device has high waste utilization rate, working efficiency and conversion rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass, solid waste and fuel charging device working method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass, solid waste and fuel charging device.    Circulation fluidization bed gasification furnace (1)    Cyclone separators (2,10)    Feeding pipe (4)    Slag (8)    Circulation fluidization bed boiler (9)    Flue part (12)
NOVELTY - A methanol gasoline power accelerator comprises 21-27 pts. wt. isooctanol, 12-15 pts. wt. aminoacetaldehyde diethyl acetal, 5-7 pts. wt. 1,5-cyclooctadiene, 6-9 pts. wt. 2-acetylbenzofuran, 10-13 pts. wt. propargyl alcohol, 15-20 pts. wt. n-propanol, 3-5 pts. wt. zinc naphthenate, 3-5 pts. wt. dinonylnaphthylsulfonic acid, 5-7 pts. wt. polyoxyethylene fatty amine, and 3-5 pts. wt. pentamethyldiethylenetriamine.    USE - Methanol gasoline power accelerator (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of methanol gasoline power accelerator; and    (2) usage method of methanol gasoline power accelerator.
NOVELTY - Carbon powder processing device comprises a ball mill (1), a feeding cylinder (2), a kneading unit (4), a motor (6) and a hopper (8), where the ball mill is connected to the kneading unit through feeding cylinder. The kneading unit is provided with the motor. The kneading unit is connected to a mixer. The lower part of the kneading unit is connected with the hopper. The hopper is connected with a transmission cylinder of a drying tower.    USE - Carbon powder processing device.    ADVANTAGE - The carbon powder processing device is cost-effective and easy to operate, and turns waste into treasure with high fixed carbon value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for processing carbon powder, which involves:    (A) keeping waste mushroom bag material having carbon powder into the ball mill;    (B) ball milling the obtained material to 80-100 meshes and then the ball milled material is kept in the inner feeding cylinder of a seal spiral conveying machine;    (C) kneading the obtained material into a kneading machine and then stirring the kneaded material to obtain fine powder;    (D) mixing the obtained powder with binding agent in an adhesive feeding device;    (E) stirring the obtained material and then entering the stirred material into bottom of the receiving hopper and the discharge port;    (F) keeping the obtained material into the molding machine through a conveyor and then molding the obtained material in the inner transmitting cylinder; and    (G) entering the molded material into the drying tower after baking and the adjusting the temperature to obtain the desired product.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a carbon powder processing device.    Ball mill (1)    Feeding cylinder (2)    Kneading unit (4)    Motor (6)    Hopper (8)
NOVELTY - The processing device has a ball mill (1) that is connected with a kneading machine (4) through a feeding cylinder (2). The inner portion of the kneading machine is set with a gravity mixer and is connected with a motor (6). The lower portion of the kneading machine is connected with a hopper (8). The hopper is connected with a molding machine (10) through a conveyor belt (9), and is set in a transmission cylinder. The molding machine is connected with a drying tower (11). The feeding cylinder is set with a spiral conveying machine (3). A discharge port (7) is connected with hopper.    USE - Device for processing carbon powder incense of waste mushroom bag.    ADVANTAGE - The operability of the processing device is strong. The cost of the processing device is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for processing carbon powder incense of waste mushroom bag.    Ball mill (1)    Feeding cylinder (2)    Spiral conveying machine (3)    Kneading machine (4)    Motor (6)    Discharge port (7)    Hopper (8)    Conveyor belt (9)    Molding machine (10)    Drying tower (11)
NOVELTY - The system comprises an inlet, a discharge port, an outlet and a fermentation storage body. The inlet is provided with the fermentation storage body. The discharge port is located at a bottom of the fermentation storage body. The fermentation storage body is fitted with the discharge port and a screw conveyor. The inlet is connected to an air feed system. The air feed system comprises a tubular piston and a cylinder. A vertical section of the cylinder is connected to the discharge port. A horizontal section of the tubular piston is connected to a reciprocating mechanism.    USE - The system is useful for fermenting agricultural biomass (claimed).    ADVANTAGE - The system is capable of fermenting the agricultural biomass with high yield and quality and reduced labor intensive.    DETAILED DESCRIPTION - The system comprises an inlet, a discharge port, an outlet and a fermentation storage body. The inlet is provided with the fermentation storage body. The discharge port is located at a bottom of the fermentation storage body. The fermentation storage body is fitted with the discharge port and a screw conveyor. The inlet is connected to an air feed system. The air feed system comprises a tubular piston and a cylinder. A vertical section of the cylinder is connected to the discharge port. A horizontal section of the tubular piston is connected to a reciprocating mechanism and provided with a funnel shaped inlet. A bottom of the fermentation storage body is provided with a water outlet. The outlet is passed through a boiler, a heat pump, an external pipeline and a slurry tank. The screw conveyor is provided with a lifting mechanism, an injection nozzle and a coaxial rotating handle. The tubular piston is provided with a reciprocating tank, a connecting rod and a surface insulating layer. An INDEPENDENT CLAIM is included for a method for fermenting agricultural biomass using the system.
NOVELTY - Preparation of chiral-( alpha )-cycloalkyl glycine involves esterifying glycine as starting material to obtain glycine t-butyl ester, adding benzophenone, dissolving resultant product in hydrocarbon solvent, condensing the resultant product using p-toluenesulfonic acid, adding halogenated cycloalkane, dissolving resultant product in ether solvent in alkaline condition, deprotecting resultant product using strong acid to obtain DL-( alpha )-cycloalkyl glycine or DL-( alpha )-cycloalkyl glycine hydrochloride, dissolving the resultant product in solvent, acylating, and enzyme catalyzing.    USE - Preparation of chiral-( alpha )-cycloalkyl glycine (claimed).    ADVANTAGE - The method provides chiral-( alpha )-cycloalkyl glycine having excellent stability, by environmentally-friendly, economical, easy and simple process with optical purity of more than 99% and yield of 46-54%.    DETAILED DESCRIPTION - Preparation of chiral-( alpha )-cycloalkyl glycine involves esterifying glycine as starting material to obtain glycine t-butyl ester, adding benzophenone, dissolving the resultant product in hydrocarbon solvent, condensing the resultant product using p-toluenesulfonic acid as catalyst to obtain N-diphenylmethylene glycine tert-butyl ester, adding halogenated cycloalkane, dissolving the resultant product in ether solvent in alkaline condition to obtain N-diphenylmethylene-( alpha )-cycloalkyl glycine tert-butyl ester, deprotecting the resultant product using strong acid system to obtain DL-( alpha )-cycloalkyl glycine or DL-( alpha )-cycloalkyl glycine hydrochloride, dissolving the resultant product in solvent, acylating the resultant product in presence of base to obtain N-acetyl-DL-( alpha )-cycloalkyl glycine, and catalyzing the resultant product using enzyme to obtain chiral-L-( alpha )-cycloalkyl glycine or chiral-D-( alpha )-cycloalkyl glycine.
NOVELTY - Method for producing bioorganic fertilizer, involves crushing agricultural waste material to less than 20 mm, mixing with fermented wastewater until moisture content reaches 55-70 wt.%, where the mixture has pH of 6-9, adding 0.05-5 wt.% microbial agent to the mixture, fermenting the mixture using existing fermentation compost bin or by windrow composting or static compost fermentation, turning the mixture when temperature reaches 50 degrees C, maintaining at 50-70 degrees C for 5-15 days, where volume of the fermented product is 1/3-1/2, and drying the fermented product.    USE - The method is useful for producing bioorganic fertilizer (claimed).    ADVANTAGE - The method is nontoxic and environmentally-friendly, consumes less time, and increases content of organic substance in fertilizer, and quality of fertilizer.
NOVELTY - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 20-35% plant straw, 20-30% farmyard manure, 5-15% cottonseed hulls, 25-35% bran, 8-10% phosphate fertilizer and 5-10% auxiliary materials.    USE - The method is useful for preparing nutrition base for H.marmoreus and T.matsutake (claimed).    DETAILED DESCRIPTION - Method for preparing nutrition base for Hypsizygus marmoreus and Tricholoma matsutake, involves using 20-35% plant straw, 20-30% farmyard manure, 5-15% cottonseed hulls, 25-35% bran, 8-10% phosphate fertilizer and 5-10% auxiliary materials. The method involves (a) crushing plant straw into particles of 1-2 cm, and mixing the crushed materials with farmyard manure, cottonseed hulls, bran and 80-90% water, (b) performing primary fermentation of the mixture for 10-15 days, (c) adding phosphate fertilizer and auxiliary materials to the fermented mixture, and subjecting to secondary fermentation, (d) performing primary sterilization of the fermented mixture, (e) subjecting to secondary sterilization, and (f) packing the sterile mixture, where the fermentation is performed at 18-25 degrees C and humidity of 85-93%.
NOVELTY - Macrocyclic lactam derivative (I) is new.    USE - Macrocyclic lactam derivative used for preparing anticancer medicine (claimed).    ADVANTAGE - The macrocyclic lactam derivative is prepared in a simple, efficient and eco-friendly manner.    DETAILED DESCRIPTION - Macrocyclic lactam derivative of formula (I) is new.    A=1,4-dimethyl-1,2,3-triazole, phenyl, pyridyl, imidazolyl or N-methyl imidazolyl;    R=H or -(CH2)nR';    R'=amino, 1-6 alkylamino, 5-7C aryl, 5-10C heteroaryl or 6-10C arylamine; and    n=1-3.    An INDEPENDENT CLAIM is included for a method for preparing macrocyclic lactam derivatives of formula (I).
(SE201450702-A1)   NOVELTY - A heavy residue treating method involves subjecting a mixture formed of raw material comprising heavy residues originated from material of biological origin and an aqueous substance to hydrolysis at 10-280 degrees C at a pressure of 0-70 bar to obtain a hydrolyzed mixture. The hydrolyzed mixture is separated into an organic phase and an aqueous phase. The organic phase comprising the raw material and the material of biological origin is subjected to a purification treatment to obtain a purified product.    USE - Method for treating heavy residue, derived from material of biological origin, that is utilized for producing liquid fuels or fuel components (claimed).    ADVANTAGE - The method enables treating heavy residue, in an inexpensive manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for producing liquid fuels or fuel components.
NOVELTY - Production of solid fuel involves mixing aerobic microorganisms and sawdust, obtaining mixture (a1) with moisture content of 1-10%, mixing mixture (a1) and food waste having moisture content of 80-90%, forming mixture (a2) with moisture content of 50-60%, carrying out fermentation of aerobic microorganisms and food waste by drying the obtained mixture at 45-90 degrees C, obtaining dried material mixture (a3) with moisture content of 5-20%, and molding the resultant product.    USE - Production of solid fuel (claimed).
NOVELTY - Producing pellet type solid fuel, comprises collecting waste wires and waste plastic, washing collected waste wires and waste plastic, crushing, introducing crushed waste wires and waste plastic into water, removing polyvinyl chloride sunk in water, separating polyethylene, polypropylene and polyvinyl chloride floating on water, and thermoforming polyethylene, polypropylene and polyvinyl chloride.    USE - The method is useful for producing pellet type solid fuel (claimed).    ADVANTAGE - The method is environmentally friendly (claimed), and reduces use of fossil fuel.
NOVELTY - The system has an air separation device (1) connected with a gasification furnace (2) i.e. high temperature gas outlet, that is connected with a high temperature heat exchanger (3). A gas entrance end of the high temperature heat exchanger is fixed with a compressor (13). The high temperature gas outlet is fixed with a particle removal device (4) that is connected with a desulfurizing device (5). The desulfurizing device is connected with a mercury removing device outlet (6) that is fixed with a water gas conversion device (7). An electric generator (15) is fixed with a turbine (14).    USE - Integrated-type coal gasification molten carbonate fuel cell generation system.    ADVANTAGE - The system increases heat usage rate, and has high working efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of an integrated-type coal gasification molten carbonate fuel cell generation system.'(Drawing includes non-English language text)'    Air separation device (1)    Gasification furnace (2)    High temperature heat exchanger (3)    Particle removal device (4)    Desulfurizing device (5)    Mercury removing device outlet (6)    Water gas conversion device (7)    Compressor (13)    Turbine (14)    Electric generator (15)
NOVELTY - One is suitable for biological treatment of municipal organic waste and agriculture organic waste and device, including garage type dry fermentation device and percolate treatment device, the garage type dry fermentation section is for putting material to ferment cabin closeness, heating heat preservation, when temperature after rise to Anaerobic requirement temperature, closing the aeration system, open spray system, to carry out inoculating material, fermentation, fermentation reaction, open aeration system, air replacement, open door, complete fermentation. And wherein percolate disposing process section, the fermentation product is a filter liquor one portion through spray pump I enter into drop filtering sprinkler, the rest percolate transporting part to EGSB reactor, EGSB reacting outlet water through spray pump II transport to vertical to sprinkle head. This utility model new technology is simple, suitable operation, strong practicability, can effective solve city organic waste and agriculture organic waste and environmental problem, and resource comprehensive use.
NOVELTY - Composition of the catalyst is formed in the following ratio, wt %: palladium 0.005-1, promoter 0.005-5, copromoter if necessary 0.005-5, carrier - the remaining part. The promoter on the carrier is fixed in the oxide form to the active component. Palladium particles are fixed on the carrier in the zero degree of oxidation in the electronic condition of valence orbitals of their own atoms. The catalyst is characterised by a band of an absorbing complex of carbon monoxide with palladium with the wave number of 2060-2100 cm-1 in the infrared spectrum of absorbed carbon monoxide. As the carrier applied is a highly-porous cellular carrier, produced from a metal or aluminium oxide, characterised by the porosity not less than 85%, the average size of the pores is 0.5-6.0 mm. On the highly-porous cellular carrier placed is a layer of aluminium oxide with the formation of a secondary carrier, on which the promoter and the active component palladium are successively placed. The secondary carrier aluminium oxide is characterised by the width from 10 mcm to 500 mcm, specific surface of not less than 20 m2/g, volume of the pores from 0.1 to 1.0 cm3/g and is made with the pores with a diameter over 5 nm, the volume of which constitutes 50-98% of the total volume of the pores. The secondary carrier in the general composition of the catalyst constitutes not less than 5 wt %.    USE - Chemistry.    ADVANTAGE - Improvement of thermo- and weight-exchange and diffusion characteristics with the elimination of a possibility to form local overheats of the catalyst layer and diffusion limits of the transport of initial compounds and reaction products.4 tbl, 22 ex
NOVELTY - A dejecta ferment drying a one step is a, a is a normal pressure ventilation solid aerobic fermentation device, wherein the fermentation device is a network frame a tank group or is a a network frame tank platoon and the fermentation room, network frame tank group and network frame tank fleet is equipped with sponge; fermentation room is a fluorescent temperature fermentation room is one or multi of a door and one or multi of a discharge cylinder, a condition of the fermentation environment, or fermentation room, temperature control in more than 16 degrees C, humidity at 60% the following, and it is convenient.
NOVELTY - A hydrogen production system using sunlight comprises lens (102) which condenses sunlight, optical fiber (42) which transmits condensed light, and hydrogen production apparatus (104) to which the end of optical fibers is connected and contains light guide material emitted while light-guiding the light which injected into the liquid containing water, photocatalyst, and edge part which are arranged in a container. End of optical fibers is connected to edge part of light guide materials.    USE - A hydrogen production system using sunlight (claimed).    ADVANTAGE - Sunlight can be efficiently irradiated to the photocatalyst. Photocatalyst efficiently and highly decomposes water and manufactures hydrogen gas.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view of the structure of hydrogen production system using the sunlight.    Optical fiber (42)    Sun (101)    Lens (102)    Hydrogen production apparatus (104)
NOVELTY - This utility model claims a non-power self-stirring breaking Anaerobic fermentation devicem, wherein it comprises a shell, a feeding part, an overflow liquid room, a gas room pneuma, a fermenting room and a discharging material part. the fermentation room inner mounting pneuma is set with a shell net breaking, the fermenting shell inner wall is uniformity fixed with a connected pipe, the connected pipe through the fermentation room and overflow liquid room, the connected tube is located on the tube side of liquid room with elbow, further comprising a free insert blocking tube inner elbow. This utility model is reasonable structure, the reliability is high, economic and energy-saving, simple and convenient operation, can carry out a stirring and breaking the shell, which is good for carrying out a fermentation process, increase gas generating efficiency for biogas slurry in the following without external power.
NOVELTY - The collection method involves hydrothermal processing a sludge containing a polysaccharide for 10-30 minutes at 200-230 degrees Celsius. The hydrothermal processing produces 20-35% solubilization rate of sludge. The solid component is recovered from the processed material. The saccharification is performed by hydrolyzing with an acid or an enzyme with respect to the recovered solid component.    USE - Nutrient collection method of sludge for cultivation method of algae (claimed).    ADVANTAGE - Maillard reaction and excessive decomposition reaction of a monosaccharide are avoided. Monosaccharide is obtained from sludge with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a cultivation method of algae; and    (2) an algae culture system.    DESCRIPTION OF DRAWING(S) - The drawing shows the flowchart of the nutrient collection method of sludge, and the cultivation method of algae. (Drawing includes non-English language text).
NOVELTY - 2-(2-(2-(2,6-dichlorophenylamino) phenyl)acetoxy)acetic acid or aceclofenac is prepared by reacting 2-methylpropan-2-ol and 2-chloroacetyl chloride with N,N-dimethyl aniline to give tert.-butyl-2-chloroacetate, reacting with diclofenac sodium in presence of catalytic amount of organic base and tetrabutylammonium bromide with or without solvent to form intermediate III, hydrolyzing intermediate III with formic acid or mixture of formic acid and acid catalysts, adding toluene for layer separation, distilling toluene layer to obtain crude aceclofenac, and purifying.    USE - Preparation of 2-(2-(2-(2,6-dichlorophenylamino) phenyl)acetoxy)acetic acid (claimed).    ADVANTAGE - The process is environment-friendly.    DETAILED DESCRIPTION - 2-(2-(2-(2,6-dichlorophenylamino) phenyl)acetoxy)acetic acid or aceclofenac of formula (I) is prepared by reacting 2-methylpropan-2-ol and 2-chloroacetyl chloride with N,N-dimethyl aniline to give tert.-butyl-2-chloroacetate, reacting with diclofenac sodium in presence of catalytic amount of organic base and tetrabutylammonium bromide with or without solvent to form intermediate III, hydrolyzing intermediate III with formic acid or mixture of formic acid and acid catalysts, adding toluene for layer separation, distilling toluene layer to obtain crude aceclofenac, and purifying crude aceclofenac in solvent or mixture of solvent with water..
NOVELTY - Production of selenium-enriched green vegetable comprises mixing poultry manure, straw, corn stover, corn cob, effective microorganism original liquid and sugar at mass ratio of 500-1000:1-3:1-3, fermenting, adjusting moisture content, sealing, anaerobic fermenting for 10-15 days, planting vegetables, growing, spraying selenium-enriched agent, soaking for 0.5-2 hours and transplanting.    USE - Method for producing selenium-enriched green vegetable (claimed).    ADVANTAGE - The method is simple, environment-friendly and high-yield.
NOVELTY - Alloys of the systems lithium (Li)/zinc oxide (ZnO).    USE - The alloy is useful for the fermentation of cereals, and as a catalyst in the fermentation of grains, cereal and rye to produce biofuels (claimed).    ADVANTAGE - The alloy exhibits excellent catalytic property, and can be efficiently used as catalysts used in thermal degradation of cereal grains.    DETAILED DESCRIPTION - Alloys of the systems lithium (Li)/zinc oxide (ZnO) with a new structure, where it is represented by the formula: Li2xZn1-xO. An INDEPENDENT CLAIM is included for a process for preparing the alloy represented by the formula Li2xZn1-xO, which involves synthesis of ZnO and lithium hydroxide monohydrate (LiOH.H2O), where ZnO and LiOH.H2O are mixed together in a relative to the stoichiometric proportion corresponding to LiZnO and Li2ZnO2 and the mixture is homogenized by mechanical agitation, and then compressed into tablets at 20 MPa, which are placed in a porcelain crucible, in an oven, and applying the following thermal cycle: (1) heating (10 degrees C/minute) up to T=400 degrees C, (2) isotherm plateau (24 hours), (3) heating (10 degrees C/minute) up to T=600 degrees C, (4) isotherm plateau (24 hours), (5) heating (10 degrees C/minute) up to T=700 degrees C, (6) isotherm plateau (1 hour), (7) cooling (about 5 degrees C/minute) at room temperature to obtain an alloy with a strictly described composition.
NOVELTY - Producing methane involves adding sludge and acetic acid into anaerobic reactor to obtain mixture and then maintaining pH value of mixture to 6.8-7.2. Trace elements and carbonate buffer are added into mixture and then mixture is kept for 15 days. The mixture is acidfied by Lactobacillus and symbiotic bacteria and then mixture is kept for 20-40 days at pH value 5.5-6.2 to obtain the product.    USE - Method for producing methane (claimed).    ADVANTAGE - The method enables to produce methane in high quantity due to acidic medium in anaerobic reactor.
NOVELTY - Generating marsh gas involves mixing manure, crop straw and vegetable waste in a mass ratio of 0.3-0.4:0.1-0.3:0.1-0.2 to obtain resultant mixture. The resultant mixture is fed into a fermentor comprising microbial inoculum to generate marsh gas.    USE - Method for generating marsh gas from agricultural waste by using anaerobic fermentation process (claimed).    ADVANTAGE - The method enables to generate marsh gas by ensuring conservation of resources, where the discharged agricultural wastes are processed to generate marsh gas, and thus protecting the environment from pollution.
NOVELTY - Synthetic sterically hindrance amine desulfurization agent comprises (a) 99% tert-butylamine, (b) 98% 1,3-dichloro-2-propanol, (c) 10% sodium hydroxide (saturated solution), (d) anhydrous ethanol and (e) ultrapure (UP) grade distilled water.    USE - The synthetic sterically hindrance amine desulfurization agent is useful in purification of thio-containing natural gas, refinery gas and liquefied gas.    ADVANTAGE - The desulfurization agent: has high boiling point and selectivity; and is economical and environmentally friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the sterically hindered amine desulfurization agent, comprising (i) introducing components (a), (b) and (d) into a steel reaction kettle, heating to 130-145 degrees C, and reacting for 2 hours, (ii) cooling the reaction product to 70 degrees C, adding saturated sodium hydroxide solution (10%), reacting for 0.5 hour, cooling to less than 30 degrees C under reflux condition, (iii) extracting with ethyl acetate, to obtain an upper layer extraction liquid, (iv) adding anhydrous magnesium sulfate, drying for 2 hours, and filtering, and (v) distilling, cooling to obtain a crystal.
NOVELTY - Synthesis of metolachlor comprises taking ether amine, alkali and chloroacetyl chloride at concentration ratio of 1:1.1:1.05, adding water, reacting at 25-45 degrees C, washing and vacuum dehydrating.    USE - Method for synthesizing metolachlor (claimed).    ADVANTAGE - The method is simple and solvent-free, and reduces production cost and pollution.
NOVELTY - This utility model relates to the field of chemical raw material and agricultural products deep processing and fermentation, specifically relates to a solid conical nozzle spray dispenser for falling film evaporator, comprising a real-time core conical nozzle spray distributor main body, wherein said solid core conical nozzle spray distributor main body comprises a multi-suspension with a liquid material, and is a one of a multi-suspension with a liquid material directly contact of the spray atomization dispersion of a solid conical nozzle, the solid core conical nozzle is single hole nozzle, a solid core taper under the nozzle a liquid point material the spray atomization dispersed distribution of, the spray atomization of a liquid dispersion point material lower part is the one time distribution of overflow. Because of using the a technology plan, this utility new type using solid core conical nozzle spray distribution technology, a valid o and a uniformity of a multi-suspension with a liquid film of a vertical falling film tube for a falling film evaporator, increase the using effect of falling film evaporator.
NOVELTY - This utility new type claims a improved structure of a hydrogen oxygen generate a machine group, comprising of two mirror image set into a plastic assembly base, set has a positive electrode for mounting the positive electrode plate is used for mounting the cathode and of the negative electrode plate, the anode groove and cathode nest nest groove in vertical direction is a interval distribute at two end part plastic assembly base is, in a positive electrode nest groove has a first contact shrapnel, a cathode nest groove set with a second contact elastic sheet, the positive electrode plate through the first contact elastic sheet b is inserted into this nest groove inner anode, negative electrode plate through second contact elastic sheet b nagetive nest is inserted into inner groove, and the positive electrode plate has a electric conduction screw connection at the notch position of anode nest groove, also set with negative electrode plate and connection of electric conduction screw at the notch position of cathode nest groove are set with equal upper has a positive electrode plate and a negative electrode plate, a matching is pyramid. This utility new type after the electric conduction efficiency and to increase the tip discharge circuit, a reinforcing efficiency of hydrogen and oxygen.
NOVELTY - The method involves sending a part of a formed liquid (15) to a stripping column (K1) to produce an overhead gas (21), which is enriched in hydrogen. A bottom liquid (19) is depleted with the hydrogen, and the hydrogen-depleted liquid is divided into first and second portions (27, 29). The first portion is fed in liquid form to a separation column (K2), and the second portion is vaporized and sent in gaseous form to the separation column. A methane rich stream (41) in a bottom of the separation column is withdrawn, and carbon monoxide (43) is flowed at a head of the column separation.    USE - Method for separation of cryogenic distillation of hydrogen, carbon monoxide and methane mixture.    ADVANTAGE - The methane rich stream in the bottom of the separation column is withdrawn, and carbon monoxide is flowed at the head of the column separation, thus reducing variations of temperature in an exchanger of a separation apparatus and separating the cryogenic distillation of hydrogen, carbon monoxide and methane mixture with reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for separation of cryogenic distillation of hydrogen, carbon monoxide and methane mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a pneumatic circuit diagram of an apparatus for separation of cryogenic distillation of hydrogen, carbon monoxide and methane mixture.    Stripping column (K1)    Separation column (K2)    Formed liquid (15)    Bottom liquid (19)    Overhead gas (21)    Portions of hydrogen-depleted liquid (27, 29)    Methane rich stream (41)    Carbon monoxide (43)
NOVELTY - Fertilizer comprises chitin and/or chitosan or chitin and/or chitosan-containing product, and/or culture of microorganism with chitin and/or chitosan resolution.    USE - The fertilizer is useful as product or activating agent for stimulation of rooting of plant, and increasing taste and degree value of rice (all claimed).    ADVANTAGE - The fertilizer stimulates growth of plant, increases yield of agricultural products, prepares agricultural products with high quality, and has low molecular weight.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) cultivation method of a plant, involves processing a plant with the fertilizer;    (2) method for preparing the fertilizer, involves mixing the culture of microorganism with chitin and/or chitosan resolution with chitin and/or chitosan or chitin and/or chitosan-containing product; and    (3) method for preparing low molecular weight chitin and/or chitosan, involves mixing the chitin and/or chitosan or chitin and/or chitosan-containing product, and/or culture of microorganism with chitin and/or chitosan resolution with reducing agent.
NOVELTY - Multistage cultivation of microalgae, comprises: culturing a microalgae in a culture medium in an incubator, and forming biofilm in the liquid level of the culture medium.    USE - The methods are useful for multistage cultivation of microalgae, and for manufacturing algal biomass (claimed).    ADVANTAGE - The method can be efficiently used in preparing algal biomass which is oil which can be used in preparing fuel, and where the method uses inexpensive apparatus, and lower amount of energy when processing.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of manufacturing algal biomass containing microalgae, comprises: recovering algae propagated according to the culturing process; and    (2) an apparatus for enforcing the method.
NOVELTY - This utility new type is a collecting and processing system of garbage landfill marsh gas, pipe wall and bottom of the porous collection tube set has a plurality of air inlet hole, a covering air inlet hole has a net body, and it further comprises inner ring fixing connected on upper end of the frame body in the annular clapboard is a tube of porous collection tube outside wall, the lower side surface of the annular clapboard, upper end of the porous collection tube has air pipe is mounted with a valve, outside end of exhaust pipe has a fan, further comprising through discharge pipe and a fan of a marsh gas pool, upper end of marsh gas pool set has a air outlet pipe, marsh gas pool is further equipped with a adding hopper and has mounting has a pH meter. Effective to avoid the porous collection tube is buries leachate. Especially suitable for the landfill and not reserved marsh gas collection pipeline of refuse landfill.
NOVELTY - This utility new type relates to a hydrodynamic adding one, does not consume the electric energy, energy-saving and environment-friendly, convenient mounting, operation is simple. This utility new type including feeder main body, feeder main body comprising a fixed upper shell and a lower shell, c is a shell body set with a piston mechanism, a lower shell set with lumen with a injector mechanism, a piston connecting rod in the piston mechanism across circular hole of lower shell, and injector mechanism of injector plunger in fixed connection, the main body front part set with a doser drug mechanism.
NOVELTY - A biogas microbiological purification method involves removing impurities, particularly hydrogen sulfide under anaerobic conditions using a biofilter plant bearing a trickle filled with biological fluid nutrient solution, which comprises immobilized microorganisms capable of decomposition of sulfur compounds, and spraying biofilter medium in the form of a solution containing nitrates of alkali metal salts I and II of the Periodic Table, where the concentration of nitrate ions in the medium is 20-2500 mg/l, while the concentration of the feed to the installation is 100-3000 ppm.    USE - Method for microbiological purification of biogas formed in the methane fermentation of organic deposits in a fermentation tank.
NOVELTY - This utility new type claims a fermentation tank a sterilizing waste heat steam heat recovery device, comprising fermentation tank sterilizing waste hot steam discharging pipe, cyclone separator, a heat exchanger, a water tank, circulation pump and the second heat exchanger, the fermentation tank sterilizing air inlet of waste heat steam pipe and a cyclone separator connected, the air outlet of cyclone separator connected a heat exchanger of heat inlet, cold flow outlet of the first heat exchanger by cold flow entrance of hot water circulation system and a heat exchanger connected, a water circulation device comprises pipeline connected by a hot water tank, circulation pump and the second heat exchanger, hot water circulation through a supplement water valve and water source connected. This utility new type comprises a recovery use rate is high, energy-saving and environment-friendly equal.
NOVELTY - An improved beta-glucosidase comprising a polypeptide having at least 70% sequence identity to SEQ ID NO. 2, 4, 6, 8, 10, 12 or 14, and having improved beta-glucosidase activity compared to a control beta-glucosidase comprising SEQ ID NO. 2, is new. Sequences not defined here may be defined at ftp://ftp.wipo.int/pub/published_pct_sequences/publication    USE - The improved beta-glucosidase is useful for converting cellulose-containing biomass feedstock into sugar (claimed), e.g. glucose.    ADVANTAGE - The improved beta-glucosidase has improved beta-glucosidase activity compared to a control beta-glucosidase. It has improved kinetic properties compared to the control beta-glucosidase, where the improved kinetic properties are selected from increased catalytic efficiency (Kcat/Km/minute), increased maximum velocity (Vmax), and/or increased turnover number (Kcat/minute) (all claimed). It can increase the conversion of cellobiose to glucose, and can improve saccharification efficiency.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) a polynucleotide comprising a nucleic acid encoding the improved beta-glucosidase;    (2) a vector comprising the polynucleotide;    (3) an isolated cell or culture of cells, where the cell(s) comprise the polynucleotide, and where the polynucleotide is heterologous to the cell; and    (4) a method for converting a cellulose-containing biomass feedstock into a sugar, comprising treating the biomass with the improved beta-glucosidase, or with a cell that expresses the improved beta-glucosidase.
NOVELTY - Method for increasing yeast biomass, involves culturing yeast cells in growth medium comprising at least one fermentable carbon source, and nonfermentable carbon source.    USE - The method is useful for increasing yeast biomass which is useful in food industry, biofuel industry to produce ethanol, and medicinal field to produce e.g. antibiotics.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for increasing growth rate and biomass of the yeast strains engineered to metabolize naturally nonmetabolized carbon sources.
NOVELTY - Solid waste reutilization involves mixing recycled household waste and rubble from construction with binder mass. A viscose pulp is prepared by exothermic reaction with adequate mechanical strength to serve as a binder component.    USE - Method of reusing solid waste for manufacturing bricks and related products.    ADVANTAGE - The method provides mechanically sufficient and valuable chemical substances contained in solid and semisolid waste from recycled common garbage and debris from civil engineering.
NOVELTY - A treatment agent for in-situ repairing of soil polluted with heavy metal and organic matter comprises mixture A comprising 100 mass parts Hangjin number 2 soil (RTM: Natural clay mineral), 10-30 mass parts activated carbon, 20-50 mass parts cement, and 2-5 mass parts organic flocculating agent, and mixture B comprising 16-32 mass parts sodium thiosulfate and optionally greater than or equal to 2 of 16-32 mass parts ferric oxide, 48-96 mass parts calcium sulfate, 32-80 mass parts aluminum sulfate, and/or 16-32 mass parts alkali metal carbonate in which mixture B total amount is 20-30 mass%.    USE - Treatment agent for in-situ repairing of soil polluted with heavy metal and organic matter (claimed).    ADVANTAGE - The agent effectively absorbs heavy metal and difficult biodegradable organic pollutant, avoids re-release of pollutants in water body or plants, has no negative impact on soil, achieves single and normal land farming, and reduces work amount and difficulty.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparation of treatment agent which involves uniformly mixing raw materials of mixture A, uniformly mixing raw materials of mixture B, adding mixture B to mixture, and uniformly mixing to obtain powder-shaped mixture; and    (2) use of treatment agent for in-situ repairing of soil polluted with heavy metal and organic matter which involves applying of treatment agent having 1-5 cm thickness to soil surface polluted with heavy metal, applying treatment agent having 20 cm thickness in polluted topsoil, and uniformly mixing through turning.
NOVELTY - Conversion of microbial fermentation liquid fertilizer animal manure into organic fertilizer comprises taking 0.5-1 pt. wt. effective microorganisms, adding 0.5-1 pt. wt. actinomycetes and 0.5-1 pt. wt. rhizobia bacteria, mixing, and standing for 1-2 hours to obtain microorganism liquid; taking 150-250 pts. wt. crop straw powder or weed powder, 750-850 pts. wt. animal excrement powder, and 350-400 pts. wt. water, mixing, adding microorganism liquid, and anaerobic fermenting; adding microzyme and photosynthetic bacteria, and anaerobic fermenting; and drying and granulating.    USE - Method for converting microbial fermentation liquid fertilizer animal manure into organic fertilizer (claimed).    ADVANTAGE - The method is simple and leads to probiotics and other beneficial microorganism. The raw materials effectively utilize soil nutrients, phosphate, potassium, and nitrogen fixation. The fertilizer has reduced dosage and good efficiency, does not easily decompose plant nutrients, effectively removes soil compaction, and increases production.    DETAILED DESCRIPTION - Conversion of microbial fermentation liquid fertilizer animal manure into organic fertilizer comprises taking 0.5-1 pt. wt. effective microorganisms, adding 0.5-1 pt. wt. actinomycetes and 0.5-1 pt. wt. rhizobia bacteria, mixing, and standing for 1-2 hours to obtain microorganism liquid; taking 150-250 pts. wt. crop straw powder or weed powder, 750-850 pts. wt. animal excrement powder, and 350-400 pts. wt. water, mixing, adding microorganism liquid, and anaerobic fermenting for 4-15 days; adding 0.5-1 pt. wt. microzyme and 0.5-1 pt. wt. photosynthetic bacteria, and anaerobic fermenting for 4-10 days; and drying and granulating.
NOVELTY - This new utility model claims of one jet cleaning of blanching machine, it includes material transfer system, orderly installed on material transmission system upper part of circulation water jet washing system, the clean water jet wash out system, air blowing dewatering system and steam jet blanching system. This new utility model providing the jet cleaning scalding, structure reasonable design, may strong operability, automatic degree high, using suitable, clean process and the corresponding medicine material damage, high cleanliness, clean large amount, work intensity low, can continue production, energy saving, environmental protection, application range is very wide.
