NOVELTY - Method of producing sodium alginate and co-producing ethanol and organic fertilizer involves pre-processing kelp using cellulase and protease complex enzyme, carrying out ethanol fermentation by monosaccharide and oligosaccharide kelp cellulolytic microorganisms, where the fermentation broth containing a small amount of kelp residue is used for preparing organic fertilizer, extracting and separating the pre-treated kelp with alginic acid by dilute alkali digestive process and condensing mixture by ion exchange method to obtain high-quality sodium alginate.    USE - The method is useful for producing sodium alginate and co-producing ethanol and organic fertilizer (claimed).    ADVANTAGE - The method has high extraction rate and promotes high-value utilization of kelp and develops marine biomass energy.
NOVELTY - Insect repellent composition prepared by extracting a cinnamon cortex extract by heating the cinnamon bark in ethanol having the concentration of 25-45 vol.% at the pressure condition of -2.5 kgf/cm2 at the temperature of 40-125 degrees C, separating the solid content and the extraction solvent of the cinnamon bark, and distilling the extraction solvent in an ambient pressure condition using a fractional distillation method, is claimed.    USE - The insect repellent composition is useful as mosquito or Acarus control agent, and is useful for spraying on cloths, bedclothes and wall.    ADVANTAGE - The composition prevents the culex access in the human body in an environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing an insect repellent composition comprising extracting a cinnamon cortex extract by heating the cinnamon bark in ethanol having the concentration of 25-45 vol.% at the pressure condition of -2.5 kgf/cm2 at the temperature of 40-125 degrees C, separating the solid content and the extraction solvent of the cinnamon bark, and distilling the extraction solvent in an ambient pressure condition using a fractional distillation method.
NOVELTY - A catalyst comprises polcyclic N-oxyl compound (I).    USE - Catalyst used for oxidation of primary and secondary alcohols used in synthesis of organic compounds used as pharmaceutical products, pharmaceutical raw materials and agrochemicals.    ADVANTAGE - The catalyst has high activity even when used in air oxidation process, and provides high-value-added organic compounds by an easy and environmentally-friendly process.    DETAILED DESCRIPTION - A catalyst comprises polcyclic N-oxyl compound of formula (I) and/or its derivative.    R1=H or alkyl;    R2=H, or 1-5C alkyl or 6-10C aryl (all optionally substituted);and    X=group containing hetero atom, excluding nitroxide (-NO.- group).    An INDEPENDENT CLAIM is included for alcohol oxidation method, which involves oxidizing alcohol in the presence of alcohol oxidation catalyst and co-oxidation agent.
NOVELTY - The system comprises a machine frame. The machine frame is provided with a fermentation tank. The fermentation tank is provided with a feeding port and an exhaust port. A lower end of the machine frame is provided with a discharging opening. The discharging opening is internally provided with a stirring blade. An upper part of the machine frame is provided with a cycloidal pinwheel speed reducer. An outer wall of the fermentation tank is provided with a heater, an oil smoke purifier and a deodorization tower.    USE - Used as fine fertilizer manufacturing system.    ADVANTAGE - The system simply manufactures the fine fertilizer in an economical manner.    DETAILED DESCRIPTION - The system comprises a fine fertilizer manufacturing machine, where the machine comprises a machine frame. The machine frame is provided with a fermentation tank. The fermentation tank is provided with a feeding port and an exhaust port. A lower end of the machine frame is provided with a discharging opening. The discharging opening is internally provided with a stirring blade. An upper part of the machine frame is provided with a cycloidal pinwheel speed reducer. An outer wall of the fermentation tank is provided with a heater, an oil smoke purifier and a deodorization tower. The heater is a plate-type heater. The plate-type heater is adhered on an outer wall of the fermentation tank. The deodorization tower comprises a tower body. A lower part of the tower body is provided with an air inlet. A top part of the tower body is provided with an air outlet. The oil smoke purifier comprises a gas purifier and a fan. The gas purifier and the fan are connected with each other.
NOVELTY - Bio-bacterium fertilizer comprises 1-3 pts. wt. of biocontrol streptozotocin, 35-85 pts. wt. of potassium humate, 10-50 pts. wt. of nanometric silicon dioxide, 2-6 pts. wt. of enzyme active material, and 2-6 pts. wt. of surfactant, where the biocontrol streptozotocin is Bacillus subtilis and Trichoderma harzianum.    USE - The bio-bacterium fertilizer is useful for preventing and treating crop pests and diseases (claimed).    ADVANTAGE - The bio-bacterium fertilizer prevents the infection of plant and emulational plant pathogenic bacteria, promotes the growth of crop without use of pesticide, and reduces the environment pollution so as to improve yield and quality of the plant.
NOVELTY - Spraying liquid comprises 0.0005-0.0007 wt.% of effective microorganism (EM) original dew, 0.12-0.2 wt.% of sugar, 0.00007-0.00009 wt.% of sodium selenite, 0.0009-0.0012 wt.% of molybdate, 0.0008-0.0011 wt.% of manganese sulfate, 0.0008-0.0012 wt.% of sodium borate, 0.0016-0.0022 wt.% of zinc sulfate, 68-83 wt.% of yeast cake cypress liquid and balance amount of water, where the yeast cake cypress liquid is prepared by adding the cake cypress type raw material and fertilizer and then fermenting until the water content is 60-65%.    USE - Used as spraying liquid.    ADVANTAGE - The spraying liquid can be simply prepared with good absorption rate and stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing spraying liquid comprising (a) mixing the sodium selenite, manganese sulfate, sodium borate and zinc sulfate with a proper amount of water and then dissolving to obtain a liquid, (b) crushing the cake cypress type raw material and then adding with fertilizer and water and fermenting for 22-26 hours to obtain the yeast cake cypress liquid, (c) diluting the EM original dew with water and then adding with cake cypress yeast solution, stirring and fermenting for 2-9 hours to obtain the fermentation liquid to adjust a pH value to 6-8, (d) diluting the sugar, fermentation liquid and water and then turning for 12 hours, fermenting for 2-4 days and filtering to obtain a solution II, and (e) adding the solution I and solution II and then stirring, standing for 22-26 hours and filtering to obtain the product.
NOVELTY - Active organic fertilizer comprises 60-78 wt.% sludge, 20-30 wt.% livestock excrement, 1-10 wt.% ammonium bicarbonate, and 0.1-1 wt.% fermenting microorganism.    USE - Used as an active organic fertilizer.    ADVANTAGE - The fertilizer comprises mineral nutrition and has high organic matter content, also comprises mixed organic matter containing vitamin, amino acid, humic acid and lignin salt; is provided with strong chemical activity and biological activity; is provided with function of chelating and slow release; and is used as best resource for producing organic and inorganic fertilizer. The method has simple preparation process and is easy to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing active organic fertilizer, comprising (i) providing each raw material according to percentage by weight, (ii) mixing the raw materials and composting and fermenting at high temperature, and (iii) dehydrating the material after fermenting, crushing, and screening to obtain the active organic fertilizer.
NOVELTY - Extraction of natural taurine from abalone viscera involves pretreating raw material by adding abalone viscera in water, cooking at high temperature, collecting broth, treating with activated carbon at room temperature to obtain effluent for taurine preparation, adding ethanol, concentrating supernatant, centrifuging precipitate, adding activated carbon, stirring, filtering, adding filtrate with 3 times the volume of absolute ethanol to remove impurities, standing, crystallizing, filtering and drying to obtain taurine crystal.    USE - Method for extracting natural taurine from abalone viscera (claimed).    ADVANTAGE - The method is simple, has low extraction cost, has high extraction rate, energy-saving and environment-friendly.    DETAILED DESCRIPTION - Extraction of natural taurine from abalone viscera comprises pretreating raw material by adding abalone viscera in water cooking at high temperature, collecting broth, treating with activated carbon at room temperature to obtain effluent for taurine preparation, adding ethanol to effluent, centrifuging to obtain precipitate and supernatant, adding 95% ethanol to obtain 60-80% final concentration, concentrating supernatant, adding 4-6 times the volume of absolute ethanol, standing at 4 degrees C for greater than or equal to 12 hours, centrifuging precipitate, adding 4-5 times amount of hot water at 70-80 degrees C, adding activated carbon, stirring, filtering, adding filtrate with 3 times the volume of absolute ethanol to remove impurities, standing at 4 degrees C, crystallizing for greater than or equal to 24 hours, filtering and drying to obtain taurine crystal.
NOVELTY - Extraction of natural taurine comprises pretreating raw materials by cleaning shellfish, cooking at high temperature, collecting broth, concentrating to solid weight content of 5-10%, adding ethanol to obtain precipitate and supernatant, preferably adding 95% ethanol to obtain 50-80% final concentration, concentrating supernatant, crystallizing, filtering, removing impurities by adding 3-4 times volume of absolute ethanol, concentrating filtrate, standing at 4 degrees C, crystallizing for greater than or equal to 24 hours, filtering and drying to obtain coarse taurine crystals.    USE - Method for extracting natural taurine (claimed).    ADVANTAGE - The method is simple, has low extraction cost, has high extraction rate, energy-saving and environment-friendly.
NOVELTY - Photo-curing coating material comprises 5-90 wt.% of modified vegetable oil, 5-45 wt.% of active diluent and 5 wt.% of photo initiator.    USE - The photo-curing coating material is useful for preparing a slow-release water-storing fertilizer (claimed).    ADVANTAGE - The photo-curing coating material is prepared in a simple and cost-effective manner without using organic solvent and without soil and water pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing a photo-curing coating material comprising adding pre-polymer modified plant oil and active diluent, heating at room temperature in a light-tight container, adding a photo-initiator into the mixture, and uniformly mixing at room temperature; and    (2) use of a photo-curing coating material in the preparation of slow-release water-storing fertilizer comprising uniformly spraying the photo curing coating material to a disk or drum, continuously rolling a fertilizer particle surface, and radiation-curable solidifying using an UV light to obtain a slow release and release control fertilizer.
NOVELTY - Hydrogen and oxygen generator comprises rectangular plate (7) processed with sealing groove (1), lower end provided with protrusions (2), at least one air outlet hole (3). A first pole piece separating fixed mounting hole (4) is rhombus, and second pole piece separating fixed mounting hole (9) provided with horizontally arranged electrolyte circulating pump outlet pipe hole (5) and electrolyte circulating pump population pipe hole (6).    USE - Hydrogen and oxygen generator for electrolysis electrode sheet.    DESCRIPTION OF DRAWING(S) - The drawing shows a main view of hydrogen and oxygen generator.    Sealing groove (1)    Protrusions (2)    Air outlet hole (3)    First separating fixed mounting hole (4)    Electrolyte circulating pump outlet pipe hole (5)    Electrolyte circulating pump population pipe hole (6)    Rectangular plate (7)    Second pole piece separating fixed mounting hole (9)
NOVELTY - Fertilizer comprises 40-60 wt.% of silicate and 40-60 wt.% of an organic active fertilizer raw material.    USE - Used as a fertilizer.    ADVANTAGE - The fertilizer has a long term administration and improved utilization rates, and is environment friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the fertilizer comprising mixing the silicate and organic active fertilizer raw material in a stacker with height of 0.8-1.2 m at 65 degrees C for 4-5 times and 5-7 days to obtain a mixed product, fermenting the mixed product, and crushing and screening.
NOVELTY - Organic, inorganic or microbial fertilizer comprises 205-215 pts. wt. nitrogenous fertilizer, 175-190 pts. wt. phosphate fertilizer, 155-165 pts. wt. potash fertilizer, 425-435 pts. wt. alcohol waste residue, 0.8-1.2 pts. wt. hexyl alcohol esters of diethylamine group, 2.8-3.3 pts. wt. colloidal suspension of Bacillus, 2.8-3.3 pts. wt. B.megaterium, and 2.8-3.3 pts. wt. B.subtilis.    USE - The organic, inorganic or microbial fertilizer is useful for fruit crop (claimed).    ADVANTAGE - The fertilizer improves people demand to more fruits, increases growth rate, does not leave any residue on the fruit, and does not cause any harm to the people.
NOVELTY - Organic, inorganic or microbial fertilizer comprises 205-215 pts. wt. nitrogenous fertilizer, 200-210 pts. wt. phosphate fertilizer, 175-185 pts. wt. potash fertilizer, 390-401 pts. wt. alcohol waste residue, 0.8-1.2 pts. wt. hexyl alcohol esters of diethylamine group, 2.8-3.3 pts. wt. colloidal suspension of Bacillus, 2.8-3.3 pts. wt. B.megaterium, and 2.8-3.3 pts. wt. B.subtilis.    USE - The organic, inorganic or microbial fertilizer is useful for fruit crop (claimed).    ADVANTAGE - The fertilizer meets nutritional requirements of different plants, and is rapidly utilized by the plants.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the organic, inorganic or microbial fertilizer, which involves mixing nitrogenous fertilizer, phosphate fertilizer, potash fertilizer, alcohol waste residue and hexyl alcohol esters of diethylamine group, fermenting the mixture, granulating the fermented mixture, and adding colloidal suspension of Bacillus, B.megaterium, and B.subtilis with the above-mentioned granules.
NOVELTY - For producing biological diesel oil raw material to a pre-heating system, to solve the problems that producing biodiesel with the raw material oil heating cost is high, wherein the technical solution is pre-heating system comprises a heat source, a heating device and a collecting device, a heating device comprises a heating chamber, is provided with a pre-heating chamber, a radiating pipe, a pre-heating chamber by the inner part of the net is provided with separate holding chamber and the radiating pipe is a barrel containing chamber, a radiating pipe is provided with containing chamber of the radiating pipe, a pre-heating chamber by means of heat pipe and the heat source, the oil outlet of the pre-heating chamber is connected with the collecting device. The technical effect is generated by the boiler waste gas to heat the solid raw material oil, the heat energy of the exhaust gas is fully used, but also saves the energy consumption and reduces the production cost of the biodiesel;
NOVELTY - The utility model claims a fertilizer production device, specifically to a urea formaldehyde sustained release compound fertilizer with urea buffer tank, comprising a shell and a lower side of the bracket is supported on the shell, wherein the shell comprises an inner cavity is connected with the upper part of the buffer shell and the lower part of a shell body, the upper end of the buffer shell is inserted in the feeding pipe, wherein the buffer shell is provided with a partition board, the partition board is hinged to the side wall of the buffer shell, because of adopting the said structure, the utility model is the one kind of urea formaldehyde sustained release compound fertilizer production and in the process of the high voltage raw material into a feeding tube with urea buffer tank, a plurality of buffer, which increases the length of the buffer material, the buffering effect is ideal, and it will not lead to excessive damage to the instrument is more convenient to use by impact pressure, saves the manpower and material resources.