NOVELTY - Preparing biomass involves filling seawater in photobioreactor and then cultivating microalgae. Greenhouse gasses and compressed air are supplied into photobioreactor. Nutrients are supplied into photobioreactor. Cultivated microalgae are cultured to obtain microalgae culture. The microalgae culture is disinfected and then centrifuged to obtain biomass. The obtained biomass is dried and then hydrolysed to obtain hydrolyzed product. The hydrolyzed product is dried at 200-350 degrees C for 25-90 degrees C to obtain the final product.    USE - Method for preparing biomass used for as food for animals or fish (claimed).    ADVANTAGE - The method enables to prepare biomass by utilizing greenhouse gasses mainly carbon dioxide and is eco-friendly.
NOVELTY - Sarcandra glabra fertilizer comprises 60-80 pts. wt. sheep manure, 80-100 pts. wt. rabbit manure, 40-60 pts. wt. silkworm excrement, 15-17 pts. wt. nitrogen fertilizer, 13-15 pts. wt. phosphate fertilizer, 14-16 pts. wt. potassium fertilizer, 10-12 pts. wt. Caryopteris ovata, 20-30 pts. wt. protein slurry, 8-10 pts. wt. furfural residue, 3-5 pts. wt. amino acid, 2-4 pts. wt. humic acid, 20-30 pts. wt. lard residue, and 120-130 pts. wt. water.    USE - Fertilizer for Sarcandra glabra (claimed).    ADVANTAGE - The fertilizer improves soil environment and increases crop yield. Production process does not generate pollution and plant quality is ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by mixing raw materials, crushing, sealed fermenting for 5-7 days, and granulating.
NOVELTY - A fluorescent quantum dot comprises gadolinium (Gd)-doped silver sulfide (Ag2S) quantum dot. The Gd doping amount is based on a Gd/silver (Ag) mole ratio of (1:10)-(1:160).    USE - Fluorescent quantum dot used in magnetic resonance imaging (claimed) as contrast agent.    ADVANTAGE - The fluorescent quantum dot has low toxicity and high stability, and can have dual function as core magnetic resonance imaging contrast agent as it exhibits visible and near-infrared wave band-adjustable fluorescence property. It can be prepared using simple process which is easy to operate, green and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fluorescent quantum dot, comprising:    (1) dissolving silver acetate, gadolinium chloride, oleic acid and hexadecyl mercaptan in octadecene, raising the temperature to 50-120 degrees C;    (2) injecting with sulfur-hexadecyl mercaptan solution, and then holding for 20 minutes to form Gd-doped Ag2S quantum dot; and    (3) adding with acetone or ethyl alcohol to enable quantum dot precipitation, and then dispersing in chloroform or hexane solvent to obtain purified Gd-doped Ag2S quantum dot.    In step (1), the gadolinium chloride and silver acetate are utilized based on a Gd/Ag mole ratio of (1:10)-(1:160); and the oleic acid and hexadecyl mercaptan are utilized as ligand in an amount which is based on stoichiometric ratio. In step (2), the sulfur is utilized based on predetermined stoichiometric amount.
NOVELTY - Grapes organic fertilizer comprises 1-3 pts. wt. potassium chloride, 2-4 pts. wt. ammonium chloride, 1-3 pts. wt. urea, 1-3 pts. wt. ammonium phosphate, 4-6 pts. wt. chicken manure, and 1-3 pts. wt. humic acid. It is prepared by pulverizing chicken manure; putting into fermenter; adding amino acid inactive probiotic bacteria to obtain probiotic mixture; pulverizing potassium chloride, ammonium chloride, urea and monoammonium phosphate; putting materials into mixer; adding probiotic mixture; mixing; putting mixture into granulator; and adding humic acid.    USE - Grapes organic fertilizer.    ADVANTAGE - The fertilizer has simple preparation, long-term efficiency, multifunctional effect, enhances soil fertility by modifying physical and chemical properties of soil, has rich organic matter, improves grapes quality, prevents soil acidification and salinization, and enhances soil aggregate structure.    DETAILED DESCRIPTION - Grapes organic fertilizer comprises 1-3 pts. wt. potassium chloride, 2-4 pts. wt. ammonium chloride, 1-3 pts. wt. urea, 1-3 pts. wt. ammonium phosphate, 4-6 pts. wt. chicken manure, and 1-3 pts. wt. humic acid. It is prepared by pulverizing chicken manure; putting into fermenter; adding amino acid inactive probiotic bacteria to obtain probiotic mixture; pulverizing potassium chloride, ammonium chloride, urea and monoammonium phosphate; putting materials into mixer; adding probiotic mixture; mixing; putting mixture into granulator; adding humic acid; granulating; drying granulated particles; cooling; sieving to remove particles that do not meet specifications; coating granules with coating film; drying; weighing and packaging; and inspecting.
NOVELTY - Preparation of cellulose bead involves mixing alkali/urea water or alkali/thiourea water solution, cooling to - 12-- 5 degrees C, adding cellulose, stirring to dissolve, removing foam, edulcorating, drawing mixture into syringe by injection extrusion, adding curing liquid and washing with distilled water.    USE - Method for preparing cellulose bead (claimed).    ADVANTAGE - The method has wide applicability and good stability. It is inexpensive, convenient, non-toxic, environmental-friendly, and suitable for large scale preparation.
NOVELTY - The cell has an anode room filled with inner containing lead ion waste water. A cathode room is filled with electric production germ and cathode liquid, where nucleotide sequence of the electric production germ is SEQ ID No.1 and the cathode liquid is selected from sodium acetate, ammonium Perchlorate and potassium hypochlorite. A graphite plate surface is fixed in the anode room and the cathode room. The anode room is mounted with a graphite plate.    USE - Process leaded sewage micro-organism fuel cell for profitable industry.    ADVANTAGE - The cell effectively separates lead ion and lead-containing sewage, and effectively degrades and removes ammonia nitrogen and organic matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a graphical view illustrating a process leaded sewage micro-organism fuel cell.'(Drawing includes non-English language text)'
NOVELTY - Phyto fortifying material preparation involves mixing a sugar source and a protein source, and then mixing them with microbial metabolites. The obtained material is performed for dissolution, and then fermented them under aerobic conditions and thermophilic controlled.    USE - Method for preparing phyto fortifying material used as bioenhancer fertilizer for growing plants (Claimed).    ADVANTAGE - The method enables to prepare phyto fortifying material in eco-friendly manner, and ensures reduced toxicity or hazard to humans or animals.
NOVELTY - The carbonization gas is recovered from feedstock in a low temperature gasifier (1), and is converted to synthesis gas in a high temperature gasifier (2) by partial oxidation with subsequent partial reduction. A cooling device (30) is provided in downstream of high-temperature gasifier to cool synthesis gas to a temperature at which alkalis in synthesis gas remains in gaseous phase and having no stickiness of coke particles in synthesis gas. A cyclone device (4) is provided in downstream of cooling device to separate coarse fraction of coke particles from synthesis gas.    USE - Method for partial gasification of solid organic feedstock e.g. biomass.    ADVANTAGE - The partial gasification of solid organic feedstock is improved and the effective utilization of the residual coke is ensured.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for partial gasification of solid organic feedstock.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for partial gasification of solid organic feedstock.    Low temperature gasifier (1)    High temperature gasifier (2)    Cyclone device (4)    System for partial gasification of solid organic feedstock (10)    Cooling device (30)
NOVELTY - The system (100) has a low temperature gasifier system utilized for recovery of tar-containing carbonization gas by smoldering feed material. A high temperature gasifier system is utilized for conversion of the carbonization gas by partial oxidation and subsequent partial reduction of synthesis gas. The low temperature gasifier system comprises two independently operated low temperature gasifiers (101). The high temperature gasifier system comprises multiple independently operated high temperature gasifiers (102). Each low temperature gasifier is made of different feed materials.    USE - System for partial gasification of solid organic feed material i.e. charcoal or biomass such as old forest residue timber or energy woods, for cleaning pipe lines. Can also be used for agricultural residual substances such as straws or chaff.    ADVANTAGE - The system comprises two independently operated low temperature gasifiers and/or independently operated high temperature gasifiers, so that optimum utilization of capacity of the system can be achieved in a simple manner. The system can be constructed with maximum capacity of the high temperature gasifier system or an individual high temperature gasifier, thus saving investment costs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for partial gasification of solid organic feed material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a system for partial gasification of solid organic feed material.    System for partial gasification of solid organic feed material (100)    Low temperature gasifiers (101)    High temperature gasifiers (102)    Spacer (105)    Common spacer line (110)
NOVELTY - The sludge disposal system has digester (1) which generates sewage gas that contains methane gas by introducing sludge with a total solids (TS) concentration of 4 to 12 percent, and performs anaerobic digestion of the sludge and digested sludge. A dehydrator (3) spin-dehydrates the digested sludge and obtains a dewatering cake, and a drying machine (4) dries the dewatering cake and obtains dried sludge. A sewage-gas supply line (GL1-GL3) supplies sewage gas emitted to the digester to the heating apparatus (2) and heat supply apparatus (5).    USE - Sludge disposal system.    ADVANTAGE - Reduces the carbon dioxide discharge amount since the quantity of the supplementary fuel used inside the whole system can also be reduced. Achieves moisture content reduction of the dewater cake since the dehydration of a digested-sludge concentrate can also be improved. Improves the efficiency since the heat amount required for the heating of digester and heat supply for carbonization can be supplemented 100 percent.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sludge disposal method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a sludge disposal system. (Drawing includes non-English language text).    Digester (1)    Heating apparatus (2)    Dehydrator (3)    Drying machine (4)    Heat supply apparatus (5)    Sewage-gas supply line (GL1-GL3)
NOVELTY - Concentration of methane gas involves flowing gas containing methane gas in primary side of gas permeable film (24) of gas permeable film module (14) in which inside is equipped with gas permeable film such that primary side and secondary side of film are isolated, and pouring liquid to secondary side of gas permeable film of the gas permeable film module.    USE - Concentration of methane gas discharged from anaerobic digestion of waste materials e.g. livestock excrement, city garbage refuse and sludge of sewage works.    ADVANTAGE - The method enables simple and economical concentration of methane gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for concentration apparatus (1) of methane gas, which consists of gas permeable film module equipped with gas permeable film, gas supply unit (10) to supply gas containing methane gas in primary side of the gas permeable film, and liquid supply unit (12) to supply liquid to the secondary side of the gas permeable film.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the concentration apparatus.    Concentration apparatus (1)    Gas supply unit (10)    Liquid supply unit (12)    Gas permeable film module (14)    Gas permeable film (24)
NOVELTY - The manufacturing method involves heating and dry-distilling biomass using the continuous dry distillation system installation of the heat tracing. The temperature increase rate is between 300 to 400 degrees Celsius or less. The biomass is a palm tree core shell (8).    USE - Manufacturing method of biomass charcoal for sintered-ore manufacture.    ADVANTAGE - Produces the biomass charcoal suitable for sintering use in high yield and high production rate without using complicated apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows the outline of the external heating type rotary kiln used for experiment. (Drawing includes non-English language text).    External heating type rotary kiln (1)    Heating part (2)    Heating wire (3)    Thermocouple (4)    Drive part (5)    Palm core shell hopper (6)    Seal cover (7)    Palm tree core shell (8)
NOVELTY - Sequestration of carbon from flue gases emitted by municipal solid waste to energy plant involves burning a mixture of oxidant and municipal solid waste to generate flue gas and products of combustion, streaming the generated flue gas and the products of combustion into a high-temperature reactor, adding fuel and water to high-temperature reactor to produce hydrogen and reaction products in balanced steam-fuel-reformation reaction, transferring reaction products to a low-temperature reactor, and combining the reaction products with sodium hydroxide to form sodium carbonate.    USE - Sequestration of carbon from flue gases emitted from incineration of municipal solid waste e.g. energy plant food, kitchen waste, green waste, paper waste, glass, bottles, cans, metals, plastics, fabrics, clothes, batteries, construction and demolition waste, dirt, rocks, debris, electronic appliances, computer equipment, paints, chemicals, light bulbs and fluorescent lights, fertilizers, and medical waste.    ADVANTAGE - The method enables sequestration of carbon with suppressed generation of chlorine and carbon emission. The refuse derived fuel gases produced by burning municipal solid waste will not be released to the atmosphere but directed to reactor for further conversion to hydrogen and bicarbonate.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the series of reactors for sequestration of carbon.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heated at 85-125 degrees C for 25 minutes to obtain the mixture. The mixture is stirred for 25 minutes and then centrifuged to obtain urea phosphate, where molar ratio of phosphoric acid and carboxamide is 2:1.3-1.7. Ammonium hydroxide is added into urea phosphate and then stirred to obtain to obtain another mixture, where pH of mixture is 3.1-3.7. the obtained mixture is cooled to 25 degrees C to obtain crystal. The crystal is filtered and then centrifuged to obtain ammonium dihydrogen phosphate and filter liquid.    USE - Method for preparing fertilizer used for orange tree (claimed).    ADVANTAGE - The method enables to prepare fertilizer that reduces waste, is economic and eco-friendly.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heated at 85-125 degrees C for 25 minutes to obtain the mixture. The mixture is stirred for 25 minutes and then centrifuged to obtain urea phosphate, where molar ratio of phosphoric acid and carboxamide is 2:1.3-1.7. Ammonium hydroxide is added into urea phosphate and then stirred to obtain to obtain another mixture, where pH of mixture is 3.1-3.7. the obtained mixture is cooled to 25 degrees C to obtain crystal. The crystal is filtered and then centrifuged to obtain ammonium dihydrogen phosphate and filter liquid. Element is added into filter liquid, heated at 35 degrees C and then dried for 25 minutes to obtain the product.
NOVELTY - Preparing fertilizer involves stirring urea and phosphoric acid at pH of 3.6-4.4 for 80-125 minutes. Ammonium hydroxide is reacted with reaction mixture at 102-107 degrees C. The mixture slurry is crystallized at 23-28 degrees C. The crystallization is stopped when nitrogen and phosphorus contents are adjusted. The crystallized slurry is filtered to obtain filtrate and ammonium dihydrogen phosphate cake. Trace elements are mixed with obtained filtrate to obtain solution that is heated at 30 degrees C for 34 minutes to obtain fertilizer.    USE - Method for preparing fertilizer used for cultivating sweet wormwood (claimed).    ADVANTAGE - The method enables to prepare fertilizer in eco-friendly and cost-effective manner, and ensures high purity and no discharge of liquid waste.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carboxamide in mol ratio of 1.2-1.4:1 at 100-130 degrees C for 160-200 minutes by using a container to obtain a mixture. The mixture is cooled to 20-40 degrees C and separated to obtain intermediate product. Intermediate product is mixed with ammonium hydroxide in mol ratio of 1:4-6 and stirred at 15-25 degrees C for 40-60 minutes to maintain pH value to 8-9 to obtain a product. The product is cooled and crystallized by using a crystallizer to obtain filter liquid, and then nitrogen (12-14%), phosphorus (6-7%) and potassium (12-14%) are mixed.    USE - Method for preparing fertilizer for nutritioning apple (claimed).    ADVANTAGE - The method enables to prepare fertilizer in a cost-effective manner, does not discharges waste liquid to pollute environment. The fertilizer is suitable for growing apple.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carboxamide in mol ratio of 1.2-1.4:1 at 100-130 degrees C for 160-200 minutes by using a container to obtain a mixture. The mixture is cooled to 20-40 degrees C and separated to obtain intermediate product. Intermediate product is mixed with ammonium hydroxide in mol ratio of 1:4-6 and stirred at 15-25 degrees C for 40-60 minutes to maintain pH value to 8-9 to obtain a product. The product is cooled and crystallized by using a crystallizer to obtain filter liquid, and then nitrogen (12-14%), phosphorus (6-7%) and potassium (12-14%) are mixed to obtain a filter cake. Ammonium dihydrogen phosphate is mixed with the filter cake and then trace elements are added to obtain a product. The product is heated in a drier at 26-30 degrees C with speed of 3 degrees C per minute to obtain fertilizer.
NOVELTY - Preparing compound fertilizer involves mixing phosphoric acid (70-74%) and urea in mol ratio of 2:1.4-1.6 at 90-120 degrees C for 28 minutes, and then stirred at speed of 6 degrees C per minute to separate urea phosphate. Ammonium hydroxide is mixed with urea phosphate to maintain pH value to 3.2-3.6 and then nitrogen, phosphorus and potassium materials slurry are added to obtain a mixture. The mixture is cooled and crystallized by using a crystallizer to separate ammonium dihydrogen phosphate by-product and obtain a filter liquid. Trace elements are added in the filter liquid to obtain a mother liquid.    USE - Method for preparing ammonium dihydrogen phosphate by-product and compound fertilizer used for grapefruit tree (claimed).    ADVANTAGE - The method enables to prepare compound fertilizer in a cost-effective manner, and reduces discharge of waste liquid to protect environment. The compound fertilizer is suitable for growing grapefruit tree.    DETAILED DESCRIPTION - Preparing compound fertilizer involves mixing phosphoric acid (70-74%) and urea in mol ratio of 2:1.4-1.6 at 90-120 degrees C for 28 minutes, and then stirred at speed of 6 degrees C per minute to separate urea phosphate. Ammonium hydroxide is mixed with urea phosphate to maintain pH value to 3.2-3.6 and then nitrogen, phosphorus and potassium materials slurry are added to obtain a mixture. The mixture is cooled and crystallized by using a crystallizer to separate ammonium dihydrogen phosphate by-product and obtain a filter liquid. Trace elements are added in the filter liquid to obtain a mother liquid. The mother liquid is heated to dry at 38 degrees C for 24 minutes to obtain compound fertilizer.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heating at 100-120 degrees C for 100-120 minutes to obtain mixture, where molar ratio of phosphoric acid and carboxamide is 1.1-1.3:1. The mixture is cooled to 30-45 degrees C to obtain intermediate. Alkaline potassium salt is added into intermediate and then mixed to obtain to obtain another mixture, where mixture pH value is 10-12. The obtained mixture is cooled to obtain crystal. The crystal is filtered to obtain filtrate, where filtrate comprises nitrogen, phosphorus, potassium in molar ratio of 9-11:1:5.5-6.5.    USE - Method for preparing fertilizer (claimed) used for bamboo.    ADVANTAGE - The method enables to increase yield of bamboo, does not produce waste discharge and thus does not pollute environment.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heating at 100-120 degrees C for 100-120 minutes to obtain mixture, where molar ratio of phosphoric acid and carboxamide is 1.1-1.3:1. The mixture is cooled to 30-45 degrees C to obtain intermediate. Alkaline potassium salt is added into intermediate and then mixed to obtain to obtain another mixture, where mixture pH value is 10-12. The obtained mixture is cooled to obtain crystal. The crystal is filtered to obtain filtrate, where filtrate comprises nitrogen, phosphorus, potassium in molar ratio of 9-11:1:5.5-6.5. Trace element and bamboo are added into filtrate and then heated at 25-30 degrees C to obtain third mixture. The obtained mixture is dried for 40-60 minutes to obtain the product.
NOVELTY - Preparing fertilizer used for improving growth of lettuce, involves mixing phosphoric acid and carboxamide and heating to obtain mixture, cooling mixture to obtain intermediate and adding alkaline potassium salt Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heating at 85-105 degrees C for 3-5 hours to obtain mixture, where molar ratio of phosphoric acid and carboxamide is 1.6-2.1:1. The mixture is cooled to 55-85 degrees C to obtain intermediate. Alkaline potassium salt is added into intermediate and then mixed to obtain another mixture, where mixture pH value is 8-9.5.    USE - Method for preparing fertilizer used for lettuce (claimed).    ADVANTAGE - The method enables to prepare fertilizer in a cost effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heating at 85-105 degrees C for 3-5 hours to obtain mixture, where molar ratio of phosphoric acid and carboxamide is 1.6-2.1:1. The mixture is cooled to 55-85 degrees C to obtain intermediate. Alkaline potassium salt is added into intermediate and then mixed to obtain another mixture, where mixture pH value is 8-9.5. The obtained mixture is cooled to obtain crystal. The crystal is filtered to obtain filtrate, where filtrate comprises nitrogen, phosphorus pentoxide, and potassium oxide in molar ratio of 2-2.4:1-2:1.8-2.4. Trace element is added into filtrate and then heated at 45-55 degrees C to obtain third mixture. The obtained mixture is dried for 0.6-0.9 hours to obtain the product.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heating at 95-160 degrees C for 4-5 hours to obtain mixture, where molar ratio of phosphoric acid and carboxamide is 1.3-1.6:1. The mixture is cooled to 30-35 degrees C to obtain intermediate. Calcium carbonate is added into intermediate and then mixed with yeast to obtain fermentation mixture, where mixture pH value is adjusted to 3.2 using phosphoric acid. The obtained mixture is cooled to obtain crystal. The crystal is filtered to obtain filter cake, where filter cake comprises 20-25% nitrogen, 6-11% phosphorus, and 6-17% potassium.    USE - Method for preparing fertilizer used for improving growth of millet (claimed).    ADVANTAGE - The method enables to prepare fertilizer that increases yield of millet.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carboxamide and then heating at 95-160 degrees C for 4-5 hours to obtain mixture, where molar ratio of phosphoric acid and carboxamide is 1.3-1.6:1. The mixture is cooled to 30-35 degrees C to obtain intermediate. Calcium carbonate is added into intermediate and then mixed with yeast to obtain fermentation mixture, where mixture pH value is adjusted to 3.2 using phosphoric acid. The obtained mixture is cooled to obtain crystal. The crystal is filtered to obtain filter cake, where filter cake comprises 20-25% nitrogen, 6-11% phosphorus, and 6-17% potassium. Sodium hydroxide and phosphoric acid are added into filter cake and then filtered to obtain filtrate. Formaldehyde solution is added into filtrate and then heated to obtain third mixture. Trace element is added into obtained mixture, recrystallized the mixture and then granulated to obtain granules. The granules are dried to obtain the product.
NOVELTY - Preparing copper bismuth sulfide crystal involves dissolving copper(II) chloride and bismuth(III) nitrate in ethylene glycol and then adding diethyl dithiocarbamate to obtain mixture. The obtained mixture is filtered and then washed with deionized water to obtain precursor, where molar ratio of copper(II) chloride and bismuth(III) nitrate is 3:1. The precursor is completely dissolved in solvent, ligand is added into it and then stirred to obtain another mixture. The obtained mixture is centrifuged and then washed to obtain the product.    USE - Method for preparing copper bismuth sulfide crystal used for diagnozing and treating cancer (claimed).    ADVANTAGE - The method enables to prepare copper bismuth sulfide crystal in a simple, cost-effective and eco-friendly manner.
NOVELTY - Processing cow dung involves collecting cow dung and transporting into anaerobic reactor. The cow dung is fermented in an anaerobic reactor to covert nitrogen-containing organic matter into ammonia and methane. The cow dung is treated in aerobic reactor to obtain solid waste.    USE - Method for processing cow dung used as fertilizer (claimed).    ADVANTAGE - The method enables to process cow dung in a simple and cost-effective manner.
NOVELTY - Material fermentation involves including carriers and beneficial microbial agents, and then mixing them. The obtained material is dried at low-temperature, granulated, and then packed to obtain the finished product.    USE - Method for fermenting material used as biological organic fertilizer (claimed).    ADVANTAGE - The method enables to ferment material in simple and cost-effective manner, ensures improved sustainable development of animal husbandry.
NOVELTY - Green fertilizer composition comprises 1-2 pts. wt. deciduous tree leaves, 10-30 pts. wt. milkvetch, 3-5 pts. wt. Camellia and 1-2 pts. wt. paper.    USE - Green fertilizer composition used for preventing and curing underground pests of crop (claimed).    ADVANTAGE - The green fertilizer composition is prepared in eco-friendly manner, ensures improved soil environment and prevented soil compaction.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a green fertilizer composition, which involves:    (A) mixing raw materials under phosphorus smoking environment for 15-20 minutes;    (B) forming cushion layer of the obtained material, and then spraying lime water on the obtained material and sealing them;    (C) fermenting the obtained material at 65-70 degrees C for 3-5 days; and    (D) piling the fermented material, and then fermenting the obtained material at 50-65 degrees C for 20-25 days to obtain the finished product.
NOVELTY - Organic fertilizer comprises 0.015-0.02 pts. wt. sodium selenate, 28-36 pts. wt. bran, 8-10 pts. wt. soybean, 4-5 pts. wt. vegetables, 12-15 pts. wt. chicken manure, 40-50 pts. wt. water, 0.6-0.7 pts. wt. complex microbial fermentation agent, 2-3 pts. wt. nutritional agent, and 15-20 pts. wt. corn powder.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer is rich in nutrients and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) drying bran and then crushing it to obtain bran powder;    (B) mixing soybean shell, vegetables and chicken manure to obtain mixture;    (C) mixing complex microbial fermentation, nutritional agent, bran powder and mixture, and then fermenting at 25-35 degrees C for 4 days to obtain fermentation material; and    (D) adding sodium selenate into fermentation material and then mixing to obtain the product.
NOVELTY - Copper passivation of pig manure involves mixing fresh pig manure with crushed wheat stick and 6.3% sepiolite powder. The obtained mixture is mixed with 2.5-10% coal ash and 1.5-6% stone powder, and then the obtained material is mixed with water. The obtained mixture is performed for aerobic fermentation for 40 days to obtain the finished product.    USE - Method for performing copper passivation of pig manure (claimed) used as fertilizer for preventing root rot.    ADVANTAGE - The method enables to perform copper passivation of pig manure, ensures improved growth of plants.
NOVELTY - Biological organic fertilizer preparation involves taking 100-200 pts. wt. active sludge, 100-180 pts. wt. traditional Chinese medicine slag, 0.15-1.5 pts. wt. biological active agent, 10-15 pts. wt. fly ash and balanced amount of animal protein, and then mixing active sludge and traditional Chinese medicine slag. The obtained mixture is mixed with animal protein, fly ash and biological active agent, and then water content of the obtained material is regulated. The obtained material is fermented at 55-65 degrees C for 3-5 days, and then at 60-70 degrees C for 15 days to obtain the finished product.    USE - Method for preparing biological organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare biological organic fertilizer in a simple manner, ensures reduced odor and improved purification.
NOVELTY - Preparing fertilizer involves adding phosphoric acid and carboxamide in a container and then heating at 80-130 degrees C for 160-190 minutes to obtain mixture. The mixture is cooled at 20-40 degrees C to obtain crystal. The crystal is centrifuged to obtain the intermediate, where molar ratio of phosphoric acid and carboxamide is 1.2-1.4:1. Monocalcium phosphate and alkaline calcium salt is added into intermediate and then heated at 60-80 degrees C to obtain mixture, where pH value of mixture is 8-9.    USE - Method for preparing fertilizer used for promoting growth of wheat (claimed).    ADVANTAGE - The method enables to prepare fertilizer in a simple, cost-effective and eco-friendly manner.    DETAILED DESCRIPTION - Preparing fertilizer involves adding phosphoric acid and carboxamide in a container and then heating at 80-130 degrees C for 160-190 minutes to obtain mixture. The mixture is cooled at 20-40 degrees C to obtain crystal. The crystal is centrifuged to obtain the intermediate, where molar ratio of phosphoric acid and carboxamide is 1.2-1.4:1. Monocalcium phosphate and alkaline calcium salt is added into intermediate and then heated at 60-80 degrees C to obtain mixture, where pH value of mixture is 8-9. The mixture is filtered and then phosphorus pentoxide, potassium oxide and calcium dihydrogen phosphate are added to obtain another mixture. Microelements are added into obtained mixture and then dried to obtain the product.
NOVELTY - Preparing fertilizer involves reacting phosphoric acid and carboxamide in vessel at 80-120 degrees C for 190-210 minutes. The mixture is cooled to 20-40 degrees C to obtain crystal that is centrifuged to obtain intermediate. Ammonia is reacted with intermediate in vessel for 50-70 minutes at 15-25 degrees C at pH 8-9. The reaction mixture is cooled to obtain crystals and then filtered to obtain filtrate and filter cake of ammonium dihydrogen phosphate. The filtrate is mixed with microelement and filter cake to adjust potassium, nitrogen and phosphorus to get mixture that is dried at 26-30 degrees C to obtain product.    USE - Method for preparing fertilizer used for cultivating grape (claimed).    ADVANTAGE - The method enables to prepare fertilizer in cost-effective and eco-friendly manner without discharging waste liquid.
NOVELTY - Organic fertilizer comprises 80-100 pts. wt. tea cake, 30-70 pts. wt. peanut bran, 10-20 pts. wt. ammonium dihydrogen phosphate, 50-80 pts. wt. straw, 30-50 pts. wt. fermented livestock manure, 15-30 pts. wt. humic acid and 8-15 pts. wt. potassium chloride.    USE - Organic fertilizer used for cultivating tea plant (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing organic fertilizer, which involves:    (A) mixing and crushing tea cake, peanut bran and wheat straw to obtain mixture;    (B) mixing mixture with ammonium dihydrogen phosphate, fermented livestock manure, humic acid and potassium chloride with obtained mixture to obtain another mixture;    (C) heating obtained mixture at 30-35 degrees C; and    (D) sealing, sterilizing and drying obtained mixture to obtain product.
NOVELTY - Fertilizer composition comprises 9-11 pts. wt. nitrogenous fertilizer, 5-7 pts. wt. phosphate fertilizer, 8-10 pts. wt. potash fertilizer, 20-30 pts. wt. ammonium sulfate, 13-15 pts. wt. humic acid, 1-3 pts. wt. fermented tobacco stalk, 1-3 pts. wt. Daphne giraldii, 0.7-0.9 pts. wt. (50%) emulsifiable concentrate, 18-20 pts. wt. potassium chloride, 2-4 pts. wt. abamectin residue and 30-40 pts. wt. kelp.    USE - Fertilizer composition used for cultivating leek (claimed) and preventing underground insects.    ADVANTAGE - The fertilizer composition ensures improved yield of leek plant.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a liquid fertilizer composition, which involves:    (A) mixing raw materials with stirring, and then heating them to obtain slurry; and    (B) granulating the obtained material to obtain the finished product.
NOVELTY - Fertilizer composition comprises 1-4 pts. wt. ammonium bicarbonate, 30-35 pts. wt. mushroom residue, 10-20 pts. wt. potassium fulvate, 40-50 pts. wt. chicken manure, 3-8 pts. wt. carboxymethyl chitosan, 6-12 pts. wt. ammonium chloride, 1-5 pts. wt. ferrous sulfate, 10-20 pts. wt. peat, 6-10 pts. wt. rice bran, 4-8 pts. wt. wheat bran, 5-10 pts. wt. leaf, 10-15 pts. wt. feather, 20-40 pts. wt. rice straw, 12-15 pts. wt. monoammonium phosphate, 10-25 pts. wt. carbamide, 6-10 pts. wt. potassium sulfate, 6-10 pts. wt. ammonium sulfate, 4-6 pts. wt. azadirachtin and 2-8 pts. wt. zinc sulfate.    USE - Fertilizer composition used for cultivating flowering plants (claimed).    ADVANTAGE - The fertilizer composition has doubled the effect of fertilizer and pesticide, and is eco-friendly in nature.    DETAILED DESCRIPTION - Fertilizer composition comprises 1-4 pts. wt. ammonium bicarbonate, 30-35 pts. wt. mushroom residue, 10-20 pts. wt. potassium fulvate, 40-50 pts. wt. chicken manure, 3-8 pts. wt. carboxymethyl chitosan, 6-12 pts. wt. ammonium chloride, 1-5 pts. wt. ferrous sulfate, 10-20 pts. wt. peat, 6-10 pts. wt. rice bran, 4-8 pts. wt. wheat bran, 5-10 pts. wt. leaf, 10-15 pts. wt. feather, 20-40 pts. wt. rice straw, 12-15 pts. wt. monoammonium phosphate, 10-25 pts. wt. carbamide, 6-10 pts. wt. potassium sulfate, 6-10 pts. wt. ammonium sulfate, 4-6 pts. wt. azadirachtin, 2-8 pts. wt. zinc sulfate, 2-6 pts. wt. Borax (RTM: Sodium tetraborate) and 2-5 pts. wt. microbial fermentation product. An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves mixing raw materials, and then granulating them to obtain the finished product.
NOVELTY - Multifunctional biofertilizer comprises 5-9 pts. wt. Lactobacillus acidophilus, 4-8 pts. wt. diammonium phosphate, 3-7 pts. wt. sodium alginate, 1-5 pts. wt. ferrous sulfate, 1-5 pts. wt. humic acid, 2-6 pts. wt. sheep manure, 1-4 pts. wt. surface active agent, 2-4 pts. wt. potassium chloride, 3-9 pts. wt. celestite powder, 4-7 pts. wt. oyster shell powder, 1-5 pts. wt. animal bone powder, 4-10 pts. wt. ammonium citrate, 2-5 pts. wt. sweet potato, 2-4 pts. wt. agar, 6-9 pts. wt. monocalcium phosphate, 1-3 pts. wt. bentonite and 4-11 pts. wt. bran.    USE - Multifunctional biofertilizer.    ADVANTAGE - The multifunctional biofertilizer improving soil structure, increases soil fertility, and reduces pollution of soil.    DETAILED DESCRIPTION - Multifunctional biofertilizer comprises 5-9 pts. wt. Lactobacillus acidophilus, 4-8 pts. wt. diammonium phosphate, 3-7 pts. wt. sodium alginate, 1-5 pts. wt. ferrous sulfate, 1-5 pts. wt. humic acid, 2-6 pts. wt. sheep manure, 1-4 pts. wt. surface active agent, 2-4 pts. wt. potassium chloride, 3-9 pts. wt. celestite powder, 4-7 pts. wt. oyster shell powder, 1-5 pts. wt. animal bone powder, 4-10 pts. wt. ammonium citrate, 2-5 pts. wt. sweet potato, 2-4 pts. wt. agar, 6-9 pts. wt. monocalcium phosphate, 1-3 pts. wt. bentonite, 4-11 pts. wt. bran and 0.5-2 pts. wt. Bacillus licheniformis.
NOVELTY - Organic-inorganic compound containing fertilizer comprises 8-14 pts. wt. shale, 1-3 pts. wt. microelement, 5-9 pts. wt. phosphate, 5-7 pts. wt. water soluble silicon, 4-9 pts. wt. yellow phosphorus residue, 3-7 pts. wt. potassium nitrate, 6-10 pts. wt. peanut cake powder, 2-4 pts. wt. diammonium phosphate, 8-14 pts. wt. corn straw, 5-10 pts. wt. gypsum, 4-8 pts. wt. ammonium sulfate part, 3-8 pts. wt. Lactobacillus, 0.5-3 pts. wt. polyacrylamide and 2-6 pts. wt. plant ash.    USE - Organic-inorganic compound containing fertilizer used for crop.    ADVANTAGE - The organic-inorganic compound containing fertilizer is cost-effective, improves soil structure, and increases fertility of soil.
NOVELTY - Fertilizer comprises 7-14 pts. wt. royal jelly, 5-10 pts. wt. ammonium nitrate, 10-15 pts. wt. egg shell powder, 10-15 pts. wt. acrylamide, 3-7 pts. wt. monocalcium phosphate, 1-3 pts. wt. Bacillus stearothermophilus, 5-9 pts. wt. bentonite, 5-8 pts. wt. ferrous sulfate, 4-10 pts. wt. oyster shell powder, 4-8 pts. wt. cotton seed, 4-8 pts. wt. Phellodendron, 2-7 pts. wt. earthworm manure, 5-7 pts. wt. pyrophosphate, 5-7 pts. wt. straw ash, 3-7 pts. wt. amino acid and 1-5 pts. wt. brown sugar.    USE - Fertilizer used for tobacco (claimed).    ADVANTAGE - The fertilizer increases quality of tobacco, ensures to fix soil and maintain soil fertility in efficient manner, and has long-term effect.
NOVELTY - Separating and purifying abamectin ointment, is claimed.    USE - The method is useful for separating and purifying abamectin ointment (claimed).    ADVANTAGE - The method is capable of simply, economically and energy-efficiently separating and purifying the avermectin ointment in an environmentally friendly manner.