NOVELTY - The utility model claims a fertilizer production device, specifically to a method for producing a nitric-sulphuric compound fertilizer high tower, comprising a shell body, a motor and a stirring shaft in the shell, the stirring shaft is connected with the output shaft of the motor is connected with a temperature measuring end is inserted into the shell, wherein the upper end of the shell, wherein one side of the feeding port is further provided with a feeding port, a shell, wherein a feeding port of the right lower part is provided with placing plate, the plate one end of which is fixedly connected to the stirring shaft, because of adopting said structure, this utility model is the one kind of producing sulphur-based high tower compound fertilizer melting tank by the rotation of the stirring shaft so as to make the feeding plate for placing the plate raw material, stirring, does not need manual calculation time and adding raw material, saving the time of the worker, and avoids the secondary discharging, improves the production quality of the fertilizer.
NOVELTY - Bag culture compound nutritional matrix for tomatoes, comprises 30% furfural residue, 20-40% cow dung, and 30-50% crushed maize straws. Preparation method involves adding 1-1.5 kg water retaining agent, 1.5-2 kg urea and 2-2.5 kg potassium sulfate to the fermented compound per cubic meter.    USE - As bag culture compound nutritional matrix for tomatoes (claimed).    ADVANTAGE - The bag culture compound nutritional matrix is wide in raw material source, cost-effective, environmentally-friendly and suitable for standardized and large-scale production, saves resources, and solves problems of successive cropping obstacle of facility soil and poor utilization of soils.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the nutritional matrix, which involves (a) mixing furfural residue and cow dung, and crushing mixture to 2-4 cm long corn stalks, (b) mixing crushed mixture uniformly, until moisture content of the mixture reaches 55-65%, and fermenting the mixture, (c) pulverizing the mixture to granules, (d) adding 1-1.5 kg water retaining agent, 1.5-2 kg urea and 2-2.5 kg potassium sulfate to the fermented compound per cubic meter to pulverized mixture, and mixing the mixture, and (e) obtaining product.
NOVELTY - Mushroom and tobacco seedling nursery substrate, comprises 60-80 pts. wt. mushroom waste material, 20-40 pts. wt. mountain sand and tobacco floating seedling nursery nutrient solution, 0.5-1.5x 106 water and tobacco floating seedling nursery nutrient solution, 150-200 pts. wt. urea, 60-100 pts. wt. phosphorus pentoxide, 150-250 pts. wt. potassium hydroxide, 60-80 pts. wt. superphosphate, 15-35 pts. wt. magnesium, 0.07-0.3 pts. wt. borax, and 0.3-0.7 pts. wt. zinc sulfate.    USE - As mushroom and tobacco seedling nursery substrate.    ADVANTAGE - The substrate is composted and fermented mature bacterial residue, the bonded silica sand is natural weathered bonded silica sand, and the two raw materials have the advantages of extensive sources, convenience in taking the materials, low cost, and simple assembly. The seedling nursery cost is reduced, and exploitation of grass carbon resource is avoided for conductive to environmental protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the seedling nursery substrate, which involves adding mushroom waste material to lime, adjusting pH of mixture, adding organic material to the mixture and decomposing the mixture, adding remainder raw materials to the mixture, mixing the mixture, and packing to obtain product.
NOVELTY - A water-in-oil-type biodiesel-based drilling fluid comprises 70-90 volume parts biodiesel oil, and 10-30 volume parts calcium chloride aqueous solution. The drilling fluid further comprises 2-6 vol.% calcium oxide, 1-6 vol.% organic soil, 2-8 vol.% emulsifier, 2-8 vol.% wetting agent, 2-6 vol.% filtrate reducer and 0-200 vol.% weighting material, with respect to the total volume of the biodiesel and the calcium chloride aqueous solution.    USE - Water-in-oil-type biodiesel-based drilling fluid (claimed).    ADVANTAGE - The water-in-oil-type biodiesel-based drilling fluid has excellent operating performance, anti-collapse suppressing property, lubricating performance, and biological degradability, and is economical.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of water-in-oil-type biodiesel-based drilling fluid, which involves stirring bio-diesel oil at high speed, adding emulsifier and wetting agent, fully-dispersing under the stirring condition, adding the obtained product into calcium chloride solution, organic soil, fluid reducer, and calcium oxide, weighing material, stirring for 40 minutes to 1 hour, and allowing to stand for 24 hour or more.
NOVELTY - A fuel additive comprises polyoxyethylene dioleate, hydrocarbon, ferrocene or ferrocene derivative and water.    USE - Fuel additive is used for gas fuel, liquid fuel e.g. methanol fuel and aqueous fuel, and solid fuel (all claimed).    ADVANTAGE - The energy-saving fuel additive has favorable chemical stability, increases combustion efficiency of fuel, effectively reduces discharge capacity of harmful substances including carbon monoxide and nitrogen oxide, and reduces environment pollution.
NOVELTY - A biological organic fertilizer comprises 30-100 pts. wt. of sweet potato, 2-50 pts. wt. of rice bran, 1-15 pts. wt. of honey, 20-30 pts. wt. of humic acid, 2-8 pts. wt. of water, 20-30 pts. wt. of chicken manure, 5-20 pts. wt. of shell powder, 5-20 pts. wt. of oil slag, and 10-30 pts. wt. of soil.    USE - As biological organic fertilizer (claimed).    ADVANTAGE - The biological organic fertilizer solves the problem of the environment pollution. The preparation method is simple and easy to operate; and is suitable for large-scale industrial production.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the biological organic fertilizer involving mixing sweet potato, chicken manure and rice bran, crushing to 100-120 meshes, putting into a fermenting tank, adding biological bacteria, molasses, humic acid, shell powder, water and oil soil slag; uniformly mixing, putting into a fermenting tank, at 3-40 degrees C, sealing to ferment for 7-10 days to obtain the fertilizer.
NOVELTY - A pesticidal composition comprises flufenzine as first component and abamectin, etoxazole or fenpropathrin as second component, where ratio is 1:80-80:1.    USE - Pesticidal composition i.e. wettable powder, water dispersible granule, suspension, emulsion in water, micro-emulsion or microcapsule used for preventing and treating pest particularly Cnaphalocrocis medinalis, Chilo suppressalis, Tryporyza incertulas, diamondback moth, cabbage caterpillar, rice planthopper, aphid, red spider, yellow spider, yellow tea mite, Tetranychus cinnabarinus, Tetranychus urticae, Psylla chinensis or leafhopper in rice, wheat, cotton, fruit tree and vegetable and tea tree (claimed).    ADVANTAGE - The composition has synergistic effect, reduces dosage of pesticides, is environment-friendly, enhances adhesion and is resistant to flushing of rainwater.
NOVELTY - Preparation of Camellia sinensis slag ecological organic fertilizer comprises providing 500-700 pts. wt. C. sinensis slag, 150-250 pts. wt. animal excrement, and 150-250 pts. wt. C. sinensis meal, and adding the raw materials with 0.4-2.4 wt.% (based on the total weight of the raw materials) strain. The C. sinensis slag is the waste residue after C. sinensis leaves or flower extraction. The strain is actinomycetes, fungi, bacteria, and/or yeast.    USE - Preparation of C. sinensis slag ecological organic fertilizer (claimed) used for improving soil and soil permeability, preventing and treating soil pests, and adjusting and promoting the growth e.g. of golden camellia tree.    ADVANTAGE - The method solves the problems of environmental pollution and waste of resources.
NOVELTY - Pesticidal suspended seed coating agent comprises active components are clothianidin and an active component B chosen from tebuconazole and thiram, where the weight ratio of the clothianidin and an active component B is 100:1-1:100.    USE - The pesticidal suspended seed coating agent is useful for treating diseases caused by insect pest in seed of wheat, corn, soybean, peanut, cotton, Sorghum and other crop, where the insect pests including aphids, midge, whiteflies, wireworms, grubs, cutworms, and thrips and the diseases are rice blast, corn head smut, wheat smut, and Sorghum head smut (all claimed).    ADVANTAGE - The agent exhibits favorable film formation property, uniform coating, high suspension percentage, high safety, low toxicity, and slow-release action, reduces the pesticide consumption, is safe for human and livestock, as it does not have chemical injury, and has favorable environmental compatibility.
NOVELTY - Cultivation of raw mushroom soil furrow bed, involves mixing cultivation material with biogas slurry, adding 0.1 wt.% potassium permanganate, sterilizing with clean water, and planting material having moisture content of 63-65 wt.%.    USE - For cultivation of raw mushroom soil furrow bed (claimed).    ADVANTAGE - The method has success planting rate of 100%, has short production period, provides improved mushroom product quality, increased yield, saves high temperature sterilizing rate, saves energy source, do not damage ecological environment, and increase the emission of carbon dioxide.
NOVELTY - The system has a yeast conveyor unit that is provided with several groups of fermentation conveying units (6). Fermentation conveyors (7) are sequentially and three-dimensionally installed from low to high order to form a fermentation conveying unit. Several material fermentation conveyors are connected in a straight line. The material provided from an input end of the fermentation conveyor positioned on high level is fermented. The fermented material is provided through the output end of the fermentation conveyor positioned on lower level.    USE - Automatic environmental protection fermentation system of organic material.    ADVANTAGE - By adopting the three-dimensional level-by-level design, the utilization rate and fermentation efficiency of material fermentation plant can be increased. As the recovery treatment is performed on foul fermentation exhaust gas, the cleaning environmental protection process can be achieved effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the automatic environmental protection fermentation system of organic material.    Dosing device (1)    Material stirring device (2)    Material crushing device (3)    Fermentation conveying unit (6)    Fermentation conveyor (7)
NOVELTY - Slow release fertilizer comprises 1000 pts. wt. dry straw, 2000 pts. wt. biogas, 400-500 pts. wt. urea, 60-90 pts. wt. potassium dihydrogen phosphate, 80-110 pts. wt. boric acid, 40-50 pts. wt. chromium chloride, 40-50 pts. wt. manganese chloride, 100-120 pts. wt. zinc sulfate, 2-5 pts. wt. salicylic acid, 2-5 pts. wt. ethylene, 20-30 pts. wt. polyaspartic acid, 15-20 pts. wt. Trichoderma spp., 9-15 pts. wt. Micromonospora, and 20-30 pts. wt. Polyangium cellulosum.    USE - The slow release fertilizer is useful for providing drought resistance to wheat straw (claimed).    DETAILED DESCRIPTION - Slow release fertilizer comprises 1000 pts. wt. dry straw, 2000 pts. wt. biogas, 400-500 pts. wt. urea, 60-90 pts. wt. potassium dihydrogen phosphate, 80-110 pts. wt. boric acid, 40-50 pts. wt. chromium chloride, 40-50 pts. wt. manganese chloride, 100-120 pts. wt. zinc sulfate, 2-5 pts. wt. salicylic acid, 2-5 pts. wt. ethylene, 20-30 pts. wt. polyaspartic acid, 15-20 pts. wt. Trichoderma spp., 9-15 pts. wt. Micromonospora, and 20-30 pts. wt. Polyangium cellulosum, and is prepared by selecting the normal gas for 2 months and biogas, irradiating Micromonospora, and Polyangium cellulosum carbon isotope C 060 for 10 minutes, performing anaerobic fermentation, adding chopped straw, biogas and potassium dihydrogen phosphate into the fermentation tank, adding the above-mentioned microorganism, stirring uniformly, fermenting for 30 days at 35-45 degrees C, opening fermentation tank and adding urea and Trichoderma urea, stirring uniformly, closing the fermentation tank to ferment, keeping the temperature in the fermentation tank to 45-50 degrees C for 3-5 days, raising the temperature to 60-75 degrees C and fermenting for 6-30 days, and maintaining the temperature of the fermentation tank to 50-55 degrees C, reducing to normal temperature, adding the remaining raw material into the tank, mixing, bagging and packaging product.
NOVELTY - A baby mosquito bellyband comprises 2.5-3 kg lotus leaf, 0.8-1 kg jasmine flower, 2-2.2 kg mosquito, 1.8-2 kg fragrant camphor leaf and 3-3.5 kg folium Artemisiae argyi.    USE - Baby mosquito bellyband.    ADVANTAGE - The bellyband has simple preparation and no poison and side effect, and is convenient to use and environment-friendly.
NOVELTY - An organic compound fertilizer comprises furfural residue, bean platinum powder, peanut cake, straw, chicken slaughterhouse waste, pepper, ginkgo skin, common Cnidium fruit, cortex meliae, Quisqualis, Chinese gall, ilex pubescens, radix Sophorae flavescentis, alkali, venenum bufonis, camphor, semen momordicae, golden larch bark, strontium carbonate, diammonium phosphate, potassium chloride, zinc sulfate, boric acid, manganous sulfate, medical stone powder, jennite powder, bentonite, thiourea, diatomite, powdered rock phosphate, sodium humate and raw materials.    USE - Organic compound fertilizer.    ADVANTAGE - The fertilizer has better weeding effect, and is free from pollution.    DETAILED DESCRIPTION - An organic compound fertilizer comprises 10-15 pts. wt. furfural residue, 20-30 pts. wt. bean platinum powder, 15-20 pts. wt. peanut cake 15-20 pts. wt. straw, 10-20 pts. wt. chicken slaughterhouse waste, 20-30 pts. wt. pepper, 20-30 pts. wt. ginkgo skin, 20-30 pts. wt. common Cnidium fruit, 10-30 pts. wt. cortex meliae, 15-25 pts. wt. Quisqualis, 1-15 pts. wt. Chinese gall, 5-15 pts. wt. ilex pubescens, 5-10 pts. wt. radix Sophorae flavescentis, 55-60 pts. wt. of alkali, 10-15 pts. wt. venenum bufonis, 5-15 pts. wt. camphor, 5-15 pts. wt. semen momordicae, 10-15 pts. wt. golden larch bark, 45-55 pts. wt. strontium carbonate, 35-45 pts. wt. diammonium phosphate, 20-30 pts. wt. potassium chloride, 5-10 pts. wt. zinc sulfate, 1-2 pts. wt. boric acid, 1-2 pts. wt. manganous sulfate, 5-10 pts. wt. medical stone powder, 25-30 pts. wt. jennite powder, 5-10 pts. wt. bentonite, plus minus 20-25 pts. wt. thiourea, 5-15 pts. wt. diatomite, plus minus 10-20 pts. wt. powdered rock phosphate, 10-20 pts. wt. sodium humate and 5-15 raw materials.
NOVELTY - A micro-organism fertilizer comprises 1-3 pts. wt. Bacillus megaterium, 3-5 pts. wt. Streptomyces jingyangensis, 6-10 pts. wt. multi-microbial inoculum, 1000-1100 pts. wt. organic fertilizer, 350-500 pts. wt. inorganic fertilizer, 30-40 pts. wt. fertilizer, 22-28 pts. wt. adhesive, 0.2-0.6 pts. wt. auxiliary agent, 45-55 pts. wt. Japanese Artemisia rupestris, 40-50 pts. wt. semen momordicae, 1-15 pts. wt. Stellera chamaejasme, 5-10 pts. wt. radix Sophorae flavescentis, 5-10 pts. wt. golden larch bark, 10-15 pts. wt. pepper.    USE - Micro-organism fertilizer for preventing and treating Orchid anthracnose.    ADVANTAGE - The fertilizer increases quantity of probiotics in soil, blooming duration time and blossom quantity and reduces morbidity of anthracnose, and is pollution-free, and has disinsection and sterilization effect and and low residue.    DETAILED DESCRIPTION - A micro-organism fertilizer comprises 1-3 pts. wt. Bacillus megaterium, 3-5 pts. wt. Streptomyces jingyangensis, 6-10 pts. wt. multi-microbial inoculum, 1000-1100 pts. wt. organic fertilizer, 350-500 pts. wt. inorganic fertilizer, 30-40 pts. wt. fertilizer, 22-28 pts. wt. adhesive, 0.2-0.6 pts. wt. auxiliary agent, 45-55 pts. wt. Japanese Artemisia rupestris, 40-50 pts. wt. semen momordicae, 1-15 pts. wt. Stellera chamaejasme, 5-10 pts. wt. radix Sophorae flavescentis, 5-10 pts. wt. golden larch bark, 10-15 pts. wt. pepper, 20-30 pts. wt. Ginkgo skin, 20-30 pts. wt. common Cnidium fruit, 20-30 pts. wt. cortex meliae, 10-30 pts. wt. Quisqualis, 15-25 pts. wt. nutgall, 1-15 pts. wt. pubescent holly root, 5-15 pts. wt. fructus ulmi, 55-60 pts. wt. outside skin, 10-15 pts. wt. weed and 5-15 camphor. An INDEPENDENT CLAIM is also included for a method for preparing a micro-organism fertilizer for preventing and treating Orchid anthracnose.
NOVELTY - An algae synergistic high-tower compound fertilizer comprises 0.05-1.2 pts. wt. algae synergistic agent, 40-77 pts. wt. urea and 17-59 pts. wt. auxiliary fertilizer, where the auxiliary fertilizer comprises mono-ammonium phosphate or diammonium phosphate, potassium sulfate or potassium chloride, calcium carbonate powder or dolomite powder according to a weight ratio of 10-30:10-30:1-10.    USE - Algae synergistic high-tower compound fertilizer.    ADVANTAGE - The fertilizer has wide raw material source, deliquescence property, convenient transportation and application and high utilization rate, and promotes growth and yield of crops, inhibits soil urease, reduces nutrient loss and avoids secondary pollution, and can be prepared in a simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an algae synergistic high-tower compound fertilizer, which involves preparing the algae synergistic agent by adding natural algae with corn flour, adding inorganic acid or inorganic alkali and sugar with the obtained mixture followed by fermenting, filtering, evaporating and concentrating the obtained liquid to obtain the algae synergistic agent, preparing an urea melting liquid by adding the urea with the algae synergistic agent, preprocessing the auxiliary fertilizer by crushing and heating the fertilizer, adding the auxiliary fertilizer with the urea melting liquid, performing natural cooling granulation process, and collecting and sieving the obtained material to obtain a finished product.
NOVELTY - 1-Adamantyl methanol is oxidized to obtain adamantyl carboxaldehyde. Adamantyl carboxaldehyde as raw material is processed to obtain adamantyl (amino)acetic acid as intermediate. Adamantyl (amino)acetic acid is reacted with concentrated sulfuric acid and nitric acid, pH of resulting mixture is adjusted to 14 or more under alkaline condition. Butyl dicarbonate is added to resulting mixture, pH is adjusted to 3-4, reacted and the product is separated, to obtain (t-butoxy)carbonyl-amino-2-(3-hydroxyadamantan-1-yl)acetic acid (amantadine).    USE - Production of (t-butoxy) carbonyl-amino-2-(3-hydroxyadamantan-1-yl)acetic acid used for producing saxagliptin (claimed).    ADVANTAGE - The method environmentally-friendly provides amantadine compound with high yield and high purity, under mild reaction condition, by a simple process.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of saxagliptin, which involves reacting amantadine and pyrrolidine amide compound.
NOVELTY - Preparation of canthaxanthin involves dissolving ( beta )-carotene into an organic solvent, dropwise adding sodium periodate aqueous solution as an oxidizing agent, adding sodium iodide as a catalyst, then stirring, and reacting. The organic solvent is halogenated hydrocarbon containing 1-6 carbon atoms, and/or fatty acid ester containing 3-10 carbon atoms.    USE - Preparation of canthaxanthin (claimed).    ADVANTAGE - The method enables economical and environmentally-friendly preparation of canthaxanthin under mild reaction conditions by a simple process.
NOVELTY - Preparation of cediranib involves carrying out one-step condensation reaction of 6-methoxy-7-(3-pyrrolidin-1-yl-propoxy)-3,4-dihydroquinazolin-4-one and 4-fluoro-5-hydroxy-2-methylindole in presence of an organic alkali and a condensating agent to obtain cediranib.    USE - Preparation of cediranib used as raw material for medicine.    ADVANTAGE - The cediranib is economically prepared by simple and environmentally-friendly method under mild reaction condition.
NOVELTY - A resveratrol galactoside preparation method involves selecting resveratrol as a raw material, a cheap lactose substrate as a galactosyl donor, glycosidase modified by a molecule with a microorganism source as a tool enzyme and adapting single-step transglycosylation reaction.    USE - Method for preparing resveratrol galactoside.    ADVANTAGE - The method enables preparing resveratrol galactoside in a simple and eco-friendly manner.
NOVELTY - This utility model claims a rural household ecological processing system, belonging to the field of environment protection living garbage treating device and its device, comprising a storage bin, the storage bin are connected by the pull rope switch with one end of the uniform distributing pipe, and the uniform distributing pipe is a telescopic pipe, the lower part capable of extending into the compost, the compost can placed on the placing tank; the fertilizer barrel compost is full a composting barrel lifting mechanism for composting barrel claims compost tank, the barrel is put compost barrel is put upper end cover plate is provided with a sealing device, the fertilizer barrel lifting mechanism is set on the beam. This utility model is environment-friendly, practical, saving land resource and high efficiency at the same time using waste resource, suitable for wide area south and north are suitable, especially suitable for a lack of the rural area, social benefit is obvious.
NOVELTY - A commercialized organic material decomposition agent is prepared by: (a) selecting and breeding a strain and identifying the safety of the strain; (b) preparing a seed solution, including preparing a seed solution, a culture medium and a secondary seed solution; (c) carrying out stack-retting fermentation, including setting a stack-retting fermentation culture medium formula and fermentation conditions of the formula; and (d) drying, powdering, metering and packaging a stack-retting product, thus preparing the organic material decomposition agent.    USE - Preparation of commercialized organic material decomposition agent (claimed).    ADVANTAGE - The production cost is low, the process is simple and mature, the use is convenient, and the decomposition application effect is remarkable.
NOVELTY - A potato composite microbial slow-release fertilizer comprises 10-40 wt.% composite microbial inoculum and 60-90 wt.% inorganic fertilizer. The composite microbial inoculum comprises 40-60 wt.% Bacillus megaterium, 20-30 wt.% Bacillus cereus, and 20-30 wt.% nitrogen-fixing Paenibacillus. Each of the microbial inoculum comprises bacterial strain and adsorbent. The bacterial strain has bacterial inoculum count of 106 to 108/g.    USE - Potato composite microbial slow-release fertilizer used for preventing soil-borne disease.    ADVANTAGE - The slow-release fertilizer provides nutrients in potato at different stages, utilizes raw materials having wide source, and has low cost and simple preparation technique.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the potato composite microbial slow-release fertilizer, comprising mixing composite microbial inoculum and inorganic fertilizer, and uniformly stirring.
NOVELTY - A 1-(2-(2-hydroxyethoxy)ethyl)piperazine is prepared by (1) reacting piperazine and piperazine dihydrochloride in solvent to prepare piperazine monohydrochloride, (2) reacting piperazine monohydrochloride and 2-(2-chloroethoxy)ethanol in solvent, (3) filtering to recover piperazine dihydrochloride, drying, (4) evaporating to remove solvent, to obtain high-purity 1-(2-(2-hydroxyethoxy)ethyl)piperazine crude product, (5) performing vacuum reduced pressure rectification, and collecting fraction.    USE - Preparation of 1-(2-(2-hydroxyethoxy)ethyl)piperazine (claimed).    ADVANTAGE - Preparation process is low-cost, environment-friendly, lowers disubstituted compound impurity content, and improves product purity.    DESCRIPTION OF DRAWING(S) - The drawing shows an infrared spectrum of 1-(2-(2-hydroxyethoxy)ethyl)piperazine.
NOVELTY - Fertilizer comprises 60 wt.% attapulgite mineral powder, 10 wt.% livestock manure, 10 wt.% weathered coal, 15 wt.% trace element and 5 wt.% fermentation strain.    USE - As fertilizer.    ADVANTAGE - The fertilizer is cost-effective and slow-release as attapulgite mineral powder forms a micro matrix with nutrients, thus is form an unique controlled release and adsorbs heavy metals in soil, improves air permeability of soil, reduces soil hardening, chemical fertilizer and pesticide and pollution, thus is environmentally-friendly, eliminates viral disease, optimizes ecological environment and micro ecological balance of the soil, thus the crop is matured in advance with improved quality and free of toxin and other harmful substances.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) mixing 20-40 wt.% attapulgite mineral powder with auxiliary material and adding fermentation strain (A), and mixing uniformly and piling the mixture and performing anaerobic fermentation at 45-60 degrees C for 25-35 days, where the inlet and outlet temperature are maintained at 50 degrees C, (b) mixing fermentation strain (B), weathered coal, trace element, remaining attapulgite mineral powder and fermented material obtained in step (a), and adding water and piling the mixture and performing second time fermentation at 25-35 degrees C for 25-35 days to obtain fermented material, and (c) drying the fermented material, until the moisture content reaches 15% or less, sieving and grinding the dried mixture into 5 mm to obtain the product.
NOVELTY - Method for reducing risk of cadmium contamination in rapeseed, involves applying clay mineral chosen from sepiolite and montmorillonite clay minerals and organic fertilizers, uniformly stirring mixture, applying the mixture on soil, manually or mechanically tilling the soil, maintaining moisture content of the soil for 10-30 days to grow vegetables, stabilizing mixture, planting cadmium-rejecting plant variety canola by sowing seeds, applying nitrogen, potassium and phosphorus compound fertilizer, irrigating the soil, and harvesting the canola after 30-50 days.    USE - The method is useful for reducing risk of cadmium contamination in rapeseed (claimed).    ADVANTAGE - The method prepares soil having excellent passivation capability, accumulates minimal amount of cadmium, simultaneously improves soil adsorption, ion exchange and complex reaction and soil self-cleaning capability and soil fertility conditions, reduces bio-availability of cadmium and accumulation of cadmium, improves cadmium-rejecting breed, and is cost-effective.    DETAILED DESCRIPTION - Method for reducing risk of cadmium contamination in rapeseed, involves applying 1-4 kg/m2 clay mineral chosen from sepiolite and montmorillonite clay minerals having mesh size of 100-200 and 1-4 kg/m2 organic fertilizers, preferably chicken manure in vegetable garden soil contaminated with cadmium, uniformly stirring the mixture, applying the mixture on 0-20 cm soil, manually or mechanically tilling the soil, maintaining moisture content of the soil to 65-75% for 10-30 days to grow vegetables, stabilizing the mixture for 10-30 days, and planting cadmium-rejecting plant variety canola by sowing 1-2 g/m2 seeds, applying 20-30 kg/acre nitrogen, potassium and phosphorus compound fertilizer, irrigating the soil using water without causing any heavy metal pollution, maintaining moisture content of the soil to 70%, and harvesting the canola after 30-50 days.
NOVELTY - A diethyl phosphonic acid copper bactericide is new.    USE - Diethyl phosphonic acid copper bactericide.    ADVANTAGE - The bactericide is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of phosphonic acid diethyl copper fungicide comprising mixing chloroform and ethanol, where ratio is 1:4, adding 20 ml phosphorus trichloride, stirring at 6-8 degrees C at 1 hour, absorbing with hydrogen chloride gas and 5% sodium hydroxide solution, pouring into beaker with 10% sodium carbonate solution, washing 3 times with deionized water, separating, and distilling under reduced pressure to give diethyl phosphite; adding to iodine and 10% equimolar ammonia and carrying out amination at 40 in water bath for 48 hours; and adding with copper sulfate, vigorously stirring, refluxing to 50-55 degrees C for 8-8.5 hours, cooling to room temperature, filtering, washing with deionized water and drying.
NOVELTY - A kind of cultivating straw ferment feed microbial inoculum, belonging to the technical field of agriculture. In order to improve feed quality fermenting steam exploded wood fibre straw, wherein the straw ferment feed microbial inoculum of enzyme activity, the device is set with an ultraviolet sterilizing lamp, an electric heating pipe is set in the tank body, a circulating water pump, starting the device, removing the culture liquid chlorine in the microbial inoculum production is shortened to one day and microbial growth, enzyme activity compared with traditional method is greatly increased by traditional several days
NOVELTY - A fluoroalkyl sulfonic acid derivative surfactant (I) and its salt (II) are new.    USE - Fluoroalkyl sulfonic acid derivative surfactant and its salts used for textile, leather, papermaking, chemical industry, oil field or fire protection (claimed).    ADVANTAGE - The surfactant is easily degraded and environment-friendly. The preparation is simple and low-cost.    DETAILED DESCRIPTION - A fluoroalkyl sulfonic acid derivative surfactant of formula (I) and its salt of formula (II) are new.    Rf'=CF3CF2CF2O(CF(CF3)CF2)n-OCF(CF3)-; and    n=1-3.    An INDEPENDENT CLAIM is included for preparation of fluoroalkyl sulfonic acid derivative surfactant and its salt.
NOVELTY - A lenalidomide intermediate is prepared by performing reduction reaction in which reducing agent is ammonium formate or formic acid.    USE - Preparation of lenalidomide intermediate (claimed).    ADVANTAGE - Preparation process is simple, low-cost, and quickly performed at normal temperature and pressure and avoids usage of hydrogen.    DETAILED DESCRIPTION - A lenalidomide intermediate of formula (I) is prepared by performing reduction reaction scheme (A) in which reducing agent is ammonium formate or formic acid.