NOVELTY - Polyether modified trisiloxane (I) is new.    USE - (I) is useful as a wetting agent, aqueous coating additives, wood additives and pesticide (all claimed).    ADVANTAGE - (I) can be simply and economically prepared with high efficiency in an eco-friendly manner.    DETAILED DESCRIPTION - Polyether modified trisiloxane of formula (I) is new.    R=H, -CH3 or -C2H6;    m=0-10; and    n=5-15.    An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - Organic ammonium phosphate composition comprises animal bone powder, charcoal powder or coal powder and rice sprout powder, organic ammonium phosphate composition is prepared by mixing raw materials, and then fermented them to obtain the finished product.    USE - Organic ammonium phosphate composition.    ADVANTAGE - The organic ammonium phosphate composition ensures improved root, pole stem, substantial fruit growth.
NOVELTY - The method involves conveying a secondary uniform mixture to a pressurized tubular reactor and inducing flow of the secondary uniform mixture in the reactor with a sufficient residence time and sufficient temperature to allow thermal hydrolysis of organic matter in the secondary uniform mixture. Recovered steam is produced within a recovery steam production unit to leave the secondary uniform mixture at an exit of the tubular reactor. The secondary uniform mixture at the exit of the production unit is cooled at a certain temperature for digestion of the hydrolyzed organic matter.    USE - Thermal hydrolysis method for continuously treating organic material containing sludge in an agribusiness industry, a slaughter-house and a home. Uses include but are not limited to a domestic waste water, or non-digested sewage sludge, fats or molasses, industrial waste, household water organic matter and draining organic matter.    ADVANTAGE - The method enables degrading problems during improving energy production by using biogas, and reducing volume of muds. The method enables avoiding thermal and mechanical stresses in an inexpensive manner. The method enables reduce consumption of energy and optimizing condensation of the vapor in mud in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a thermal hydrolysis device for continuously treating sludge containing organic material.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a thermal hydrolysis device.    Drain (1)    Hopper (2)    Pump (3)    Primary dynamic mixing injector (5)    Digester (22)
NOVELTY - The arrangement has gasification equipment (3) that is provided with a unit for gasifying fuel (F) at a low temperature. A separator (4) is arranged between the gasification equipment and combustion plant so that all product gas (G) is conveyed into the combustion plant flows from the gasification equipment through the separator into the combustion plant. The separator has unit that is provided for purifying the product gas of solids (S). The gasification equipment is a circulating fluidized bed gasifier.    USE - Arrangement for burning poor-grade fuel such as wet biomass, sludge, recycled fuel and waste coals.    ADVANTAGE - The alkali metals content are removed from the product gas that to be conveyed into combustion equipment. The corrosion of super-heaters provided in the combustion plant is reduced. The harmful substances or compounds such as chlorine and phosphor are removed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for burning fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of the arrangement for burning fuel.    Gasification equipment (3)    Separator (4)    Fuel (F)    Product gas (G)    Solid (S)
NOVELTY - Catalyst composition comprises: 0.1-15 wt.% at least one metal comprising group Ib, group IIb, group IVb, group Vb, group VIb, group VIIb, group VIII or noble metals; 30-96 wt.% at least one support; and 4-50 wt.% at least one solubilizing agent comprising ammonia solution, piperidine, pyrrolidine, morpholine, piperazine hydrate, 2-methylcyclohexyl amine, cyclohexylamine or hexamethyleneimine.    USE - The composition is useful for conversion of biomass to crude bio oil (claimed).    ADVANTAGE - The composition: provides quality crude oil; is stable and prepared simply; and provides a simple, high yielding, and energy and time saving process for the conversion, preferably hydrothermal conversion of biomass to crude bio oil.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparation of the catalyst composition having metal, support and solubilizing agent comprising obtaining support, preparing at least one dispersion containing metal or metal compound, adding solubilizing agent to the dispersion, obtaining a mixture of dispersion, where the dispersion comprises solubilizing agent, impregnating the mixture in solid support to obtain a metal impregnated support and drying the metal impregnated support followed by calcining and reducing to obtain the catalyst composition; and    (2) conversion (c1) of biomass to crude bio oil comprising preparing and/or collecting a biomass slurry comprising 5-35 wt.% biomass, preparing the catalyst composition, adding 1-20 wt.% catalyst composition to the biomass to the slurry to obtain a mixture and heating the mixture at 200-350 degrees C and at a pressure of 70-250 bars for 10-180 minutes to obtain the crude bio oil and a residue containing catalyst.
NOVELTY - Nutritional liquid comprises 85-90 wt.% waste mash, 5-6 wt.% potassium dihydrogen phosphate, 0.02-0.5 wt.% boron, 0.03-0.7 wt.% zinc, 0.05-0.6 wt.% molybdenum, 0.1-0.5 wt.% vitamin C and 1.5-3 wt.% liquid inoculated with Bacillus mucilaginosus, Bacillus megaterium and nitrogen-fixing Paenibacillus azotofixans.    USE - Nutritional liquid used for promoting flowering in dragon fruit plant (claimed).    ADVANTAGE - The nutritional liquid improves quality and yield of dragon fruit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing nutritional liquid, which involves:    (A) cooling waste mash to below 40 degrees C;    (B) mixing remaining raw materials and liquid inoculated with Bacillus mucilaginosus, Bacillus megaterium and nitrogen-fixing Paenibacillus azotofixansto with cooled mash for 72 hours to obtain another mixture; and    (C) adding vitamin C in obtained mixture to get product.
NOVELTY - A natural mineral water containing sewage treatment agent comprises 65-75 pts. wt. clinoptilolite, 10-15 pts. wt. kaolinite, 5-10 pts. wt. clay material with high cation exchange capacity, 1-2 pts. wt. quartz sand, 6-8 pts. wt. volcanic ash and 2-3 pts. wt. medical stone.    USE - Natural mineral water containing sewage treatment agent,    ADVANTAGE - The sewage treatment agent has high efficiency, better convenience, environmental protection and economical efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a natural mineral water containing sewage treatment agent, which involves selecting raw material such as clinoptilolite, kaolinite, clay material with high cation exchange capacity, quartz sand, volcanic ash and medical stone, crushing the raw material, and sieving through 350-400 meshes to obtain corresponding powder, mixing corresponding powder, heating the mixed powder at 160-170 degrees C, cooling, and packing to obtain finished product.
NOVELTY - A Microbacterium keratanolyticum (Mk-6) strain having a preservation number of CCTCC N0: M 2014279, is new, where the strain is deposited in China Center for Type Culture Collection at June 24, 2014.    USE - Microbacterium keratanolyticum (Mk-6) strain for use in a municipal sewage treatment plant for biologically removing phosphorus (claimed).    ADVANTAGE - The strain has environmental adaptability, high and stable phosphorus removal efficiency and no secondary pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for culturing a Microbacterium keratanolyticum (Mk-6) strain, which involves storing Mk-6 strain at -20 degrees C, coating 20 mu l glycerol and keartin solution on a plate of beef extract peptone solid medium at 28 degrees C for 24 hours after a single colony is picked in 0.3 ml sterile water, taking 100 mu l peptone beef extract and applying to a solid medium plate, and placing 15 ml peptone beef extract broth is placed in 28 degrees C at a speed of 170 rpm.
NOVELTY - Producing furans involve obtaining a first hydrolyzate chain with high concentrations of pentoses, which are extracted from hemicellulose fractions of a lignocellulosic biomass by acid hydrolysis under mild conditions. The second hydrolyzate chain is obtained by enzymatic hydrolysis of lignocellulosic biomass to obtain high concentrations of glucose using enzymatic mixture.    USE - Method for producing furans from hydrolyzed lignocellulosic waste (claimed).    DETAILED DESCRIPTION - Producing furans involve obtaining a first hydrolyzate chain with high concentrations of pentoses, which are extracted from hemicellulose fractions of a lignocellulosic biomass by acid hydrolysis under mild conditions. The second hydrolyzate chain is obtained by enzymatic hydrolysis of lignocellulosic biomass to obtain high concentrations of glucose using enzymatic mixture. The obtained first hydrolyzate chain with high concentrations of pentoses and second hydrolyzate chain with high concentrations of glucose, are mixed, and then heated at 70-170 degrees C and equilibrium pressure to allow the conversion of pentoses to hydroxymethylfurfural, and then performing conversion of hydroxymethylfurfural to obtain furan as desired product.
NOVELTY - A compact modular multifunctional automatic carbon isotope-labeled positron emission tomography (PET) drug synthesizer has methyl bromide or methyl iodide synthesis module, carbon isotope methylation synthesis module, PET drug separation system and control system. The methyl bromide or methyl iodide synthesis module is directly connected to the PET drug separation system, or carbon isotope methylation synthesis module and PET drug separation system.    USE - Compact modular multifunctional automatic synthesizer is used for manufacturing carbon isotope-labeled positron emission tomography drug.    ADVANTAGE - The compact modular multifunctional automatic synthesizer has excellent stability, flexibility, maintainability and reliability, and is operated by safe, environmentally-friendly and simple process.    DETAILED DESCRIPTION - A compact modular multifunctional automatic carbon isotope (11C)-labeled positron emission tomography (PET) drug synthesizer has methyl bromide (11CH3Br) or methyl iodide (11CH3I) synthesis module, carbon isotope methylation synthesis module, PET drug separation system and control system. The methyl bromide or methyl iodide synthesis module is directly connected to the PET drug separation system, or carbon isotope methylation synthesis module and then connected to PET drug separation system. The control system is used for connecting and controlling the methyl bromide or methyl iodide synthesis module, carbon isotope methylation synthesis module and PET drug separation system.
NOVELTY - Method (M1) for preparing saccharide from lignocellulosic biomass involves adding a lipolytic enzyme during enzymatic saccharification process of the lignocellulosic biomass.    USE - The method is useful for preparing saccharide (claimed) which is useful in preparation of lactic acid, bioethanol, and biodiesel.    ADVANTAGE - The method prepares 2 times or more glucose and 2.5 times or more ethanol compared with existing method, prevents decrease in activity of cellulase, reduces usage amount of lipolytic enzyme and non-ionic surfactant, and is cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for preparing ethanol by simultaneous saccharification and fermentation process which involves adding lipolytic enzyme and non-ionic surfactant to the biomass.
NOVELTY - The medicator has a plastic material fixed with a polypropylene material. A silicone material is fixed with an eye stop piece.    USE - Portable folding type ophthalmic medicator for a cellular phone accessory and a key chain use by an infant.    ADVANTAGE - The medicator effectively improves convenience of a user. The medicator is safe to use and environment-friendly. The medicator can be prevented from being vibrated. The medicator safely protects an eye from contamination.
NOVELTY - Method for producing fermentation product from starchy biomass involves (a) crushing the starchy biomass and liquefying the crushed biomass, (b) subjecting the liquefied biomass to solid-liquid separation, and (c) carrying out simultaneous saccharification and fermentation process of the resulting biomass to obtain product.    USE - The method is useful for producing fermentation product chosen from 2,3-butanediol, bioethanol, biohydrogen, and feed raw material from starchy biomass, preferably cassava, corn, mill, rice, barley or potato (all claimed).
NOVELTY - A florfenicol preparing method involves utilizing out oil-in-water (O/W) emulsion mode.    USE - Method for preparing florfenicol.    ADVANTAGE - The method enables preparing the florfenicol in a safe, environment-friendly, efficient, stable and cost-effective manner.
NOVELTY - Tobacco sprout inhibition method involves (A) selecting kerosene and vegetable oil in a weight ratio of 20:80, or alternatively selecting kerosene, alcohol and vegetable oil in a weight ratio of 20:5:75, uniformly stirring, and obtaining a sprout inhibitor; (B) applying the sprout inhibitor to a bud for 3-5 days; (C) removing bud from the tobacco plant; and (D) examining the growth of the tobacco plant.    USE - The method is useful for inhibiting tobacco sprout.    ADVANTAGE - The sprout inhibitor does not pollute tobacco plant hence environmentally friendly.
NOVELTY - Fertilizer comprises 20-30 pts. wt. ammonium sulfate, 8-15 pts. wt. monoammonium phosphate, 15-25 pts. wt. potassium sulfate, 4-10 pts. wt. sulfur, 2-4 pts. wt. ferrous sulfate, 0.02-0.04 pts. wt. malathion, 25-35 pts. wt. livestock and poultry manure, 10-12 pts. wt. rapeseed cake, 0.8-1.5 pts. wt. fermentation agent, 20-30 pts. wt. plant ash and 1-5 pts. wt. 1-aminobenzotriazole (ABT).    USE - As fertilizer for apple trees (claimed).    ADVANTAGE - The fertilizer is cost-effective, prepared by simple method, and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for production of the fertilizer by deodorizing and detoxifying livestock and poultry manure, drying the manure, pulverizing the dried product, adding rapeseed cake and fermentation agent to the pulverized product, fermenting the mixture for 36-72 hours, adding ammonium sulfate, monoammonium phosphate, potassium sulfate, sulfur, ferrous sulfate, malathion, plant ash and ABT to the fermented product, stirring the mixture, drying the mixture at 60-80 degrees C, and milling the dried product.
NOVELTY - Producing water soluble silicate comprises mixing silica and sodium bicarbonate, heating the mixture at a temperature of 1650-1700 degrees C in a furnace, maintaining a temperature of the mixture for a certain period of time, and cooling the hot mixture at room temperature.    USE - The method is useful for producing a water soluble silicate (claimed), which is useful in pesticides, fertilizer, chemicals used in water treatment, automotive industries, medicines, cosmetics, and biotechnology field.    ADVANTAGE - The method is capable of producing the water soluble silicate with high purity in an economical and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water-soluble silicate produced by the method.
NOVELTY - Salicin purification involves taking Chinese Tamarisk, and drying and crushing Chinese Tamarisk to obtain 40 mesh sieve powder. Ultrafiltration and nanofiltration Chinese Tamarisk powder is performed, and then placed for crystalline precipitation. The Chinese Tamarisk crystals are kept in a solvent system containing ethyl acetate, ethanol and water. Separation of salicin is performed through high-performance liquid chromatography- evaporative light scattering detector.    USE - Method for purifying salicin (claimed).    ADVANTAGE - The method enables to purify salicin with high purity in a simple and eco-friendly manner.
NOVELTY - Invention relates to agriculture, particularly to nursery and gardening. The substrate includes sawdust and additionally contains a compound mineral fertiliser, ash and a preparation having a composting property, with the following content of components, wt %: sawdust - 80-90, compound mineral fertiliser - 3-5, ash - 3-5, preparation having a composting property - 4-10, wherein the sawdust is pretreated with potassium permanganate. The compound mineral fertiliser used is, pts.wt: ammonium nitrate - 3, superphosphate - 1.5, potassium sulphate - 0.5. The preparation having a compositing property used is Vozrozhdenie.    USE - Chemistry.    ADVANTAGE - Use of the substrate reduces cases of plants dying during planting and improves the quality of seedlings.3 cl, 2 tbl, 8 ex
NOVELTY - Solid and liquid organic wastes are mixed on the site, the clamps are formed with the implementation of technological passages between them, the substrate is populated with earthworm of species Eisenia foetida, after obtaining the desired product and biomass of worms the cycle of waste disposal is repeated. Solid organic wastes are used in an amount of 25-30% by volume of liquid and semiliquid organic wastes. During mixing, biohumus and river sand is additionally added into the substrate in an amount of 10 kg and 1 kg, respectively, per one ton of the substrate. The clamps are formed with the width of 10-12 m and the height of 3-4 m, the length equal to the length of the biohumus site. After populating the substrate with worms, every 15-18 days the substrate is additionally mixed. In sub-zero air temperature the clamp surface is irrigated with water to create ice crust. Readiness degree of the substrate for populating with worms is determined by the temperature, humidity and acidity of the substrate.    USE - Agriculture.    ADVANTAGE - Accelerated processes of fermentation and self-heating in clamps.
NOVELTY - Reactor for aerobic fermentation of organic waste comprises a cylindrical housing of the reactor, mounted vertically, at that in the housing at least one disc is rigidly secured, along the axis of the cylindrical housing at least one axis is fixed, on which over each of the stationary disc a movable disc is mounted, made with the ability of rotation about the said axis via respective drive, the stationary and the fixed discs divide the housing in height into sections, the reactor housing is equipped with a system for loading wastes into the upper section of the reactor and the device for discharging the finished product under the lower section. The device for movement of loose solid wastes comprises a cylindrical housing mounted vertically, and inside the housing at least one disc is rigidly fixed, along the axis of the cylindrical housing at least one axis is fixed, on which over each of the stationary disc a movable disc is mounted, made with the ability of rotation about the said axis via respective drive, the stationary and the fixed discs divide the housing in height into sections.    USE - Agriculture.    ADVANTAGE - Inventions enable to simplify the design of the reactor, to increase the effectiveness of aeration.13 cl, 12 dwg
NOVELTY - This utility new type relates to a improved is organic fertilizer fermenting pool. The purpose is provide a raw material a. obtain accurate is organic fertilizer fermenting pool, comprising fermenting pool and temperature control system, has set with temperature control system and electric connection of temperature sensor in inner part of fermentation pool, a fermenting pool is a side wall set, set and has a sliding matching of inner rod, two end in the slide pole is respectively located at inner of fermentation pool outside two side, a sliding rod b a vertical to the side wall, a sliding rod inner end of movement track is at a position to slide the inner side of side wall back, a temperature sensor fixing inner end of sliding pole b between a side wall and a midpoint location and this side wall of relative side wall in between. This utility new type can obtain raw material inner layer to a temperature so as to more accurately for the fermentation temperature of raw material process b.
NOVELTY - Energy food fertilizer plant system comprises a biogas plant (4), which is filled with a separated manure, fermenter space, post-fermentation space, biogas room, insertion device, discharge device, device for discharging the biogas, apparatus for heating, a drying system comprising storage tank and drying chambers and a fish breeding plant comprising fish tanks.    USE - Used as an energy food fertilizer plant system.    ADVANTAGE - The energy food fertilizer plant system: increases transportability of the substrate; allows recovery of raw liquid manure in an optimized fermentation process, and is environmentally efficient.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of energy food fertilizer plant system (Drawing includes non-English language text).    Liquid manure (2)    Mobile separator (3)    Biogas plant (4)    Separator (5)    Stream (8)
NOVELTY - A a synthesis air ammonia recovery device, comprising ammonia storage tank has a purge pipeline, without power ammonia recovery device, ammonia tower A, the reciprocating pump A, ammonia water tower B, the reciprocating pump B tail pneuma and removing blow air pipeline. Without power ammonia recovery device one end connected to tail pneuma de-blowing pipeline, a connection to a water ammonia tower A; water ammonia tower A outlet connected to reciprocating pump A, a reciprocating pump A and a water ammonia tower A to entrance, water ammonia tower B connected to outlet water ammonia tower B entrance the water ammonia tower B exit one end connected water ammonia tower A entrance, one end a reciprocating pump B, a reciprocating pump B connected to ammonia water tower B entrance, water ammonia tower A outlet connected to tail pneuma to blowing pipeline. This utility new type not only a the ammonia in a purge, at the same time reduces the influence of blowing air for combustion temperature and reduce the emission of economic benefit and environmental protection benefit is obvious nitrogen oxide.
NOVELTY - This utility new type claims a a droppings organic compound fertilizer preparation system, said system comprising a droppings ferment, dry livestock manure and crushing, mixing uniformly and packaging composite co-four sub-system of the droppings ferment sub-system a detection table, a leavening agent preparing device, preparing a droppings, livestock manure stir a leavening agent, fermenting pool, and a first belt machine compose water pH by dry livestock manure and crushing a inlet sub-system by a dry animal manure, second belt machine, dry livestock manure crusher, third belt machine, dry livestock manure and fourth sieving belt machine compose the composite uniformly mixing sub-system by a mixing, fifth belt machine of farm, sixth belt machine, seventh belt machine and farmyard manure crusher constitute, packaging sub-system by a ferry belt machine, organic composite fertilizer granulating machine, the eighth belt machine,, wherein joint machine and entering belt machine compose. This utility new type can reduce the labour intensity, increase working efficiency, reduce two times pollute and ensure product quality.
NOVELTY - This utility new type provide a a a breeding device, solving the problems of organic liquid fertilizer in fermentation process of odour can not produce a problem of, comprising a tank body, a jar body upper part is set with feeding pipe has the jar body is set with bottom has discharge tube, jar body is set with the bottom and the outside air has connected for a jar body in the air of the air pipe network. This utility new type has set with external air and a connected air pipe network at the bottom in the tank body, a air pipe network in the air, discharging of air, ozone generate in a fermentation process is a. And set with heating rod has a inner tank body, a valid is a fermentation temperature, increase the fermentation production of work efficiency.
NOVELTY - This utility new type claims a sludge aerobic compost fermentation is a bi-directional stir mix device, wherein it comprise a mounting in a walking bridge frame has a sludge fermentation groove (1), the mounting has a back and forth is stir device walking in the walking upper bridge frame (1) (2), the stir device (2) comprise in has two terminal a, a bracket of two end and mounted in a transmission chain of a two terminal a, a transmission chain mounted this has a multi-blades, a bracket one end hinged with a stir. (2) a the other end b of stir device (2) of the lower part and a hinged point of a bracket around a lower part. This utility new type structure is simple and practical, the use of special structure form with respect to the past energy saving more than 50%, power range in 20 to 50 between, a depth is 3 to 3.5, the sludge can turn forwards to below a polishing process, a continuous operation of the inner target in fermentation groove.
NOVELTY - This utility new type claims a without power from one ventilation aerobic compost device. Comprising a tube, a top cover, a top cover at upper part of tube, a top cover set with feeding wherein. A seepage filtered liquid seepage filtered liquid from a bottom inner tube in uniform arrangement along the vertical vent pipe, the vent pipe from the bottom of the tube to the upper part of the top cover arrangement uniform air hole, the lower part is set with discharge tube wherein, lower part of tube set with percolate the water pipe and valve, the tube arrangement is ventilating hole and ventilating pipe is vertical arrangement accelerate the air flow of inner device, a lower without power condition, realize the aerobic environment of inner device feeding wherein a agricultural solid waste from a top is dosed into the device, under a function of aerobic microorganism and rapid decay is a stable organic fertilizer, discharging from the discharging wherein a part below a, compost in produce process of the water pipe. This utility new type device without power consumption, corrosion efficiency is high, the operation is simple and easy..
NOVELTY - This new utility model provide a kind of one L-extracting device of tryptophan, when using the device, is mainly for L-tryptophan fermentation liquid heating sterilization, after acid regulating, by tubular ultra-filter membrane filtering obtain filtration clear liquid and filtering liquid, ultra-filter membrane filtering clear liquid through evaporation concentration, obtain crystalline L-tryptophane crystal and crystallized mother liquid, L-tryptophane crystal dissolution and later by roll ultra-filter membrane filtering decolouring, ultra-filter membrane decolouring liquid through evaporation and concentration, crystallizing and drying obtain L-tryptophan. This new utility model simplified of extracting technique of L-tryptophan, increase of product purity of L-tryptophan, increase of use rate of product and by-product, at the same time reducing of production waste liquid equal to and pollute environment. The utility model is new extraction device with a certain of economic benefit and environmental benefit.
NOVELTY - This utility new type provides a thio acid erythromycin extraction device, a retention side outlet of entrance, nanofiltration membrane comprises has ultra-filtration film, nanofiltration membrane, extracting tower, erythromycin fermentation liquid conveying pipe. b. ultra-filtration film interception side of entrance of the ultra-filtration film of permeability side b... b nanofiltration membrane extracting tower, permeability of entrance side, ceramic film at the bottom of extracting tower b. ceramic film. b. the middle tank, the middle tank equipped with a sodium thiocyanate has storage tank, the middle tank connected in turn and crystallizing kettle, solid-liquid separating device, a drying. This utility new type relative traditional erythromycin extraction device, extracting erythromycin A comprises high yield, high purity, operation process is simplified, reduces solvent cost and industrial pollute at least equal.
NOVELTY - The operating method involves transferring dewatered high-pressure hydrogen from the gas-liquid separation unit (22), and providing a Peltier element (94) for variably controlling temperature of the high-pressure hydrogen, which adjusts the humidity of the high-pressure hydrogen. The Peltier element is placed on the hydrogen supply pipe, and a control unit variably controls a current applied to the Peltier element.    USE - Operating method for water electrolysis system used in producing fuel cells.    ADVANTAGE - Capable of minimizing energy consumption for hydrogen dehumidification, which exhibits improved economic efficiency, convenience, and operational efficiency. The power consumption of the Peltier dehumidifier for dehumidifying hydrogen, and the amount of cooling water supplied to the heat exchanger can be reduced to curb energy consumption, and thus, economic efficiency and convenience can be improved, thus, the overall operational efficiency of the water electrolysis system can be improved easily using a simple and economical structure. The high-pressure hydrogen can be dehumidified to a desired water concentration using a minimum amount of cooling water and minimum Peltier power consumption, which improves the operational efficiency of the water electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the water electrolysis system.    Gas-liquid separation unit (22)    Oxygen discharge pipe (86)    Drain line (90)    Peltier element (94)    Back pressure valve (120)
NOVELTY - Preparing fully fermented oxytetracycline calcium particles comprises adding calcium carbonate into oxytetracycline broth, mixing, reacting to obtain oxytetracycline calcification solution; adding hydrochloric acid, adjusting the pH to 4.5-6.5 to obtain acidified solution; adding the acidified solution into high pressure diaphragm plate and frame filter, squeezing the filter cake to obtain oxytetracycline calcium cake, mixing with wet material, grinding and crushing to obtain wet oxytetracycline calcium powder; and granulating.    USE - The method is useful for preparing fully fermented oxytetracycline calcium particles (claimed).    ADVANTAGE - The method overcomes the disadvantages of high energy consumption, and is environmentally-friendly. The calcium particles are firm and beautiful, have good fluidity, are difficult to crush, and convenient to use.    DETAILED DESCRIPTION - Preparing fully fermented oxytetracycline calcium particles comprises (a) adding calcium carbonate into oxytetracycline broth, mixing, reacting for 1-5 hours, to obtain oxytetracycline calcification solution; (b) adding hydrochloric acid into oxytetracycline calcification solution, and adjusting the pH to 4.5-6.5, to obtain acidified solution; (c) adding the acidified solution into high pressure diaphragm plate and frame filter, squeezing the filter cake to obtain oxytetracycline calcium cake with 40-50% moisture content; (d) mixing the oxytetracycline calcium cake with wet material, grinding and crushing to obtain wet oxytetracycline calcium powder; and (e) granulating the oxytetracycline calcium wet powder, sieving, drying, and screening.
NOVELTY - The method involves applying ceramic adhesive to joint portions of constituent portions so that a flow path for guiding fuel or oxidant gas within a fuel cell module (4) is fabricated. The applied ceramic adhesive is dried and hardened. The drying and hardening comprises hardening applied ceramic adhesive at a predetermined first temperature. The solvent elimination and hardening step comprises removing the solvent remaining within the ceramic adhesive hardened to further harden the ceramic adhesive by raising to a second temperature.    USE - Method for manufacturing solid oxide fuel cell apparatus.    ADVANTAGE - The cracking which tends to produce failures in airtightness, is reliably avoided, while work efficiency is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a solid oxide fuel cell module.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the solid oxide fuel cell apparatus.    Fuel cell module (4)    Generating chamber (10)    Heat exchanger (34)    Electromagnetic valve (35)    Inverter (54)
NOVELTY - Organic-inorganic complex liquid fertilizer comprises 20-25 wt.% bio-organic fertilizer, 8-10 wt.% ammonium nitrate, 3-6 wt.% ammonium phosphate, 3-6 wt.% phosphoric acid, 5-10 wt.% potassium nitrate, 5-10 wt.% potassium tartrate and water (remaining amount).    USE - Used as organic-inorganic complex liquid fertilizer.    ADVANTAGE - The method is simple. The fertilizer has high utilization rate.
NOVELTY - Bacillus subtilis microbial air disinfectant comprises 2-5 pts. wt. glycerol, 1-3 pts. wt. glutaraldehyde, 5-10 pts. wt. polyacrylic acid, 2-5 pts. wt. triethylene glycol, 4-8 pts. wt. propylene glycol, 2-9 pts. wt. citric acid and 50-80 pts. wt. water.    USE - The Bacillus subtilis microbial air disinfectant useful in livestock and poultry farms.    ADVANTAGE - The disinfectant enables less nutrition to aerobic bacteria; can be sprayed in environment for rapid growth and metabolism of a variety of enzymes and other antimicrobial substances, thus inhibiting pathogens; is safe to humans and animals; is environmentally friendly; has strong pertinence; has no side effects; reduce the use of chemical disinfectants.
NOVELTY - The device has a floating body fixed with a polyphenyl plate and a UPVC plastic hard tube and formed with a through hole. An UPVC pipe is fixed with a support frame and a water purifying water carrier e.g. elastic filler or carbon fiber. The floating body is connected with a micro-organism part along vertical direction. A contact part and the microorganism part are arranged on a surface of a floating body according to the purification effect.    USE - Three-dimensional biological sewage treatment device.    ADVANTAGE - The device improves water purification efficiency and satisfies agricultural organic waste water processing requirement, and has high commonality and wide range of application.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a three-dimensional biological sewage treatment device.'(Drawing includes non-English language text)'
NOVELTY - The filter has a filter plate whose side surfaces are mounted with a plate frame. Upper part of an electrode plate is formed with a supporting hole that is matched with a feeding hole. A wiring post surface is arranged on a silver plating treatment surface and connected with a pulse direct current electric source. Positive and negative ends of the pulse direct current electric source are connected with two sides of a binding post. The filter plate is connected between the sides of the electrode plate. The electric source is connected with a connecting plate through a square copper wire.    USE - Electric penetration plate sludge frame press filter.    ADVANTAGE - The filter can improve dryness effect of the plate frame so as to improve biomass boiler capacity. The filter main body can be produced at low cost.    DETAILED DESCRIPTION - The filter plate is stainless steel plate. An INDEPENDENT CLAIM is also included for an electric penetration plate sludge frame press filter treating method.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of an electrode plate.
NOVELTY - This utility model claims a urea waste recovery device, comprising prilling tower, has a groove o a urine groove, bottom of prilling tower provided with a liquid outlet, a liquid outlet leading to a o groove has a guide groove, after the a o groove inner leading-out pipeline and a pump connected, on one hand, to urine groove, and the other aspect through a device outside of a pool, in pipeline leading to the groove and a urine pool is mounted has a control valve. This utility new type has simple structure, when a wash tower urea adhesive tower scar block, good effect, which not only can reduce the waste of urine, but also reduces the pollutant emission, and realize the clean production development of green environment-friendly idea.
NOVELTY - The cleaning treatment method involves culturing algae (12) in to-be-processed object (2) of state which contains nutritive salt or organic substance, mixing portion of algae which contains or produces combustion component, such as hydrocarbon, oil, and fat, and portion of activated-sludge microorganisms (11) generated by activated sludge method, and setting mixture as sludge mixture, and discharging portion of sludge mixture as surplus sludge from biological reactor (3).    USE - Cleaning treatment method for purifying to-be-processed object, such as liquid waste and waste water, e.g. organic waste water, and excrement.    ADVANTAGE - Content of combustion component in surplus sludge discharged from processor is increased since algae which contains or produces combustion component, and sludge are mixed, and surplus sludge can be effectively utilized as fuel or combustion improver.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a purification apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram showing biological reactor in purification apparatus. (Drawing includes non-English language text).    To-be-processed object (2)    Biological reactor (3)    Activated-sludge microorganisms (11)    Algae (12)    Diffuser (15)    Air blower (17)
NOVELTY - The equipment has a decomposition tank (2) which decomposes the biodegradable waste water (1), and obtains decomposing water (6). A membrane separation activated-sludge layer obtains the concentrated water (14) which restores a metal as fine-particles from the decomposing water by microorganisms, and contains metal containing sludge (20). A solid-liquid separator recovers metals from the supernatant liquid (17) by an isolation unit (18), using the sedimentation tank which makes the sludge in the concentrated water settle, and obtains a supernatant liquid.    USE - Waste water treatment equipment used in water resources such as water and sewer service, inside water, and well water, and in automobile-industry field.    ADVANTAGE - Since the solid-liquid separator recovers metals from the supernatant liquid by the isolation unit, using the sedimentation tank which makes the sludge in the concentrated water settle, and obtains the supernatant liquid, the metals are recovered and the effect of making the collection process easy is acquired, without implementing the complicated process and control for recovering metal.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the platinum containing biodegradable waste water treatment equipment. (Drawing includes non-English language text)    Waste water (1)    Decomposition tank (2)    Decomposing water (6)    Concentrated water (14)    Supernatant liquid (17)    Isolation unit (18)    Sludge (20)
NOVELTY - Methanation reactor (10) for reacting hydrogen with at least one carbon-containing compound and produce methane, comprises: a hollow body (105) configured to receive a bed of catalyst particles (106) and having an inlet (110) for carbon-containing compound and hydrogen; and an outlet (115) for methane and water. The reactor further comprises an inlet for injecting cooled water into the liquid phase in the hollow body.    USE - The methanation reactor is useful for producing methane.    ADVANTAGE - The methanation reactor: is simple, economical, energy efficient and provides methane at good yields with co-production of thermal energy, while regulating the temperature to achieve optimum methanation reaction, and eliminating carbonyl production and coke formation on the catalyst surface; and enables various steps of methanation reaction to perform simultaneously.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a methanation method for reacting hydrogen with the carbon-containing compound and produce methane, comprising introducing carbon-containing compound and hydrogen into the hollow body, conducting methanation reaction between hydrogen and carbon-containing compound and removing methane and water, where the method further comprises injecting cooled water into into liquid phase in the hollow body during the step of methanation reaction.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the methanation reactor.    Methanation reactor (10)    Hollow body (105)    Bed of catalyst particles (106)    Inlet for carbon-containing compound and hydrogen (110)    Outlet for methane and water (115)
NOVELTY - Methanation reactor (10) for reacting hydrogen with at least one carbon-containing compound to produce methane, comprises: a hollow body (105) configured to receive a fluidized bed and having an inlet (110) for carbon-containing compound; an outlet for methane and water (115) produced by a methanation reaction; a heat exchanger (120) at least partially passing through the hollow body and at least partially immersed in the fluidized bed; and means for introducing saturated steam within the heat exchanger, where the superheated steam is in contact with the wall of the exchanger.    USE - The methanation reactor is useful for producing methane.    ADVANTAGE - The methanation reactor is simple, economical, energy efficient and provides methane at good yields with co-production of thermal energy, while regulating the temperature to achieve optimum methanation reaction by utilizing the temperature sensor, and avoid carbonyl formation.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for methanation process for reacting with hydrogen with at least one carbon-containing compound and to produce methane, comprising introducing the carbon-containing compound into the hollow body, removing methane and water produced by the methanation reaction, transmitting saturated vapor to the heat exchanger, and exchanging heat between the steam and the reaction mixture within the hollow body at which the superheated steam is progressively into contact with the wall of the exchanger.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the methanation reactor.    Methanation reactor (10)    Hollow body (105)    Inlet for carbon-containing compound (110)    Outlet for methane and water (115)    Heat exchanger (120)
NOVELTY - Method for culturing microorganisms, involves culturing microorganisms in region surrounded by water-absorbing polymer gel, and substrate comprising nutrient and water, where at least one portion of the water-absorbing polymer gel covers the substrate.    USE - The method is useful for culturing microorganisms chosen from fungi, microalga, and diatom, and yeast, preferably Botryococcus sp., Chlamydomonas sp., Chlorococcum sp., Chlamydomonas sp., Ceratocystis sp.,Characium sp., Protosiphon sp., or Haematococcus sp., more preferably microalgae strain B.sudeticus FERM BP-11420, and Chlorococcum sp. FERM BP-22262 (claimed).    ADVANTAGE - The method is simple to perform, and cost-effective.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for preparing biomass, involves processing the obtained culture and recovering biofilms from the culture; and (2) microorganism, preferably Chlorococcum sp. RK261 strain comprising (a) 8S ribosomal RNA (rRNA) nucleotide sequence of the Chlorococcum sp. RK261 capable of exhibiting at least 95% or 99.99% sequence homology, or Chlorococcum sp. 18S rRNA gene comprising nucleotide sequence exhibiting 99.94% sequence homology of the SEQ ID NO: 2, or (b) Chlorococcum sp. FFG039 strain (FERM BP-22262) or same property in taxonomy.