NOVELTY - A dihydropyridine is prepared by (A) using compounds (VII) and (VIII) as raw materials in solvent to obtain intermediate, and (B) removing protecting group in solvent.    USE - Preparation of dihydropyridine for antihypertensive drug clevidipine butyrate.    ADVANTAGE - Preparation process is simple, convenient to operate, environment-friendly, and low-cost, and has easy to obtain materials, high yield, and stable product quality.    DETAILED DESCRIPTION - A dihydropyridine of formula (IV) is prepared by (A) using compounds of formulae (VII) and (VIII) as raw materials, performing cyclization reaction in solvent to obtain intermediate of formula (IX), and (B) removing protecting group in solvent.    R1, R2=Me, t-Bu, and compounds of formulae (1)-(7) in which if R1 is Me, then R2 is t-Bu or compounds of formulae (1)-(7), and if R2 is Me, then R1 is t-Bu or compounds of formulae (1)-(7).    .
NOVELTY - A letrozole is prepared by adding 1,2,4-triazole sodium salt and polar aprotic solvent at room temperature, adding 4-(bromomethyl) benzonitrile, extracting after reaction is finished with 3N hydrochloric acid, combining aqueous phase, adding to base solution for crystallization, filtering 4-(1H-(1,2,4-triazole-yl)methyl)benzonitrile; (2) adding potassium tert.-butoxide and polar aprotic solvent in 4-necked flask, reducing temperature to - 30-- 32 degrees C, controlling temperature at less than or equal to - 20 for 60 minutes, extracting with 3N hydrochloric acid, filtering inorganic salts, and dropwise adding filtrate.    USE - Preparation of letrozole for pharmaceuticals (claimed).    ADVANTAGE - Preparation process is low-cost and environment-friendly, has improved product yield, does not contain reduced pressure distillation process thus shortening reaction time, avoids the use of low-polarity highly-flammable reagents such as n-heptane, reduces operation risk, improves production safety, and adopts common reagents.    DETAILED DESCRIPTION - A letrozole is prepared by adding 1,2,4-triazole sodium salt and polar aprotic solvent at room temperature, adding 4-(bromomethyl) benzonitrile, extracting after reaction is finished with 3N hydrochloric acid, combining aqueous phase, adding to base solution for crystallization, filtering 4-(1H-(1,2,4-triazole-yl)methyl)benzonitrile; (2) adding potassium tert.-butoxide and polar aprotic solvent in 4-necked flask, reducing temperature to - 30-- 32 degrees C, controlling temperature at less than or equal to - 20 for 60 minutes, extracting with 3N hydrochloric acid, filtering inorganic salts, dropwise adding filtrate to ice-water, controlling temperature at 0-10 degrees C for 1 hour to recrystallize, vacuum filtrating, washing with water to obtain crude letrozole, and recrystallizing.
NOVELTY - Triterpene compound i.e. (1R,4S,7S,10R,11S,15R,16S,18R,21S)-7-hydroxy-21-(hydroxymethyl)-4,10,11,15,18,21-hexamethyl-9,25-dioxahexacyclo(14.7.2.0(1,15).0(4,14).0(5,11).0(18,23))pentacosane-8,24-dione (I) is new.    USE - (I) is useful for preventing and treating hepatitis B (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) preparing (I) and    (2) use of (I) in preparing medicine for preventing and treating hepatitis B.
NOVELTY - Method for preparing protein feed, involves (a) mixing straw with liquid culture medium to obtain solid state culture medium, and (b) inoculating Neurospora crassa into the culture medium for performing solid fermentation.    USE - The method is useful for preparing protein feed (claimed) which is used as feed for agriculture and animal husbandry.    ADVANTAGE - The method is simple, uses single strain, can be controlled easily, saves resources, as agricultural waste is used as raw material, protects environment, and provides great economic benefit. The protein feed can be used with other feed, easily digested and absorbed, has improved feed conversion rate, partially replaces soybean meal or fishmeal in existing feeds, has crude protein content of 55-65 %mass, and is rich in lysine, threonine and vitamin B12, and is safe, as it causes no toxic side effects.
NOVELTY - A composite microbial organic fertilizer contains 5-30 pts. wt. humic acid, 10-30 pts. wt. crop straw carbon or 20-30 pts. wt. rice bran powder, and 10-30 pts. wt. animal wastes, and is prepared by crushing crop straw carbon or rice bran powder and humic acid to 80-100 meshes, heating animal wastes to dry and sterilize, mixing to form carrier material, adding 3-5 pts. wt. biological agent to 800-900 pts. wt. carrier material, stirring uniformly, adjusting humidity to 20-30%, fermenting in closed pit at 10-50 degrees C for 48-60 hours, granulating, and removing less than or equal to 18% water content at 40 degrees C.    USE - Composite microbial organic fertilizer for inhibiting soil-borne disease and promoting growth on continuous cropping field of strawberry.    ADVANTAGE - The microbial fertilizer reduces use of pesticide, chemical fertilizer and hormones, avoids pollution, improves soil and product quality, has low cost, achieves yield increasing rate of 10-30%, and has advanced blossoming and fruit yielding in which yield increasing rate achieves 10-30%.
NOVELTY - Method for producing fertilizer involves (a) adding fertilizer raw materials to melting device to obtain molten slurry, (b) granulating molten slurry using high tower granulator, (c) cooling and sieving the granules, and (d) subjecting the granules to anti-caking treatment, where microbial fertilizer is added in step (b) and/or step (d).    USE - The method is useful for producing fertilizer (claimed).    ADVANTAGE - The produced fertilizer has characteristics of chemical fertilizer, uniform nutrients, large particle strength, stable product quality, and good anti-blocking performance, can replenish nutrient elements required for growth of crops and is convenient to use.
NOVELTY - Microbial agent comprises 2-6x 1010 colony forming unit (cfu)/g Mucor, 2-6x 1010 cfu/g Trichoderma virens, 2-6x 1010 cfu/g Geotrichum candidum, 2-8x 109 cfu/g Saccharomyces cerevisiae, 3-5x 1011 cfu/g Geobacillus stearothermophilus, 2-6x 1011 cfu/g thermophilic Lactobacillus, 2-8x 1010 cfu/g white-rot fungi, 2-8x 1010 cfu/g brown rot fungi, 3-7x 108 cfu/g Pseudomonas putida, 2-6x 1011 cfu/g nitrifying bacteria, Chlorella 1-4x 106 cfu/g, and 2-5x 107 Cyanobacteria.    USE - The microbial agent is useful for composting straw and manure (claimed), and in production biofertilizer.    ADVANTAGE - The agent shortens composting period, improves composting degree, accelerates biodegradation of organic matters, alleviates ozone generation and diffusion during composting process, reduces loss of nutrient substances such as nitrogen, and can be applied to composting of different straw and manure raw materials.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for composting straw and manure, which involves (a) adding composition which comprises 50-70 wt.% manure, 27.9-48.9 wt.% straw, 1-2 wt.% glucose, and 0.1-0.2 wt.% microbial agents, to compost, maintaining moisture of reaction at 50-60%, carbon/nitrogen (C/N) ratio at 25-30:1 and pH at neutral or slightly alkaline, and fermenting compost at more than 60 degrees C for 20-30 days, where mixing materials for every 2-3 days.
NOVELTY - A soil fertility improver is prepared by utilizing bacterial residues comprising 20-50 pts. wt. Oyster mushroom bacterial residue, 20-50 pts. wt. Flammulina velutipes bacterial residue, 10-40 pts. wt. Agaricus bisporus bacterial residue and 0-30 pts. wt. edible fungus bacterial residue, the bacterial residues comprise 10-50 pts. wt. cotton seed hull, 5-50 pts. wt. corn cob, 0-50 pts. wt. wood flour, 10-50 pts. wt. wheat straw, 10-30 pts. wt. wheat bran, 5-15 pts. wt. dried chicken manure, 5-10 pts. wt. soybean meal and 2-5 pts. wt. calcium hydroxide.    USE - Soil fertility improver.    ADVANTAGE - The soil fertility improver is easiness in obtaining raw materials and significant soil fertility improvement effect, and can realize re-utilization of the waste bacterial residues and realize the sustainable development of circular agriculture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing soil fertility improver.
NOVELTY - Manufacture of 4-(2-hydroxyethyl)-1,3-dihydro-2H-indol-2-one involves protecting hydroxyl group of 2-methyl-3-nitrophenyl alcohol, forming 2-methyl-3-(2-alkoxyethyl)nitrobenzene (V), reacting compound (V) with diethyl oxalate, forming 2-nitro-6-(2-alkoxyethyl)phenacetyl formic acid (VI), reacting compound (VI) with hydrogen peroxide to form 2-nitro-6-(2-alkoxyethyl)phenylacetic acid (VII), reducing compound (VII) and carrying out ring closing reaction on compound (VII), forming 4-(2-alkoxyethyl)-1,3-dihydro-2H-indol-2-one (VIII), and hydrogenating compound (VIII).    USE - Manufacture of 4-(2-hydroxyethyl)-1,3-dihydro-2H-indole-2-ketone used as intermediate for ropinirole.    ADVANTAGE - The 4-(2-hydroxyethyl)-1,3-dihydro-2H-indole-2-ketone is manufactured efficiently and economically with high yield and high purity, by simple method.    DETAILED DESCRIPTION - Manufacture of 4-(2-hydroxyethyl)-1,3-dihydro-2H-indol-2-one involves reacting 2-methyl-3-nitrophenyl-acetic acid with a chloroformate mixed anhydride, reducing, forming 2-methyl-3-nitrophenyl alcohol, protecting hydroxyl group of 2-methyl-3-nitrophenyl alcohol, forming 2-methyl-3-(2-alkoxyethyl)nitrobenzene of formula (V), reacting 2-methyl-3-(2-alkoxyethyl)nitrobenzene with diethyl oxalate, forming 2-nitro-6-(2-alkoxyethyl)phenacetyl formic acid of formula (VI), reacting compound (VI) with hydrogen peroxide to form 2-nitro-6-(2-alkoxyethyl)phenylacetic acid of formula (VII), reducing compound (VII) and carrying out ring closing reaction on compound (VII), forming 4-(2-alkoxyethyl)-1,3-dihydro-2H-indol-2-one of formula (VIII), and hydrogenating compound (VIII).    R1=phenyl optionally substituted by halo, hydrocarbyl, nitro, 1-6C alkyl, 1-6C alkoxy or 1-6C alkylamino;and    R2=ethyl or H.
NOVELTY - Odor and heavy metals removal powdery form composition having pH of 7.5-9.5, comprises 60-80 wt.% red mud having particle size of 6-10 mu m and containing 25-45% ferric oxide, 15-25% aluminum oxide, 10-20% silica, 4-10% titania, and small amount of calcium oxide and sodium oxide; 20 wt.% magnesium oxide having a particle size of 3-5 mu m; 0-7 wt.% calcium oxide having a particle size of 70-80 mu m; 0-7 wt.% titania having a particle size of 0.25-0.35 mu m; 0-3 wt.% zeolite having a particle size of 250-350 mu m; and 0-3 wt.% bentonite having a particle size of 170-190 mu m.    USE - The odor and heavy metals removal composition is useful for producing compost (claimed).    ADVANTAGE - The composition effectively and economically removes the odor and heavy metal of the livestock manure, and reduces the sawdust and rice hull of the manure. The composition provides high quality compost without odor, heavy metals and soil contamination.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing compost using the odor and heavy metals removal composition, comprising introducing 10 kg/1 m2 of livestock manure in a belt press inlet part of a flocculation tank for the solid-liquid separation of livestock manure and then dehydrating by activating physical agitation reaction, mixing 70-75 wt.% dehydration cake derived from the dehydration step with 30-25 wt.% mixture of sawdust, rice hulls, rhytidome, fallen leaves, rice straw and/or weed, fermenting the mixture for 15 days by supplying blower by 12 hours per day and progressing flip process twice daily, and ripening the fermented mixture by ventilating only with air for one week.
NOVELTY - Method for preparing compost with soil improvement effect, involves (a) obtaining cow dung, pig ordure and fowl droppings with respect to rice straw, and adding components including rice hulls and sawdust to obtain mixture, (b) mixing the natural microorganisms supported on the mudstone with minerals including cobalt, germanium and selenium, (c) adding the mixtures obtained in the steps (a) and (b), and performing primary fermentation, and (d) mixing the product with mineral e.g. cobalt and microorganisms supported mudstone, and ripening the mixture.    USE - The method is useful for preparing compost with soil improvement effect (claimed).    ADVANTAGE - The method does not generate bad smell, overcomes the problem of insufficient trace element, and improves soil conditioning effect.    DETAILED DESCRIPTION - Method for preparing compost with soil improvement effect, involves (a) obtaining cow dung, pig ordure and fowl droppings with respect to 100 pts. wt. rice straw, and adding 150-200 pts. wt. components chosen from rice hulls and sawdust to obtain mixture, (b) mixing the natural microorganisms supported on the mudstone with 3-5 pts. wt. minerals including cobalt, germanium and selenium, (c) adding the mixture obtained in the step (a) with the mixture obtained in the step (b), controlling the water content at 60-65%, and performing primary fermentation at 50-70 degrees C for 2-3 days, and (d) mixing the obtained fermented product with 1-2 pts. wt. mineral including cobalt, germanium and selenium and microorganisms supported mudstone, and ripening the mixture at room temperature for 2-3 weeks to obtain product.
NOVELTY - Preparing 1-(4-hydrazinophenyl) methyl-1,2,4-triazole, comprises reacting 1H-1,2,4-triazole with formaldehyde and 4-hydrazinophenyl boronic acid.    USE - The process is useful for preparing 1-(4-hydrazinophenyl) methyl-1,2,4-triazole, which is useful for preparing rizatriptan benzoate (all claimed), which is useful to treat migraine. No biological data given.    ADVANTAGE - The process provides 1-(4-hydrazinophenyl) methyl-1,2,4-triazole at low temperature without using costly metal catalyst, reducing agents, such as tin(II) chloride, in an economical and environmentally friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing rizatriptan benzoate, comprising reacting 1H-1,2,4-triazole with formaldehyde and 4-hydrazinophenyl boronic acid to give 1-(4-hydrazinophenyl) methyl-1,2,4-triazole.