NOVELTY - Nanosheets comprise metal-molybdenum carbide.    USE - Nanosheets are used for carbon-supported catalyst (claimed) used for hydrogen evolution reaction.    ADVANTAGE - The carbon-supported catalyst comprising nanosheets has excellent hydrogen evolution reaction electrocatalytic activity.    DETAILED DESCRIPTION - Nanosheets comprise metal-molybdenum carbide of formula: MaMobCx.    M=Ni, Co, Cu, Fe, Ga, Ge, Mn, Cr, V, Ti, Zr, Sc, Y, Nb, Hf, Ta, La or Ce.    An INDEPENDENT CLAIM is included for the following    (i) carbon-supported hydrogen evolution reaction catalyst.    (ii) Metal-tungsten nitride nano sheets comprising MaWbN, wherein M is selected from the group consisting of Ni, Co, Cu, Fe, Ga, Ge, Mn, Cr, V, Ti, Zr, Sc,Y, Nb, Hf, Ta, La and Ce
NOVELTY - Obtaining organic fertilizer involves performing aerobic and anaerobic fermentation of 40-50 wt.% ruminants excrete matter and commercial waste of vegetative material and then carrying out composting process.    USE - Method for obtaining organic fertilizer (claimed).    ADVANTAGE - The method enables to obtain organic fertilizer without chemical additives. Plant absorbs nutrients from organic fertilizer.
NOVELTY - Formation of solid fuel (F) involves adjusting moisture content of sewage sludge (D) to 20-30 wt.%, and compression-molding of sewage sludge to pellets.    USE - Formation of solid fuel (claimed).    ADVANTAGE - The method enables continuous and efficient manufacture of pellet-form solid fuel having excellent handleability in conveyance and storage property. The amount of heat as fuel is improved by addition of pulverized coal to sewage sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid fuel-formation apparatus, which consists of moisture content adjustment unit (G) which adjusts the moisture content of sewage sludge, and compacting machine (P) which compression-molds sewage sludge.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure explaining the formation of solid fuel.    Sewage sludge (D)    Powdered coal (E)    Solid fuel (F)    Moisture content adjustment unit (G)    Sludge drying machine (K)    Compacting machine (P)    Fine coal addition apparatus (S)    Sludge hydration apparatus (T)
NOVELTY - Production of biological organic fertilizer comprises collecting excrement, straw, mushroom waste, and biogas; adding adsorption material and water and mixing; adding biological fermenting bacteria and fermenting; aging in polarized field; crushing and grading-screening; and granulating, drying, cooling, sieving, weighing, and packing.    USE - Method for producing biological organic fertilizer (claimed).    ADVANTAGE - The fertilizer has no pollution and high fertilizer effect and is convenient to use.
NOVELTY - A pseudoginseng base fertilizer comprises 18-22 pts. wt. sheep manure, 8-12 pts. wt. plant ash, 1-2 pts. wt. calcium magnesium phosphate fertilizer, 2-4 pts. wt. calcium superphosphate, 0.001-0.002 pt. wt. ammonium molybdate, 0.02-0.06 pt. wt. boron fertilizer, 0.05-0.09 pt. wt. zinc fertilizer, and 45-70 pts. wt. green manure. The plant ash is soaked in human feces/urine.    USE - Base fertilizer for pseudoginseng (claimed).    ADVANTAGE - The base fertilizer provides balanced nutrients required for pseudoginseng growth, improves stress resistance and immunity of pseudoginseng, ensures vigorous growth of pseudoginseng, and directly increases pseudoginseng yield (up to 250 kg/mu, which is 25% higher than the yield without using base fertilizer).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by mixing raw materials, and sealed fermenting.
NOVELTY - Preparation of ammonium dihydrogen phosphate preparation by-product i.e. special pineapple fertilizer comprises mixing phosphoric acid and urea, heating, reacting under stirring condition, separating urea phosphate material slurry, slowly adding ammonium hydroxide, regulating pH, stirring, obtaining material slurry containing nitrogen and phosphorus, adding into a cooling crystallizer, cooling, filtering, separating ammonium dihydrogen phosphate, adding the filtrate with trace element and potassium element, obtaining mother liquid, drying and controlling the water content.    USE - Preparation of ammonium dihydrogen phosphate preparation by-product i.e. special pineapple fertilizer (claimed).    ADVANTAGE - The method provides high purity ammonium dihydrogen phosphate, reduces the cost, provides fertilizer, which satisfies the maximum nutritional content needed for pineapple, reduces the waste of element, and avoids soil pollution caused by fertilizer residue.    DETAILED DESCRIPTION - Preparation of ammonium dihydrogen phosphate preparation by-product i.e. special pineapple fertilizer comprises mixing phosphoric acid and urea at 2.7:1.7-2.3 mol ratio, where phosphoric acid concentration is 69-72%, heating at 5 degrees C/minute to 105-120 degrees C, reacting under stirring condition for 24 minutes, separating urea phosphate material slurry, slowly adding ammonium hydroxide, regulating pH at 3.6-3.9, stirring, obtaining material slurry containing nitrogen and phosphorus, adding into a cooling crystallizer, cooling to 25 degrees C, filtering, separating ammonium dihydrogen phosphate, adding the filtrate with trace element and potassium element, obtaining mother liquid, drying the mother liquid in drying machine at controlled temperature of 36 degrees C for 24 minutes, controlling the water content at 4% and obtaining special pineapple fertilizer.
NOVELTY - Preparation of sodium dihydrogen phosphate and loquat complex fertilizer comprises mixing urea and phosphoric acid , increasing the temperature, reacting under stirring condition, separating intermediate, adding sodium hydroxide, regulating the pH, reacting, obtaining mother liquid, adding into cooling crystallizer, conducting cooling crystallization, monitoring the mother liquid component content, filtering, obtaining filter cake i.e. sodium dihydrogen phosphate, adding the filtrate with loquat required elements, raising the temperature, drying and obtaining loquat complex fertilizer.    USE - Preparation of sodium dihydrogen phosphate and loquat complex fertilizer (claimed).    ADVANTAGE - The method provides fertilizer, which satisfies the loquat nutritional elements, and avoids soil environmental pollution caused by filter residue, thus, achieves high environment protection.    DETAILED DESCRIPTION - Preparation of sodium dihydrogen phosphate and loquat complex fertilizer comprises mixing urea and phosphoric acid at 2:2.4-2.9 mol ratio, increasing the temperature to 111-119 degrees C, reacting under stirring condition at 70-80 revolutions/minute for 2.2 hours, separating intermediate, adding sodium hydroxide, regulating the pH at 3.2-3.7, reacting for 80-98 minutes, obtaining mother liquid containing nitrogen, phosphorus and sodium, adding the mother liquid into cooling crystallizer, conducting cooling crystallization, monitoring the mother liquid component content, when nitrogen content is 15.2-15.7%, phosphorus pentoxide content is 7.2-7.7% and sodium content is 4.2-4.7%, stopping the crystallization, filtering, obtaining filter cake i.e. sodium dihydrogen phosphate, adding the filtrate with loquat required elements, raising the temperature at 3 degrees C/minute to 24 degrees C, drying for 30 minutes to water content of 4.5%, and obtaining loquat complex fertilizer.
NOVELTY - Production of organic fertilizer comprises feeding animal waste raw material in bucket and processing; conveying raw material through conveying pipeline into organic fertilizer degradation device; launching engine motor, stirring raw materials and bacteria, regulating temperature using electric heating oil or water at a temperature of product demand, and fermenting and degrading; conveying through conveying pipeline to second degradation device; controlling reaction temperature and fermenting and degrading; and placing in material bucket, packing, and discharging.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The device reduces organic fertilizer production time and is easy to clean, easy to change when damaged, and automatic. The method is simple and convenient to operate, has high organic fertilizer synthesis efficiency, and reduces putrid to minimize environment pollution at a great degree.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic fertilizer degradation device comprising degradation groove, stirrer, stir shaft, electric heater, hot oil or water pipe, speed reducer, transmission belt, motor, and first and second cavities.
NOVELTY - A fruit-tree fertilizer comprises 2-4 pts. wt. cow manure, 1.5-2 pts. wt. mushroom waste, 1-2 pts. wt. fruit dregs, 1.5-2 pts. wt. straw waste, 0.1-0.2 pt. wt. calcium-magnesium phosphate fertilizer, 0.1-0.2 pt. wt. trace element fertilizer, and 0.2-0.4 pt. wt. bran or rice bran powder.    USE - Fertilizer for fruit trees.    ADVANTAGE - The fertilizer has pH of 6.5-8.2, low heavy metal content, and short fermentation time; improves fruit tree pest resistance and disease resistance; promotes fast growth rate; prevents soil compaction; improves soil water retention and fertilizer retention; and increases fertilizer utilization rate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of fertilizer by uniformly mixing raw materials and stacking; and adding 0.1-0.2 wt.% fermentation agent, and fermenting while turning once every 2-3 days for 15-20 times.
NOVELTY - Rice blast control agent comprises material I comprising 70 g nano-complex monovalent copper, and 10 g silicon dioxide, and material II comprising 200 g wormwood, 250 g rhizoma calami, 200 g tomato leaves, 10 g sweet potato powder, and 50 g fermenting strain I, where the fermenting strain I comprises 10 g red circular yeast, 20 g white Geotrichum candidum, and 20 g Bacillus megaterium.    USE - The agent is used for preventing and treating rice blast, and increasing stress tolerance.    ADVANTAGE - The agent does not generate drug resistance, does not pollute the environment, promotes growth of plant, restrains rice blast, and provides rice growth required amino acids.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing rice blast control agent comprising (i) preparing nano copper containing rice blast control agent raw material, (ii) adding the raw material into an iron pot, adding 2500 cc water, heating, cooking until hot, simmering and maintaining flame and scalding for 2 hours, filtering residue, obtaining filter liquid, placing into the glass fermentation kettle, naturally reducing the temperature to 30 degrees C, (iii) adding fermenting strain I, carrying out fermentation for 7 days, maintaining temperature at 32-35 degrees C, stirring and oxygenating, (iv) then adding nano monovalent copper complex, stirring for 0.5 hours, maintaining the temperature at 55 degrees C, and (v) adding silicon dioxide, stirring for 0.5 hours, maintaining temperature at 55 degrees C to obtain the product.
NOVELTY - The organic fertilizer production device has separating device which is connected to stir fermentation device, screen machine feeding device, screen machine and granulating machine through transmitting device. The ends of the tension rollers are connected through bolt and nut. The head of the bolt is higher than width of through groove. The supporting column is fixed to the regulating pedestal. The end of screw is passed through the support column and propped against the portions of the tightening rollers.    USE - Organic fertilizer production device with screen machine feeding device.    ADVANTAGE - The fertilizer is used conveniently, when the piling and fermenting process is performed effectively and rapidly. The automatic production of the organic fertilizer is realized effectively. The artificial cost of the organic fertilizer is reduced. The production efficiency of the organic fertilizer is increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the organic fertilizer production device.    Hopper (141)    Transmission mechanism (142)    Tightening device (143)    Belt transmission portions (1421,1422)    Tension roller (1423,1424)
NOVELTY - A carbon dioxide gas is decomposed into carbon monoxide. A thermochemistry catalytic reaction is performed using carbon monoxide, water molecule and nitrogen gas as raw materials and a catalyst chosen from platinum, ruthenium and iron, to obtain ammonia.    USE - Manufacture of ammonia used as fertilizer.    ADVANTAGE - The method enables environmentally-friendly manufacture of ammonia with excellent workability since fossil fuel is not used as raw material.
NOVELTY - Method for preparing liquid fertilizer, involves performing liquid separation of livestock manure, adding hydrogen peroxide to separated liquid, oxidizing the separated liquid, and fermenting oxidized liquid under aerobic condition.    USE - The method is useful for preparing liquid fertilizer (claimed).    ADVANTAGE - The method rapidly prepares liquid fertilizer.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for apparatus which comprises oxidation unit for performing the oxidation step, and fermentation unit for performing the fermenting step.
NOVELTY - A method for increasing cetane number of hydrocarbon involves providing a hydrocarbon feedstock, introducing hydrocarbon feedstock, oxidation source, water-soluble acid, oxidation source, and catalyst into cavitation reactor, and operating cavitation reactor with cooling or heat exchange to control temperature inside the cavitation reactor, promote cetane-increasing oxygenation reaction between hydrocarbon feedstock and oxidation source, and yield liquid hydrocarbon product having a cetane number which is 15% or more than the cetane number of the hydrocarbon feedstock.    USE - Method for increasing cetane number of hydrocarbon used in fuels e.g. diesel and biodiesel.    ADVANTAGE - The method enables efficient increase in cetane number of hydrocarbon and minimizes the formation of water-soluble sulfones.    DETAILED DESCRIPTION - A method for increasing cetane number of hydrocarbon, involves providing a hydrocarbon feedstock having boiling range more than naphtha, introducing the hydrocarbon feedstock, an oxidation source, a water-soluble acid and oxidation source, and optionally a catalyst into a cavitation reactor, and operating the cavitation reactor with cooling or heat exchange to control the temperature inside the cavitation reactor, promote cetane-increasing oxygenation reactions between the hydrocarbon feedstock and oxidation source, minimize formation of water-soluble sulfones, and yield liquid hydrocarbon product having a cetane number which is 15% or more than the cetane number of the hydrocarbon feedstock.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the method for increasing cetane number of hydrocarbon.    Hydrocarbon feed stock (102)    Cavitation reactor (106)    Phase separator (108)    Light hydrocarbon gases (110)    Recycled oxidation source (116)
NOVELTY - Benzyl azide (A) is reacted with vinyl acetate (B) at 110-130 degrees C for 9-16 hours to obtain 1-benzyl-1H-(1,2,3)triazole (II) which is purified by crystallization and debenzylated with palladium/carbon at 100-120 degrees C for 8-14 hours to obtain crude 1H-(1,2,3)triazole (I) which is purified by vacuum distillation.    USE - Production of 1H-(1,2,3)-triazole used as intermediate for synthesizing N-substituted 1,2,3-triazole. Uses include but are not limited to dyestuffs, photo stabilizers, corrosion inhibitors, pharmaceutical and agrochemicals.    ADVANTAGE - The process is simple and starts from readily available starting material which makes the process economical. Vinyl acetate is easy to handle and is inexpensive. Since acetylene gas is not used in the manufacturing process, need for special attention to control the plant scale or special equipment is eliminated. The process is environmentally-friendly and safe, and enables manufacture of 1H-triazole with yield.    DETAILED DESCRIPTION - Benzyl azide of formula (A) is reacted with vinyl acetate of formula (B) in a closed vessel, at 110-130 degrees C for 9-16 hours to obtain 1-benzyl-1H-(1,2,3)triazole of formula (II). The compound (II) is purified by crystallization in presence of a solvent to obtain high quality 1-benzyl-1H-(1,2,3)triazole of formula (II). The purified product is debenzylated with palladium/carbon in presence of solvent in a closed vessel, at 100-120 degrees C for 8-14 to obtain crude 1H-(1,2,3)triazole of formula (I) which is purified by high vacuum distillation. An INDEPENDENT CLAIM is included for large scale production of compound (II).
NOVELTY - Purifying an alcohol by pervaporation, comprises contacting an alcohol with an article (A1) comprising a nanofibrous scaffold possessing at least one zeolite, where the nanofibrous scaffold comprises fibers having a diameter of 1-20000 nm, and a hydrophilic barrier layer having a thickness of 0.25-20 mu m possessing at least one zeolite on at least a portion of a surface of the nanofibrous scaffold, where the hydrophilic barrier layer comprises a polymer, and the article separates water from the alcohol.    USE - The method is useful for purifying an alcohol by pervaporation (claimed), preferably to produce fuel grade ethanol.    ADVANTAGE - The method: provided energy efficient purification of alcohol by pervaporation and provides fuel grade ethanol with very low energy consumption; combines both permeation and evaporation to enhance the removal of water from ethanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for purifying an alcohol by pervaporation, comprising: contacting an alcohol with an article (A2) comprising: a substrate; a nanofibrous scaffold comprising fibers having a diameter of 1-20000 nm applied to a surface of the substrate; and a hydrophilic barrier layer having a thickness 1-10 mu m on the nanofibrous scaffold on a surface opposite a surface applied to the substrate, where the hydrophilic barrier layer comprises a polymer in combination with at least one zeolite, where the zeolite is present in at 1-10 wt.% based on the hydrophilic barrier layer, and the article separates water from the alcohol.
NOVELTY - Fertilizer comprises 60-70 pts. wt. organic matter, 2-5 pts. wt. complex microbial strains, 5 pts. wt. potassium humate, 5-10 pts. wt. nitrogenous fertilizer, 5-10 pts. wt. phosphate fertilizer, 2-5 pts. wt. potassium fertilizer, 3-6 pts. wt. trace element and 1-2 pts. wt. rare earth element, where organic matter is animal protein and plant source.    USE - Fertilizer used for improving water quality (claimed) and promoting breeding in fish.    ADVANTAGE - The fertilizer has high dissolution and utilization rate, promotes growth of beneficial algae, is nutritional to fish, prevents disease in fish, and increases dissolved oxygen.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing fertilizer, which involves:    (A) mixing organic matter and complex microbial strains and then fermenting for 8-9 days to obtain fermented product;    (B) adding potassium humate, nitrogenous fertilizer, phosphate fertilizer and potassium fertilizer into fermented product and then stirring to obtain mixture, where water content of mixture is 20%; and    (C) crushing mixture, adding trace element and rare earth element into mixture and then mixing in mixer to obtain the product.
NOVELTY - Preparing fertilizer involves adding 20-25 kg calcium magnesium phosphate and organic garbage into biogas fermented residue and then stacking organic garbage layer on biogas fermented residue layer, where layer thickness of organic garbage and residue layer is 65-85 cm and 45-65 cm respectively. Soil layer is applied on stacking layer and then kept for 15-120 days. Concentrated sodium hydroxide is added on stacking layer and then mixed to obtain mixture. The mixture is crushed and then dried to obtain the product.    USE - Method for preparing fertilizer (claimed).    ADVANTAGE - The method enables to prepare fertilizer with high yield in a simple manner.
NOVELTY - Fertilizer composition comprises 26-29 pts. wt. nitrogen fertilizers, 18-20 pts. wt. phosphate fertilizer, 15-19 pts. wt. cattle manure, 14-16 pts. wt. potash fertilizer, 11-13 pts. wt. quicklime powder, 9-11 pts. wt. zinc sulfate, 7-9 pts. wt. green manure ryegrass, 5-8 pts. wt. Bacillus preparation, 3-5 pts. wt. Borax (RTM: Sodium tetraborate), 1-3 pts. wt. triadimefon, 2-4 pts. wt. thiophanate methyl, 7-9 pts. wt. plant ash, 3-5 pts. wt. selenium humate fertilizer and 50-60 pts. wt. water.    USE - Fertilizer composition used for cultivating towel gourd (claimed).    ADVANTAGE - The fertilizer composition ensures improved yield and disease resistance ability of towel gourd, and improved soil permeability and water-retaining property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) mixing raw materials uniformly for 10 minutes; and    (B) drying the obtained material to obtain the finished product.
NOVELTY - Fertilizer composition comprises 22-24 pts. wt. Lespedeza bicolor green fertilizer, 18-20 pts. wt. ammonium sulfate, 17-19 pts. wt. mildew fertilizer, 14-16 pts. wt. potassium chloride, 11-13 pts. wt. calcium superphosphate, 9-12 pts. wt. prepared chicken manure, 6-8 pts. wt. plant ash, 3-5 pts. wt. humic acid, 8-10 pts. wt. cotton seed cake fertilizer, 7-9 pts. wt. manganese sulfate, 3-5 pts. wt. borax, 2-4 pts. wt. molybdenum trioxide, 1-3 pts. wt. amino acid, 2-3 pts. wt. water retention agent, 2-4 pts. wt. anticropping agent and 50-60 pts. wt. water.    USE - Fertilizer Composition used for cultivating mustard (claimed).    ADVANTAGE - The fertilizer composition ensures improved natural taste and anti-disaster ability, and improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) mixing raw materials uniformly, and then fermenting them for 5 hours; and    (B) drying the obtained material, and then packaging them to obtain the finished product.
NOVELTY - Liquid fertilizer preparation involves filtering glutamic acid fermentation liquid, decoloring, concentrating and crystallizing, separating ammonium sulfate crystal and preparing fertilizer.    USE - Method for preparing liquid fertilizer (claimed).    ADVANTAGE - The method enables to prepare liquid fertilizer in cost-effective manner.
NOVELTY - Organic fertilizer composition preparation involves crushing fruit and tree to obtain particle with 0.2-0.6 cm. The obtained material is cooked at 120-300 degrees C and 3-8 kilograms/cm2 pressure for 3-10 hours. The obtained material is mixed with nitrogen fertilizer, and then fermented to obtain organic fertilizer. The obtained material is mixed with probiotic, and then packed them into a bag to obtain the finished product.    USE - Method for preparing organic fertilizer composition (claimed).    ADVANTAGE - The method enables to prepare organic fertilizer composition in convenient manner that provides complete nutrition, ensures improved soil property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a cooking device, which comprises comprising boiler, stewing container, left side plate, right side plate, front side plate, a rear side plate and walking wheel.
NOVELTY - Fertilizer composition comprises 20-30 pts. wt. nitrogenous fertilizer, 8-10 pts. wt. potash fertilizer, 15-17 pts. wt. phosphate fertilizer, 6-8 pts. wt. peat, 3-5 pts. wt. limestone powder, 6-8 pts. wt. lees, 1-3 pts. wt. of 50% phoxim, 3-5 pts. wt. abamectin, 4-6 pts. wt. cypermethrin and 0.5-0.7 pts. wt. boron.    USE - Fertilizer composition used for cultivating spinach (claimed) for preventing underground insects.    ADVANTAGE - The fertilizer composition ensures improved spinach production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) mixing raw materials, and then heating them; and    (B) granulating the obtained material to obtain the finished product.
NOVELTY - Preparing a dicoumarin compound comprises reacting (a) a 4-hydroxycoumarin compound with an aromatic aldehyde compound comprising a benzaldehyde compound (I), pyridine-4-carbaldehyde (II), (E)-3-phenylprop-2-enal (III), 1,3-benzodioxole-5-carbaldehyde (IV) or furan-2-carbaldehyde (V) in the presence of an aqueous solution of alkaline functional ionic liquid catalytic system and a solvent, and (b) stirring the mixture at room temperature.    USE - The process is useful for preparing a dicoumarin compound (claimed).    ADVANTAGE - The process is capable of easily and economically preparing the dicoumarin compound with high yield using non-corrosive catalytic system and without requiring organic solvent and heating steps, thus reducing environmental pollution.    DETAILED DESCRIPTION - Preparing a dicoumarin compound comprises reacting (a) a 4-hydroxycoumarin compound with an aromatic aldehyde compound comprising a benzaldehyde compound of formula (I), pyridine-4-carbaldehyde of formula (II), (E)-3-phenylprop-2-enal of formula (III), 1,3-benzodioxole-5-carbaldehyde of formula (IV) or furan-2-carbaldehyde of formula (V) in the presence of an aqueous solution of alkaline functional ionic liquid catalytic system and a solvent, and (b) stirring the mixture at room temperature. The alkaline functional ionic liquid catalytic system is diaminomethylene-ammonium ion of formula (i), acetate ion (CH3COO-), propionate ion (C2H5COO-), lactate ion (CH3CHOHCOO-), butanoate ion (C3H7COO-), tetrafluoroborate ion (BF4-), hexafluorophosphate ion (PF6-), bisulfate ion (HSO4-) or dihydrogen phosphate ion (H2PO4-).    X = phenyl (substituted with F, Cl, Br, OH, NO2, CH3, CF3, OCH3 or CHO) or H;    R1-R4 = CH3 or C2H6; and    R5, R6 = H, CH3 or C2H6.
NOVELTY - Foliar fertilizer preparation involves taking 75-85 pts. wt. fresh sisal hemp waste water, 0.5-1.0 pts. wt. organic acid, 2-3 pts. wt. trace element, 1-2 pts. wt. pest repellent and 0.1-0.5 pts. wt. surfactant, and then removing residue from the sisal hemp waste water. The filtered material is mixed with the remaining raw materials, and then fermented at 30-50 degrees C for 10-15 days to obtain the finished product.    USE - Method for preparing foliar fertilizer used for promoting growth of tea (claimed).    ADVANTAGE - The method enables to prepare foliar fertilizer in cost-effective and eco-friendly manner, ensures improved yield of tea.
NOVELTY - Method for producing 1,3-propanediol, involves fermenting Halanaerobium hydrogenoformans with source of glycerol.    USE - The method is useful for producing 1,3-propanediol which is useful for producing biodiesel.    ADVANTAGE - The method is cost-effective.
NOVELTY - Producing fuel in the form of pellets having a high calorific value of 4100 KW/T at a humidity of 6.5%, and a low calorific value of 3790 KW/T at a humidity of 6.5%, comprises providing vine shoot and then grinding with the humidity of less than 30%, performing baling process and double grinding process, followed by extracting impurities, filtering, mixing and conveying, pre-cooling, and distributing the pellets.    USE - The method is useful for producing fuel in the form of pellet (claimed).    ADVANTAGE - The method is capable of producing the fuel in the form of pellet with high calorific value in an environmentally friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a device for processing maize straw into pellets, comprising a receiving unit equipped with a unit of fluidizing maize straw, a processing unit equipped with a shredder, where the processing has an open space in which mills are arranged in series, a cyclone separator, a collecting vessel, a mixing conveyor, a mixing conveyor, a granulator (9), and a vibrating screen conveyor; and    (2) the plant fuel having a high calorific value of 4100 KW/T at a humidity of 6.5%, and a low calorific value of 3790 KW/T at a humidity of 6.5%.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for producing fuel in the form pellets (Drawing includes non-English language text).    Cylindrical motor (6)    Conditioner (7)    Conveyor (8)    Granulator (9)    Pre-cooling section. (10)
NOVELTY - Producing fuel in the form of pellet, comprises providing vine shoot powder having a humidity of less than 30% and then drying.    USE - The method is useful for producing fuel in the form of pellet (claimed).    ADVANTAGE - The method is capable of producing the fuel in the form of pellet with high calorific value in an environmentally friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a device for processing vine shoots, comprising a crusher and a processing unit; and    (2) pellets based on vine shoots having a high calorific value of 5270 KW/T at a humidity of 7.5%, and a low calorific value of 4930 KW/T at a humidity of 7.5%.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of a device for producing fuel in the form pellets (Drawing includes non-English language text).    Cylindrical motor (6)    Conditioner (7)    Conveyor (8)    Granulator (9)    Pre-cooling section. (10)
NOVELTY - Manufacture of levulinic acid from fructose involves using linear or cyclic ethylene glycol-based compound as a solvent, in presence of solid acid catalyst, at reaction temperature of 100-200 degrees C.    USE - Manufacture of levulinic acid used as main component of biofuel and biochemical.    ADVANTAGE - The method enables efficient, environmentally-friendly and economical manufacture of levulinic acid with high yield, and in which the solvent and the catalyst are efficiently separated, collected, and reused, and reduces dependency on petroleum with respect to greenhouse gas regulations.
NOVELTY - The system has a stripping tower (9) whose bottom portion is connected with an upper portion of an extracting rectifying tower (2). An alkane water washing tower (8) is provided with a hydrogen inlet and outlet heat exchanger (18). A hydrogenation heat separating jar (20) is connected with a hydrogenation cooler (21). A compressor suction jar (24) and compressor (25) are connected with alkane after water washing tower after closing the hydrogen inlet and outlet heat exchanger. A hydrogenation separating device (29) is connected with an iso-butane product tower (32).    USE - Preparation system of iso-butane.    ADVANTAGE - The solvent waste heat recovery is improved so that the economic benefit of system is increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a separation method of iso-butane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the preparation system of iso-butane.    Extracting rectifying tower (2)    Alkane water washing tower (8)    Stripping tower (9)    Hydrogen inlet and outlet heat exchanger (18)    Hydrogenation heat separating jar (20)    Hydrogenation cooler (21)    Compressor suction jar (24)    Compressor (25)    Hydrogenation separating device (29)    Iso-butane product tower (32)
NOVELTY - Enzyme composition comprises glucoamylase and alpha -amylase, and optionally protease.    USE - The enzyme composition is useful for producing a fermentation product from starch-containing material (claimed). The fermentation product includes ethanol.    ADVANTAGE - The enzyme composition enables to produce fermentation product with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing a fermentation product from starch-containing material, which involves (a) saccharifying a starch-containing material at a temperature below the initial gelatinization temperature, and (ii) fermenting using a fermentation organism, where saccharification and/or fermentation is performed in the presence of the enzymes chosen from glucoamylase and alpha -amylase, and optionally protease.
NOVELTY - A feed containing biomass-derived pyrolysis oil is contacted with hydrogen at 50-350 degrees C in presence of catalyst comprising 5 wt.% or more group VIII metal(s) (A), calculated based on elemental metal with respect to total weight of the catalyst, group V element(s) (B), and refractory oxide (C) chosen from titania, zirconia and/or silica.    USE - Conversion of biomass-derived pyrolysis oil used for preparing biofuels and/or biochemicals. Uses include but are not limited to conversion of biomass-derived pyrolysis oil anti-oxidants, corrosion inhibitors, ashless detergents, dehazers, dyes, lubricity improvers, mineral fuel components, petroleum derived gasoline, diesel and/or kerosene fractions.    ADVANTAGE - The method enables economical and safe conversion of biomass-derived pyrolysis oil using a stable catalyst.
NOVELTY - Pre-coating material comprises a metallic substrate made of a catalytic material based on ceramic particles. The particles are inorganic, heat-resistant, chemically inert and crystallized, and have a mean diameter (D50) 0.01-1 mu m. The particles comprise at least one chemical element contained in the metallic substrate and at least one chemical element contained in the catalytic material.    USE - The pre-coating material is useful in a metal foam for the formation of catalyst, which is useful for hydrogenation reaction, reforming reaction and partial oxidation, and for the synthesis of methanol or ammonia (all claimed).    ADVANTAGE - The pre-coating material has improved thermal conductivity and sufficient stability. The catalytic foam is easy to prepare and handle, and exhibits controlled pore geometry, and improved thermal and mechanical strength.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a metal foam comprising, on its surface, a layer of pre-coating material;    (2) a method of producing the metal foam, comprising (a) mixing ethanol, ammonia and a surfactant at a temperature of 50-70 degrees C, (b) dissolving precursor metal salts of the pre-coating material, (c) adding metal salts dissolved in the mixture obtained in step (a), (d) cooling the mixture to room temperature, (e) processing the cooled mixture for 5-24 hours, (f) immersing the metal foam in the mixture, (g) removing the excess mixture to open the pores of the previously immersed metal foam, (h) drying the pre-coated foam, and (i) calcining the pre-coated foam and then dried at a temperature of 400-900 degrees C;    (3) a catalyst comprising the metal foam and a catalytic material that is joined to the metal foam by the particles; and    (4) a method of manufacturing the catalyst, comprising coating the metal foam with a catalyst slurry, and then heating at a temperature of 300-550 degrees C, to consolidate the catalyst deposition.
NOVELTY - A 3-aminopyrrolidine compound (II), is new.    USE - New 3-aminopyrrolidine compound is used for preparing (S,S)-2,8-diazabicyclo(4.3.0) nonane (claimed).    ADVANTAGE - The (S,S)-2,8-diazabicyclo(4.3.0) nonane is economically prepared using 3-aminopyrrolidine compound, by simple and environmentally-friendly process.    DETAILED DESCRIPTION - A 3-aminopyrrolidine compound of formula (II), is new.    R=amino protecting group;    Z=oxygen or 2H;and    Y'=chloro, bromo, iodo or hydroxy sulfonate, when Z is 2H, or H, hydroxy or 1-6C alkoxy, when Z is oxygen.    INDEPENDENT CLAIMS are included for the following:    (1) usage of 3-aminopyrrolidine compound (II) in preparation of (S,S)-2,8-diazabicyclo(4.3.0) nonane, which involves carrying out intramolecular ring closure reaction of compound (II) through functional group (Y'), group (Z) and amino group, obtaining (4aS,7aS)-octahydro-1H-pyrrolo(3,4-b)pyridin-2-one derivative of formula (Ia) or (4aS,7aS)-octahydro-1H-pyrrolo(3,4-b)pyridine derivative of formula (Ib), and reducing compound (Ia) and removing protecting group, or removing protecting group from compound (Ib);    (2) preparation of 3-aminopyrrolidine compound (II); and    (3) enzymatic synthesis of (S,S)-2,8-diazabicyclo(4.3.0) nonane, which involves reacting amine derivative of formula (IIIa) or (IIIb) in presence of transaminase and hydrolase by one-pot synthesis method.
NOVELTY - The present invention provides a Re-188-liposome automated synthesis apparatus, which comprises: configuring respective unit modules together and executing an automation procedure through a control software, so as to complete the four stages needed in the present invention: marking reaction, embedding reaction, separation/purification, and adjustment/filtration. When this device is in use, it is only necessary to place the reaction drugs into a specific reaction flask, turn on the power and use the gas pressure regulating valve to introduce reactive gases to facilitate the adjustment of the desired pressure. After starting the operating system of the present invention, an automated drug preparation procedure can be completed in a short time, it can be used in clinical diagnosis and treatment, and can save the production cost and avoid pollutions caused by manual operation.
NOVELTY - A rice cultivating method involves selecting robust woody branches, cutting lower lateral branches, placing in good nutrition soil bag, cutting mother plant and another strain of plant. The cultivation field is managed after planting by spraying water, fertilizing, enhancing soil permeability, irrigating dry soil and ditching. The field is subjected to weeding and pruning, followed by controlling pest by preventing rice plant from aphids, scale insects, spider mites and white wax moth cicada, picking flowers in second year, pouring 1-2% bio-pesticides and organic fertilizers.    USE - Method for cultivating rice.    ADVANTAGE - The method enables cultivating rice with high-quality and high-grade organic rice.    DETAILED DESCRIPTION - A rice cultivating method involves selecting one year robust woody branches, removing blade, removing 4-5 small branches, cutting lower lateral branches, placing in good nutrition soil bag, wrapping the bag with plastic membrane enzyme, maintaining soil moisture for 35-40 days, cutting mother plant and another strain of plant. The cultivation field is managed after planting by spraying water, fertilizing, enhancing soil permeability, irrigating dry soil, ditching, spraying liquid fertilizer, replanting, maintaining temperature at 12 degrees C, spraying the foliage with warm water at 6 degrees C and maintaining good ventilation. The field is subjected to weeding by cutting grass roots. The rice plant is subjected to pruning after rice plant grown to 15-20 cm, followed by growing rice plant after second year with main bud germination and new branches having strong potential health care and good leaf, controlling pest by preventing rice plant from aphids, scale insects, spider mites and white wax moth cicada, picking flowers in second year, pouring 1-2% bio-pesticides and organic fertilizers before 1 month of picking, picking the edge every 20-25 day.
NOVELTY - Recovery of vegetable oil from waste clay involves extracting vegetable oil from waste clay, separating extraction solvent and oil by fractionation method, collecting extraction solvent and oil, reusing the recovered extraction solvent, adding methanol and sulfuric acid to the extracted oil, esterifying the reaction mixture to obtain free fatty acid-esterified oil, adding esterified oil to methanol and basic catalyst, transesterifying to obtain methyl ester of glycerol, separating, neutralizing, washing, distilling, and removing residual basic catalyst, methanol and water.    USE - Recovery of vegetable oil used for producing high-value biodiesel.    ADVANTAGE - The method enables efficient recovery of vegetable oil from waste clay. The vegetable oil efficiently and economically provides high-value biodiesel with high recovery rate of 88%.    DETAILED DESCRIPTION - Recovery of vegetable oil from waste clay involves extracting vegetable oil from waste clay, separating extraction solvent and oil by fractionation method, collecting extraction solvent and oil, reusing the recovered extraction solvent, adding methanol and sulfuric acid to the extracted oil, esterifying the reaction mixture to obtain free fatty acid-esterified oil containing less than 2% or free fatty acid, adding esterified oil to methanol and basic catalyst, transesterifying at 70-80 degrees C for 60-90 minutes to obtain methyl ester of glycerol, separating methyl ester of glycerol, neutralizing, washing, distilling, and removing residual basic catalyst, methanol and water. The molar ratio of methanol and oil is 6-8. The weight ratio of sulfuric acid and oil is 0.01-0.02. The weight ratio of the basic catalyst and oil is 0.01-0.02.