NOVELTY - Generation of hydrogen by electrolysis using standard gas generator comprises reacting oxidant and high-temperature copper oxide in converter, reacting with equimolar water, entering carrier gas in electrolytic cell through humidifier and humidifying.    USE - Method for generating hydrogen by electrolysis using standard gas generator (claimed).    DESCRIPTION OF DRAWING(S) - The drawing shows a process flowchart of hydrogen generation.    Voltage stabilizer (2)    Mass flow meter (3)    Humidity generator (4)    Electrolytic tank (6)    Dehydration device (7)
NOVELTY - This utility model claims a rural beautiful environment-friendly energy, which is composed of a biogas slurry filtering and purifying tank, a tank, an anaerobic fermenting tank, a filter for marsh liquid, wherein the feeding pool is connected with the anaerobic fermenting tank by pipeline, the anaerobic fermenting tank of the biogas generated by the biogas slurry into filtering and purifying tank by the biogas slurry filter process, the biogas slurry in filtering and purifying tank is provided with a drainage water pump, the water pumping pump is connected with the squatting pan through pipeline, the squatting pan is connected with the feeding tank through a pipeline, the advantages of using a toilet excrement fermenting, the energy recycling, using the biogas flushing toilet after purifying, it can save water, the washing, washing, washing, sewage and so on to be reused, which avoids the pollution to the environment, is helpful to realize toilet rectify and reform, which avoids the disorder.
NOVELTY - Preparation of hydrogen-rich gas involves providing sludge as raw material into a sealed reactor in presence of air, carrying out hydrothermal reaction at 200-500 degrees C for 5-15 minutes under 10-30 MPa to obtain gas and solid component, and providing the resultant product into gas-liquid separator to obtain hydrogen-rich gas, in which the solid component is subjected to desalter and carbonation process is carried out to obtain carbon sludge.    USE - Preparation of hydrogen-rich gas (claimed).    ADVANTAGE - The method economically provides hydrogen-rich gas with reduced energy consumption by simple process.
NOVELTY - Preparing beta-artemether involves dissolving beta-artemether raw material in methanol, ethanol, ethylene glycol or isopropanol, adding acetone aqueous solution to dissolve, cooling and crystallizing, filtering, washing by acetone aqueous solution, drying to constant weight to obtain the product.    USE - For preparing beta-artemeth from artmether mother liquor (claimed), for production of organic synthetic dye mother liquor.    ADVANTAGE - The method has high transforming efficiency. The alpha-artemether is converted into beta-artemether is a more than 55% in conversion rate of refined product of beta-artemether purity up to more than 99%, improves the production efficiency and reduces the waste, the technology is simple, the operation is convenient, it does not need the complex apparatus and technique.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for artemisia using dimethyl ether production of organic synthetic dye mother liquor beta-artemether involving preparing: artemether mother liquid is concentrated to dry to obtain crystal, b) reacting the toluene and methylene dichloride mixed solvent (volume ratio is 1:3 to 5), adding methanol to make the crystal completely dissolve, at between room temperature and 60 degrees C, adding p-methyl benzene sulfonic acid, reacting for 3-5 hours, c) processing the reaction solution 0.5 to 1 hour, filtering, adding water to wash, then using anhydrous magnesium sulfate, concentrating until it is dry, d) crystallizing: the condensate in step c), adding methanol to dissolve, cooling and crystallizing, filtering, drying to constant weight, obtaining the wormwood methyl ether crude product, e) in the step d) to obtain crude product, adding acetone aqueous solution to dissolve, cooling and crystallizing, filtering, using acetone aqueous solution, drying to constant weight to obtain the product.
NOVELTY - Ammonium phosphate is prepared from intermediate-low grade phosphate ore, and intermediate-low grade phosphate ore reacts with excess sulfuric acid in an extraction tank to produce wet-process phosphoric acid. Phosphate ore slurry is added to phosphoric acid storage tank for second time to recycle excess sulfuric acid in the phosphoric acid, and the phosphoric acid reacts with ammonia gas to produce ammonium phosphate products. Reacted sludge is recycled to the extraction tank.    USE - Novel acid saving method for preparing ammonium phosphate (claimed).    ADVANTAGE - The method efficiently and economically provides ammonium phosphate from intermediate-low grade phosphate ore, with reduced consumption of sulfuric acid.
NOVELTY - An organic zinc-rich fertilizer for strawberries comprises zinc rapeseed cake (40-65 pts.wt.), organic nitrogen fertilizer (20-25 pts.wt.), organic phosphate fertilizer (10-15 pts.wt.), organic potash fertilizer (10-20 pts.wt.) and micronutrient fertilizer (1-2 pts.wt.), as raw materials.    USE - As organic zinc-rich fertilizer for strawberries (claimed).    ADVANTAGE - The organic zinc-rich strawberry mixed special fertilizer can be prepared by using waste of organic fertilizer, which not only reduces the cost, but also is economic and environmentally friendly, at the same time through the cake rich in zinc element, the cake is rich in lysine, constant and microelement can be enriched zinc element, to obtain the organic zinc-rich strawberry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic zinc-rich fertilizer for strawberries involving 1) mixing the raw materials, according to the weight ratio, in to granulator; 2) adding water, heating at 7-75 degrees C and preparing slurry, where the water content of the slurry is 10%, and 3) granulating to obtain the fertilizer.
NOVELTY - Preparation of chitosan oligosaccharide iodide seaweed biological fertilizer comprises taking chitosan seaweed as raw material; adding sodium alginate; performing composite enzymolysis; and chelating to obtain biological fertilizer.    USE - Preparation of chitosan oligosaccharide iodide seaweed biological fertilizer.    ADVANTAGE - The method produces chitosan oligosaccharide iodide seaweed biological fertilizer that is environment friendly, highly efficient, promotes yield, retains healthcare function, has strong and lasting bactericidal effect, and no residue and without pollution.
NOVELTY - Tobacco stem selenium-rich organic fertilizer is prepared by providing tobacco stem, crushing, adding water to obtain moisture content of 60%, adding urea and fulvic acid dissolved in water, adjusting the pH, uniformly mixing, adding selenium ore powder, inoculating activated fermentation bacteria liquid, covering the stack with plastic film, fermenting, turning once every 2 days, stacking and fermenting for 28 days, and drying to water content of 17-18 wt.%. The selenium ore powder has particle size of less than 0.15 mm and selenium content of not less than 180 mg/kg.    USE - Tobacco stem selenium-rich organic fertilizer.    DETAILED DESCRIPTION - Tobacco stem selenium-rich organic fertilizer is prepared by providing tobacco stem, crushing to a particle size of less than 2 mm, adding water to obtain moisture content of 60%, adding urea and fulvic acid dissolved in water, adjusting the pH at 8.5 by potassium hydroxide, uniformly mixing, adding selenium ore powder, inoculating activated fermentation bacteria liquid, covering the stack with plastic film, fermenting, turning once every 2 days, where turning is conducted for 5 times, stacking and fermenting for 28 days, and drying to water content of 17-18 wt.%. The selenium ore powder has particle size of less than 0.15 mm and selenium content of not less than 180 mg/kg.
NOVELTY - An algae fertilizer comprises 40-50 pts. wt. nitrogen fertilizer, 10-20 pts. wt. phosphate fertilizer, 10-20 pts. wt. potash fertilizer, 5-10 pts. wt. algae synergistic agent, 10-15 pts. wt. distillers grain, and 5-10 pts. wt. adhesive.    USE - Algae fertilizer.    ADVANTAGE - The fertilizer is rich in nutrients, nitrogen-containing organic matter, potassium, calcium, magnesium, iron, zinc, iodine, minerals and vitamins that can be easily absorbed by plants and soil. Further, the fertilizer forms a chelating system for nutrient slow release and to prolong fertilizer effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the algae fertilizer, comprising crushing nitrogen fertilizer, phosphate fertilizer and potash fertilizer into powder, passing through 100-mesh sieve, uniformly mixing, adding algae synergistic agent into the mixture, then adding distillers grain and polyacrylamide adhesive, uniformly stirring, and granulating.
NOVELTY - A straw mushroom stock seed culture material comprises 70-75 wt.% sheep manure, 12-18 wt.% corn cob, 4-6 wt.% rice, 4 wt.% dry soil, 2.5 wt.% lime powder and 1 wt.% gypsum powder.    USE - Straw mushroom stock seed culture material.    ADVANTAGE - The material has vigorous growth of hypha, strong activity and high working efficiency. The method kills Escherichia coli in manure, parasitic ovum and weed seed, environment-friendly and widens cultivating raw material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of straw mushroom stock seed culture material comprising drying raw materials for 1-2 days and using UV light to kill bacteria; mixing sheep manure with water, piling to 1-1.2 m high and 2-3 m width, where amount of each stack is 250-500 kg; stack fermenting, making 10-15 cm diameter vertical holes, where stomata density is 1/m3 and covering with grass to ferment; turning when temperature reaches to 60 degrees C, maintaining at 24 hours, mixing with corn cobs, husks, dried mud, lime powder, gypsum powder, mixing in dry state and turning for 2 times for 3-4 days; stopping fermentation when there's no ammonia odor and moisture content is 45% and mixing with corn cob to moisture content of 62%; bottling in polypropylene culture flasks and covering with breathable foam caps; and autoclaving culture medium, sterilizing at 100 degrees C for 1 hour, warming to 121 degrees C for 2 hours and naturally cooling to below 25 degrees C.
NOVELTY - Separation and purification of nucleoside from trichosanthes leaf involves crushing trichosanthes leaves, adding water to crushed product, heat reflux-extracting, evaporating extract to relative density of 1.2 or less, adding 70-95% ethanol to product, allowing to standstill for 72 hours, filtering under reduced pressure and obtaining crude extract, dissolving extract in water, purifying using HPD826 macroporous resin column chromatography, eluting with water, concentrating under reduced pressure and then further purifying.    USE - Separation and purification of nucleoside e.g. adenosine and purine, from trichosanthes leaf (claimed).    ADVANTAGE - The method efficiently and economically separates and purifies nucleoside from trichosanthes leaf, having high purity without causing pollution to environment.    DETAILED DESCRIPTION - Separation and purification of nucleoside from trichosanthes leaf involves crushing trichosanthes leaves, adding water to crushed product, heat reflux-extracting, evaporating extract to relative density of 1.2 or less, adding 70-95% ethanol to product, allowing to standstill for 72 hours, filtering under reduced pressure and obtaining crude extract, dissolving extract in water, purifying using HPD826 macroporous resin column chromatography, eluting with water, concentrating under reduced pressure, and further purifying in YMC ODS-AQ column using methanol-water as mobile phase with detection wavelength of 254 nm.
NOVELTY - A crop drought-resisting and protecting growth promoter is obtained by mix-reacting papermaking pulp waste liquid or dry medium material diluted with water, a reinforcing agent, and a tackifier, and drying. The weight ratio of papermaking pulp waste liquid and reinforcing agent is 1:0.2-0.6. The weight ratio of papermaking pulp waste liquid and tackifier is 1:0.002-0.006. The pulp waste liquid is obtained by magnesium sulfite pulping process, contains 90-95 wt.% lignosulfonate, and has a pH of 4-6.    USE - Crop drought-resisting and protecting growth promoter (claimed).    ADVANTAGE - The crop drought-resisting and protecting growth promoter is nontoxic and harmless, does not cause secondary pollution, and can be maintained naturally for 180 days.    DETAILED DESCRIPTION - A crop drought-resisting and protecting growth promoter is obtained by mix-reacting papermaking pulp waste liquid or dry medium material diluted with water, a reinforcing agent, and a tackifier, and drying. The weight ratio of papermaking pulp waste liquid and reinforcing agent is 1:0.2-0.6. The weight ratio of papermaking pulp waste liquid and tackifier is 1:0.002-0.006. The pulp waste liquid is obtained by magnesium sulfite pulping process, contains 90-95 wt.% lignosulfonate, and has a pH of 4-6. The reinforcing agent is urea-formaldehyde resin. The tackifier is polyvinyl alcohol or acrylamide. An INDEPENDENT CLAIM is included for preparation of crop drought-resisting and protecting growth promoter.
NOVELTY - A high energy, low-carbon synthetic fuel comprises 40-75 wt.% methanol or ethanol, 5-30 wt.% acetone, 5-25 wt.% water, 0.5-3 wt.% catalyst, 5-10 wt.% combustion improver and 5-20 wt.% emulsifier.    USE - High energy, low-carbon synthetic fuel for furnace.    ADVANTAGE - The high energy, low-carbon synthetic fuel contributes to energy saving, reduces emission, is economical, and highly reliable.
NOVELTY - Processing of brown coal involves grinding brown coal having moisture content of 2-3% and density of 1-2 T/m3, to granularity of 16-20 meshes, adding biomass, curing agent having granularity of 10 meshes and smoke suppressant having granularity of 25 meshes, mixing uniformly, obtaining compression-molded coal, introducing the obtained coal into plating tank containing waterproof liquid and coating on a surface of the coal.    USE - Processing of brown coal (claimed).
NOVELTY - Preparation of biomass alcohol hydrocarbon fuel oil involves acidifying 5-25% animal oil and vegetable oil by taking dilute sulfuric acid as an acidifying agent, reacting at 50-800 degrees C for 1-3 hours, adjusting pH of solution to 3-7, removing the lower aqueous layer and repeatedly washing with water for 1-2 times and obtaining fatty acid oil glyceride, adding 100 pts. wt. methanol to a stirrer in constant reactor hopper, adding 20-50 pts. wt. acid oil and 0-10 pts. wt. water and stirring and obtaining methanol-acid oil-water homogeneous mixture.    USE - Preparation of biomass alcohol hydrocarbon fuel oil used for boiler.    ADVANTAGE - The method efficiently and economically provides biomass alcohol hydrocarbon fuel oil having high heat value, and reduced sulfur content and dust.    DETAILED DESCRIPTION - Preparation of biomass alcohol hydrocarbon fuel oil involves acidifying 5-25% animal oil and vegetable oil by taking dilute sulfuric acid as an acidifying agent, reacting at 50-800 degrees C for 1-3 hours, adjusting pH of solution to 3-7, removing the lower aqueous layer and repeatedly washing with water for 1-2 times and obtaining fatty acid oil glyceride, adding 100 pts. wt. methanol to a stirrer in constant reactor hopper, adding 20-50 pts. wt. acid oil and 0-10 pts. wt. water and stirring and obtaining methanol-acid oil-water homogeneous mixture, adding obtained mixture into heating apparatus with thermometer and a funnel, reacting at 25-50 degrees C, adding 2-20 pts. wt. emulsifier, stirring, and then gradually adding 20-80 pts. wt. coal tar and reacting.
NOVELTY - A cleaning agent comprises 5-25 pts. wt. alkyl glucoside, 3-15 pts. wt. polyoxyethylene (20) sorbitan monolaurate, 3-10 pts. wt. cocamidopropyl betaine, 0.5-4 pts. wt. plant growth regulator, 0.5-3 pts. wt. sodium hydroxymethylglycinate and 70-100 pts. wt. distilled water.    USE - Cleaning agent used for potted plants (claimed).    ADVANTAGE - The cleaning agent is chemically stable, bactericidal, safe and environment-friendly.
NOVELTY - Treating oil containing waste water from restaurant, comprises (1) passing the waste water in neutralizing tank and then a floatation tank for processing to remove oil, and (2) allowing the waste water to pass into hydrolysis acidification tank and high efficient anaerobic reactor for anaerobic treatment of waste water.    USE - The method is useful for treating oil containing waste water from restaurant (claimed) to produce methane.    ADVANTAGE - The method treats the oil containing waste water from restaurant with reduced energy consumption, operation cost and labor intensity and simple operation process.
NOVELTY - Acid biological bacteria mixture comprises 2.0 pts. wt. biological bacteria fertilizer, 100-200 pts. wt. auxiliary material, 1.0 pts. wt. lysine, 0.001-0.002 pts. wt. BA-6 cytokinin, 0.006 pts. wt. chitin, 9-10 pts. wt. nitrifying bacteria, and 2.0 pts. wt. humic acid.    USE - Acid biological bacteria mixture.    ADVANTAGE - The acid biological bacteria mixture solves raw soil problems and secondary salinization problems. It produces high lysine content vegetables. It restores soil environment for production of fruits and vegetables with rich nutrition. It achieves environmental protection, balanced nutrition, and meets needs of economic development cycle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of acid biological bacteria mixture by mixing lysine, BA-6 cytokinin, and chitin according to proportion; stirring and uniformly mixing; adding biological bacteria fertilizer and auxiliary material; uniformly stirring to form mother strain; adding nitrifying bacteria and humic acid; putting them in mixer; uniformly stirring; spraying liquid mixture into solid raw material; and continuously and uniformly stirring.
NOVELTY - Slow release fertilizer comprises 1000 pts. wt. dry straw, 2000 pts. wt. biogas, 200-300 pts. wt. urea, 50-70 pts. wt. potassium dihydrogen phosphate, 40-60 pts. wt. boric acid, 40-50 pts. wt. chromium chloride, 50-80 pts. wt. manganese chloride, 100-120 pts. wt. zinc sulfate, 12-20 pts. wt. polyaspartic acid, 12-20 pts. wt. Aspergillus flavus, 9-15 pts. wt. Micromonospora, and 20-30 pts. wt. Polyangium cellulosum.    USE - The slow release fertilizer is useful for providing drought resistance to cotton straw (claimed).    DETAILED DESCRIPTION - Slow release fertilizer comprises 1000 pts. wt. dry straw, 2500 pts. wt. biogas, 200-300 pts. wt. urea, 50-70 pts. wt. potassium dihydrogen phosphate, 80-110 pts. wt. boric acid, 60-80 pts. wt. chromium chloride, 50-80 pts. wt. manganese chloride, 100-120 pts. wt. zinc sulfate, 16-25 pts. wt. polyaspartic acid, 15-20 pts. wt. Trichoderma spp., 9-15 pts. wt. Micromonospora, and 20-30 pts. wt. Polyangium cellulosum, and is prepared by selecting the normal gas for 2 months and biogas, performing anaerobic fermentation, adding chopped straw, biogas and potassium dihydrogen phosphate into the fermentation tank, adding the above-mentioned microorganism, stirring uniformly, fermenting for 30 days at 35-45 degrees C, opening fermentation tank and adding urea and Trichoderma urea, stirring uniformly, closing the fermentation tank to ferment, keeping the temperature in the fermentation tank to 45-50 degrees C for 3-5 days, raising the temperature to 60-75 degrees C and fermenting for 6-30 days, and maintaining the temperature of the fermentation tank to 50-55 degrees C, reducing to normal temperature, adding the remaining raw material into the tank, mixing, bagging and packaging product.
NOVELTY - Slow release fertilizer comprises 1000 pts. wt. dry straw, 2500 pts. wt. biogas, 200-300 pts. wt. urea, 50-70 pts. wt. potassium dihydrogen phosphate, 80-110 pts. wt. boric acid, 60-80 pts. wt. chromium chloride, 50-80 pts. wt. manganese chloride, 100-120 pts. wt. zinc sulfate, 16-25 pts. wt. polyaspartic acid, 15-20 pts. wt. Trichoderma spp., 9-15 pts. wt. Micromonospora, and 20-30 pts. wt. Polyangium cellulosum.    USE - The slow release fertilizer is useful for providing drought resistance to tobacco stalk (claimed).    DETAILED DESCRIPTION - Slow release fertilizer comprises 1000 pts. wt. dry straw, 2500 pts. wt. biogas, 200-300 pts. wt. urea, 50-70 pts. wt. potassium dihydrogen phosphate, 80-110 pts. wt. boric acid, 60-80 pts. wt. chromium chloride, 50-80 pts. wt. manganese chloride, 100-120 pts. wt. zinc sulfate, 16-25 pts. wt. polyaspartic acid, 15-20 pts. wt. Trichoderma spp., 9-15 pts. wt. Micromonospora, and 20-30 pts. wt. Polyangium cellulosum, and is prepared by selecting the normal gas for 2 months and biogas, performing anaerobic fermentation, adding chopped straw, biogas and potassium dihydrogen phosphate into the fermentation tank, adding the above-mentioned microorganism, stirring uniformly, fermenting for 30 days at 35-45 degrees C, opening fermentation tank and adding urea and Trichoderma urea, stirring uniformly, closing the fermentation tank to ferment, keeping the temperature in the fermentation tank to 45-50 degrees C for 3-5 days, raising the temperature to 60-75 degrees C and fermenting for 6-30 days, and maintaining the temperature of the fermentation tank to 50-55 degrees C, reducing to normal temperature, adding the remaining raw material into the tank, mixing, bagging and packaging product.
NOVELTY - Extracting salidroside from Rhodiola rosea comprises: (i) cleaning Rhodiola rosea herb, decocting with water for 3-4 hours, allowing it to stand for 2 hours and filtering to obtain a filtrate; (ii) concentrating the filtrate to 1/5-1/4th to its original volume; (iii) washing the concentrated filtrate using 80-90% ethanol and purified water to obtain a primary extract; (iv) passing the primary extract via macro-porous resin column, eluting with 50-60% ethanol and mixing the crude eluent extracts; (v) allowing the crude extract to stand for some time, filtering and drying.    USE - The method is useful for extracting salidroside from Rhodiola rosea (claimed).    ADVANTAGE - The method: is simple, economical, highly efficient and convenient to operate; has controlled conditions; and extracts high-purified product.
NOVELTY - The method involves storing oratosquilla samples in casing at a temperature of about 4 degrees c. The random sample of oratosquilla is removed. The sample is weighed and accommodated in vaporizing furnace containing 0.5 grams of magnesium oxide powder. Sample receiving pipe is immersed in boric acid. The sample titration process is performed using hydrochloric acid. The sample is wrapped in plastic wrapper and sealed. Sample detection signal to noise ratio is analyzed to obtain prediction model. Freshness of sample is analyzed using prediction model and accurate detection data is obtained.    USE - Method for analyzing freshness of oratosquilla under refrigerated conditions.    ADVANTAGE - The freshness of the oratosquilla sample can be detected easily and quickly. Strong, accurate and reliable detection result can be obtained. The damage of sample during the freshness detection process can be prevented effectively.    DETAILED DESCRIPTION - The oratosquilla freshness detection process is performed using a sulfide sensor, hydrogen sensor, gas sensor, alcohol sensor, methane sensor, hydroxypropul butyl alkyl sensor, and nitrogen oxide sensor.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the process of analyzing freshness of oratosquilla under refrigerated conditions. (Drawing includes non-English language text)
NOVELTY - Weeding composition comprises thifensulfuron, tribenuron and oxyfluorfen in a weight ratio of 30:2:7.    USE - Used as a weeding composition containing thifensulfuron, tribenuron and oxyfluorfen.    ADVANTAGE - The composition has wide weeding spectrum, long lasting time, quick weeding effect on wheat and corn fields, and low dosage; and controls and improves the environment from pollution.
NOVELTY - A phenylenediamine compound (I) is new.    USE - New phenylenediamine compound is used as antioxidant for manufacturing biodiesel (all claimed).    ADVANTAGE - The biodiesel containing the phenylenediamine compound has excellent oxidative stability.    DETAILED DESCRIPTION - A phenylenediamine compound of formula (I) is new.    R1,R2=H, halo, 1-20C alkyl, 6-20C aryl, 1-20C alkoxy, 6-20C aryl, 1-20C alkyl, hydroxyl 1-20C alkyl, or 3-20C cycloalkyl.
NOVELTY - Biological organic fertilizer comprises 80-90 pts. wt. decaying vegetable leaf, 13-17 pts. wt. silkworm excrement, 10-14 pts. wt. phosphate fertilizer, 4-5 pts. wt. sawdust, 8-10 pts. wt. phoenix tree leaf, 1-3 pts. wt. Pipewort, 2-5 pts. wt. tobacco leaf, 4-6 pts. wt. turnip, 2-3 pts. wt. attapulgite, 1-2 pts. wt. biogas fluid, 1-2 pts. wt. borax, 9-15 pts. wt. flour, 63-70 pts. wt. swill, 11-17 pts.wt. brown sugar and 75-80 pts. wt. animal feces.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer improves soil quality and soil structure, so that ecological balance and nutrition of the soil are enhanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biological organic fertilizer, which involves adding 6-8 times of water with flour, heating the flour at 80-90 degrees C, adding the decaying vegetable leaf, the silkworm excrement, the phosphate fertilizer into the flour, stirring and dispersing the flour for 20-30 minutes to obtain a first mixture, drying and granulating the dispersed flour to obtain a product, preparing sugar fermentation liquid by dissolving the brown sugar in 1.8-2 times clean water, adding 10-15% fermenting agent 1-2% wintergreen and 0.1-0.3% alum into the dissolved brown sugar, fermenting the mixture at 30-40 degrees C for 15-20 days, adding 1-2% borax into the fermented mixture and agitating the mixture to obtain fermentation liquid, adding the saw dust, the phoenix tree leaves, the Pipewort and the water into the fermentation liquid for 3-5 hours to obtain a second mixture, stacking and mixing the first and the second mixture with the rest raw material, adding humic acid and Chinese herbal medicine to the mixing material followed by drying the mixing material to obtain a finished product, where the Chinese herbal medicine comprises 14-20 pts. wt. Herba houttuyniae, pts. wt. unbracteolated spurge root and 6-7 pts. wt. stemona.
NOVELTY - A microorganism fertilizer comprises Bacillus subtilis, Trichoderma reesei, fertilizer hametz, organic fertilizer, inorganic fertilizer, trace element, plant growth regulator, adhesive, Artemisia rupestris, semen Momordicae, Stellera chamaejasme, Radix sophorae flavescentis, golden larch bark, pepper, Ginkgo skin, common Cnidium fruit, cortex meliae, Quisqualis, nutgall, pubescent holly root, fructus ulmi and camphor.    USE - Microorganism fertilizer for preventing cabbage downy mildew.    ADVANTAGE - The fertilizer has high yield of cabbages and improved plant growth and quality of the cabbages and soil.    DETAILED DESCRIPTION - A microorganism fertilizer comprises 3-5 pts. wt. Bacillus subtilis,1-4 pts. wt. Trichoderma reesei, 4-8 pts. wt. fertilizer hametz, 1000-1100 pts. wt. organic fertilizer, 350-500 pts. wt. inorganic fertilizer, 65-85 pts. wt. trace element, 5-7 pts. wt. plant growth regulator, 25-35 pts. wt. adhesive, 45-55 pts. wt. Artemisia rupestris, 40-50 pts. wt. semen Momordicae, 1-15 pts. wt. Stellera chamaejasme, 5-10 pts. wt. Radix sophorae flavescentis, 5-10 pts. wt. golden larch bark, 10-15 pts. wt. pepper, 20-30 pts. wt. Ginkgo skin, 20-30 pts. wt. common Cnidium fruit, 20-30 pts. wt. cortex meliae, 15-25 pts. wt. Quisqualis, 1-15 pts. wt. nutgall, 5-15 pts. wt. pubescent holly root, 55-60 pts. wt. fructus ulmi and 5-15 pts. wt. camphor. An INDEPENDENT CLAIM is also included for a method for preparing microorganism fertilizer.
NOVELTY - A potato soft rot controlling microorganism fertilizer comprises Bacillus polymyxa, a fertilizer leavening agent, an organic fertilizer, a plant growth regulator, adhesive, an inorganic fertilizer, soapberry peel, hairy holly, Stellera chamaejasme, hops, pepper, Ginkgo skin, common Cnidium fruit, Cortex meliae, Quisqualis, Chinese gall and Radix sophorae flavescentis.    USE - Microorganism fertilizer for controlling potato soft rot.    ADVANTAGE - The fertilizer reduces bacterial and fungal diseases on leaves of a plant, improves quality and yield of the potato, increases probiotic bacteria in soil and improves soil condition.    DETAILED DESCRIPTION - A potato soft rot controlling microorganism fertilizer comprises 0.4-0.6 pts. wt. Bacillus polymyxa, 0.2-0.4 pts. wt. fertilizer leavening agent, 90-110 pts. wt. organic fertilizer, 0.5-0.8 pts. wt. plant growth regulator, 1-3 pts. wt. adhesive, 30-60 pts. wt. inorganic fertilizer, 55-60 pts. wt. soapberry peel, 5-15 pts. wt. hairy holly, 1-15 pts. wt. Stellera chamaejasme, 5-10 pts. wt. hops, 25-30 pts. wt. pepper, 25-30 pts. wt. Ginkgo skin, 26-30 pts. wt. common Cnidium fruit, 17-30 pts. wt. Cortex meliae, 16-25 pts. wt. Quisqualis, 1-15 pts. wt. Chinese gall and 5-10 pts. wt. Radix sophorae flavescentis. An INDEPENDENT CLAIM is also included for a method for preparing a potato soft rot controlling microorganism fertilizer, which involves mixing pig manure, chicken manure, dairy manure and pigeon dung to obtain organic fertilizer, adding fertilizer leavening agent with pure water, heating the obtained mixture to obtain activated solution, adding the organic fertilizer with the activated liquid, and heating and decomposing the obtained mixture to obtain a finished product.
NOVELTY - A pure biomass carbon barbecue comprises 0-80 pts. wt. bamboo chip carbon powder, 0-70 pts. wt. wood chip carbon powder, 20-80 pts. wt. cotton stalk carbon powder, 20-25 pts. wt. adhesive and 1-2 pts. wt. boron mud, where granularity of the cotton stalk carbon powder is less than 1 mm and the adhesive is prepared by uniformly mixing carboxymethyl cellulose, alpha starch and water at weight ratio of 0.5:1:5.    USE - Pure biomass carbon barbecue.    ADVANTAGE - The barbecue is prepared at low cost in a simple manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing pure biomass carbon barbecue, which involves crushing the bamboo chip carbon powder, wood chip carbon powder and the cotton stalk carbon powder, mixing and stirring the crushed powder, adding boron mud to the crushed powder, adding the adhesive to the mixture, stirring and mixing the mixture to obtain mixed material, pressing the mixed material in a grinding tool, demolding the pressed material to obtain a carbon block and drying and solidifying the obtained carbon block to obtain a finished product.