NOVELTY - Thymol glycereth complex comprising thymol, glycereth and citric acid, is new.    USE - The composition is useful for: manufacturing water-soluble intermediates and oral care cleaning products; and treating skin diseases caused by fungi, Staphylococcus aureus, Escherichia coli, molds, Salmonella and other microorganisms.    ADVANTAGE - The composition can be easily prepared with high yield, good bactericidal effect and reduced pollution in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesizing the complex comprising adding thymol, glycereth and citric acid into a stainless steel device, uniformly mixing, where the stainless steel device is made of glass, heating the mixture at 50-80 degrees C, reacting the heated mixture, adjusting pH value, and uniformly stirring.
NOVELTY - Apparatus comprises: a primary processing unit (100) provided with a hopper on upper side for storing leaves humus, a rotary shaft for crushing the stored leaves humus, a blast pipe for supplying hot air and drying the leaves humus at lower portion of the rotary shaft, and a transferring screw for discharging the dried leaves humus; a fermentation broth automatic supply unit (200) for supplying water and beneficial microorganisms into the leaves humus; and an agitating part (300) for mixing the water and beneficial microorganisms with leaves hummus.    USE - The apparatus is useful for manufacturing natural fertilizer using minerals containing humus (claimed).    ADVANTAGE - The apparatus improves productivity.    DETAILED DESCRIPTION - Apparatus comprises: a primary processing unit (100) provided with a hopper on upper side for storing leaves humus, a rotary shaft for crushing the stored leaves humus, a blast pipe for supplying hot air and drying the leaves humus at lower portion of the rotary shaft, and a transferring screw for discharging the dried leaves humus; a fermentation broth automatic supply unit (200) for supplying water and beneficial microorganisms into the leaves humus; an agitating part (300) for mixing the water and beneficial microorganisms with leaves hummus; a sorting unit (400) for separating the mixed leaves hummus of a constant size; and a packing unit (500) for packing the selected leaves hummus.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic representation of the apparatus for manufacturing natural fertilizer using minerals containing humus.    Primary processing part (100)    Fermentation broth automatic supply unit (200)    Agitating part (300)    Sorting unit (400)    Packing unit (500)
NOVELTY - The stable foam comprises a mixture of saturated or unsaturated acids or fatty alcohols, vegetable or animal origin fat containing 8-22C, and 3-50C hydrocarbons or alcohols of vegetable, animal or oil. Organic alkali agents or inorganic non-ionic or anionic surfactants, preservatives, binders, and water are also included. A propellant gas is provided for expansion and formation of stable foam. Flame retardants, softeners, pigments, dyes, textile cosmetics, and antimicrobials are additionally included in the stable foam.    USE - Stable foam used as vehicle for applying chemical treatments to woven or non-woven substrates, and for use in finishing of products (foulards, knife or drums), continuous or semi-continuous dyeing processes, and in printing machine, rotary cylinder machines, painting machines, carousel machines for print (all claimed).    ADVANTAGE - The stable foam can be bottled in aerosol cans, pressure cylinders of fire extinguishers, and provides improvement in textile and non-woven articles.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a cylinder, which includes an injector base for foam cylinder, and gun propellant gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the foaming machine.    Base foams (B1,B2)    Foam cylinder (C1)    Gas cylinder (C2)    Pressure gage (PRI)    Valves (V1,V2)
NOVELTY - The apparatus (20) has solid electrolyte which is inserted into anode (30) and cathode (80). A restoration prevention layer (50) is arranged between the cathode and the solid electrolyte. The ratio of the restoration prevention layer is made larger than the solid electrolyte containing the element with the largest ionization tendency among the constitutent elements of the solid electrolyte. A sacrificial reduction zone (60) is provided between the restoration prevention layer and the cathode. A glue layer (70) is provided between the sacrificial reduction zone and the cathode.    USE - Hydrogen storage apparatus.    ADVANTAGE - Deterioration of the reductive reaction of the solid electrolyte in the cathode vicinity is prevented. The adhesiveness of cathode and solid electrolyte is improved with the reduction product produced in the sacrificial reduction zone. The hydrogen permeability of cathode is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the hydrogen storage apparatus. (Drawing includes non-English language text)    Hydrogen storage apparatus (20)    Anode (30)    Restoration prevention layer (50)    Sacrificial reduction zone (60)    Glue layer (70)    Cathode (80)
NOVELTY - The method involves removing carbon dioxide from biogas through biogas cool-down nitrogen. A biogas pipeline (1) is fixed to a compressor (2) for increasing pressure by 1. 5 MPa. The biogas is made to flow through a preliminary heat exchanger (3). Crude biogas is directed to a preliminary purification column (7), where separation of water and removal of hydrogen sulfide are carried out in the biogas. Liquid nitrogen is cooled at temperature of -62 to -72 degree Celsius. The biogas is passed to a biogas separator (13), where carbon dioxide is separated by removing other impurities from methane.    USE - Method for purifying biogas.    DESCRIPTION OF DRAWING(S) - The drawing shows a hydraulic circuit diagram of a biogas purification system.    Biogas pipeline (1)    Compressor (2)    Preliminary heat exchanger (3)    Preliminary purification column (7)    Biogas separator (13)
NOVELTY - The device has a concentrating tank (2) which is provided with first stainless steel slurry pump and polyethylene pipeline (8). A neutralizing tank (3) is set with sodium hydroxide aqueous solution inlet (10) and salt outlet (11). A mixing machine (5) has third material slurry pump and pipeline (12), finished product outlet (21) and conveyor (20). A crusher (4) is set with a mono-ammonium phosphate inlet (13), ammonium sulfate inlet (14), potassium sulfate inlet (15), boric acid inlet (16), sodium meta-silicate inlet (17), calcium chloride inlet (18) and magnesium sulfate inlet (19).    USE - Mechanical device for producing fish fertilizer containing composite amino acid and micro-element.    ADVANTAGE - The device structure is reasonable and the production process is simple. The waste pollution is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of mechanical device for producing fish fertilizer.    Concentrating tank (2)    Neutralizing tank (3)    Crusher (4)    Mixing machine (5)    Pipelines (8,12)    Sodium hydroxide aqueous solution inlet (10)    Salt outlet (11)    Mono-ammonium phosphate inlet (13)    Ammonium sulfate inlet (14)    Potassium sulfate inlet (15)    Boric acid inlet (16)    Sodium meta-silicate inlet (17)    Calcium chloride inlet (18)    Magnesium sulfate inlet (19)    Conveyor (20)    Finished product outlet (21)
NOVELTY - Synthesis of prosulfuron comprises reacting 2-Amino-4-methoxy-6-methyl-1,3,5-triazine , 2-aminobenzenesulfonic acid and 3,3,3-trifluoroprop-1-ene to obtain 2-(3,3,3-trifluoro-1-propenyl)benzenesulfonic acid, hydrogenating to obtain 2-(3,3,3-trifluoropropyl)benzenesulfonic acid, reacting with phosgene, ammonia and N,N-dimethylformamide to obtain 2-(trifluoromethyl)benzene-1-sulfonamide and reacting with dimethyl carbonate and 2-amino-4-methoxy-6-methyl-1,3,5-triazine.    USE - Method for synthesizing prosulfuron used as herbicide for broadleaf and gramineous weeds (claimed).    ADVANTAGE - The prosulfuron has low toxicity and environment-friendly.
NOVELTY - Method (M1) of culturing microalgae involves (a) (i) performing first culture of microalgae in a culture medium inside an incubator until a biofilm is formed on the liquid surface of the culture medium, and (ii) collecting at least portion of the biofilm formed on the liquid surface in the first culture and microalgae on the bottom surface of the incubator, and (b) performing a second culture of left-over microalgae on the bottom surface of the incubator until a biofilm is formed on the liquid surface of the culture medium.    USE - The method is useful for culturing microalgae, preferably green algae for producing algal biomass, preferably oil. The microalgae are chosen from Botryococcus sp., preferably B.sudeticus (FERM BP-11420), Chlamydomonas sp., Chlorococcum sp. (FERM BP-22262), Tetracystis sp., Characium sp. and Protosiphon sp. (all claimed).    DETAILED DESCRIPTION - Method (M1) of culturing microalgae involves (a) (i) performing first culture of microalgae in a culture medium inside an incubator until a biofilm is formed on the liquid surface of the culture medium, where the microalgae are retained on the bottom surface of the incubator, and (ii) collecting at least portion of the biofilm formed on the liquid surface in the first culture and microalgae on the bottom surface of the incubator, and (b) performing a second culture of left-over microalgae on the bottom surface of the incubator until a biofilm is formed on the liquid surface of the culture medium. An INDEPENDENT CLAIM is included for method (M2) of producing algal biomass, which involves (a) culturing the microalgae as mentioned in the method (M1), and (b) recovering product from second biofilm liquid surface formed in the culture medium.
NOVELTY - Detachable air supplying device comprises a discharging unit (12) for discharged air into the compost, a detachable end portion (11) for facilitating entry of the compost to an outer pipe (16), and an opening portion for passing air transferred form an inner pipe within the outer pipe. The inner pipe is connected to a ventilation pump and a ventilation pipe for forcibly injecting air. The device has multi-tube structure for injecting air into the compost.    USE - The device is useful for composting (claimed).    ADVANTAGE - The device can be maintained and operated easily, exhibits flexibility during adjusting installation angle, adjusts the amount of oxygen, humidity and temperature, and is economical.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the detachable air supplying device.    Detachable end portion (11)    Discharging unit (12)    Engaging portion (15)    Outer pipe (16)    Screwed connecting unit (17)
NOVELTY - An esomeprazole sodium enteric-coated tablet comprises a tablet core comprising esomeprazole sodium; and coating layers including an alkaline protective layer, an isolation layer, and an enteric layer. The alkaline protection layer comprises an alkaline film former, a lubricant, opacifier, stabilizer, and solvent. The isolation layer comprises a film former, lubricant, opacifier, and solvent. The enteric layer comprises a film-former, plasticizer, lubricant, opacifier, stabilizer, and solvent.    USE - An esomeprazole sodium enteric-coated tablet.    ADVANTAGE - The enteric-coated tablet has short production period, thus environment, temperature, and humidity does not affect tablet efficacy.    DETAILED DESCRIPTION - An esomeprazole sodium enteric-coated tablet comprises a tablet core comprising esomeprazole sodium; and coating layers including an alkaline protective layer, an isolation layer, and an enteric layer. The alkaline protection layer comprises a coating liquid including an alkaline film former, a lubricant, opacifier, stabilizer, and solvent, where the coating liquid has a pH value of 8-13. The isolation layer comprises a coating liquid including a film former, lubricant, opacifier, and solvent, where the coating liquid has a pH value of 7-8. The enteric layer comprises a coating liquid including a film-former, plasticizer, lubricant, opacifier, stabilizer, and solvent, where the coating liquid has a pH value of 5-6. An INDEPENDENT CLAIM is included for preparing the esomeprazole sodium enteric-coated tablet, comprising preparing a tablet core by mixing esomeprazole sodium, filler, stabilizer, disintegrant, binder, and lubricant; granulating; drying at 50 degrees C; tableting; and coating with coating layers including alkaline protective layer, isolation layer, and enteric layer.
NOVELTY - Production of calcite comprises removing impurities of calcite, crushing into 1 cm diameter particles, grinding, fuming to 170 degrees C for 3-5 hours through high-temperature oven, cooling to room temperature, and grinding; and sieving, re-grinding coarse particles while collecting fine particles, and mixing for 25 minutes.    USE - Method for production of calcite (claimed).    ADVANTAGE - The method saves sterilization method and production time which simplifies the process, improves production efficiency, and it has optimized process conditions, good crystal water removal effect, and reduced temperature and energy consumption.
NOVELTY - This utility new type relates to a one real time control sequencing batch sewage treatment device, comprising a inlet water pump, biological selecting pool, sequencing batch sewage processing pool, adding a medicament, a dosing pump, a water decanter, air blower, a sludge concentration meter, ultrasonic wave liquid level meter, a PH, a DO, ORP a, ammonia nitrogen on-line monitor a DA/AD data converter, a PLC control cabinet, a remote control computer, said inlet water pump in turn a biological selecting pool, sequencing batch sewage processing pool, inner the sequencing batch sewage processing pool set with a sludge concentration meter, ultrasonic wave liquid level, and set with a pH a, a DO, ORP and a ammonia nitrogen on-line monitor at a side pool wall, are a DA/AD data converter, a PLC control cabinet through Ethernet and remote control computer through a cable. According to characteristic point of instrument detection data for judging reaction finishing time, when using a real time effective to prevent aeration, aeration time or a too long caused by the sludge expansion and waste electric energy.
NOVELTY - A combined anaerobic fermentation tank, belongs to the biomass energy technology field, relating to a a municipal organic wastes combined Anaerobic fermentation tank, this tank comprises tank cover, a tank body and cloth disk, tank body outside wall has a heat insulation layer, a lower part mounting has feeding pipe and discharging bottom, middle part has mounted in the discharge tube and a tube, the upper part has a mounting feeding pipe and material discharging tube, a cloth disk mounting tank body inner cylinder wall upper, tank cover b cover the top part of tank body, a tank cover has discharge pipe equipped with a safe valve, this tank further comprises heating tube, lower feeding pipe and lower discharge pipe, heating pipe mounting inner cylinder b is tank body wall upper, lower feeding pipe and lower discharge pipe mounted in a tank body upper part of material disk outside wall, lower feeding pipe and centre axis of lower discharge pipe and tank body wall outside a lower feeding pipe and a lower discharging pipe mounted between the tangent point less than 50 degrees, the utility model is new type comprises structure is simple and reasonable, the operation energy consumption and low fermentation efficiency is high, it is suitable for industrial production\, wherein it effectively increases the fermentation efficiency.
NOVELTY - Preparation of cultivation material comprises cutting 50-60 pts. wt. bamboo shoot shell into sections, crushing into 2-3 cm particles, adding 0.8-1.2 pts. wt. 1.8-2.5% calcium carbonate and water, soaking for 8-10 hours, taking out, and drying; and adding with 10-20 pts. wt. mushroom residue, 8-10 pts. wt. wheat bran, 0.8-1.2 pts. wt. sucrose and 0.8-1.2 pts. wt. gypsum powder, Bone Powder mixing, adjusting pH to 8, adding into bag, and high-temperature steaming to carry out sterilization to 100-130 degrees C for 5-8 hours.    USE - Method for preparation of cultivation material used for mushroom (claimed), preferably oyster mushroom.    ADVANTAGE - The method is environment-friendly, reduces production cost, and increases growing speed and yield of mushroom.
NOVELTY - The system has a reinforced nitration pool (2) connected with a strengthening denitrification pool (4). An aeration pipe (18) is mounted with an aeration head (9). A top part of the reinforcing nitration pool is provided with an IN pool gas inner circulation pipe (6) and an IN pool discharge pipe (14). A strengthening denitrification pool (4) is set with an ID pool gas outside circulation pipe (11). A deaerator (3) is fixed with an inner land-fill gas air inlet pipe (1) through a deoxidizing air inlet pipe (12). The depositing pool is fixed with a sludge reflux pipe (8).    USE - Strengthening nitrogen denitrification process system.    ADVANTAGE - The system has high denitrogen efficiency, better stable effect, simple process, simple structure and low operation cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a side sectional view of a strengthening nitrogen denitrification process system.    Inner land-fill gas air inlet pipe (1)    Reinforced nitration pool (2)    Deaerator (3)    Strengthening denitrification pool (4)    IN pool gas inner circulation pipe (6)    Sludge reflux pipe (8)    Aeration head (9)    ID pool gas outside circulation pipe (11)    Deoxidizing air inlet pipe (12)    IN pool discharge pipe (14)    Aeration pipe (18)
NOVELTY - The system has a water pipe (2) provided with an upper part of a rectangular groove body (16). An upper part of a water collecting pipe (5) is connected with the rectangular groove body. An upper layer degradation mechanism (11) is provided with a lower layer degradation mechanism (12). A water plant (10) is connected with the rectangular groove body. A multi-hole aeration pipe group (7) is connected with an air pump (13) that is connected with a solar energy plate power supply device (14), where the solar power supply device is mounted on the rectangular groove body.    USE - Hidden layer solar intermittent aeration wetland system for sewage processing field for cooling region of a small town.    ADVANTAGE - The system discharges sewage in national standard, increases water quality of sealing period operation and reduces utilization rate of water dissolve oxygen, and has low operation cost and simple operation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a hidden layer solar intermittent aeration wetland system.    Water pipe (2)    Water collecting pipe (5)    Multi-hole aeration pipe group (7)    Water plant (10)    Upper layer degradation mechanism (11)    Lower layer degradation mechanism (12)    Air pump (13)    Solar energy plate power supply device (14)    Rectangular groove body (16)
NOVELTY - The device has a liquid storage container (8) connected with a machinery transmission device (4). An opening (11) is formed on a temporary manure storing container (1). An activity plate is fixed on a squatting pan. A through hole is formed on the temporary manure storing container. A fermentation container (3) is connected with a scraping device (2) and filled with microorganism microbial inoculum. The machinery transmission device is connected with a stirrer (31). A heating device (32) is integrated with the fermentation container.    USE - Domestic sewage processing device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a domestic sewage processing device.    Temporary manure storing container (1)    Scraping device (2)    Fermentation container (3)    Machinery transmission device (4)    Liquid storage container (8)    Opening (11)    Stirrer (31)    Heating device (32)
NOVELTY - A straw granule inorganic microorganism fertilizer comprises crop straw, inorganic fertilizer, attapulgite powder and plant growth-promoting agent. The microorganism fertilizer is prepared by grinding crop straw stick, sieving, adding inorganic fertilizer and attapulgite after stirring; carrying out normal fertilizer extruding, pelleting, drying, cooling, and obtaining fertilizer; and uniformly spraying microorganism microbial inoculum of bacteria suspension in fertilizer surface layer.    USE - Straw granule inorganic microorganism fertilizer.    ADVANTAGE - The microorganism fertilizer improves soil structure, has fast fertilizer effect, has long time effect, promotes soil beneficial bacterium, increases fertilizer use efficiency, and promotes growing.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram illustrating a preparation method of the straw granule inorganic one microorganism fertilizer. (Drawing includes non-English language text).
NOVELTY - An aminoglucose hydrochloride is prepared by dissolving acetyl glucosamine in water, adding strong alkali, heating, heat preserving, adding concentrated hydrochloric acid and salt, regulating pH at 3-5, neutralizing, decoloring, cooling, crystallizing, separating, and drying.    USE - Method for preparing aminoglucose hydrochloride (claimed).    ADVANTAGE - The method has strong hydrolysis reaction pertinence, less side effect, less strong alkali amount, labor protection and environment-friendly pressure, high product yield and short hydrolysis reaction time, and is suitable for industrial production.
NOVELTY - Separation of hesperetin from orange peel comprises mixing extraction solvent and orange peel; heating to 60-70 degrees C, and heat-preserving for 4-6 hours; filtering using 300 meshes bag filter, centrifuging at 4000 revolutions/minute, and clarifying to obtain clear hesperetin extract; heat preserving the extract at 60 degrees C, concentrating at reduced pressure, adding 4-6 times water, and crystallizing; plate-frame filter press filtering, washing with water, and vacuum drying at 60-70 degrees C; and adding solid sodium hydroxide to adjust pH to neutral, and recovering alcohol.    USE - Method for the separation of hesperetin from orange peel (claimed).    ADVANTAGE - The method is simple, inexpensive, and environment-friendly.    DETAILED DESCRIPTION - Separation of hesperetin from orange peel comprises mixing extraction solvent and orange peel, where the mass ratio of orange peel and extraction solvent is 1: 15-20; heating to 60-70 degrees C, and heat-preserving for 4-6 hours; filtering using 300 meshes bag filter, centrifuging at 4000 revolutions/minute, and clarifying t obtain clear hesperetin extract; heat preserving the extract at 60 degrees C, concentrating at reduced pressure to obtain an alcohol content of 10-20%, adding 4-6 times water, crystallizing, and standing for 12-24 hours; carrying out plate-frame filter press filtering, washing with water, and vacuum drying at 60-70 degrees C to obtain hesperetin; and adding solid sodium hydroxide to adjust pH to neutral, and recovering alcohol.
NOVELTY - The network disk-shaped a sewage treatment biological carrier, plastic silk layers by overlapping with irregular network eye composed of screen plate, table area 500-1400m2 a m3, the void ratio 70-90 %, plastic diameter is 0.5-1.0 mm, average interval of irregular pitch 10-30 mm. Sewage treatment network disk-shaped biology carrier is disk-shaped, or a semi disk, or is spliced into disc-shaped. Active sludge amount is larger, the high activity, sewage treatment efficiency high, effect is better, the space is small, the cost is low. And a property of biological carrier a table area, a biological film of update speed and other factors. Table area of a larger, activated sludge quantity is large, a affect a property of a factor. Adhesion, activated sludge quantity is larger. Biological film update speed is quicker, sludge activity. Adhesion and biological film update speed is affect a property is an important factor.
NOVELTY - This utility new type claims a novel biogas pool, comprising biogas pool, further provided with a feeding pipe, the feeding pipe is located on the marsh gas pool, a feeding pipe of discharge wherein extending to liquid surface of marsh gas pool, a feeding pipe side is further provided with a washing device, the washing device comprises vacuum pump and water storage tank, said water storage tank is set on the marsh gas pool, water storage tank through water pipe and a feeding pipe, a vacuum pump mounted dd water pipe a, this utility new type through washing device, realize the pool water of pool in inner inner feeding pipe for adding a new bilateral marsh gas pool inner material, at the same time using a washing water feeding pipe, material of fermentation for marsh gas and a product, this utility new type device structure is simple, the operation is convenient and wide applicability.
NOVELTY - The device has an anaerobic fermenting chamber (1) connected with a door by a hopper body. An upper part of a connected pipe (9) is arranged with a cloth that is connected with a multi-nozzle (10). A biogas reflux pump (4) is mounted with a biogas slurry feed tube (2). A marsh gas output pipe (7) is connected with the hopper body. An upper end of an air pipe (8) is connected with the hopper body. A heat preservation cotton is arranged with an upper belt. The biogas liquid discharge pipe (6) is arranged with a flow meter (13).    USE - Dry type anaerobic fermentation device for husbandry marsh gas preparation.    ADVANTAGE - The device realizes the fermentation process in a simple and quick manner, and better inner heat preservation effect. The device avoids incomplete fermentation, and reduces energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a dry type anaerobic fermentation device.    Anaerobic fermenting chamber (1)    Biogas slurry feed tube (2)    Biogas reflux pump (4)    Biogas liquid discharge pipe (6)    Marsh gas output pipe (7)    Air pipe (8)    Connected pipe (9)    Multi-nozzle (10)    Flow meter (13)
NOVELTY - The device has an Anaerobic digestion part, a gas collecting part and a sampling part material part. The Anaerobic digestion part is provided with an Anaerobic digestion bottle, a constant temperature stir system, a gas collecting part, an air outlet, a one-way valve, a pneuma pipe and a gas volume meter and gas collecting bag. The Anaerobic digestion bottle has a volume of 100 to 1000 or 200-500 mL. A bottle wall of the anaerobic digestion bottle is provided with a baffle plate. The width of the baffle plate and the bottle is of specific ratio.    USE - Potential device for producing biomass biochemical for biomass anaerobic digestion test research.    ADVANTAGE - The device produces the biomass biochemical in a simple manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a potential device for producing biomass biochemical.
NOVELTY - A gypsum rubrum is prepared by using microwave for calcite in liquid medium carrying out crude process step.    USE - Method for preparation of gypsum rubrum (claimed).    ADVANTAGE - The method has simple operation, does not pollute environment, and can provide stable product quality.
NOVELTY - Ecological orange pest control based on predatory mites comprises using predatory citrus psyllid and citrus red mite, as a base and using mineral oil emulsion or/and matrine as an auxiliary pesticide.    USE - The method is useful for ecological orange pest control based on predatory mites (claimed).    ADVANTAGE - The method: is simple; utilizes low toxicity pesticide, thus protecting natural enemy to a larger extent; and reduces the generation of 3 wastes to enable sustainable pest control.
NOVELTY - Organic crop fertilizer comprises 20-45 pts. wt. carbon phosphorus potassium, 10-25 pts. wt. organic fertilizer leavening agent, 25-35 pts. wt. humic acid, 20-30 pts. wt. poly-aspartic acid, 15-25 pts. wt. calcium-magnesium phosphate fertilizer, 25-45 pts. wt. dicyandiamide, 10-45 pts. wt. ammonium molybdate heptahydrate, 10-35 pts. wt. plant additive, 20-45 pts. wt. soil regulator, 10-15 pts. wt. peptone, 20-35 pts. wt. urea particles and 5-10 pts. wt. rare earth additive.    USE - Used as an organic crop fertilizer.    ADVANTAGE - The fertilizer: ensures easy control of its amount during fertilization process; has simple preparation process; and is suitable to increase soil organic substances, activate original humus, improve soil cation exchange capacity, improve soil activity, increase soil absorption performance and buffering performance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing the fertilizer, comprising (a) crushing carbon phosphorus potassium, humic acid, polyaspartic acid, calcium-magnesium phosphate fertilizer, dicyandiamide, ammonium molybdate heptahydrate, peptone and urea particles by a crusher, transferring into a fermentation tank, adding organic fertilizer leavening agent, adding 12-15% water , uniformly mixing in a mixing machine, sealing and fermenting, (b) removing the material, allowing to stand at room temperature for 3-5 hours, adding plant additive, soil regulator and rare earth additive, mixing uniformly for 20-40 minutes, (c) subsequently, drying the material until the water content is 2-5% at 80-120 degrees C, and (d) transferring the qualified material into a plate type granulator, and granulating until the particle diameter is 4-5 mm.
NOVELTY - Ammonium nitrate and potassium nitrate production and wastewater recycling system comprises potassium chloride dissolution device (1), potassium nitrate crystallization device (2), potassium nitrate centrifugal separator (3), mixing tank (4), concentrator (5), ammonium chloride crystallization device, condensate collection system, membrane separation system, water desalination system and ammonium chloride centrifugal separator.    USE - Ammonium nitrate and potassium nitrate production and wastewater recycling system.    ADVANTAGE - The system is environment-friendly and cost-saving.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of ammonium nitrate and potassium nitrate comprising crystallizing potassium nitrate, concentrating, placing condensate from ammonium chloride crystallization device into the condensate collection system, collecting condensate by returning directly into the potassium chloride dissolution apparatus as dissolved water or purifying through membrane separation system, introducing separated water into the water desalination system while returning remaining membrane separation concentrated liquid into the potassium chloride dissolution apparatus, returning the obtained ammonium chloride mother liquor into potassium chloride dissolution device and recycling.    DESCRIPTION OF DRAWING(S) - The drawing shows a structure schematic diagram of ammonium nitrate and potassium nitrate production and wastewater recycling system.    Potassium chloride dissolution device (1)    Potassium nitrate crystallization device (2)    Potassium nitrate centrifugal separator (3)    Mixing tank (4)    Concentrator (5)
NOVELTY - Method for producing acetic acid from biomass feedstock involves subjecting biomass feedstock to chemical treatment, performing solid-liquid separation, culturing acetic acid producing microorganism in liquid fractions, and producing acetic acid from cultured product.    USE - The method is useful for producing acetic acid from biomass feedstock (claimed).
NOVELTY - A catalyst comprises a carrier containing complex oxide of cerium and zirconium, and a catalyst active metal supported by the carrier and containing 0.1-10 %mass cobalt with respect to 100 %mass carrier. The complex oxide is manufactured by sol gel process, and has oxygen defect.    USE - Catalyst is used in apparatus for fuel cell system for manufacturing hydrogen-containing gas (all claimed).    ADVANTAGE - The catalyst has excellent self-heating ability, and enables manufacture of hydrogen-containing gas with high yield.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of catalyst, which involves producing complex oxide by sol gel process, fixing the catalyst active metal in the complex oxide, introducing oxygen defect in the complex oxide, and reducing the complex oxide;    (2) manufacture of hydrogen-containing gas, which involves supplying a hydrocarbon gas and an oxygen gas at normal temperature to the catalyst, heating the catalyst, contacting hydrocarbon gas with the heated catalyst, and reforming the hydrocarbon gas; and    (3) hydrogen production apparatus, which consists of a modification unit to modify hydrocarbon gas and to obtain hydrogen gas, a hydrocarbon gas supply unit connected to the modification unit and to supply the hydrocarbon gas to the modification unit, an oxygen gas supply unit connected to the modification unit and to supply oxygen gas to the modification unit.
NOVELTY - A photochemical electrode (201) consists of a metal region containing metal or metallic compound, and a thin metal film layer which is film coated periodically, such that a portion of surface excite a surface plasmon using the metal region containing metal or metallic compound.    USE - Photochemical electrode is used in apparatus for generating hydrogen and device for reducing carbon dioxide (all claimed) for generating carbon monoxide and formic acid.    ADVANTAGE - The photochemical electrode has improved reaction promotion efficiency due to improvement of excitation efficiency of surface plasmon by excitation light.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrogen-generating apparatus (200);    (2) generation of hydrogen;    (3) carbon dioxide-reducing device; and    (4) reduction of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of hydrogen-generating apparatus.    Hydrogen-generating apparatus (200)    Photochemical electrode (201)    Cathode chamber (202)    Light source (203)    Counter electrode (204)
NOVELTY - The method involves acquiring a captured image, which is obtained by hot-pressing corresponding to an electrolytic membrane, where a transfer sheet (20) is imaged for the catalyst layer formation after the peeling. The catalyst residual unit is detected from the captured image by performing the light or dark determination. The binding region is formed while adjoining the adjacent catalyst residual unit, where a mask area is appointed based on the binding region when the binding region is more than a predetermined size.    USE - Method for inspecting a catalyst coating film for the fuel cells manufactured using a transfer sheet for the catalyst layer formation.    ADVANTAGE - The captured image obtained by hot-pressing corresponding to an electrolytic membrane is acquired, where a transfer sheet is imaged for the catalyst layer formation after the peeling, and hence ensures increasing the detection accuracy of the inferior goods in an effective manner and improves the detection precision of an inspection apparatus in a reliable manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an inspection apparatus for a catalyst coating film for the fuel cells. (Drawing includes non-English language text).    Catalyst coating film (10)    Electrolytic membrane sheet (11)    Catalyst layer (12)    Transfer sheet (20)    Camera (100)    Electronic controller (120)
NOVELTY - Method for composting organic waste involves (a) collecting organic waste, and crushing the waste, (b) mixing the waste with sawdust, cocopeat and rice bran, (c) subjecting mixture to first fermentation process using pig urine and aerobic microorganisms, (d) stirring the obtained primary fermentation product, (e) mixing secondary fermentation product with pig urine and calcium silicate, and (f) performing aging of resulting mixture and packing product.    USE - The method is useful for composting organic waste (claimed).    DETAILED DESCRIPTION - Method for composting organic waste involves (a) collecting organic waste, where the collected waste is fed into an input hopper, dehydrating the collected waste, screening dehydrated waste and crushing screened waste, (b) transferring the crushed organic waste into a mixing tank, and mixing the resulting organic waste with 50-60 wt.% sawdust, 10 wt.% cocopeat and 5 wt.% rice bran, (c) subjecting the obtained mixture to first fermentation process using pig urine and aerobic microorganisms for 6-7 days to obtain primary fermentation product, (d) stirring the obtained primary fermentation product at 70-80 degrees C and performing secondary fermentation of resulting product, (e) mixing the secondary fermentation product with pig urine and calcium silicate in ratio of 1:0.5 and ripening the resulting mixture for 13-15 days, and (f) performing aging of resulting mixture for 20 days or more and packing product.
NOVELTY - Preparing agricultural antibiotic-containing flies booby trap agent comprises (i) milling 5-10 wt.% brown sugar, 1-5 wt.% fishmeal, 84-93 wt.% wheat bran and 1-5 wt.% fresh maggots, mixing, adding water to adjust the moisture content to 40-60%, sealing, and slightly fermenting to obtain attractant; (ii) adding 5% fendona as insecticidal factor into the attractant in the mass ratio of 1:10, to obtain flies killing attractant agent; and (iii) adding the veterinary use ciprofloxacin hydrochloride into 0.1-0.5 wt.% flies killing attractant agent.    USE - The method is useful for preparing agricultural antibiotic-containing flies booby trap agent (claimed).    ADVANTAGE - The method does not pollute the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for use method of the flies booby trap agent, comprising adjusting the moisture content of booby trap agent to 40-60%, placing 200 g booby trap agent in a shallow dish, moisturizing, placing in a breeding environment, where the flies get attracted to brown sugar, fishmeal and wheat bran fermentation odor and fresh maggots milled material, and thus feed on the booby trap agent, where the fendona can rapidly kill the flies the commensal bacteria is partially removed from gut, produce offspring less than normal flies, and thus achieves sustainable control effect.
NOVELTY - One with a maintenance rehabilitation effect of hydrogen and machine, comprises one power supply unit, one electric connection of the electrolytic unit and this power source unit, and one and this electrolysis unit is connected the pneuma unit. This electrolysis unit including electrolytic groove is one containing electrolyte, and a phase interval is set with multi-b of a plate in this electrolytic groove, the electrode plate can be electrolyte containing b of electrolyte in this electrolytic groove to generate hydrogen and oxygen. This air supply unit including one and this electrolytic groove connected to a conveying pipe of the hydrogen and oxygen electrolysis groove in this produce of the, and set with one b this conveying pipe and used for absorbing moisture in a wet-removing, by this conveying pipe the output of hydrogen and oxygen can be directly used for human body. Absorbing mixed gas of hydrogen and oxygen, and it can promote metabolism and antioxidant with a effect, so it can achieve the purpose of maintenance and rehabilitation.
NOVELTY - A Chinese herbal medicine preparation comprises walnut, red Chinese yam, rhizoma corydalis, radix clematidis, rhizoma ligustici wallichii, Angelica, cortex moutan, musk, Salvia, safflower, medlar, kuan jin teng, Eucommia ulmoides vine, frankincense, myrrh, herba epimedii, radix angelicae, borneol, tuckahoe and Dendropanax dentigerus root and stem.    USE - Chinese herbal medicine preparation in the form of agent used for curing lumbar intervertebral herniation (all claimed).    ADVANTAGE - The preparation has short treatment course and no side effect, and is nontoxic and is convenient to use. The method has unique process and has low cost, is simple, energy-saving and environment-friendly, obviously shortens production period, and reduces production cost and energy consumption.    DETAILED DESCRIPTION - A Chinese herbal medicine preparation comprises 21-25 pts. wt. walnut, 18-24 pts. wt. red Chinese yam, 20-25 pts. wt. rhizoma corydalis, 20-24 pts. wt. radix clematidis, 20-25 pts. wt. rhizoma ligustici wallichii, 20-25 pts. wt. Angelica, 12-16 pts. wt. cortex moutan, 11-16 pts. wt. musk, 25-35 pts.wt. Salvia, 18-22 pts. wt. safflower, 13-17 pts. wt. medlar, 10-18 pts. wt. kuan jin teng, 10-15 pts. wt. Eucommia ulmoides vine, 10-15 pts. wt. frankincense, 10-15 pts. wt. myrrh, 20-26 pts. wt. herba epimedii, 10-15 pts. wt. radix angelicae, 10-15 pts. wt. borneol, 16-20 pts. wt. tuckahoe and 12-16 pts. wt. Dendropanax dentigerus root and stem. An INDEPENDENT CLAIM is included for preparation of Chinese herbal medicine preparation comprising grind crushing all raw materials into powder, mixing uniformly, water leaching at 25-35 degrees C for 12 hours, boiling with low heat for 10-15 minutes, heating with low heat for 0.5-3 hours, filtering, and sterile filling.
NOVELTY - Preparing Tongxieyaofang ning granule involves mixing radix paeoniae alba, green tangerine orange peel, Allium macrostemon and bighead Atractylodes rhizome in weight ratio of 1.6:1.6:1:1 to obtain a mixture. The mixture is soaked into water (8-15 times) and then extracted twice by using an ultrasonic multi-functional extraction tank at 48-52 degrees C for 1-2 hours to obtain extraction liquids. Extraction liquids are filtered to obtain medicinal liquid and medicinal residue. Medicinal residue is extracted into water at 50 degrees C for 1-2 hours and filtered to obtain medicinal liquid.    USE - Method for Tongxieyaofang ning granule (claimed).    ADVANTAGE - The method enables to prepare Tongxieyaofang ning granule in a safe and eco-friendly manner. Tongxieyaofang ning granule has high paeoniflorin content.    DETAILED DESCRIPTION - Preparing Tongxieyaofang ning granule involves mixing radix paeoniae alba, green tangerine orange peel, Allium macrostemon and bighead Atractylodes rhizome in weight ratio of 1.6:1.6:1:1 to obtain a mixture. The mixture is soaked into water (8-15 times) and then extracted twice by using an ultrasonic multi-functional extraction tank at 48-52 degrees C for 1-2 hours to obtain extraction liquids. Extraction liquids are filtered to obtain medicinal liquid and medicinal residue. Medicinal residue is extracted into water at 50 degrees C for 1-2 hours and filtered to obtain medicinal liquid. Medicinal liquids are combined, concentrated and spray dried to obtain extract powder. Cyclodextrin and dextrin are mixed with extract powder and then purified water is added at 85-90 degrees C for 0.5-1.5 hours and cooled. Cooled product is crystallized, filtered and dried to obtain beta-cyclodextrin compound. Egg white is added in the beta-cyclodextrin compound and then granulated through 10-60 meshes sieve to obtain granule, which is packaged in a bag.
NOVELTY - The deodorant contains 60-90 wt.% lactic acid fermentation liquid, 1-10 wt.% bacillus fermentation liquid, 9-30 wt.% yeast mixing fermentation liquid, yellow serofluid, 0-10 wt.% white granulated sugar and brown sugar. Lactic acid is selected from lactobacillus, bead bifid bacterium or pediococcus piece. The bacillus is selected from bacillus subtilis, bacillus licheniformis, bacillus coagulans and bacillus cereus or bacillus brevis. Yeast is selected from saccharomyces cerevisiae yeast, grape juice yeast, hansenula, torulopsis, candida and yeast or geotrichum candidum.    USE - Microorganism deodorant. Uses include but are not limited to rubbish, sewage, livestock, poultry animal house and food processing factory.    ADVANTAGE - The deodorant is eco-friendly, and ensures better deodorization and air purification effect of a food processing factory, better amonia nitride removing effect of above 90% and hydrogen selenide removing rate of above 70%, reduces soybean curd cost and avoids pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a microorganism deodorant preparation method.
NOVELTY - The jar has a vacuum jar body whose inner wall is provided with an inner chamber and fixed with a heat conductor i.e. heat conducting oil. The vacuum jar body is mounted with a heating device that is connected with a power supply socket through a lead. A vacuum pumping hole of the jar body is fixed with an annular block. The heating device is equipped with a constant-temperature heater with a temperature sensor or PTC heating module with the temperature sensor. The power supply socket and a direct current power source or AC power source are connected with each other.    USE - Environment-friendly constant temperature vacuum double-layer cupping jar for vacuum extraction device.    ADVANTAGE - The jar enters jar body of heat and drug properties of Chinese medicine into body of local temperature stimulation of the skin so as to ensure better recovery effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of an environment-friendly constant temperature vacuum double-layer cupping jar.
NOVELTY - The removal device has cyclone air outlet pipeline (22) that is connected to a umbrella-shaped dust remover corresponding to air inlet (31). The air outlet of the housing (2) is located at top of shell and the water curtain dust remover and air outlet is connected. A water curtain dirt catcher is set into pneuma, in which between the air outlet set with multi-high-low strewed is a water curtain baffle plate. An umbrella-shaped baffle (16) exists horizontal downward of a cyclone ash into head of the shell, and umbrella-shaped dust remover outlet (14) connected to a raw material pipeline.    USE - Removal device for fertilizer exhaust dust.    ADVANTAGE - Enables to saves energy, while having reasonable design, which makes the fertilizer exhaust dust removal device easy to popularize.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the fertilizer exhaust dust removal device.    Housing (2)    Umbrella-shaped dust remover outlet (14)    Umbrella-shaped baffle (16)    Cyclone air outlet pipeline (22)    Air inlet (31)
NOVELTY - Controlled release fertilizer microsphere comprises 60-80 pts. wt. composite fertilizer, 10-20 pts. wt. chitosan, 1-3 pts. wt. polyvinyl alcohol and 1.0-5.0 pts. wt. sodium alginate.    USE - Controlled release fertilizer microsphere.    ADVANTAGE - Controlled release fertilizer microsphere is prepared in a simple, cost-effective and eco-friendly manner, ensures improved industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a controlled release fertilizer microsphere, which involves:    (A) dissolving chitosan in acetic acid solution to prepare chitosan acetic acid solution, and then stirring the obtained material with composite fertilizer and polyvinyl alcohol with 500-1000 rotations per minute for 2-5 minutes;    (B) dissolving sodium alginate in water to prepare sodium alginate solution;    (C) dissolving chitosan and composite fertilizer, and then mixing them with potassium hydroxide to maintain 4.5-6.5 pH;    (D) adding crosslinking agent to the obtained material at 50-80 degrees C, and then stirring them at 600-1000 rotations per minute for 15-30 minutes;    (E) centrifuging the obtained material with 4000 rotations per minute for 5 minutes, and then removing the upper layer to obtain clear liquid;    (F) adding the obtained material with sodium alginate solution, and then performing ultrasonic oscillation for 10 minutes to obtain microsphere; and    (G) drying the obtained material at 60-80 degrees C for 15-30 minutes to obtain the finished product.
NOVELTY - Composition comprises 35-50 pts. wt. straw, 10-15 pts. wt. peony seed shell, 5-10 pts. wt. peony seed meal, 10-15 pts. wt. bran, 5-10 pts. wt. tea residue, 5-10 pts. wt. radix bupleuri residue, 1-5 pts. wt. potassium dihydrogen phosphate, 1-3 pts. wt. gypsum, 10-15 pts. wt. zeolite and 3-5 pts. wt. kaolin.    USE - Composition used for cultivating edible mushroom (claimed).    ADVANTAGE - The composition ensures increased air permeability and water retaining capacity of soil and improved quality and yield of mushroom.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing composition, which involves:    (A) drying and crushing straw, peony seed shell, peony seed meal, bran, tea residue and radix bupleuri residue;    (B) mixing remaining raw material, potassium dihydrogen phosphate, gypsum, zeolite and kaolin to obtain culture material;    (C) regulating water content of culture material to 65-70% and pH to 10-11;    (D) fermenting obtained material at 30-40 degrees C for 5-7 days;    (E) regulating water content fermented material to 60-65%;    (F) drying fermented material at 60-65 degrees C for 2-3 days; and    (G) mixing dry fermented material and powder to obtain product.
NOVELTY - Preparing manganese ammonium citrate involves reacting 100 pts. wt. water and 6-6.5 pts. wt. manganese sulfate with stirring to obtain manganese sulfate solution. 3-3.5 pts. wt. Sodium carbonate is added in manganese sulfate solution and filtered to obtain manganese carbonate precipitate, which is dispersed uniformly in water and 5-5.5 pts. wt. citric acid is added to obtain a transparent solution. Transparent solution is boiled, concentrated and cooled to room temperature. 15-16 pts. wt. Ammonium hydroxide is added in transparent solution with stirring uniformly and dried.    USE - Method for preparing manganese ammonium citrate (claimed) used in water soluble fertilizer, fertilizer, plant growing regulator and soil conditioning agent.    ADVANTAGE - The method enables to prepare manganese ammonium citrate is eco-friendly and cost-effective without having residue, and has improved compatibility and absorption.    DETAILED DESCRIPTION - Preparing manganese ammonium citrate involves reacting 100 pts. wt. water and 6-6.5 pts. wt. manganese sulfate with stirring to obtain manganese sulfate solution. 3-3.5 pts. wt. Sodium carbonate is added in manganese sulfate solution and filtered to obtain manganese carbonate precipitate, which is dispersed uniformly in water and 5-5.5 pts. wt. citric acid is added to obtain a transparent solution. Transparent solution is boiled, concentrated and cooled to room temperature. 15-16 pts. wt. Ammonium hydroxide is added in transparent solution with stirring uniformly and dried by using a drying tank to obtain a solid product. The solid product is cooled and crushed to obtain final product.
NOVELTY - Composite modifying agent is prepared by utilizing 260-310 pts. wt. organic fertilizer, 25-31 pts. wt. microbial inoculum, 0.03-0.07 pts. wt. difenoconazole, 0.05-0.1 pts. wt. pyrethrum, 0.03-0.09 pts. wt. Bacillus thuringiensis, 0.04-0.08 pts. wt. chlorine dioxide and 0.0.02-06 pts. wt. Lactobacillus.    USE - Composite modifying agent used for repairing heavy metal contaminated soil (claimed).    ADVANTAGE - The composite modifying agent is prepared in a simple and cost-effective manner.
NOVELTY - Remediation agent comprises 280-320 pts. wt. organic fertilizer, 28-32 pts. wt. microorganism inoculants, 0.03-0.07 pts. wt. matrine, 0.05-0.1 pts. wt. pyrethrum, 0.03-0.09 pts. wt. rotenone, 0.04-0.08 pts. wt. chlorothalonil and 0.02-0.06 pts. wt. Bacillus thuringiensis powder.    USE - Remediation agent used for processing heavy metal contaminated soil (claimed).    ADVANTAGE - The remediation agent has insecticidal and bactericidal properties.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing remediation agent, which involves:    (A) sterilizing organic fertilizer in a plastic thin film, and then removing thin film and mixing uniformly microbial inoculum;    (B) mixing matrine, pyrethrum and rotenone, drying, sieving and adding water with stirring to obtain a suspension solution;    (C) spraying suspension solution on obtained fertilizer, and drying to obtain a coated product;    (D) mixing remaining components adding water with stirring to obtain a liquid; and    (E) spraying liquid on coated product, and then drying to obtain final product.
NOVELTY - Controlled release organic fertilizer composition preparation involves mixing organic material with 30-40 part carbon or nitrogen content, 3-5% nitrogen, phosphorus and potassium, 5-15% clay or mellow, 25% ash content, 50-60% water and viable microorganism. The obtained mixture is fermented for 3-5 days, where total viable count is greater than or equal to 0.5 hundred million/g and the temperature is greater than or equal to 40 degrees C. The obtained fermented material is mixed with chemical fertilizer,and then fermented for 3-5 days to obtain the finished product.    USE - Controlled release organic fertilizer composition.    ADVANTAGE - The controlled release organic fertilizer composition is prepared in cost-effective manner.
NOVELTY - Fertilizer composition comprises 2-5 pts. wt. (particularly 3 pts. wt.) urea, 80-85 pts. wt. (particularly 82 pts. wt.) organic fertilizer, 5-10 pts. wt. (particularly 7 pts. wt.) trace element and microorganism microbial inoculum, where the microorganism microbial inoculum is 120-200 hundred million (particularly 106 hundred million) colony forming unit.    USE - Fertilizer composition used for cultivating green food that is cabbage (claimed).    ADVANTAGE - The fertilizer composition is prepared in eco-friendly manner, and ensures improved yield of cabbage and improved trace element content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing a fertilizer composition, which involves:    (A) extruding organic fertilizer, and then granulating and drying them;    (B) extruding trace element, and then granulating and drying them;    (C) extruding microorganism microbial inoculum and multifungus powder, and then granulating and drying them; and    (D) mixing all the obtained material, and then mixing them with large granule urea to obtain the finished product.
NOVELTY - Soil repairing agent comprises 280-320 pts. wt. organic fertilizer, 0.03-0.07 pts. wt. matrine, 0.05-0.1 pts. wt. pyrethrum, 0.03-0.09 pts. wt. rotenone, 0.04-0.08 pts. wt. toxaphene and 0.02-0.06 pts. wt. Bacillus thuringiensis powder.    USE - Soil repairing agent.    ADVANTAGE - The soil repairing agent has improved insecticidal effect, and is cost-effective and prepared simply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing soil repairing agent, which involves:    (A) covering organic fertilizer using a thin film;    (B) sterilizing the obtained material using ultraviolet radiation;    (C) placing pyrethrum and rotenone in a non-ferrous container at 10-20 degrees C, preferably 15 degrees C in warm water;    (D) collecting the supernatant;    (E) putting matrine, toxaphene and Bacillus thuringiensis powder in a container;    (F) stirring the obtained material uniformly;    (G) adding the obtained supernatant to the stirred material; and    (H) spraying the obtained organic fertilizer to the obtained mixture to obtain the desired product.
NOVELTY - Preparing fenofibrate (II) comprises performing esterification reaction of fenofibric acid (I) with isopropyl alcohol and nanomagnetic solid superacid catalyst.    USE - The process is useful for preparing (II), which is useful for reducing blood fat (claimed).    ADVANTAGE - The process ensures easy and simple preparation of (II) with high yield and without corrosion and pollution in an economical and eco-friendly manner.    DETAILED DESCRIPTION - Preparing fenofibrate of formula (II) comprises performing esterification reaction of fenofibric acid of formula (I) with isopropyl alcohol and nanomagnetic solid superacid catalyst.
NOVELTY - Processing waste salt of dimethyl sulfoxide comprises adding waste salt of dimethyl sulfoxide solution, nitric acid, nitric oxide and sodium nitrite into a reaction container, uniformly mixing, performing oxidation reaction, adding sodium hydroxide to the reacted mixture, carrying out neutralization reaction, crystallizing the reacted mixture, adding dimethyl sulfone, sodium nitrate and methyl sulfonate to the crystallized mixture, separating crystals, and uniformly stirring.    USE - The method is useful for processing waste salt of dimethyl sulfoxide (claimed).    ADVANTAGE - The method is capable of simply and efficiently processing the waste salt of dimethyl sulfoxide with reduced energy consumption in an eco-friendly manner.
NOVELTY - Extracting dehydrated andrographolide from Andrographis paniculata comprises providing crushed Andrographis paniculata in an extraction tank and then extracting using ethanol and filtering the residue, subjecting the extract to vacuum ethanol recovery process and then to high speed centrifugation to obtain precipitate, adding ethanol in the precipitate, filtering the ethanol solution, performing decolorization process using an ion exchange resin, adding refining agent to a decolorizing agent, and crystallizing and purifying the obtained product and then vacuum drying.    USE - The method is useful for extracting dehydrated andrographolide from Andrographis paniculata (claimed).    ADVANTAGE - The method is capable of rapidly, economically and efficiently extracting the dehydrated andrographolide from Andrographis paniculata with high purity (more than 98%) and yield.    DETAILED DESCRIPTION - Extracting dehydrated andrographolide from Andrographis paniculata comprises selecting dried Andrographis paniculata and then crushing, providing the crushed product in an extraction tank and then extracting using 75 wt.% of ethanol for three times at a temperature of 50 degrees C and filtering the residue, subjecting the extract to vacuum ethanol recovery process and then subjecting to high speed centrifugation to obtain precipitate, adding 80 wt.% of ethanol in the precipitate and then dissolving by stirring, filtering the ethanol solution using a 200 stainless steel mesh filter and then purifying, performing decolorization process using an ion exchange resin, passing the filtrate through a ceramic membrane, adding refining agent to a decolorizing agent and then stirring for 20 minutes, crystallizing the obtained product to give crystals and then purifying, and vacuum drying the crystallized product. The extraction process is carried out for 2 hours, 1.5 hours or 1 hour.
NOVELTY - Chlorine-substituted azaindole compounds (I) are new.    USE - (I) are useful for treating cardiovascular disease, diabetes and cancer.    ADVANTAGE - (I) are prepared with high yield (i.e. more than 85%) in a simple and environment-friendly manner.    DETAILED DESCRIPTION - Chlorine-substituted azaindole compounds of formula (I) are new.    R1 = H, methyl, methyl or acetyl; and    R2 = methoxy, cyclopropyl, bromine or phenyl.    An INDEPENDENT CLAIM is included for the preparation of (I).
NOVELTY - Method for disinfecting livestock manure, involves adding at least one strain of Bacillus coagulans (thermophilic bacteria), or combination of B.coagulans (thermophilic bacteria) and Bacillus subtilis (mesophilic strain) to the livestock manure, and fermenting the manure.    USE - The method is useful for disinfecting livestock manure. The B.coagulans (thermophilic bacteria) CP3424 (NITE BP-01692), or B.coagulans (thermophilic bacteria) CP3425 (NITE BP-01693) is useful in disinfectant, agent or composition for disinfecting or promoting composting of livestock manure or organic waste (all claimed).    ADVANTAGE - The method disinfects harmful bacteria along with manure.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for promoting composting of livestock manure or organic waste, involves performing the above-mentioned steps; and (3) B.coagulans (thermophilic bacteria) CP3424 (NITE BP-01692), or B.coagulans (thermophilic bacteria) CP3425 (NITE BP-01693).
NOVELTY - Trichoderma with preservation number CGMCC No. 9390 is new.    USE - Trichoderma with preservation number CGMCC No. 9390 for prevention and treatment of loquat root rot disease and promotion of loquat plant growth (all claimed).    ADVANTAGE - Process is simple and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of Trichoderma which involves culturing Trichoderma into solid culture medium, using punching machine to fight cake bacteria, removing loquat seedling trunk phloem using punching machine, placing cake bacteria into removed loquat seedling trunk phloem, sealing using preservative film with moisture to prevent seedling, culturing Trichoderma into liquid culture medium, diluting with sterile water, and pouring 500 ml diluent/loquat plant to prevent plant.    DESCRIPTION OF DRAWING(S) - The drawing shows a condition diagram of loquat plant growth after 12 days in which A is inoculated cake bacteria, and B is inoculated cake bacteria and LY1 trichoderma cake.
NOVELTY - Feed is produced by inoculating Bacillus licheniformis in culture medium, fermenting to obtain fermentation liquid, performing double-effect evaporation to obtain bacteria liquid, and spray-drying.    USE - Production of feed (claimed).    ADVANTAGE - Feed is nutritious, and preparation is simple and environment-friendly and has high yield.
NOVELTY - Bacillus cereus strain K2-1 (I) preserved under CCGMCC No: 9547 on 25-08-2014 is new.    USE - (I) is useful for the preparation of marine fungicide (claimed).    ADVANTAGE - (I) is environmentally friendly, does not produce drug resistance pathogen and can be produced with improved yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of marine fungicide, comprising: (A) taking (I), inoculating (I) into a songkhla-lake-basin culture medium and incubating at 30-40 degrees C for 12-48 hours, then inoculating into a lysogeny broth medium and activating at 30-40 degrees C, at 150-200 revolutions per minute (rpm) and for 5-10 hours to obtain activated (I); (B) inoculating activated (I) into 1-10% of a lysogeny broth medium, stirring at 150-200 rpm and 30-40 degrees C for 8-30 hours to obtain a fermentation broth; (C) extracting the obtained fermentation broth, centrifuging at 8000-10000 rpm for 5-10 minutes, removing the supernatant, transferring the supernatant to a water bath, and heating at 70-80 degrees C for 10-20 minutes to obtain a cell-free fermentation broth; (D) subjecting the cell-free fermentation broth to a column chromatography, where the column chromatography uses S printed hadex G-50 gel, is eluted with water, and has a collection time of 40-90 minutes, a sample volume of 1-5% and a flow rate 0.5-1 ml/minute; and (E) collecting and packaging.
NOVELTY - A cordycepin-rich Cordyceps recombinant rice comprises 20-50 mass% Cordyceps militaris culture medium superfine powder, 40-75 mass% broken rice, and 5-10 mass% rice floor powder.    USE - A cordycepin-rich Cordyceps recombinant rice (claimed).    ADVANTAGE - Cordycepin-rich Cordyceps recombinant rice is nutritious, has good mouthfeel, and enhances immune function, and preparation is short and environment-friendly and has reduced energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cordycepin-rich Cordyceps recombinant rice which involves crushing C. militaris culture medium to less than or equal to 40 mu m, sieving with 400 mesh sieve, crushing broken rice and rice floor powder to less than or equal to 180 mm, sieving with 80 mesh sieve, mixing at room temperature for 5-10 minutes to obtain mixed powder, adding 10-30 mass% water, stirring for 10-20 minutes, adding to double-screw extruder, performing extrusion granulation with compression zone temperature of 100-120 degrees C, feeding zone temperature of 75-90 degrees C, and screw speed of 150-200 rpm, molding, cutting into rice grain shape, drying with radio frequency plate spacing of 18 cm, frequency of 27 MHz, power of 6 kW, and material temperature of 50-60 degrees C for 5-10 minutes, drying, and cooling to room temperature.
NOVELTY - Preparation of terpene dimer involves dimerizing terpene feedstock by mixing terpene with heterogeneous acidic catalyst and solvent for controlling reaction temperature for desired time and temperature for producing crude terpene dimer, hydrogenating crude terpene dimer using hydrogenation catalyst in a hydrogen atmosphere, producing hydrogenated terpene dimer mixture, producing pure terpene dimers and byproducts by separating hydrogenated terpene dimer mixture, and generating a hydrocarbon mixture having viscosity of 20-50 cSt at 40 degrees C.    USE - Preparation of terpene dimer used as biodiesel for jet used in military application.    ADVANTAGE - The method enables efficient preparation of terpene dimer from terpene feedstock with high density, by simple and economical process.    DETAILED DESCRIPTION - Preparation of terpene dimer involves dimerizing terpene feedstock by mixing terpene with heterogeneous acidic catalyst and solvent for controlling reaction temperature for desired time and temperature for producing crude terpene dimer with chemical yield of 65-95%, hydrogenating crude terpene dimer using hydrogenation catalyst in a hydrogen atmosphere, removing hydrogenation catalyst, producing 65-95 wt.% hydrogenated terpene dimer mixture, producing pure terpene dimers and byproducts by separating hydrogenated terpene dimer mixture, and generating a hydrocarbon mixture having viscosity of 20-50 cSt at 40 degrees C.
NOVELTY - Domestic organic waste recycling equipment comprises horizontally disposed cylindrical metal container provided with spiral mixing device manually operated by crank mechanism, and force reducing device. The waste is processed by loading domestic waste daily into the device, mixing, dehydrating organic matter aerobically, composting, decanting through the lower tank sector slot, and placing on drain pan for removal and unloading.    USE - Equipment used for recycling domestic organic waste into compost.
NOVELTY - The device (10) has blower to blow air to injection pipe (38). The injection pipe is set with spray hole for spraying hot air inhaled through suction duct to organic waste put into fermenter (11). A sidewall (13) of fermenter is installed with inlet (31) to inhale air heated with heat generated during fermentation of organic waste in fermenter with aerobic. A stirrer (23) is set in pair of girder beams to transfer organic waste within fermenter. The girder beam is equipped in longitudinal direction, parallel to bottom wall (12) and between sidewalls of fermenter.    USE - Aerobic fermentation device of organic waste such as plant waste and animal waste ejected from slaughter factory.    ADVANTAGE - The aerobic fermentation of organic waste is performed effectively by providing stirrer equipped in girder beams arranged in longitudinal direction parallel to bottom wall of fermenter, to transfer organic waste within fermenter.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of the aerobic fermentation device of the organic waste.    Aerobic fermentation device of organic waste (10)    Fermenter (11)    Bottom wall (12)    Sidewall (13)    Stirrer (23)    Inlet (31)    Injection pipe (38)
NOVELTY - A Alternaria sp. (CGMCC 9277), is new.    USE - The Alternaria sp. is useful for producing secondary metabolites. The secondary metabolites are used as acaricide (all claimed) for crops.    ADVANTAGE - The method prepares fungal metabolite which kills agricultural mites even used in small concentrations, and is environmentally-friendly. The fungal metabolite is safe to use as it has no bad influence on crops and is nontoxic to crops.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for isolating the Alternaria sp.; and (2) method for producing secondary metabolites using Alternaria sp., involves (a) inoculating the Alternaria sp. into the culture medium (B), placing culture in shaker at 28 plus minus 2 degrees C, and incubating the culture at 100-140 revolutions/minute (rpm) under dark conditions to obtain fungal fermentation broth, and (b) sterilizing the fungal fermentation broth, filtering the fermentation broth, extracting the fermentation broth using ethyl acetate, and concentrating extract to obtain solid products which are fungal metabolites.
NOVELTY - Rhizobium yanglingense strain CCBAU01603 preserved under a number of CGMCC No.7895, is new.    USE - The Rhizobium yanglingense strain is useful for seedling and promoting the growth of Caragana microphylla (claimed).    ADVANTAGE - The strain is capable of rapidly promoting the growth and seedling of Caragana microphylla and ensuring the nodulation rate of Caragana microphylla, in an eco-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a culture medium for Rhizobium yanglingense strain obtained by mixing 8-12 g of inositol, 2-4 g of yeast powder, 0.1-0.3 g of magnesium sulfate, 0.05-0.15 g of sodium chloride, 0.15-0.35 g of dipotassium hydrogen phosphate and 0.15-0.35 g of potassium dihydrogen phosphate with water for constant volume to 1000 ml.
NOVELTY - Processing molasses comprises (i) allowing the molasses to contact with water at 40-50 degrees C, and carrying out solid-liquid separation to obtain a first supernatant; (ii) contacting the first supernatant with colloidal precipitation agent, and carrying out solid-liquid separation to obtain a second supernatant; (iii) adjusting the pH of second supernatant to 1.9-2.5, subjecting to still stratification and carrying out solid-liquid separation to obtain molasses supernatant liquid.    USE - The method is useful for processing molasses (claimed).    ADVANTAGE - The molasses supernatant liquid can improve the end point lysine content, acid content and conversion rate.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) molasses supernatant liquid, obtained by above mentioned molasses processing method;    (2) lysine fermentation medium, comprising molasses supernatant liquid; and    (3) producing lysine, comprising adding lysine fermenting strain into lysine fermentation medium, adding carbon source and nitrogen source, and fermentation culturing.
NOVELTY - Generating electric power and cooking fuel from biowaste utilizing algae, comprises: collecting the biowaste from various sources; processing the collected biowaste in an anaerobic biodigester to generate biogas, nutrients and manure; separating carbon dioxide and methane obtained from biogas by a scrubbing process; and feeding the algae with carbon dioxide obtained by the scrubbing process to generate biodiesel.    USE - The method is useful for generating electric power and cooking fuel from biowaste comprising fecal matter, vegetable waste and animal waste utilizing algae (all claimed), where the biowaste is in the form of domestic waste, plant waste, animal waste and industrial waste.    ADVANTAGE - The method is capable of generating the electric power and cooking fuel in an effective and economical manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for generation of electric power from biowaste and algae, comprising: a collecting module (301) adapted to receive biowaste from various natural resources; a processing module (302) further comprising anaerobic biodigester that functions by degrading the collected biowastes to produce manure, biogas and nutrient solutions; a harvesting module (303) enabled to harvest algae using carbon dioxide obtained from processing module and sunlight to produce biodiesel; and a power generation module (304) programmed to produce electric power utilizing biogases and biodiesel obtained from processing and harvesting modules.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a system for generation of electric power from biowaste and algae.    Collecting module (301)    Processing module (302)    Harvesting module (303)    Power generation module. (304)
NOVELTY - Method for preparing organic fertilizer involves (a) crushing rape straw into pieces, (b) crushing rotting agent, urea, and plant ash, (c) uniformly mixing 1000 pts. wt. crushed rape straw, 1-8 pts. wt. crushed rotting agent, 8-37 pts. wt. crushed urea, and 70-150 pts. wt. crushed plant ash, (d) performing aerobic fermentation for 15-20 days, where moisture content of the mixture during fermentation process is 35-65%, and (e) crushing fermented mixture into powder, and granulating and drying product.    USE - The method is useful for preparing organic fertilizer (claimed).    ADVANTAGE - The method enables to prepare product in a simple, convenient, environmentally-friendly, and cost-effective manner.
NOVELTY - Method for producing liquid fertilizer, involves using 65-75 pts. wt. fresh sisal wastewater, 20-30 pts. wt. inorganic fertilizer, 0.1-0.5 pts. wt. secondary nutrients, 0.05-1 pt. wt. trace element, 0.1-0.2 pts. wt. organic acid and 0.01-0.05 pts. wt. botanical fungicide, weighing the sisal wastewater, inorganic fertilizer, microelement, organic acid, secondary nutrients and botanical fungicide, uniformly stirring weighed materials in fermenting jar, performing fermentation at 30-50 degrees C for 10-15 days, filtering fermented product, and collecting filtrate.    USE - The method is useful for producing liquid fertilizer which is useful for promoting growth and yield of corn.    ADVANTAGE - The method utilizes waste materials, is environmentally-friendly and cost-effective, provides economical benefits, rapidly provides nutrients required for corn, and controls pests.
NOVELTY - Producing liquid fertilizer, involves using 65-75 pts. wt. fresh sisal wastewater, 25-30 pts. wt. inorganic fertilizer, 0.1-0.5 pts. wt. secondary nutrients, 0.05-1 pt. wt. trace element, 0.1-0.2 pts. wt. organic acid, 0.5-1 pts. wt. sweetening accelerator, and 0.01-0.05 pts. wt. insect repellent, weighing the sisal wastewater, inorganic fertilizer, microelement, organic acid, secondary nutrients, sweetening accelerator and insect repellent, stirring materials in fermenting jar, performing fermentation, filtering fermented product, and collecting filtrate.    USE - The method is useful for producing liquid fertilizer used for watermelon (claimed), where the fertilizer is useful for increasing yield of plant, and controlling pests.    ADVANTAGE - The method utilizes waste materials, is environmentally-friendly and cost-effective, provides economical benefits, and rapidly provides nutrients required for watermelon.    DETAILED DESCRIPTION - Method for producing liquid fertilizer, involves using 65-75 pts. wt. fresh sisal wastewater, 25-30 pts. wt. inorganic fertilizer, 0.1-0.5 pts. wt. secondary nutrients, 0.05-1 pt. wt. trace element, 0.1-0.2 pts. wt. organic acid, 0.5-1 pts. wt. sweetening accelerator, and 0.01-0.05 pts. wt. insect repellent, weighing the sisal wastewater, inorganic fertilizer, microelement, organic acid, secondary nutrients, sweetening accelerator and insect repellent, uniformly stirring weighed materials in fermenting jar, performing fermentation at 30-50 degrees C for 10-15 days, filtering fermented product, and collecting filtrate.
NOVELTY - Fertilizer composition and its manufacturing method, are claimed. The fertilizer comprises 70-80 pts. wt. sisal waste materials, 20-25 pts. wt. inorganic fertilizers, 0.1-0.5 pt. wt. microelements, 0.4-0.8 pt. wt. organic acids, and 0.05-0.1 pt. wt. flowering promoting agent. The sisal waste material is prepared by crushing the sisal leaves and other waste materials, and filtering the crushed product to remove sisal waste, where the sisal waste material produces feed or pectin.    USE - The fertilizer is useful for promoting growth, and blooming of flowers.    ADVANTAGE - The fertilizer utilizes waste materials, is environmentally-friendly, prepared cost-effectively and rich in nutrients, and rapidly promotes growth as compared to existing fertilizer.    DETAILED DESCRIPTION - Fertilizer composition and its manufacturing method, are claimed. The fertilizer comprises 70-80 pts. wt. sisal waste materials, 20-25 pts. wt. inorganic fertilizers, 0.1-0.5 pt. wt. microelements, 0.4-0.8 pt. wt. organic acids, and 0.05-0.1 pt. wt. flowering promoting agent. The sisal waste material is prepared by crushing the sisal leaves and other waste materials, and filtering the crushed product to remove sisal waste, where the sisal waste material produces feed or pectin. The fertilizer is prepared by mixing the above-mentioned raw materials, adding the mixture in uniformly closed fermentation tank, fermenting the mixture at 30-50 degrees C for 10-15 days, filtering the fermented mixture and collecting filtrate.
NOVELTY - Method for preparing tea powder involves washing fresh leaves of Dendrobium nobile, performing microwave drying at 500-3000 W for 5-60 minutes, where moisture content of dried leaves is 50%, cutting dried leaves into pieces, again performing microwave drying at 500-3000 W for 5-30 minutes, where moisture content of dried leaves is 12%, and crushing dried product.    USE - The method is useful for preparing tea powder (claimed).    ADVANTAGE - The method enables to prepare product in a cost-effective and environmentally friendly manner with reduced energy consumption, and improved quality. The prepared product is rich in nutrients.
NOVELTY - Preparing fertilizer involves mixing phosphoric acid and carbamide in mol ratio of 1.2-1.4:1 at 120-150 degrees C for 130-150 minutes with heating rate of 4 degrees C/minute in a reaction kettle. Mixture is centrifuged and cooled to 35-45 degrees C obtain material slurry. Preparation of potassium dihydrogen phosphate involves alkaline potassium salt is mixed in the intermediate slurry in mol ratio of 1.3:1 and stirred at speed of 200-250 revolutions per minute for 40-60 minutes to maintain pH value 8-9 to obtain nitrogen-phosphorus-potassium slurry. Nitrogen-phosphorus-potassium slurry is cooled and crystallized, and then filtered to obtain filter cake.    USE - Method for preparing fertilizer used for kidney bean (claimed).    ADVANTAGE - The method is cost-effective and eco-friendly, enables to prepare fertilizer that is absorbed by soil effectively.    DETAILED DESCRIPTION - Preparing fertilizer involves mixing phosphoric acid and carbamide in mol ratio of 1.2-1.4:1 at 120-150 degrees C for 130-150 minutes with heating rate of 4 degrees C/minute in a reaction kettle. Mixture is centrifuged and cooled to 35-45 degrees C obtain material slurry. Alkaline potassium salt is mixed in the intermediate slurry in mol ratio of 1.3:1 and stirred at speed of 200-250 revolutions per minute for 40-60 minutes to maintain pH value 8-9 to obtain nitrogen-phosphorus-potassium slurry. Nitrogen-phosphorus-potassium slurry is cooled and crystallized, and then filtered to obtain filter cake and filter liquid. Filter liquid comprises nitrogen (5-6%) phosphorus pentoxide (2.8-3.1%), potassium hydroxide (5.2-6.0%). Trace element compound is mixed with filter liquid to obtain a product, and then heated at 25-35 degrees C for 40-60 minutes in a drier with speed of 5 degrees C/minute to obtain fertilizer.
NOVELTY - Calcium biphosphate composite fertilizer preparation involves mixing phosphoric acid and carboxamide in molar ratio 1.2-2.4:1 at 80 degrees C for 2-3 hours. The obtained material is mixed with calcium salt mixed solution for 10-15 minutes at 3-3.5 pH. The obtained material is crystallized, and then nitrogen, phosphorus pentoxide, calcium ion is adjusted in mole ratio of 0.9-1.1:0.9-1.1:0.01-0.03. The obtained material is filtered, and then potassium nitrogen and phosphorus component, and trace element are added to the obtained material.    USE - Method for preparing calcium biphosphate composite fertilizer used for chili (claimed).    ADVANTAGE - The method enables to prepare calcium biphosphate composite fertilizer in cost-effective and eco-friendly manner, ensures reduced wastage.    DETAILED DESCRIPTION - Calcium biphosphate composite fertilizer preparation involves mixing phosphoric acid and carboxamide in molar ratio 1.2-2.4:1 at 80 degrees C for 2-3 hours. The obtained material is mixed with calcium salt mixed solution for 10-15 minutes at 3-3.5 pH. The obtained material is crystallized, and then nitrogen, phosphorus pentoxide, calcium ion is adjusted in mole ratio of 0.9-1.1:0.9-1.1:0.01-0.03. The obtained material is filtered, and then potassium nitrogen and phosphorus component, and trace element are added to the obtained material, where content of potassium, nitrogen and phosphorus are in ratio 1.1:1.5:1.3. The obtained material is heated at 40-50 degrees C for 2 hours to obtain the finished product.