NOVELTY - A sugar-containing organic fertilizer comprises 10 pts. wt. sugar residue, 32 pts. wt. humic acid, 10 pts. wt. amino acids, 15 pts. wt. plant ash, 10 pts. wt. lignin, 15 pts. wt. traditional Chinese medicine dregs, and 8 pts. wt. bentonite.    USE - Sugar-containing organic fertilizer.    ADVANTAGE - The fertilizer is environment-friendly, rich in nutrients and able to promote sugar conversion. The method is simple and convenient.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of sugar-containing organic fertilizer comprising weighing raw materials, mixing, stirring, and crushing; fermenting at 71 degrees C for 9 days, turning every 2-3 days, mixing, and controlling pH value at 6-7.8; and granulating, drying, and screening.
NOVELTY - Branch processing of paper sludge comprises paper sludge sedimentation, aerating sewage and dehydrating primary settling sludge to obtain first branch processing product used as paper raw material; separating solid biological sludge, oxidizing using Fenton oxidation method, decoloring sewage and subjecting separated biological sludge to dehydration treatment to obtain second branch processing product used as organic fertilizer; adding polyacrylamide, and chemically dehydrating sludge to obtain third branch processing product for a power boiler raw material and cement accessory material.    USE - A branch processing method of paper sludge (claimed).    ADVANTAGE - The method eliminates the land-filling of dewatered sludge and potential hazards, and changes waste into treasure.    DETAILED DESCRIPTION - Branch processing of paper sludge comprises:    (A) paper sludge sedimentation for 5-6 hours to separate sewage and primary settling sludge;    (B) aerating sewage in aeration tank, and subjecting the primary settling sludge to dehydration treatment to make the mass fraction 50%, i.e. obtaining first branch processing product used as paper raw material;    (C) after 8-12 hours sewage aeration, performing sewage sedimentation for 2-4 hours, and separating out solid biological sludge;    (D) oxidizing using Fenton oxidation method, decoloring the sewage and subjecting the separated biological sludge to dehydration treatment to make the mass fraction 18-20% or 30-40%, i.e. obtaining second branch processing product used as organic fertilizer;    (E) adding polyacrylamide such that each ton of sewage contains 0.5-1.0 ppm polyacrylamide;    (F) sewage separating and secondary decoloring; and    (G) chemically dehydrating the sludge to make the total weight 40-45%, i.e. obtaining third branch processing product for a power boiler raw material and cement accessory material.
NOVELTY - Organic fertilizer fermentation free turning device comprises data processing device, temperature adjusting device, and temperature detecting device. The temperature adjusting device comprises fan, main pipe, branch pipe, buffer filter net cooling air and cooling pipe. The temperature detection device collects internal temperature of organic material, and generates corresponding temperature value. The data processing device controls blower to stop working when first temperature value is greater than second temperature value.    USE - Organic fertilizer fermentation free turning device.    DETAILED DESCRIPTION - Organic fertilizer fermentation free turning device comprises data processing device, temperature adjusting device, and temperature detecting device. The temperature adjusting device comprises fan, main pipe, branch pipe, buffer filter net cooling air and cooling pipe. The cooling pipe is provided with a gas hole and cooling air buffer filter net covered on the cooling pipe. The temperature detection device collects internal temperature of organic material, and generates corresponding temperature value. The data processing device collects temperature value, judges first temperature value and the preset temperature value of the corresponding collection, controls the fan to cool air into the cooling tube and the organic material stack by use of cold air buffer filtering net, judges the collected temperature value and a corresponding second temperature preset value, and controls the blower to stop working when the first temperature value is greater than the second temperature value.
NOVELTY - The utility model claims a marsh gas comprehensive utilization system, wherein the system comprises fuel gas power generation set, coal burning boiler, marsh gas fermentation tank, a solar water heater, a water tank and a mixing tank. Combustion gas output of gas inlet of electric machine is connected with a water-gas separating tank, an air outlet pipe of the water-gas separating tank is connected with the marsh gas fermentation tank is connected with the water-gas separating tank is provided with a water pipe, the water pipe and the fuel coal boiler, gas generating set according to the order network cabinet and the booster station connected with the national grid, gas exhaust pipe of the electric machine passes through the water tank is connected with the atmosphere, the water pipe I and the marsh gas fermentation tank is connected with the water tank, the upper part of coal burning boiler is provided with a hot water outlet pipe, a hot water outlet pipe and the marsh gas fermentation tank is connected with the water outlet pipe of the solar water heater is connected with the adjusting pool, the adjusting pool is connected with a filter tank, filter tank and the marsh gas fermentation tank, marsh gas fermentation tank is connected with the biogas liquid tank. This utility model can realize integrated cultivation, biogas, biogas fertilizer, generating electricity in one body to reach the purpose of recycling economy.
NOVELTY - A microbial organic fertilizer comprises a viable bacteria preparation comprising Bacillus amyloliquefaciens SB177 strain (A), a viable bacteria preparation comprising Paenibacillus spp. TX-4 strain (B), Streptomyces corchorusii NF0919 strain (C), humic acid (D), and clay (E). The weight ratio of A: B: C: D: E= 8: 8: 5-10: 70-80: 3-5.    USE - A microbial organic fertilizer used for strawberry (claimed).    ADVANTAGE - The fertilizer has rich nutrition, and prevents continuous cropping obstacles problem of strawberry.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the viable bacteria preparations A or B, comprising fermenting at 60 degrees C, and drying, where the live spore has a concentration of greater than or equal to 1x 101 colony-forming unit/g, and has a water content 3-5%.
NOVELTY - Production of an organic cultivating substrate comprises mixing 80-85 pts. wt. cattle waste residue, and 15-20 pts. wt. municipal domestic sludge; carrying out aerobic fermentation, and crushing to obtain large particle fermented material and a small particle fermented material at a ratio of 1.3:1-1.2; and uniformly mixing the small particle fermented material with large particle fermented material.    USE - Method for the production of an organic cultivating substrate (claimed).    ADVANTAGE - The organic cultivating substrate has low heavy metal content, and is environment-friendly.
NOVELTY - Preparation of an organic fertilizer comprises adding calcium oxide to microbial fermentation dreg to adjust pH value to 5.5-8.5; adding silkworm powder, uniformly mixing, and carrying out natural stacking fermentation for 7-20 days; and granulating, drying, and controlling water content at less than 30 mass%.    USE - Method for the preparation of an organic fertilizer (claimed).    ADVANTAGE - The method is simple and inexpensive, and has high yield is high. The fertilizer is environment-friendly.
NOVELTY - Method for extracting curcumin, involves (a) drying and crushing ginger, and (b) subjecting the crushed product to supercritical carbon dioxide extraction at 10-50 MPa, preferably 30 MPa and 30-90 degrees C, preferably 50 degrees C for 60-150 minutes, preferably 120 minutes, uniformly mixing 95% ethanol (entrainer), ginger pieces, and carbon dioxide extraction solvent in a ratio of 1-1.5:15-50:0.5-1.5, preferably 1:30:1.5, and drying the obtained product.    USE - The method is useful for extracting curcumin (claimed).    ADVANTAGE - The method is simple, environmentally-friendly, and convenient to perform, and causes no adverse reaction on the final product.
NOVELTY - A urotropine is produced by dissolving pesticide byproduct containing formaldehyde, methenamine, and paraformaldehyde in water, introducing ammonia gas, gradually increasing temperature to 60-80 degrees C, controlling pH value to 9-10, decreasing temperature to 20 degrees C, preserving heat for 1 hour, filtering, and centrifuging to obtain crystal in which amount of urotropine is less than or equal to 96%.    USE - Production of urotropine (claimed).    ADVANTAGE - Production process is simple, easy to operate, and environment-friendly.
NOVELTY - Cultivating black fungus, involves (a) selecting fungal strain and extracting fungal mycelium in mid January, (b) crushing straw uniformly and mixing with sawdust, wheat bran and cotton seed skins to obtain mixture, (c) inoculating the fungal strain into sterilized mixture and maintaining the spawn at indoor temperature and in dark environment for 3 months, (d) placing the spawn directly in natural light and fresh air and spraying water, and (e) harvesting the grown mushroom.    USE - The method is useful for cultivating black fungus (claimed).    ADVANTAGE - The method reduces the proportion of sawdust and avoids toxic chemical products, thus is green and environmentally-friendly, and enables to add a variety of other agricultural products e.g. husk waste, thus is reduces cost and significantly improves the growth rate of the black fungus and its product and enhance mineral and protein content and variety of vitamins, thus is rich in nutrition.
NOVELTY - This utility model claims a method for extracting methane from biogas, wherein the biogas from the impurity-extracting methane device comprises a separation chamber, a cooling device, a methane gas and a pipeline, and the front end is provided with an inlet valve, the back end is provided with an outlet valve, the pipeline connected with the suction device, separating the cooling device chamber of the separation chamber is connected with the pipeline is provided with the first gas separating valve with the pipeline, a methane gas cylinder is connected with the pipeline and is provided with a second air valve is set between the methane gas with the pipeline, separating chamber is further equipped with a heating device. The utility model passes through the structure, it can improve the methane purity, it does not need extra energy.
NOVELTY - An avanafil is prepared by carrying out substitution reaction on 6-amino-1, 2-dihydro pyrimidine-2-keto-5-carboxylic acid ethyl ester and 3-chloro-4-methoxy benzyl chloride to obtain 6-(3-chloro-4-methoxy benzyl amino)-1,2-dihydro pyrimidine-2-keto-5-carboxylic acid ethyl ester, carrying out condensation with S-hydroxymethyl pyrrolidine to generate 4-((3-chloro-4-methoxy benzyl)amino)-2-(2-(hydroxymethyl)-1-pyrrole alkyl) pyrimidine-5-carboxylic acid ethyl ester, carrying out hydrolysis, and carrying out acylation reaction.    USE - Preparation of avanafil (claimed).    ADVANTAGE - Preparation process is simple in process, economic and environmental-friendly, and suitable for the requirements of industrialization amplification.    DETAILED DESCRIPTION - An avanafil of formula (I) is prepared by carrying out substitution reaction on 6-amino-1, 2-dihydro pyrimidine-2-keto-5-carboxylic acid ethyl ester and 3-chloro-4-methoxy benzyl chloride to obtain 6-(3-chloro-4-methoxy benzyl amino)-1,2-dihydro pyrimidine-2-keto-5-carboxylic acid ethyl ester, carrying out condensation with S-hydroxymethyl pyrrolidine to generate 4-((3-chloro-4-methoxy benzyl)amino)-2-(2-(hydroxymethyl)-1-pyrrole alkyl) pyrimidine-5-carboxylic acid ethyl ester, carrying out hydrolysis, and carrying out acylation reaction.
NOVELTY - This utility model claims a mobile vehicle-mounted kitchen garbage processing system, comprising a vehicular platform, wherein further comprising a lifting device, a crushing device and a biological treatment device, a lifting device, a crushing device and a biological treatment device are mounted on the vehicle platform, the outlet of the inlet, a crushing device is connected with the crushing device of the lifting device is connected with the biological treatment device through the connecting device. This utility model is a moving device, which is convenient for the garbage processing, which avoids the transportation process of the garbage, a crushing device and a biological treatment device, a garbage crushing, the biological fermenting, stirring uniformly, and then drying to obtain the finished product, fertilizer or feed.
NOVELTY - A vinasse organic fertilizer comprises 35-42 wt.% vinasse, 55-65 wt.% chicken manure and 1-2 wt.% biological strains.    USE - Vinasse organic fertilizer.    ADVANTAGE - The fertilizer is prepared in an economical manner with high efficiency, and is convenient to apply.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a vinasse organic fertilizer, which involves preparing the raw materials of vinasse and chicken manure, mixing the vinasse with the chicken manure according to corresponding proportion, adding corresponding proportion of biological strains into the mixed raw materials, stirring uniformly, fermenting, crushing, screening, forming pellet or powder to obtain the finished product, and packaging the finished product.
NOVELTY - A waste chemical reaction processor has a chemical reaction vessel provided with an exhaust opening at one end, and a deodorization device, where the bottom of the chemical reaction vessel is provided with a reaction tank for temporarily storing processed material discharged from the chemical reaction mechanism.    USE - Waste chemical reaction processor for processing waste for producing organic fertilizer (all claimed).    ADVANTAGE - The processor has better effect of deodorization and sterilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing the waste.
NOVELTY - A chicken manure residues and sludge compost utilized organic cultivation substrate sludge stacking fertilizer preparation method involves preparing chicken manure residues and sludge compost, where the residues are solid chicken manure residues obtained by separating flushing sewage of a large-scale chicken farm through a solid-liquid separator. The compost is obtained by mixing urban living sludge and edible fungi residue cultivation waste residues, and the mixture is fermented. The resulted material is crushed, and large material particle is filtered to obtain a finished product.    USE - Method for preparing organic cultivation substrate sludge stacking fertilizer produced from chicken manure residues and sludge compost.    ADVANTAGE - The method enables preparing organic cultivation substrate sludge stacking fertilizer with better physical and chemical properties, low salinity, high organic content and moderate nutrients.    DETAILED DESCRIPTION - A chicken manure residues and sludge compost utilized organic cultivation substrate sludge stacking fertilizer preparation method involves preparing chicken manure residues and sludge compost with a ratio of 18-21:1, where the chicken manure residues are solid chicken manure residues obtained by separating flushing sewage of a large-scale chicken farm through a solid-liquid separator. The sludge compost is obtained by mixing urban living sludge and edible fungi residue cultivation waste residues, and the mixture is fermented at 60-65 degrees C until temperature of the mixture reaches 35-45 degrees C. The fermentation material is crushed, followed by filtering large material particle, where weight ratio of the small material particle and large material particle is 1:1-1.2.
NOVELTY - A sludge resource recycling method involves placing sludge into a storage pool, and adding 5-30 wt. % crushed straw. The mixture is mixed in a mixing machine. 0.5-2 wt.% aerobic composition is added for fermenting microbial compound. 8-12 wt.% deodorant is added to the microbial compound. The aerobic composition is stacked for fermentation by applying ventilation fermentation process to obtain organic fertilizer, where stacking temperature is 45-650 degrees C for 14-18 days and humidity is 40-50 %.    USE - Method for recycling sludge resource.    ADVANTAGE - The method enables recycling sludge resource with degrading organic matters and heavy metal and enables killing microorganism and weed seeds.