NOVELTY - Bio-organic fertilizer comprises 10-25 wt.% water soluble nitrogen, potassium and potash fertilizer, 15-25 wt.% biological filler, 1-5 wt.% biological bacterium, 1-3 wt.% ferrous sulfate, 1-15 wt.% humic acid and balanced molasses alcohol waste containing 35-95 wt.% organic matter.    USE - Bio-organic fertilizer used for planting lotus (claimed) and preventing lotus root decay.    ADVANTAGE - The bio-organic fertilizer is economic.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing bio-organic fertilizer, which involves:    (A) mixing solution of nitrogenous fertilizer, phosphate fertilizer, biological filler, ferrous sulfate and molasses alcohol waste to obtain mixture;    (B) fermenting mixture with biological bacterium and humic acid in fermentation pool for 16-28 hours at room temperature;    (C) granulating fermented materials; and    (D) drying granules to obtain product.
NOVELTY - Synthesis of terpene ester involves acylating terpene alcohol and carboxylic acid anhydride in presence of dicationic sulfonic acid group-functionalized ionic liquid catalyst,lauryl alcohol , cooling, precipitating ionic liquid catalyst from the reaction system, filtering, recycling ionic liquid catalyst, and distilling liquid mixture under reduced pressure.    USE - Synthesis of terpene ester (claimed).    ADVANTAGE - The method is environmentally-friendly, and enables efficient and economical synthesis of terpene ester with high selectivity and high yield.
NOVELTY - The system has a potassium nitrate crystal vacuum device whose discharge port is communicated with a feed port of a secondary centrifuge device whose discharge port is connected with an inlet of washing tank. A triple-effect circulation pump (8) is connected to three-way separating room with a branch pipe. A triple-effect discharging pump (9) is connected with a two-effect heater (5). A pre-heater (15) is connected to bottom of a triple-effect heater (3) through a pipeline. The pre-condensed liquid outlet of a condenser (14) is connected to a vacuum system (1) through a pipeline.    USE - System for continuous production of potassium nitric acid.    ADVANTAGE - The continuous production of potassium nitric acid is achieved, and the production capacity is enlarged. The labor intensity and the production time are reduced, and the efficiency of potassium nitric acid production is increased. The crystallization process is performed accurately, and the quality of potassium nitrate crystal is improved. The concentrate temperature of chlorine-containing material is reduced, thus the energy consumption is reduced. The stability of ammonium chloride product quality is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for continuous production of potassium nitric acid.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the system for continuous production of potassium nitric acid.    Vacuum system (1)    Triple-effect heater (3)    Two-effect heater (5)    Triple-effect circulation pump (8)    Triple-effect discharging pump (9)    Condenser (14)    Pre-heater (15)
NOVELTY - A composite soil conditioner comprises biogas residue, wood vinegar, mineral powder, soluble chitosan, sodium diethylenetriamine pentaacetate, surfactant, tobacco, trehalose, rhamnolipid biosurfactant, flocculating component, penetrant, Enteromorpha powder, modified zeolite, zinc-magnesium-boron type inoculant, nano additive, promoter, pentaerythritol triacrylate and ionic liquid.    USE - Composite soil conditioner is used for soil improvement and repair (claimed).    ADVANTAGE - The composite soil conditioner has excellent soil improvement and recovering performance, improves utilization of crop fertilizer and soil permeability, and avoids side effects of cadmium and other heavy metals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of composite soil conditioner, which involves mixing biogas residue, wood vinegar, mineral powder, soluble chitosan, sodium diethylenetriamine pentaacetate, surfactant, tobacco, trehalose and rhamnolipid biosurfactant, milling, adding flocculating component, penetrant, Enteromorpha powder, modified zeolite, zinc-magnesium-boron type inoculant, nano additive and promoter to the resultant product, mixing, grinding the resultant product, adding pentaerythritol triacrylate and ionic liquid to the resultant product, and stirring.
NOVELTY - Emulsified pesticide comprises 2-8 pts. wt. chlorfenapyr, 3-7 pts. wt. knotweed, 3-8 pts. wt. diafenthiuron, 3-5 pts. wt. hexaconazole, 5-9 pts. wt. essential oils, 4-6 pts. wt. emulsifier, 3-9 pts. wt. potassium dihydrogen phosphate, 2-6 pts. wt. Andrographis, 3-7 pts. wt. Bacillus sphaericus powder, 4-6 pts. wt. Ginkgo extract, 2-6 pts. wt. camphor, 3-5 pts. wt. ash, 1-3 pts. wt. silicon and 2-6 pts. wt. Cnidium.    USE - Emulsified pesticide.    ADVANTAGE - The emulsified pesticide is eco-friendly and cost-effective.
NOVELTY - Pesticidal composition comprises 6-14 pts. wt. lavender oil, 3-9 pts. wt. hairyvein agrimony, 4-8 pts. wt. Cynanchum komarovii, 2-7 pts. wt. Rhizobia powder, 2-8 pts. wt. lentinan polysaccharide, 4-9 pts. wt. dyers woad leaves, 3-7 pts. wt. dandelion, 2-6 pts. wt. nitrifying bacteria powder, 1-6 pts. wt. Cynanchum extract, 3-8 pts. wt. fructus cnidii, 5-7 pts. wt. Tripterygium wilfordii alkaloid, 3-5 pts. wt. synergistic agent, 4-6 pts. wt. brassinolide, 5-8 pts. wt. purslane and 2-6 pts. wt. pokeweed.    USE - The pesticidal composition is useful for human and livestock.    ADVANTAGE - The composition is environmentally-friendly and nontoxic.
NOVELTY - Method of sewage water treatment is offered. Sewage waters polluted with oil products are filtered. Basalt fibre BSTVst modified by cationic starch, oxyamil OPV-1, with Rhodotorula sp. BKM Y-2993D strain cells with cell titre 106 CFU/cm3 immobilized on it is used for filtration.    USE - Biotechnologies.    ADVANTAGE - Enhanced efficiency of oil-polluted sewage water treatment.1 tbl, 1 ex
NOVELTY - A microbial inoculum comprises complex microbial inoculants comprising Bacillus subtilis, Bacillus licheniformis, plant Lactobacillus, Hansenula, and Saccharomyces cerevisiae yeast.    USE - Microbial inoculum for use in municipal sewage treatment (claimed).    ADVANTAGE - The microbial inoculum has good degrading effect, and can effectively improve the biodegradability of sewage, and reduce poor biodegradability of chemical oxygen demand(chromium) and biochemical oxygen demand(5) of municipal sewage.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following: (1) a method for preparing a microbial inoculum, which involves taking first stage culture by activating culture of Bacillus subtilis, Bacillus licheniformis, plant Lactobacillus, Hansenula, and Saccharomyces cerevisiae yeast, respectively, inoculating the obtained five strains after activation in a liquid culture medium, growing viable cell count of Bacillus subtilis reached to (1-9)x 109 mL, Bacillus licheniformis to (1-9)x 109 mL, Lactobacillus to (1-9)x 107 mL, Hansenula to (1-9)x 108 mL, Saccharomyces cerevisiae to (1-9)x 108 mL, and centrifuging to stop bacterial culture, mixing obtained bacterial strain with powdery composite wet cells and activated charcoal as a carrier at the mass ratio of 1:(2-3) and drying obtained mixture at 25-35 degrees C, until the moisture content is 15-20% (2) use of microbial inoculum for municipal sewage treatment by removing ammonia nitrogen, sterilizing with microbial inoculum, removing a strain of composite microorganism and ammonia nitrogen, preferably nitrifying germ (3) a sewage treatment method by using microbial inoculum.
NOVELTY - Composition comprises 5-40% pyraclostrobin and 40-2000 million colony-forming unit (CFU)/g Bacillus subtilis strain DJ-6.    USE - The composition in the form of wettable powder, emulsion, suspension or water-dispersible granule is useful for preventing and treating wilt in strawberry (all claimed).    ADVANTAGE - The composition is environmentally-friendly, prepared simply and cost-effectively, and increases yield and quality of strawberry.
NOVELTY - Compound fertilizer comprises inorganic nutrients, organic matter, microorganism and seaweed extract.    USE - As compound fertilizer in form of liquid, granule or powder.
NOVELTY - Fertilizer comprises 20-22 parts mass chicken manure, 15-17 parts mass peat, 16-18 parts mass ammonium bicarbonate, 13-15 parts mass calcium superphosphate, 11-13 parts mass green manure containing calopo, 9-12 parts mass potassium dihydrogen phosphate, 10-12 parts mass peanut meal fertilizer, 7-9 parts mass ferrous sulfate, 6-8 parts mass ammonium polyphosphate, 4-6 parts mass zinc oxide, 2-5 parts mass calcium oxalate, 3-6 parts mass humic acid, 2-4 parts mass brassinolide, 1-3 parts mass sulfur suspending agent and 50-60 parts mass water.    USE - The fertilizer is useful for promoting bean plant and root growth.    ADVANTAGE - The bean fertilizer is nutritious and prepared by simple method, prevents formation of disease spots, improves bean yield and quality, and promotes disease and insect resistance abilities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer which involves mixing 21 parts mass chicken manure, 16 parts mass peat, 17 parts mass ammonium bicarbonate, 14 parts mass calcium superphosphate, 12 parts mass green manure containing calopo, 11 parts mass potassium dihydrogen phosphate, 11 parts mass peanut meal fertilizer, 8 parts mass ferrous sulfate, 7 parts mass ammonium polyphosphate, 5 parts mass zinc oxide, 3 parts mass calcium oxalate, 4 parts mass humic acid, 3 parts mass brassinolide, 2 parts mass sulfur suspending agent and 55 parts mass water uniformly, homogenizing mixture, fermenting for 2.5 hours under closed condition and drying fermented mixture to obtain the product.
NOVELTY - A treatment agent comprises 30-40 pts. wt. sepiolite-based mineral, 10-20 pts. wt. organic plant fertilizer additive and 30-40 pts. wt. seaweed.    USE - Agent is used for treating heavy metal-contaminated soil.    ADVANTAGE - The treatment agent increases propagation of microorganisms, quickly reduces heavy metal content in soil, and changes soil structure.
NOVELTY - A Bacillus megaterium strain TDB-2 (CCTCC M 2012352), is new.    USE - The B.megaterium strain TDB-2 is used in preparation of microbial degradation agent for degrading triazophos (all claimed).    ADVANTAGE - The B.megaterium strain efficiently degrades triazophos by simple and environmentally-friendly method.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) microbial degradation agent comprising the B.megaterium strain TDB-2; and (2) method for preparing the microbial degradation agent, involves (a) picking single colonies of the strain from culture plate, (b) inoculating the single colonies in seed medium, and culturing until logarithmic growth phase, and (c) inoculating 1-3% culture in production medium, culturing until logarithmic phase and packaging obtained product.
NOVELTY - A gypsy moth chitinase 5 gene comprising a 1895 base pair sequence (SEQ ID NO: 1) fully defined in the specification, is new.    USE - The gypsy moth chitinase 5 gene or chitinase 5 gene lethal fragments is useful for controlling gypsy moth pest (all claimed).    ADVANTAGE - The gypsy moth chitinase 5 gene is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) gypsy moth chitinase 5 gene lethal fragments comprising 472 base pair sequence (SEQ ID NO: 2) fully defined in the specification; (2) method for preparing the gypsy moth chitinase 5 gene; and (3) method for preparing the gypsy moth chitinase 5 gene lethal fragments, involves obtaining nucleotide sequence of the chitinase 5 gene, designing upstream primer comprising a 41 base pair sequence (SEQ ID NO: 3) fully defined in the specification, and downstream primer comprising a 44 base pair sequence (SEQ ID NO: 4) fully defined in the specification, combining the obtained chitinase 5 recombinant gene with pEASY-T1 plasmid, performing PCR amplification using the combined gene-plasmid as template, obtaining fragments of the SEQ ID NO: 2 and purifying the obtained sequence using MicroElute (RTM: Not defined).
NOVELTY - Synthesizing (S)-(+)-2-chlorophenylglycine methyl ester involves dissolving racemic 2-chlorophenylclycine methyl ester in sodium phosphate buffer solution to obtain reaction solution, which is heated at 30 degrees C in a water bath reactor to obtain racemic product. Penicillin G acylase as biological enzyme is added to the obtained racemic product, and then kept for reacting under controlled stirring speed i.e. 100-500 revolutions per minute for 20-60 hours to obtain desired product.    USE - Method for synthesizing (S)-(+)-2-chlorophenylglycine methyl ester by biological-enzymatic process (claimed).    ADVANTAGE - The method enables to synthesize highly optical pure (S)-(+)-2-chlorophenylglycine methyl ester with good enantiomeric value excess value more than 95% in a simple and environment friendly manner.
NOVELTY - The gasifier (1) has a masonry combustion body (C) attached with air primary combustion inlets (E). A tempered glass panel (G) and heat exchanger openings are attached with the combustion body that is attached with a mixing unit (7). A mixture is provided in an air environment with heated air that is generated during gasification process, where mixed air is sucked by a set motor and a fan (8) for removing the heated air in the gasifier. Three shackles are internally coated with brick or refractory cement.    USE - Concurrent flow biomass gasifier for drying grain and heating aviaries in a poultry.    ADVANTAGE - The gasifier can dry grain in lighting environments in an inexpensive manner, and prevents chicken meat and grain from being damaged in an easy manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a concurrent flow biomass gasifier.    Masonry combustion body (C)    Air primary combustion inlets (E)    Concurrent flow biomass gasifier (1)    Tempered glass panel (6)    Mixing unit (7)    Fan (8)
NOVELTY - (Meth)acrylate or alkyl (meth)methyl acrylate production involves performing transesterification of methyl methacrylate and methyl acrylate in presence of linear or branched alcohol containing 2-22 carbon atoms.    USE - Method for producing (meth)acrylate or alkyl (meth)methyl acrylate used for obtaining homopolymer esters for use as additives for enhancing cold flow properties of fuels, particularly biofuels, such as diesel oil, biodiesel, biokerosene, kerosene, gasoline, ethanol and methanol (all claimed).    ADVANTAGE - The method enables producing (meth)acrylate or alkyl (meth)methyl acrylate with excellent performance.
NOVELTY - Obtaining biofuel involves performing metathesis of olefins present in vegetable oils, purifying obtained product, inserting substrate into a suitable reactor, and then pressurizing with the reactant gas. Suitable catalyst and terminating reagent i.e. butyl vinyl ether are added to product. Basic catalysis of product is performed, and then acid catalyzed to obtain a product. Byproducts are removed, and the hydrogenated and reduced in presence of a catalyst to obtain the desired product.    USE - Method for obtaining biofuel (claimed).
NOVELTY - A waste dregs generated from fabrication of cellulose, recovering method involves preparing sludge dregs. Pelletizing and drying process is performed, followed by crushing the mixture in ball mill with hot, with the lumps formed in the previous step, which are discharged and milled together with the dregs with an average particle size of 10 micron during for 60- 80 minutes, passing the mixture after grinding into classification system in vibrating sieves with openings of 40-80 mesh, for retaining the particles, sending into endless screw, adding 1 vol.% flowing agent, and storing in bags.    USE - Method for recovering waste dregs generated from fabrication of cellulose.    DETAILED DESCRIPTION - A waste dregs generated from fabrication of cellulose, recovering method involves preparing sludge dregs by receiving500-1000 Kg/hr mud-dregs in the form of slurry, providing into rotary furnace, burning in furnace at of 280-380 degrees C. Pelletizing and drying process is performed by pelletizing and drying the dregs which while adding 0.8-1.2% binder such as starch, as a mist through the sprinkler nozzle mouth in the drier, forming film through the heat generated by the burner, forming material layer of groats in unequal and still moist form with approximately 10% humidity, followed by crushing the mixture in ball mill with hot, with the lumps formed in the previous step, which are discharged and milled together with the dregs with an average particle size of 10 micron during for 60- 80 minutes, passing the mixture after grinding into classification system in vibrating sieves with openings of 40-80 mesh, for retaining the particles, sending into endless screw, adding 1 vol.% flowing agent, and storing in bags.
NOVELTY - Method for fermenting galactosyl algal biomass, involves degrading algal biomass, obtaining degraded products, inducing cell activation by culture, and performing anaerobic fermentation process of the degraded products after induction of cell activation. The cell comprises galactose operon containing yeast or Escherichia coli. The cells are cultured in culture broth or solid galactose medium.    USE - The method is useful for fermenting galactosyl algal biomass which is used for preparing biofuels or chemical intermediates (all claimed) such as ethyl alcohol, butyl alcohol, isobutyl alcohol, propanol, 1,3-propylene glycol, 1,4-propylene glycol, alcohol organic substance and alkane organic substance.
NOVELTY - Acetic acid and hydrogen feedstock are preheated, hydrogenated, and passed through a reactor (r1). The obtained crude ethanol product is deacidified, and the mixture is separated into distillate containing ethanol. At least portion of distillate is provided to light tower, and separated into lighter distillate residue containing ethanol. At least one portion of lighter distillate residue from the light tower is provided to dehydration tower. The dehydration-tower distillate containing ethanol is subjected to azeotropic separation or membrane separation, to obtain fuel ethanol.    USE - Production of fuel ethanol (claimed).    ADVANTAGE - The method enables efficient production of fuel ethanol, with reduced energy consumption.    DETAILED DESCRIPTION - Acetic acid and hydrogen feedstock are preheated, hydrogenated, and passed through a reactor (r1) containing a hydrogenation catalyst, to obtain crude ethanol product. The crude ethanol product is fed to ethanol deacidification column, and deacidified, and the mixture is separated into distillate containing ethanol, ethyl acetate, and deacidification-column effluent. At least portion of distillate is provided to light tower, and separated into lighter distillate residue containing ethanol, acetaldehyde, acetone and ethyl acetate. The lighter distillate residue containing ethanol is removed. At least one portion of lighter distillate residue is recycled to reactor (r1), or preheated. At least one portion of lighter distillate residue from the light tower is provided to dehydration tower, and separated into dehydration-tower distillate containing ethanol and water-containing residue. The dehydration-tower distillate containing ethanol is subjected to azeotropic separation or membrane separation, to obtain fuel ethanol.
NOVELTY - An oilfield sewage processing method involves culturing and screening algae, analyzing each algae tolerance for biodegradable sewage, identifying dominant algal species, and immobilizing the identified algae in oil field sewage.    USE - Method for processing oilfield sewage.    ADVANTAGE - The method enables processing oilfield sewage in a most stable manner, degrading aromatic hydrocarbons in short time, and controlling sewage processing time reasonably by increasing chemical oxygen demand (COD) concentration.
NOVELTY - Luminescent compounds (I) is new.    USE - Luminescent compound used as marker for peer-to marking of biofuels, such as biodiesel, diesel, ethanol, gasoline or kerosene (claimed).    DETAILED DESCRIPTION - Luminescent compounds of formula (I) is new.    R=alkyl alcohols of formula R'-OH; and    R'=2-16C alkyl group.    An INDEPENDENT CLAIM is included for a method for preparing luminescent compound marker of formula (I).
NOVELTY - Obtaining fatty acid esters involves using clay minerals comprising talc, pyrophyllite, smectite, vermiculite and saponite.    USE - Method for obtaining fatty acid esters through heterogeneous catalysis used as biodiesel (claimed).
NOVELTY - Obtaining neolignans, particularly eupomatenoid-3, eupomatenoid-5 and conocarpan involves extracting Piper regnellii at 60 degrees C for 280 minutes, and pressure is 244.1 bar, carbon dioxide density is 0.78g/ml, and flow of extraction liquid is 3 ml/minute.    USE - Method for obtaining neolignans, particularly eupomatenoid-3, eupomatenoid-5 and conocarpan used as antimycobacterial agent for preparing medicament against Mycobacterium tuberculosis (all claimed).    ADVANTAGE - The method enables to obtain neolignans, particularly eupomatenoid-3, eupomatenoid-5 and conocarpan in quick and eco-friendly manner, and does not need of organic solvent.
NOVELTY - This utility new type relates to one used for precipitating a precipitation jar is sludge, it comprising a tank body, a jar body set with centre cylinder, bottom of the tank body are set with mud collecting cone, between adjacent mud collecting cone set with sludge outlet pipe, sludge outlet pipe set with drain pipe, centre cylinder upper end set with gas-liquid separator, a gas-liquid separator comprising tube, tube upper end set with liquid entrance, inside set with multi-group tube aeration device, the aeration device comprise upper end and narrow lower end width of flow-dividing cone and upper end lower end width is narrow, the flow-dividing cone sleeve, and the flow-dividing cone of the outer circumference is less than the maximum outer circumference of guide cover. This utility new type through set with multi-cone and a flow guide cover, a biogas multi-time, at the same time the air and biogas slurry form convection continuously, so as to make the liquid fully, reduce the produce of bubble, so as to reduce the affect of for sludge settling effect. The device needs to outside without increasing the energy consumption and increase of part is fixed, almost without maintenance cost. The device operation is simple and practical.
NOVELTY - This utility new type claims a one round pool body composite Anaerobic marsh gas pool, comprising pool body, six level Anaerobic pool and reservoir, pool body and six level Anaerobic pool through the overflow pipe, the pool body left side connecting with a feeding pipe, a stir shaft, pool body inner pool body is set with a multi-orderly arrangement of V-shaped baffle plate one and a belt wheel is set with a driving end of the driving device and a platform, a driving device and stir shaft a, inner overflow pipe set with a zigzag baffle plate, level Anaerobic pool bottom part set with connected wherein, a six-level Anaerobic pool side connecting with a drain-pipe, pool body and six level Anaerobic pool inner are set with a sludge pump, sludge pump are through each through sludge reflux pipeline and the feeding pipe a, pool body and six level Anaerobic pool top set on the pneuma valve, this pneuma valve connecting with the air pipe, and and a reservoir, a platform and sludge pump connecting wire, one is a reasonable structure can continuously feed, with a stir, and high safety of round pool body composite Anaerobic marsh gas pool.
NOVELTY - This utility new type claims a one biomass gasification furnace feeding device, comprising a furnace body, further comprising a, a feeding tube and a fixed connection and extends into a shape of the inner furnace body, a feeding inner tube set with the material feeding part comprising rotating shaft and the rotating shaft of the external motor a is set on a rotating shaft and a spiral feeding piece, a feeding tube and the horn hopper through the start-shaped valve fixing connection. The advantages of it is capable of a speed of raw material entering into the furnace, for effective of raw material crushing, effective to prevent the outside air entering into the furnace body.
NOVELTY - This new type utility claims one a feeding seal type biomass gasification furnace, comprising a furnace body, further comprising a, a feeding tube, a star valve and a fixed connection and extends into a shape of the inner furnace body, a star valve comprising shell setting b and inner shell of impeller is set with edge seal impeller and surface for inner housing of the flexible sealing element, a feeding pipe and a star valve feeding wherein a fixed connection, wherein a feed horn inlet valve and a start-shaped fixed connection. The advantages of it is flexible sealing element part can prevent the outside air entering into the furnace body, so as to effectively avoid explosion accident happen.
NOVELTY - This utility new type claims a one tower type biomass gasification furnace, comprising a furnace body, a feeding device conveying feeding of a dust-removing device is set on the bottom of the furnace body is further used for including driving apparatus for rotating a drive system, ash removing device inside support with a tower-shaped fire grate, furnace body inner side top part is set with several heat pipe and parallel to the axial line of the furnace body, the bottom and dust-removing device of furnace body exist gap between the bottom and dust-removing device of furnace body through liquid seal between, a tower-shaped fire grate extends into the inner furnace body and the furnace body side wall and exist gap, further comprising air b of fan inner tower-shaped fire grate. The advantages of it is capable of rapid crushing and slag entering into apparatus after a dedusting device, safe efficient, part from the gas in the separating tar, reduces the tar to combustion device in a pipeline.
NOVELTY - This utility new type provide a one biomass gasification furnace feeding device, comprising, hoisting machine, the first conveying pipe, an electric gate valve, second conveying pipe and material distributing cone, a hoisting machine set with the first conveying tube, output end of the first conveying pipe set with electric gate valve, one end the second conveying pipe and the electric gate valve is a, and the other end a second conveying pipe and a distributing cone connection, a material distributing cone fixed in gasification furnace. This utility new type is convenient to install, the transmission speed is fast, does not need additional power supply, the efficiency is high, the raw material directly by hoisting machine through feeding pipeline entering into gasification furnace body, feeding way is simple, the seal effect is good.
NOVELTY - This new utility model provide a kind of one biomass gasification furnace bottom furnace steam self-motion supplement control system, comprising PLC, hot resistance module, transducer, hand operator steam adjusting valve, temperature sensor and air blower, the PLC and the frequency converter, heat resistance and hand of module connected with the output end of the frequency converter connected with the air blower, the heat resistance and the temperature sensor module connected with the output end of the hand controller connected with the steam adjusting valve. This new utility model providing the biomass gasification furnace bottom furnace steam self-motion supplement control system can automatically control bottom furnace into the steam amount, steam electric motor car regulating valve opening degree, automatic degree high, regulation effect is good, increase gasification quality.
NOVELTY - This utility new type provide a biomass pneuma in one furnace air distribution system, comprising fan, air distribution room, the first air distribution pipeline, second pipeline and third air distribution air distribution pipeline, the fan and the air distribution room connecting, the upper air distribution room set with air distributing port, a first air distribution pipeline, second pipeline and third air distribution pipeline air distribution and air distribution of the air distribution room connecting, the first distribution pipeline set with a first flow meter and a first gate valve, a second air distribution pipeline set with second flow meter and second gate valve, a third air distribution pipeline set with a third flow and third gate valve, output end of the distribution pipeline connecting the first cloth wind pipe groove, a terminal of the second air distribution pipeline a second cloth air pipe groove, a terminal of a third air distribution pipeline a third cloth air pipe groove. This utility new type regulating is convenient and flexible, operation time air supply uniformity, gasification working condition stable outlet temperature stable, gasification high strength.
NOVELTY - This utility new type claims a biomass gasification furnace one product collecting device, comprising furnace body produce a product storage device is used for cooling, purification and collecting the product, and the top of the furnace body and the furnace body parallel to the axis is set with several the first heat pipe, the storage device including the first conveying pipe is set on inner side of the top part of a furnace body, a purification furnace, a tar collector of purification furnace and a second conveying pipe conveying pipe and the first purification furnace is, the first conveying pipe located on lower side of the first heat pipe and the upper and lower two side set with through hole, inner side top part of purification furnace set with air outlet and several second heat pipe, the air outlet through third conveying pipe and an external fan connection. The advantages of it is product for a twice cooling, the tar from the gas in separate.
NOVELTY - This new utility model provide a kind of one add CO2 H2 industrial biogas production device remove O2, it comprises marsh gas tank, remove O2 water tower and CO2 tower, material pool, H2 entrance and slag pool. Wherein remove O2 water tower is negative pressure and elevated sealing tower and CO2 tower is positive pressure sealing water tower, material pool is more pressure sealing round pool of CO2 air seal add water seal, marsh gas tank for carrying out biochemical reaction, sealing the tank body and generating marsh gas. And the current technology compared with the the utility model of new marsh gas tank in O2 content is low, CO2 concentration is higher, decomposing fungus and alkyl fungus is more active, breeding the growth nutrient needs more abundant, reaction is more complete, marsh gas generation efficiency is high, quality is better, especially H2, causing part of hydrocarbon material transformation is vinyl material, when producing the same in the marsh gas producing gasoline, so, this utility new type has good popularization and application value.
NOVELTY - New waste heat comprehensive using system of marsh gas engineering, wherein the marsh gas engineering comprises a fermentation jar and a marsh slag and a marsh liquid pool, the stepped waste heat recovery system comprising a water jar, heat one lifting system and a lifting system heat. Marsh gas engineering new waste heat comprehensive using system through heat one lifting system of heat in the biogas collecting to in a water jar, then through heat in a lifting system using a little electric energy is heat in the hot water jar after heating to the heat storage jar, a direct-fired heat pump using the heat of heat heating in jar and is transmitted to the fermentation jar, maintaining biogas fermentation when the need of temperature, the use of effective discharge of biogas residue and carry a heat and reduces the fermentation to maintain the needed temperature of energy consumption, effectively keeps the methane engineering of normal operation, maintaining the virtuous circulation of system, reduces the operation cost of marsh gas engineering, the energy consumption is reduced by 50 ~ 90%, change the methane engineering is not a profit and a great of economic benefit.
NOVELTY - A clean biomass fuel comprises 10-16 pts. wt. ethanol, 25-30 pts. wt. pulverized coal, 33-46 pts. wt. sunflower stalk powder, 40-56 pts. wt. rice husk powder, 15-30 pts. wt. soybean straw, 10-16 pts. wt. peat, 20-23 pts. wt. Bauhinia branches, 11-17 pts. wt. rain tree twigs, 5-9 pts. wt. Acacia branches, 1-3 pts. wt. Aralia branches, 5-9 pts. wt. isopropanol, 5-8 pts. wt. tert-butanol, 25-40 pts. wt. potato straw powder, 30-45 pts. wt. barley straw powder, 23-46 pts. wt. broad bean stalk powder and 45-50 pts. wt. wheat straw powder.    USE - Clean biomass fuel (claimed).    ADVANTAGE - The lightweight clean biomass fuel having high combustion value, and excellent thermal efficiency and durability is manufactured by environmentally-friendly and economical process with reduced emission of sulfur dioxide and carbon dioxide.
NOVELTY - This utility new type provide the one a biomass material is biological energy conversion device, comprising: the biomass material is a biological material of a granulation machine, through the first conveyor and pelletizer is connected with a bin, and the fermentation cabin is connected, and the fermentation cabin connected a burning furnace; and the fermentation cabin and the incinerator is connected with the first steam pipeline and the steam conveying to furnace bottom of a fermentation chamber, a furnace bottom of conveying oxygen of air supply pipeline, and connected and furnace gas of a splitting furnace, through the first gas pipeline and splitting furnace connected, and cooling gas of heat exchanger, through second air pipeline and heat exchanger connected and storage gas storage tank, a second gas pipeline set with a pressurizing fan. A biomass material is biological energy conversion device, the biomass material conversion is gas, and through firstly biomass material fermenting, then carry out burning and splitting, effective increase the energy conversion efficiency, reduces the loss of biological energy, increase the economic efficiency.
NOVELTY - This new type utility claims one biomass gasification furnace is a box device, lower part is set with upper part and a square tapered square, further set with a containing space for fan air outlet pipeline and inner tank body is connected air inlet part, tank cover part seal is covered in a charging and discharging wherein a part set with opening and closing discharge wherein a gate valve device. This utility new type of construction is reasonable, design, use time, a box body through supporting frame mounted in the top of the furnace body upper part of gasification furnace, group distribution into pneuma in furnace, lower part of square tapered bottom is gradually reduced is inverted cone, the middle part is a gasification furnace, the gasification furnace is middle part shrinking, using this utility new type of gasification furnace time in working, the lower part is gradually reduced up to down is an inverted square conical, effective barrier of heat in the hearth by a material lifting opening to inner box body, the fuel concentration time heated volatile vapour, avoids the certain period of time by multi-steam and produce a gas combustion is.
NOVELTY - This utility new type claims a biomass fluidization bed one pneuma happen integrated system, comprising a feeding system, a gasification, an ash system, cooling water circulation system, spray cooling one level system, a spraying cooling a level system, circulation water recovery and circulation system and pressure system. This utility new type system technology is advanced, a biomass gas is clean efficient, produce technology of low pollution and there is no gas pollution, at the same time a zero emission waste water of the circulation system is in use process saves a process of using water, saves water resource, reduces the production of a total cost.
NOVELTY - This utility new type provide a one sewage processing system, in turn comprising a a feeding pool, marsh gas pool, solid-liquid separator, an aeration pool, deposition pool, cistern, aritificial wetland pools and, in the feeding pool set with thin, the aeration pool inner set with an aeration device, a depositing pool and sedimentation cistern adjacent set, middle through overflow wherein the connected, the aeration pool through a pipe to sedimentation pool, marsh gas pool comprising a pool body and a biogas pneuma bag group, the pool body from lower to upper in turn set with a whole flat layer, waterproof layer, insulating layer and thick sand layer, the sand layer thickness of inner is embedded with multiple heat pipe, wetland pool is pool bottom from lower to upper in turn set with, water layer, transition layer, filtering layer and covering layer. This utility new type for livestock and poultry cultivation, excrement chip such as sewage treatment, treatment effect is good, the production efficiency is high, operation cost is low, the energy consumption is low, the waste water of the water quality after processing meets the national and local related discharge standard.
NOVELTY - This utility new type is one pre-processing a biomass multi-functional gasification machine, comprising auxiliary tapered spiral propulsion drive shaft, a conical barrel, a hopper, a heat ring, insulating layer and a the pneuma hole. Directly entering into gasification host after sealed by a raw material entering into the auxiliary pre-processing, gasification host comprising host spiral propulsion drive shaft, a main material cylinder, charging the periphery set with electric heat ring and a main insulating layer, set with a gas outlet pipe, a raw material outlet end and main machine raw material inlet is sealed with a machine into a a carbon powder outlet pipe, and a fixed in a machine frame, through the auxiliary raw material pre-processing into the host after the carbonization pyrolysis gasification the produce of a gas a flammable value greatly increase, satisfying the need of cooking and is good for environment protection and new rural construction.
NOVELTY - This new type utility claims one a biomass gas cooling purification water treatment tank, comprising gas cooling tank and gas purification tank, gas cooling roof end and gas purification tank top set with a vertical multi-spray head, a gas cooling tank side wall set with horizontal spray head, gas cooling tank inner top end set with a clapboard, the gas purification tank top end upper clapboard and lower end of upper baffle plate is below the clapboard forming S type channel, wherein liquid and gas purification tank of gas purification roof end of vertical spraying head in turn connect with a purified water tank and a circulation water pump B, wherein a liquid outlet and a gas spray cooling tank in turn connect with a sewage treatment tank and circulation water pump. This utility new type of multi-element, multistage and multi-head height, it can effective remove impurities in a gas, and the gas temperature reduces the obvious, which not only can effective recovery of heat in use of gas, but also realize the sewage zero emission, environment-friendly and economical, and reduces a total cost.
NOVELTY - A one high efficient biological carbon gasification furnace, referring to a one energy saving furnace, belonging to a one environment-protecting and energy-saving type biomass gasification furnace, including high temperature thermal decomposition gasification furnace (200), an electric air blower (300), cuboid housing (100), a gas stove (400), the biomass and pyrolysis in the produce process of biological carbon and tar are at the same time conversion into a gas burning of household cooking with gasification furnace so as to realize especially energy saving environmental protection of rural family especially efficient use purpose of biomass fuel.
NOVELTY - A monomer composition containing a polymerizable monomer is suspension polymerized in the presence of dispersion stabilizer which disperses hydrophobic spherical silica particles in an aqueous medium in presence of a hydrophilic organic compound, to obtain organic resin particles. The silica particles have particle size (volume-based median diameter) of 0.005-1.00 mu m (5-1000 nm), ratio (D90/D10) of particle size distribution of less than 3, mean circularity of 0.8-1 and degree of hydrophobicity 60% or more.    USE - Manufacture of organic resin particles used in electrostatic image developing toner (claimed). Can also be used for antiblocking agent, lubricacy improvement agent, light-diffusion agent, covering composition, additive for decorative boards and artificial marble, chromatographic column packing material, display particle of Coulter counter, carrier for immunodiagnosis drugs, filler for cosmetics, paper processing agent, etc.    ADVANTAGE - The method produces organic resin particles having narrow particle size distribution, excellent fluidity and without aggregation after drying, by an environmentally-friendly process. The electrostatic charge image developing toner using the organic resin particles has stable electrical property with excellent thin line reproducibility, and produces images without fogging.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for dispersion stabilizer for suspension polymerization.
NOVELTY - This utility model claims one new plant biomass fluidization flash pyrolysis and liquefaction device, belonging to energy technology area, comprises fluidization bed pyrolysis furnace, fluidization bed pyrolysis furnace side of wall is equipped with entrance of biomass, provided with bottom, upper part set with smoke air outlet, smoke gas outlet through pipeline in turn and gas-solid separator, a condenser and gas storage cabinet connected, a gas-solid separator the lower part set with coal storage tank, a gas storage tank through coal feeding salt dissolving tank and is set with the coal powder entrance in fluidization bed pyrolysis furnace side wall of connection, fluidization bed pyrolysis furnace below also provided with combustion chamber, the combustion chamber air inlet and the gas storage cabinet connected, the air chamber, the air chamber bottom combustion air outlet chamber through pipeline is connected to the fluidization bed pyrolysis furnace at the same time and also connected air inlet pipe, upper air inlet pipe provided with a fan. This new utility model not generate second time pollute, energy saving, equipment investment, reduce production cost, increase of biomass heat conversion rate.
NOVELTY - Methanol to olefins (MTO) process and naphtha and propane cracking separation includes compressing MTO product gas, drying, entering into crude separation tower, introducing crude separation tower overhead stream comprising 2C and part 3C into naphtha and propane cracking separating cold tank, introducing the crude separation tower bottom stream comprising remaining 3C and 4C into MTO separating depropanizer, introducing the depropanizer overhead stream into MTO separation propylene rectifying tower, and obtaining propylene product from propylene rectifying tower top.    USE - MTO process and naphtha and propane cracking separation (claimed).    ADVANTAGE - The method solves the problems of large investment and low raw material product benefit.    DETAILED DESCRIPTION - Methanol to olefins (MTO) process and naphtha and propane cracking separation comprises compressing MTO product gas, drying, entering into crude separation tower, introducing crude separation tower overhead stream comprising 2C and part 3C into naphtha and propane cracking separating cold tank, introducing the crude separation tower bottom stream comprising remaining 3C and 4C into MTO separating depropanizer, introducing the depropanizer overhead stream into MTO separation propylene rectifying tower, obtaining propylene product from propylene rectifying tower top, obtaining propane in propylene rectifying tower kettle, introducing propylene rectifying tower bottom stream into naphtha and propane cracking separation debutanizer, and conducting naphtha and propane cracking separation to obtain hydrogen, ethylene, ethane, propane part, propylene part, mixed 4C and 5C and hydrocarbon products.
NOVELTY - The gasification device comprises a crusher, a drying machine, a molding machine, a first level tank, a crude purifier, a jar, a cracking device, a cooling separating device, an alkali washing jar, a fan, a first stage gas phase purifier, a desulfurizer, a gas filter, a second level gas phase purifier, an oil liquid separator. The cracking device is provided with a pipeline. The cracking device comprises a cracking kettle provided with a stirring device. The cooling separating device comprises cooling separators. The gas-liquid separators are provided with a drop-splitter.    USE - The gasification device is useful for pyrolyzing biochar (claimed).    ADVANTAGE - The device ensures the yield and quality of gas, and is capable of economically pyrolyzing the biochar in an eco-friendly manner without waste gas, waste residue and waste liquid discharge.    DETAILED DESCRIPTION - The gasification device comprises a crusher, a drying machine, a molding machine, a first level tank, a crude purifier, a jar, a cracking device, a cooling separating device, an alkali washing jar, a fan, a first stage gas phase purifier, a desulfurizer, a gas filter, a second level gas phase purifier, an oil liquid separator. The cracking device is provided with a pipeline. The cracking device comprises a cracking kettle provided with a stirring device. The cooling separating device comprises cooling separators. The gas-liquid separators are provided with a drop-splitter. A water seal tank is provided with a seal water jar that is provided with an exhaust pipe, air inlet pipe, an air outlet pipe, a water inlet and a water outlet. The water seal tank has a height distance of 25 cm. The stirring device has a speed of 8 revolutions per minute. The crude purifier is cyclone separator.
NOVELTY - Carbonized biomass gasification device comprises a crusher, dryer, molding machine, splitting furnace, tanks, purifier, cooling device, a solid-liquid separating device, a fan and washing jar that is connected to a decoking device. An oil liquid separator is equipped at bottom of the washing jar. The oil liquid separator is installed with the splitting furnace.    USE - Carbonized biomass gasification device.    ADVANTAGE - The carbonized biomass gasification device is eco-friendly.
NOVELTY - Methane from carbonaceous material co-generating liquid fuel is produced by purifying crude synthesis gas with carbonaceous material to obtain purified synthesis gas, allowing contact with Fischer-Tropsch synthesis catalyst, performing vapor-liquid separation to obtain gaseous and liquid products in which contacting is controlled to produce hydrogen and carbon dioxide gaseous products with molar ratio of 2.8-3.5, and contacting with methanation catalyst.    USE - Production of methane from carbonaceous material co-generating liquid fuel (claimed).    ADVANTAGE - Process does not require water-gas conversion, increases carbon utilization rate, low energy consumption, low carbon emission, improves economic efficiency, and has easy gas separation, little investment, and high liquid fuel density product.
NOVELTY - Production of methane involves purifying a crude synthesis gas obtained by gasification of carbonaceous material, reacting portion(s) of the purified gas with Fischer-Tropsch synthesis catalyst, vapor-liquid separating and obtaining gas products and liquid products, and reacting the obtained methanation raw material gas product with methanation catalyst. The molar ratio of hydrogen and carbon monoxide in methanation raw material gas is 2.8-3.5.    USE - Production of methane (claimed).    ADVANTAGE - The method efficiently and economically provides methane by improving utilization efficiency of carbon and reducing the load during water-gas shift process, by consuming reduced amount of energy.
NOVELTY - Lipid, fatty alcohol and 1-4 %mass sodium silicate as solid alkali are added to a reaction container and transesterified at 50-80 degrees C and pressure of 2-6 MPa. The reaction liquid is added to a conical jar at space velocity of 0.3-4/hour, fatty alcohol is distilled, and glycerin is separated. Then, 0.1-10 %mass nonionic surfactant(s) with hydrophilic-lipophilic balance value of 3-25 and film-forming material are added to the mixture, stirred, and filtered using ceramic membrane at 10-120 degrees C and pressure of 0.08-0.5 MPa to remove fatty acid monoglyceride, to obtain high-purity biodiesel.    USE - Production of biodiesel (claimed).    ADVANTAGE - The method efficiently and economically provides biodiesel with high purity and high-concentration glycerol as byproduct by simple process without requiring vacuum distillation, under constant reaction temperature.    DETAILED DESCRIPTION - Lipid, fatty alcohol and 1-4 %mass sodium silicate as solid alkali are added to a reaction container and transesterified at 50-80 degrees C and pressure of 2-6 MPa. The reaction liquid is added to a conical jar at space velocity of 0.3-4/hour, fatty alcohol is distilled, and glycerin is separated. Then, 0.1-10 %mass nonionic surfactant(s) with hydrophilic-lipophilic balance value of 3-25 and film-forming material are added to the mixture, stirred, and filtered using ceramic membrane with pore size of 0.02-1.4 mu m at 10-120 degrees C and pressure of 0.08-0.5 MPa to remove fatty acid monoglyceride, to obtain high-purity biodiesel. The film-forming material is inorganic carbon, aluminum oxide or titanium oxide. The molar ratio of fatty alcohol and lipid is 8-15:1.
NOVELTY - A biofuel comprises 5-30 pts. wt. methanol, 3-5 pts. wt. butanol, 5-10 pts. wt. ethanolamine, 10-25 pts. wt. oleic acid, 60-100 pts. wt. diesel oil, 5-20 pts. wt. 200# solvent oil, 6-15 pts. wt. lecithin, 3-8 pts. wt. naphthenic acid, 5-10 pts. wt. borane and 6-15 pts. wt. aqueous ammonia.    USE - Biofuel is used for automobile.    ADVANTAGE - The biofuel has excellent miscibility and high heat value, and is prepared by economical process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biofuel, which involves uniformly mixing methanol, butanol, ethanolamine, oleic acid, diesel oil, 200# solvent oil, lecithin, naphthenic acid, borane and aqueous ammonia, and heating at 55 degrees C for 1 hour.
NOVELTY - Manufacture of biodiesel involves adding fats, fatty alcohol and solid alkali to transesterification reactor, reacting in water bath at 50-80 degrees C under pressure of 2-6 MPa, supplying the reaction mixture into a conical flask, distilling fatty alcohol, separating glycerol, adding nonionic surfactant, and separating fatty acid monoglyceride using ceramic membrane at 10-120 degrees C under pressure of 0.08-0.5 MPa. The ceramic membrane includes ceramic support material and inorganic film material containing carbon, aluminum oxide or titanium oxide, and has pore size of 0.02-1.4 mu m.    USE - Manufacture of biodiesel (claimed).    ADVANTAGE - The method enables simple, efficient and economical manufacture of biodiesel with high purity, high yield, high glycerol concentration and suppressed decompression distillation.    DETAILED DESCRIPTION - Manufacture of biodiesel involves adding fats, fatty alcohol and solid alkali to transesterification reactor, reacting in water bath at 50-80 degrees C under pressure of 2-6 MPa, supplying the reaction mixture into a conical flask, distilling fatty alcohol, separating glycerol, adding nonionic surfactant, and separating fatty acid monoglyceride using ceramic membrane at 10-120 degrees C under pressure of 0.08-0.5 MPa. The nonionic surfactant has hydrophilic-lipophilic balance value of 3-25. The content of nonionic surfactant is 0.1-10 %mass. The ceramic membrane includes ceramic support material and inorganic film material containing carbon, aluminum oxide or titanium oxide, and has pore size of 0.02-1.4 mu m. The solid content of fat is 1-4 %mass. The molar ratio of fatty alcohol with respect to fats is 8-15:1.
NOVELTY - Composition comprises a microbial inoculant, a basic substance, anaerobic digestate, and vehicle as diluent.    USE - Composition used for improving quality of soil microbial and health of crops (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for preparing composition, which involves:    (A) mixing raw materials to obtain mixture; and    (B) fermenting mixture to obtain the product.
NOVELTY - The device has a dust removing tower (13) whose outlet is connected to lower portion of gas cooling tower (14). The outlet of cooling tower is connected to fog tower (15). The outlet of fog tower is connected to upper portion of a gas drying tower (16). The tail gas outlet of drying tower is connected to a conversion tower (17). The lower portion of conversion tower is connected to absorption tower (18). The outlet of absorption tower in lower portion is connected to discharging tower (19). The gas discharge port of the discharging tower is provided in upper portion.    USE - Desulphurization purification device for coke furnace used in preparation of gaseous fuel or methanol.    ADVANTAGE - The purification device has better desulfurization effect and saves investment cost for purification process.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the desulphurization purification device.    Dust removing tower (13)    Gas cooling tower (14)    Fog tower (15)    Gas drying tower (16)    Conversion tower (17)    Absorption tower (18)    Discharging tower (19)
NOVELTY - Gas product of ethanol to olefin process is compressed, dried, and resultant crude product is provided into a separation column including 2C and 3C components. The overhead fractions of separation column are provided into deethanizer column for carrying out steam cracking of naphtha, and bottom fractions of separation column are provided into a depropanizer column. During naphtha steam cracking process, ethylene, ethane, propane, propylene, and mixed 4C and 5C hydrocarbon products, are produced.    USE - Steam cracking of naphtha used in production of light olefin e.g. ethylene and propylene.    ADVANTAGE - The method enables economical steam cracking of naphtha.    DETAILED DESCRIPTION - Gas product of ethanol to olefin process is compressed, dried, and resultant crude product is provided into a separation column including 2C and 3C components. The overhead fractions of separation column are provided into deethanizer column for carrying out steam cracking of naphtha, and bottom fractions of separation column are provided into a depropanizer column. The overhead factions of depropanizer column are entered into propylene distillation column, and propylene product is produced at top of the propylene distillation column. The bottom fractions of depropanizer column are entered into debutanizer column. During naphtha steam cracking process, ethylene, ethane, propane, propylene, and mixed 4C and 5C hydrocarbon products, are produced.
NOVELTY - A high energy composite alcohol base gasoline comprises 14.5-63.5 pts. wt. methyl alcohol, 0.5-1.5 pts. wt. comprehensive modified additive and 30-85 pts. wt. gasoline.    USE - High energy composite alcohol base gasoline.    ADVANTAGE - The method is simple, low-cost and suitable for industrialization. The gasoline has high temperature lubricating property and low temperature ignition start.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high energy composite alcohol base gasoline comprising taking raw materials, putting into jar, stirring, and carrying out static aging.
NOVELTY - An anaerobic sludge digestion pre-processing method involves pre-treating concentrated residual sludge in pool, adding complex microbial agents, stirring for complex reaction, and processing anaerobic digestion pool according to the proportion of anaerobic sludge, where the complex microbial agent comprises Bacillus subtilis, white Streptomyces, Streptomyces griseus, Candida utilis, Aspergillus sojae, Lactobacillus bulgaricus, Lactobacillus, Lactococcus lactis, Rhodopseudomonas palustris, and Pseudomonas.    USE - Method for pre-processing anaerobic sludge digestion.    ADVANTAGE - The method enables pre-processing anaerobic sludge digestion with increased biological gas production, and increased anaerobic digestion efficiency.    DETAILED DESCRIPTION - An anaerobic sludge digestion pre-processing method involves pre-treating concentrated residual sludge in pool, adding complex microbial agents, stirring for complex reaction, and processing anaerobic digestion pool according to the proportion of anaerobic sludge, where the residual sludge containing solid suspends upto 20000-35000 mg/l, the volatility of residual sludge is more than 50%, the complex microbial agents comprises Bacillus subtilis, white Streptomyces, Streptomyces griseus, Candida utilis, Aspergillus sojae, Lactobacillus bulgaricus, Lactobacillus, Lactococcus lactis, Rhodopseudomonas palustris, and Pseudomonas and the viable count of the complex microbial agents is 5-20% and pH is 3-4.
NOVELTY - The sampler has an oval drill bit (1) formed with a sampling hole (3). A closed spiral device is provided with a supporting rod and a first blade. A corner part of the first blade is formed with a square hole. A first activity connecting rod device is provided with a handle (12), a connecting pole and a ring hook. A sample collection cylinder (10) is connected with a lower end of the oval drill bit and the closed spiral device. The sample collection cylinder is connected with a snap ring (2). A lower end of a closed stirrer is connected with a second blade.    USE - Quantitative compost sampler.    ADVANTAGE - The sampler is simple in structure, inexpensive, convenient to carry and convenient to disassemble and clean, has small volume, and reduces fertilizer body disturbance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a quantitative sample composting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a quantitative compost sampler.    Oval drill bit (1)    Snap ring (2)    Sampling hole (3)    Sample collection cylinder (10)    Handle (12)
NOVELTY - The method involves separating lignocellulosic biomass by solvent-based extraction in a lignin fraction. The lignin fraction is concentrated by solvent used in separation, where the concentrated lignin fraction is fitted with a catalytic converter and subjected to catalytic depolymerization. Residual solvent is included in the concentrated lignin fraction to catalytic depolymerization at temperatures between 150 and 350 degree Celsius. Required heat for separation of lignocellulosic biomass is generated by using carbon residue.    USE - Method for producing diesel and petrol-like products from lignin from lignocellulose.    ADVANTAGE - The method enables reducing the lignin content of the cellulose fraction, hydrolyzing the cellulosic fraction and fermenting the cellulosic fraction biochemically.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing diesel and petrol-like products from lignin from lignocellulose. '(Drawing includes non-English language text)'
NOVELTY - The pool has a fermentation pool body (1) whose side wall is provided with a double-layer hollow structure. A material wall (4) is connected to a bottom part of a water wall (5). A hollow part is fixed with a water storage tank (2), an air storage cover (3) and a cover wall (6). A top part of the air storage cover is formed with an air hole (15). A lower edge of the air storage cover is fixed with a flange. An upper edge of the cover wall is fixed with another flange. The flanges are fixed and sealed together through a bolt (8).    USE - Floating cover type biogas pool for use in a rural home.    ADVANTAGE - The pool is simple in structure, inexpensive and convenient to mount, and realizes gas feeding and discharging processes in an easy manner, and has prolonged service life.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a floating cover type biogas pool in partial section.    Fermentation pool body (1)    Water storage tank (2)    Air storage cover (3)    Material wall (4)    Water wall (5)    Cover wall (6)    Bolt (8)    Air hole (15)
NOVELTY - The anaerobic digestion reactor has an influx unit, which is connected to an end of a microorganisms apparatus body. An end of a portal (140) of a reactor main body (100) is adhered to the microorganisms tool (200), where the microorganisms apparatus body is positioned in the upper portion of a stirrer (400). The stirrer installed is in the lower part of the reactor main body that is equipped with an anaerobic digestion liquid exhausting part (160). An effluent supply unit is connected to a biogas exhausting part (130) and a gateway (150).    USE - Anaerobic digestion reactor for organic waste-water.    ADVANTAGE - The stirrer installed is in the lower part of the reactor main body that is equipped with an anaerobic digestion liquid exhausting part and an effluent supply unit is connected to a biogas exhausting part and a gateway, and thus enables to enhance the biogas production efficiency and preventing the entrance of the scum.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an anaerobic digestion reactor.    Reactor main body (100)    Biogas exhausting part (130)    Portal (140)    Gateway (150)    Anaerobic digestion liquid exhausting part (160)    Microorganisms tool (200)    Stirrer (400)
NOVELTY - The method involves cooling gaseous stream in a heat exchanging condenser (5) to predetermined temperature. The gaseous stream from the condenser is passed to a heat-exchanger (14). The gaseous stream in the heat exchange condenser is cooled to the predetermined temperature. Amount of energy required to bring about condensation or solidification of the harmful compounds in the heat exchange condenser is reduced. The clean gaseous stream is passed from the heat exchanger. Acids of condensed or solidified harmful compounds from the heat exchanging condenser are removed.    USE - Energy saving method for removing harmful compounds from a gas mixture. Uses include but are not limited to benzene, ethanol, methanol, methane, gasoline, crude oil, diesel, liquefied petroleum gas, toluene, acrylonitrile, styrene, xylene, nitrogen dioxide, hydrogen sulfide, sulfur dioxide, carbon dioxide.    ADVANTAGE - The method enables lowering the energy required to condense or freeze harmful compounds in the heat exchanging condenser, reducing pressure in areas with inflammable materials so as to reduce the risk of explosions and reduce pressure in a tank to reduce the risk of explosions. The method enables removing the harmful compounds from the gas mixtures in an easy, quick, safe, energy saving and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for removing harmful compounds from a gas mixture.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for removing harmful compounds from a gas mixture.    Main conduit (1)    Main inlet (3)    Heat exchanging condenser (5)    Outlet for removal of condensed harmful compounds (8)    Heat-exchanger (14)
NOVELTY - Extracting tetrandrine involves crushing Stephania tetrandra and then sieving the crushed material through 100 meshes sieve to obtain tetrandrine crude powder. The tetrandrine crude powder is added with acid to adjust pH value to 3.5-4.5. The obtained material is kept in an ultrasonic extraction device for extracting for 60-90 minutes and then the extracted material is centrifuged to remove supernatant. The obtained material is absorbed by macroporous cation exchange resin and then the absorbed material is washed with distilled water.    USE - Method for extracting tetrandrine (claimed).    ADVANTAGE - The method enables to extract tetrandrine in simple, cost-effective and eco-friendly manner, and with high selectivity.    DETAILED DESCRIPTION - Extracting tetrandrine involves crushing Stephania tetrandra and then sieving the crushed material through 100 meshes sieve to obtain tetrandrine crude powder. The tetrandrine crude powder is added with acid to adjust pH value to 3.5-4.5. The obtained material is kept in an ultrasonic extraction device for extracting for 60-90 minutes and then the extracted material is centrifuged to remove supernatant. The obtained material is absorbed by macroporous cation exchange resin and then the absorbed material is washed with distilled water. The washed material is eluted with 0.4-0.5 mol/L ammonia ethanol solution by adsorption resin column at a flow rate of 10 milliliters per minute. The eluted material is concentrated and dissolved in acetone and then the dissolved material is recrystallized for 2 times to obtain tetrandrine.
NOVELTY - Producing ortho-quinone involves taking red sage root, which is then pulverized to obtain powdered material and then mixed with 40% ethanol to obtain an extract. The obtained extract is filtered for 0.5-1.5 hours to collect filtrate, which is then concentrated to vaporize alcohol from it. The obtained concentrated product is then added to the adsorption column, which is stacked with polyamide resin and utilizes acid-alcohol for performing elution process. The obtained eluate is recovered by the solvent to obtain ortho-quinone in the crude extract.    USE - Method for producing ortho-quinone used for preparing anti-leukemia drug (claimed).    ADVANTAGE - The method enables to produce ortho-quinone that has good anti-tumor effect and also effectively controls proliferation of lymphocytic leukemia and myeloid leukemia, in a simple, eco-friendly and economical manner. The produced ortho-quinone efficiently exhibits its effect on tumor cell lines i.e. P-388 lymphocytic leukemia.    DETAILED DESCRIPTION - Producing ortho-quinone involves taking red sage root, which is then pulverized to obtain powdered material and then mixed with 40% ethanol to obtain an extract. The obtained extract is filtered for 0.5-1.5 hours to collect filtrate, which is then concentrated to vaporize alcohol from it. The obtained concentrated product is then added to the adsorption column, which is stacked with polyamide resin and utilizes acid-alcohol for performing elution process. The obtained eluate is recovered by the solvent to obtain ortho-quinone in the crude extract. High-speed countercurrent chromatography technique is performed to separate ortho-quinone from the crude extract.
NOVELTY - A one silkworm sand biological organic fertilizer is fermentation, wherein the fermentation shed of the silkworm sand biological organic fertilizer is a structure, fermenting shed is 50 m to 80 m, the width is 5 m to 8 m, high 3 m to 4 m, bottom shed with cement hardening, fermenting shed top is arc-shaped, the shed top fermentation using a high resistance transparent film covered periphery of fermenting shed set with activity, a multi-adjacent of fermenting shed junction with antirust metal plate, fermenting shed junction set with water tank. Open the activity surrounding the fermentation shed inner can accelerate the air flow so as to control the fermentation temperature.
NOVELTY - This utility new type provide the a one organic fertilizer reaction device, comprising reaction jar, center of reaction jar set with erect a stir shaft, stir up shaft set with stir blade, reaction jar is lower bottom middle set with discharge wherein, side wall of reaction jar lower part set with a vent wherein, reaction jar is a top outside side plate set with a vent hole, a top plate set with a feeding middle wherein the upper reaction jar is set with inclination of a conveying pipeline, the conveying pipeline set with inner auger, the lower part of conveying pipeline set with a feeding port, lower part of bottom conveying pipeline set with a water outlet, a conveying pipeline is a part set with a, blanking and reaction jar upper part of feeding wherein a. This organic fertilizer reaction device shortens the reaction time of organic fertilizer, one jar organic fertilizer fermentation time is only need one week and time.
NOVELTY - One with a steam sterilizing device of feeding jar, comprising tank body, air inlet pipeline and the feeding port, the tank body and between the pneuma pipeline directly connected, the top of the tank body, a air inlet pipeline set with pneuma pressure table and pneuma pressure control valve, the tank body is further connected with a feed pipeline, low material supplement pipeline and steam pipeline, a material supplement pipeline the jar body of middle part, a tank body and a feeding pipeline set with a number one switch valve, lower material supplement pipeline is located at the bottom of jar body, and between the lower feeding pipeline set with switch valve, a steam pipeline and a feeding pipeline respectively, lower material supplement pipeline is connected, a steam pipeline set with a number three switch valve. This utility new type has simple structure, it is not easy for microorganism fermentation jar inner cause pollution.
NOVELTY - The invention claims a MEMS methane sensor , which is suitable for coal mine use. It comprises a P type silicon substrate, forming N-type silicon on the P type silicon substrate frontage, and the N type silicon process in silicon heating element on the P-type silicon substrate, the silicon heating element comprising of two fixed end, silicon heater, two of silicon cantilever; the sensor with normal silicon material as the heating element, heating element at the same time as sensitive component, and no need to catalyst carrier and catalyst material, the sensor has low cost, high sensitivity, and consume low power, high sensitivity, measure oxygen concentration without influence, not by carbon, influence of poisoning.
NOVELTY - Preparation of rufinamide comprises reacting 2,6-difluorobenzyl alcohol and diphenylphosphoryl azide to obtain 2,6-difluorobenzyl azide, reacting with propiolate derivative (i) to obtain methyl 1-(2,6-difluorobenzyl)-1H-1,2,3-triazole-4-carboxylate derivative (ii) and reacting with ammonia or alcohol.    USE - Method for preparing rufinamide (claimed).    ADVANTAGE - The rufinamide has low toxicity and high safety. The method is simple, has low pollution and short production cycle, and is suitable for industrial production.
NOVELTY - Preparation of ritonavir comprises reacting N-(N-methyl-N-((2-isopropyl-4-thiazolyl)methyl)amino carbonyl)-L-valine and (2S, 3S, 5S)-5-amino-2-(N-((5-thiazolyl)-methoxycarbonyl)amino)-1,6-diphenyl-3-hydroxyhexane in organic solvent in the presence of 3-(diethoxyphosphoryloxy)-1,2,3-benzotriazin-4(3H)-one as condensing agent under alkali condition to carry out amide-forming reaction.    USE - Method for preparation of ritonavir (claimed).    ADVANTAGE - The method is environment-friendly, and it has effectively reduced cost of raw material, simple operation, high product yield, and easy separation and purification process.
NOVELTY - Recovery of lovastatin from lovastatin mother liquor comprises mixing lovastatin crystallization mother liquor and alkaline aqueous solution, washing, and separating organic phase; mixing acidic aqueous solution, washing, and separating organic phase; and subjecting cyclization reaction, concentrating, and crystallizing.    USE - Method for recovery of lovastatin from lovastatin mother liquor (claimed).    ADVANTAGE - The method is simple, more safe, environment-friendly and suitable for industrial continuous production, reduces solvent consumed, and it has increased recovery rate and fast recovery process.
NOVELTY - The method involves sending a duct (26) of hydrogen enriched gas (14) from a stripping column (2) to an intermediate point of denitrogenation column (4) if nitrogen content of the mixture and/or carbon monoxide enriched head gas (16) and/or nitrogen enriched gas is lower than a threshold. The portion coming from the stripping column is sent to an intermediate point of the column with a separation column, and a non-condensed gas from a head condenser of the separation column is sent to the denitrogenation column if the fluid is derived from the hydrogen impoverished liquid by distillation.    USE - Method for cryogenic separation of carbon monoxide, hydrogen, nitrogen and methane mixture by cryogenic distillation.    ADVANTAGE - The method enables compensating for the reduction of nitrogen by importation of a portion of head gas coming from the stripping column in upstream of carbon monoxide/nitrogen column toward the carbon monoxide/nitrogen column, and the head gas of the stripping column contains the hydrogen so as to increase incondensable flow directed toward the carbon monoxide/nitrogen column.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an apparatus for cryogenic separation of a carbon monoxide, hydrogen and nitrogen mixture and methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of an apparatus for cryogenic separation of carbon monoxide, hydrogen and nitrogen mixture and methane.    Stripping column (2)    Denitrogenation column (4)    Hydrogen enriched head gas (14)    Carbon monoxide enriched head gas (16)    Duct (26)
NOVELTY - The apparatus has a buffer tank (41) used for storing the biogas compacted in a compressor (31, 32). A gas separation membrane unit (21) separates carbon dioxide and methane from biogas by passing the hollow fiber membrane corporate unit to buffer tank. The heating equipment and the cooling facility are installed at the gas separation membrane units.    USE - Apparatus for collecting carbon-dioxide from bio gas for increasing new renewable energy field.    ADVANTAGE - The carbon dioxide is separated from the biogas using the hollow fiber membrane corporate unit. Hence, the carbon dioxide of the high purity is separated from the biogas and the recovery rate of methane is improved. The carbon dioxide of the high purity produced is used for the growth increase of seed or it can be used to the manufacture of the dry ice. The cost required for maintenance of management is reduced and the energy efficiency is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a configuration diagram of the apparatus for collecting carbon-dioxide from bio gas. (Drawing includes non-English language text)    First methane discharge pipe (12)    First exhaustion of carbon dioxide pipe (13)    Gas separation membrane unit (21)    Compressor (31, 32)    Buffer tank (41)
NOVELTY - A refrigerant composition comprises carbon dioxide, isobutane, propane, and 2-20 parts mass dimethyl ether with respect to 100 parts mass carbon dioxide.    USE - Refrigerant composition is used for refrigerators of freezers (claimed) used for domestic purpose.    ADVANTAGE - The refrigerant uses components having low global warming potential, has high cooling capacity and improved operational stability, and does not solidify at low temperature.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for freezer (1) provided with a freeze-preservation chamber and a refrigerator which cools the freeze-preservation chamber (3).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the structure of a domestic ultra-low-temperature freezer.    Domestic ultra-low-temperature freezer (1)    Freezer main component (2)    Freeze-preservation chamber (3)    Rotating upper cover (5)    Hinge (6)
NOVELTY - The apparatus has an ammonia meter (11) that is provided in upstream of a denitrifying confirmation unit. The confirmation unit is set to confirm the denitrifying state based on desired ratio of prescribed nitric acid, while prescribing desired ratio of nitric acid in halfway position based on measured ammonia concentration. The aeration units (6a-6d) are located in an upstream than the denitrifying confirmation unit in alignment with flow direction of nitrogen-containing water. The gas supply amount control units (10a-10d) are set to control the supply amount of gas.    USE - Apparatus for processing waste water such as domestic waste water and industrial waste water.    ADVANTAGE - The gas supply amount is appropriately controlled, according to the load of the nitrogen-containing water flowing into the reaction tank. Therefore, the proper quantity of oxygen is supplied to the reaction tank, while reducing the electric power consumption. The denitrifying process is controlled appropriately, based on the water quality of process water. The nitrogen removal rate is improved and treated water quality is improved.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method for processing waste water;    (2) a system for processing waste water;    (3) an apparatus for controlling waste water;    (4) a method for controlling waste water; and    (5) a program for controlling waste water.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the block diagram which shows the waste water treatment equipment. (Drawing includes non-English language text)    Primary sedimentation basin (1)    Reaction tank (2)    Aeration units (6a-6d)    Gas supply amount control units (10a-10d)    Ammonia meter (11)
NOVELTY - A turntable-type one turner, the transverse walking speed reducing motor (5) is power input shaft through a chain and a transverse moving trolley (3) is shaft transmission is connected with turn polishing wheel disk mounting frame (6) mounted in the transverse moving trolley (3), turn polishing wheel disk (7) through wheel shaft mounting turn polishing wheel disk mounting bracket a (6) a, turn polishing wheel disk (7) is a wheel shaft mounted with a chain wheel, turn polishing speed reducing motor (4) is power input shaft through a chain and a turn wheel polishing disk (7) is a shaft of chain wheel transmission is connected with lengthways walking speed reducing motor (8) mounted in machine frame (1) upper, lengthways walking speed reducing motor (8) is power input shaft through chain and gear and walking wheel (1-1) of transmission shaft. This utility new type has advantages is: the machine structure is simple and reasonable, to effect turning.
NOVELTY - This utility new type claims a full one isolated water electrolytic groove, wherein comprising intermediate plate, a left end plate and right end plate, a middle plate and between the left end plate set with several left plate, a left end plate and a left plate, a right plate and a left plate, a right plate and middle plate set with a hydrogen-oxygen happen room; the middle plate and right end plate set with several right plate, a right end plate and right plate, right plate and right plate, right plate and middle plate set with a hydrogen-oxygen happen room, a middle plate of middle part is cavity, middle plate connected with a through out of a right end plate, a right plate and a through out of the left end plate, an alkali liquid inlet pipe of the left plate, the middle plate is set with hydrogen and happen room is corresponding to a. type liquid inlet pipe. This utility new type avoids the hydrogen and oxygen of each string to increase effect purity hydrogen and oxygen, at the same time greatly reduces the risk of happen probability.
NOVELTY - Gaseous separation or concentration method involves contacting mixture of gas containing some gas component with separation membrane, permeating a high-permeability component in the gas mixture, concentrating the low-permeability component by separating a component with the high-permeability from gas mixture, or permeating high-permeability component from the gas mixture. The separation membrane includes zeolite film formed on inorganic porous support. The zeolite in the zeolite film has pore structure including oxygen-containing ring of less than 8 members.    USE - Separation or concentration of gas e.g. natural gas and combustion gas (all claimed), oven gas and land file gas discharged from garbage reclamation field, thermal power station and petrochemical industry.    ADVANTAGE - The method enables separation or concentration of gas with excellent separability.    DETAILED DESCRIPTION - Gaseous separation or concentration method involves contacting mixture of gas containing some gas component with separation membrane, permeating a high-permeability component in the gas mixture, concentrating the low-permeability component by separating a component with the high-permeability from gas mixture, or permeating high-permeability component from the gas mixture. The separation membrane includes zeolite film formed on inorganic porous support. The molar ratio of silica and alumina in the surface of zeolite film is 25 or more. The zeolite in the zeolite film has pore structure including oxygen-containing ring with less than 8 members. An INDEPENDENT CLAIM is included for manufacture of high-oxygen-concentration mixture of gas.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of measuring apparatus used for gas separation.    Zeolite film complex (1)    Pressure-resistant container (2)    End pin (3)    Connection portion (4)    Pressure gauge (5)
NOVELTY - This utility new type provide a one with a corn stalk, leaves powder crush the organic fertilizer of cooking device, comprising pot body and pot cover, pot body with a steam pipe at the bottom of the inner pot body is inverted conical, inverted conical cover through fixing column fixed in the bottom of the boiler body, a steam outlet tube is located below is inverted conical. This utility new type through a steam pipe in the boiler body at the bottom of the upper part set with a inverted conical one, at the same time the design of steam pipe into higher than the height of an inverted conical cover bottom part, it not only avoids the corn stalk, leaves made of powder blocking steam pipe, at the same time it also can make the steam can permeate to the pan body each a corner, the corn stalk, leaves made of powder can more quickly, the subsequent organic fertilizer of the fermentation step.
NOVELTY - Purification of celecoxib comprises dissolving celecoxib in ethanol at volume mass ratio of 3:1-10:1 mL:g at 60-78 degrees C, filtering to obtain ethanol solution, adding 70-90 degrees C hot water at volume ratio of 3:1-10:1 mL:g, standing, cooling to 5-10 degrees C, crystallizing to 0-30 degrees C for 12-24 hours, filtering, washing, and drying.    USE - Method for purification of celecoxib (claimed).    ADVANTAGE - The method is more environment-friendly, achieves high purity and product yield, and it has convenient operation. The celecoxib achieves national and international standard medicine quality, and it has unknown-impurity content of less than 0.1%.
NOVELTY - This utility new type claims a one garbage fermentation tank, comprising a guide heat oil tube, a guide heat oil coating tube at the lower part, a region outside a stainless steel plate is set with a heat-conducting oil outlet shell, the heat conducting area and heat conducting area between the shell set with insulating layer, wherein the said oil guide area is set with a safety valve, a heat guide oil inlet oil wherein a. one end height is higher than the other end of the heat-conducting oil outlet of the cylinder body at the bottom of the heat conducting oil in expansion pedestal, is set in the valve pedestal is a, set with heat conducting oil electric heating system of a pedestal in inner. This utility new type is garbage fermentation tank, to conducting a medium, the electric heating system is a heat transfer to the waste fermentation tank. Raise temperature fast speed, fermenting tank dipping tube uniform heating in a heat conducting oil, a structure is simple and compact, the mounting operation is simple, safety without safety hidden trouble.
NOVELTY - This utility new type claims a organic fertilizer walking one stir device, wherein comprising frame type bracket, lower end of bracket is set with walking mechanism, the walking mechanism comprise two parallel is a walking track and a walking wheel under the bracket, upper end of bracket is parallel set with the first rotating a rotating shaft and a second rotating shaft, upper of each set with two rotating shaft of the lifting chain wheel, and a lifting chain wheel matching with each one of lifting chain, further comprising a secondary bracket, the auxiliary bracket sleeved in inner bracket, the lower part, the assistant bracket lower part is set with auxiliary lifting chain wheel chain wheel; the each lifting chain of one end fixed in a vice-support frame and the other end around a lifting chain wheel, a rear auxiliary chain wheel fixed in a secondary support, a secondary support set with rotating power device, rotating power device drives a rotating roller, a rotating roller set with a stir.