NOVELTY - The device has a discharging port formed in one side wall of a lower part of a feeding storage bin. A manual valve controls discharging quantity, and is arranged on the discharging port. A feeding port of a screw conveyor is positioned below the discharging port of the feeding storage bin. An automatic feeding device for adding strains or microelements is arranged on the screw conveyor. A discharging port of an inclined conveyor is provided with a rotatable bag bracket that is provided with a material storage bag. Stacking fermentation is performed in a fermentation chamber by the storage bag.    USE - Small size farm organic fertilizer local fermentation device for use in an industry.    ADVANTAGE - The device has reasonable design and simple structure, and realizes local fermentation of organic fertilizer, and increases production efficiency and degree of automation so as to reduce production cost and pollution to environment. The device has energy-saving and environment-friendly effects, and achieves industrialized production condition.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of a small size farm organic fertilizer local fermentation device.
NOVELTY - The reactor has a valve pipeline system arranged with a stirring motor (8) and 0.098MPa to 4.0MPa pressure pump (9). A mechanical stirring ferment tank (1) is arranged on an upper end of a feeding port (10), where a lower end of the feeding port is provided with a fermentation residue outlet (12). An upper end and a lower end of a ceramic ultra-filtration membrane separating device (13) are connected with the mechanical stirring ferment tank and the pressure pump, respectively. The fermentation residue outlet is connected at the lower end of the mechanical stirring ferment tank.    USE - Cycle synchronization straw enzymatic hydrolysis reactor for ethanol fermentation. Can also be used for fermentation of antibiotics, amino acids and enzymes.    ADVANTAGE - The reactor can extract the yeast repeatedly and circularly using straw enzymolysis to ferment ethanol in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a cycle synchronization hydrolysis reactor.'(Drawing includes non-English language text)'    Mechanical stirring ferment tank (1)    Stirring motor (8)    Pressure pump (9)    Feeding port (10)    Fermentation residue outlet (12)    Ceramic ultra-filtration membrane separating device (13)
NOVELTY - This utility model is a multifunctional animal breeding and sunshine relate to a kind of animal breeding device is composed of body, body seat in screen house on the bottom and is fixed with it, the screen house bottom is fixed on the fermentation bed. The content of fermenting bed is provided with more than one of the stirring roller, one end is connected with the stirring fermentation bed movably, and the other end is a fermenting bed board is connected with the mixing arm, a crop crushed straw and EM bacteria in the fermentation bed. This utility model is new multifunctional animal breeding and sunshine , the structure design is reasonable, and it has good ability of cleaning animal excrement, and by the action of the crushed straw and EM bacteria in the fermentation bed, which can reduce the smell of animal excrement, has the function of sterilizing, which provides a good growing environment for the animal. The upper part of the cleaning method of excrement, not only saves time and labour force.
NOVELTY - Dark black chafer attractant comprises anisole.    USE - As dark black chafer attractant.    ADVANTAGE - The attractant can attract female and male adult dark black chafer, and is prepared simply and environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for trap, which comprises bracket, lure, hopper and collection tube, where the lure is located in bracket, bracket is provided below the hopper and the hopper is provided below the collection tube.
NOVELTY - Preparation of 3-oxo-cyclobutane carboxylic acid comprises reacting acetone and bromine in ethanol, evaporating alcohol, reacting residual acetone and hydrogen bromide; reacting with malononitrile in N,N-dimethyl formamide with tetrabutyl ammonium bromide, sodium iodide and potassium carbonate, stirring, reacting, cooling, distilling, washing, extracting, stirring, layering, washing toluene layer, drying, filtering, evaporating, distilling; dispersing, refluxing, evaporating, reacting with toluene, washing, drying, filtering, evaporating, and reacting with methyl tert-butyl ether.    USE - Method for preparing 3-oxo-cyclobutane carboxylic acid (claimed).    ADVANTAGE - The method is environment-friendly, simple, short, and low cost, and has yield coefficient of 52-68% and yield purity of 99-99.2%.    DETAILED DESCRIPTION - Preparation of 3-oxo-cyclobutane carboxylic acid comprises reacting acetone and bromine at a molar ratio of 1:1.5-1:2.5 in ethanol under room temperature for 10-16 hours, evaporating alcohol, reacting residual acetone and generated hydrogen bromide to obtain 1,3-dibromo acetone acetal; reacting malononitrile and 1,3-dibromo acetone acetal at molar ratio of 1:1-1:1.5 in N,N-dimethyl formamide with tetrabutyl ammonium bromide activating agent in the presence of sodium iodide phase transfer catalyst and potassium carbonate, stirring at 60-90 degrees C, reacting for 16-24 hours, cooling to room temperature, distilling solvent under reduced pressure, water washing, extracting with toluene, stirring and layering, washing toluene layer with water, drying, filtering, evaporating toluene under reduced pressure, further distilling toluene to obtain 3,3-dicyano acetal cyclobutanone; dispersing in 1-6 M hydrochloric acid solution, refluxing at 70-100 degrees C for 16-24 hours, evaporating, reacting with toluene, washing with water, drying, filtering, evaporating to dryness, and reacting with methyl tert-butyl ether.
NOVELTY - The utility model relates to a method for treating sewage by biological reaction kettle, comprising a reaction kettle, a filler tray, a water inlet pipe, a water outlet pipe, a sludge pipe and the air inlet pipe, the reaction kettle body is provided with 5 rows of transverse rod, the transverse rod is provided with filler tray, a water inlet pipe is arranged at the water outlet end of the reaction kettle body, a water inlet pipe of the water outlet end is connected with a crossed water outlet pipe, an air inlet pipe of the aeration pipe is connected with the reaction kettle body, the aeration pipe is provided with multiple air outlet, a water outlet pipe and a sludge pipe is set in the reaction kettle. The utility model is provided with good sewage treatment effect, which not only can fix microorganism by sewage, but also can prevent sludge expansion;
NOVELTY - Preparing anti-malarial artemisinin, comprises (i) taking artemisinin acid as a starting material, and performing reduction reaction of artemisinin acid in presence of a reaction solvent, a catalyst includes e.g. palladium loaded on charcoal, and a reducing agent to obtain dihydro-artemisinic acid; (ii) performing oxidization reaction of dihydro-artemisinic acid to obtain corresponding peroxides of dihydro-artemisinic acid; and (iii) performing acid-catalyzed rearrangement reaction of peroxide of dihydro-artemisinic acid, and then purifying to obtain the target compound artemisinin.    USE - The method is useful for preparing anti-malarial artemisinin (claimed).    ADVANTAGE - The method utilizes low cost reagents which are easily available; has short synthetic route, high reaction selectivity, environmental friendly, easy operation procedures, simple post-processing procedures, and high production yield; and is suitable for industrial production.    DETAILED DESCRIPTION - Preparing anti-malarial artemisinin, comprises (i) taking artemisinin acid as a starting material, and performing reduction reaction of artemisinin acid in presence of a reaction solvent, a catalyst includes palladium loaded on charcoal, palladium hydroxide loaded on rhodium-aluminum oxide, Raney nickel or molybdenum oxide, and a reducing agent includes hydrogen, nickel chloride or sodium borohydride, where the mol ratio of artemisinin acid and nickel chloride is 1:0.01-1, and the mol ratio of artemisinin acid, nickel chloride and sodium borohydride is 1:0.01-10:1-20.to obtain dihydro-artemisinic acid; (ii) performing oxidization reaction of dihydro-artemisinic acid to obtain corresponding peroxides of dihydro-artemisinic acid; and (iii) performing acid-catalyzed rearrangement reaction of peroxides of dihydro-artemisinic acid, and then purifying to obtain the target compound artemisinin.
NOVELTY - The system has an organic waste compost reaction chamber whose lower end is provided with a water collecting tank. A water pump is connected with a percolate collecting pool. An air distribution system is fixed at a lower end of an organic waste compost reaction chamber. A draught fan is connected with an end of the air distribution system. Another end of the air distribution system is connected with a solar system. An upper end of the organic waste compost reaction chamber is provided with a glass roof. A tarpaulin is covered on the glass roof.    USE - Compost chamber integrated system.    ADVANTAGE - The system can realize an operation process of organic ecological fermentation plant so as to avoid rubbish and ensure zero-waste discharge in northern areas during winter season.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a compost chamber integrated system.
NOVELTY - Aging method of original layered old altar wine comprises placing 25-35 pts. wt. grain, 25-35 pts. wt. sludge and 35-45 pts. wt. wine into ceramic storage jar with red cow leather, sealing pig urine in bag under dry and dark environment, removing contents of jar, washing; adding pig urine; and storing for not less than 3 years.    USE - Method for aging original layered old altar wine (claimed).    ADVANTAGE - The wine has soft and mellow taste. The method shortens aging time of wine.
NOVELTY - Method for preparing compound biological fertilizer for apple trees, involves uniformly mixing raw materials comprising kitchen wastes, tobacco straws, plant ash, distillers grain, potassium humate, bird feathers, modified fly ash, urea, ammonia water, diammonium phosphate, potassium sulfate, calcium superphosphate, cnidium fruit, Aloe, Eucalyptus leaves, pharbitis seed, Cyrtomium rhizome, zinc sulfate, magnesium sulfate, boric acid, fermented preparation and citronella oil, fermenting mixture and drying fermented mixture.    USE - The method is useful for preparing compound biological fertilizer for apple trees (claimed).    ADVANTAGE - The compound biological fertilizer is environmentally-friendly, reduces fertilization frequency and fertilizer cost, and improves utilization ratio, application of the fertilizer, and quality and yield of the apple trees.    DETAILED DESCRIPTION - Method for preparing compound biological fertilizer for apple trees, involves uniformly mixing raw materials comprising 30-40 pts. wt. kitchen wastes, 20-30 pts. wt. tobacco straws, 10-15 pts. wt. plant ash, 10-15 pts. wt. distillers grain, 16-18 pts. wt. potassium humate, 10-12 pts. wt. bird feathers, 18-22 pts. wt. modified fly ash, 12-14 pts. wt. urea, 11-13 pts. wt. ammonia water, 14-16 pts. wt. diammonium phosphate, 13-15 pts. wt. potassium sulfate, 11-13 pts. wt. calcium superphosphate, 2-4 pts. wt. cnidium fruit, 2-4 pts. wt. Aloe, 3-5 pts. wt.Eucalyptus leaves, 2-4 pts. wt. pharbitis seed, 3-5 pts. wt. Cyrtomium rhizome, 0.5-0.8 pts. wt. zinc sulfate, 0.8-1 pts. wt. magnesium sulfate, 0.7-0.9 pts. wt. of boric acid, 0.4-0.6 pts. wt. fermented preparation and proper amount citronella oil and fermenting mixture and drying fermented mixture.
NOVELTY - Method for raising pig, involves using strain-free fermented bed comprising sawdust, bran and pig manure in a mass ratio of 7:3:1.    USE - The method is useful for raising pig (claimed).    ADVANTAGE - The method is simple, cost-effective and convenient to perform.
NOVELTY - Biological foliage fertilizer comprises 0.2-3% fungal bioprotein, macroelement fertilizer, 0.5-1% wetting agent, 0.3-0.5% dispersing agent, 0.3-0.5% thickening agent, and remainder filler or water. The macroelement fertilizer is at least two of nitrogen, phosphorus and potassium, where total amount of the macroelements in the macroelement fertilizer is at least 50% to the total amount of the biological foliage fertilizer.    USE - As biological foliage fertilizer.    ADVANTAGE - The fungal bioprotein and macroelement fertilizer are complementary, and after being applied once, the biological foliage fertilizer enhances effect on preventing crop diseases, enhances crop yield, and lowers the consumption, varieties and application frequency of pesticides and fertilizers.    DETAILED DESCRIPTION - Biological foliage fertilizer comprises 0.2-3% fungal bioprotein, macroelement fertilizer, 0.5-1% wetting agent, 0.3-0.5% dispersing agent, 0.3-0.5% thickening agent, and remainder filler or water. The macroelement fertilizer is at least two of macroelements such as nitrogen, phosphorus and potassium, where total amount of the macroelements in the macroelement fertilizer is at least 50% to the total amount of the biological foliage fertilizer. The preparation of the fungal bioprotein, involves culturing at least one of Botrytis, Alternaria, rice blast fungus, toxic mold, Aspergillus flavus, Rhizoctonia solani, or Penicillium strain in culture medium, allowing fungus to grow large number of fungal spores, centrifuging the fungal spores at 5000 rotations per minute (rpm) for 30 minutes, collecting the spores, adding 5mM potassium phosphate of pH6.8 or citrate buffer to the centrifuged spore, sonicating mixture at 180 Bar high for 30 minutes, centrifuging the mixture at 5000 rpm for 30 minutes, boiling the mixture in a water bath for 15 minutes, centrifuging the mixture at 5000 rpm for 30 minutes, and collecting resulting supernatant.
NOVELTY - A phosphoric acid purifying sludge producing nitrate fertilizer is wet-processed by mixing 100-110 pts. wt. phosphoric acid having a concentration of 18-22 wt.%, 100-104 pts. wt. phosphoric acid having a concentration of 20-23 wt.%, and 110-119 pts. wt. phosphoric acid having a concentration of 20-23 wt.%; stirring; adding 300-350 pts. wt. nitric acid having a concentration of 65-68 wt.%; stirring for 5-10 minutes; and adding 95-105 pts. wt. ammonia to adjust pH value to 5-6.5.    USE - Method of wet-processing of phosphoric acid purifying sludge producing nitrate fertilizer.    ADVANTAGE - The method is simple, has low energy consumption, utilizes waste, saves energy, and reduces industrial pollution.
NOVELTY - A termite and mouse resistant irradiation crosslinking and flame retardant pyrocondensation material comprises (in parts mass) base material (100), termite-proof and rat-proof agent (0.5-10), polymeric compatibilizer and/or coupling agent (1-20), flame retardant (0-100) and antioxidant (0.5-10).    USE - Termite-proof and rat-proof pyrocondensation material for heat-shrinkable tubing for heat-shrinkable type electric cable accessory (all claimed).    ADVANTAGE - The termite-proof and rat-proof pyrocondensation material has reduced toxicity, and is environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for termite-proof and rat-proof heat-shrinkable tubing, which is obtained by melting the raw materials, mixing and granulating, extruding the granulated materials, injection molding and sleeving, irradiating the cast pipe after extruding, expanding and cooling the pipe.
NOVELTY - Processing apparatus of biomass, has preprocessor which pre-processes biomass, slurrying apparatus which slurries the pre-processed biomass, saccharification apparatus which saccharifies the slurried biomass with saccharogenic amylase, and return line which returns internal liquids in the saccharification apparatus to the slurrying apparatus.    USE - The apparatus is useful for processing biomass (claimed).    ADVANTAGE - The method suppresses contamination and increases the concentration of the final product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for processing the above-mentioned biomass.
NOVELTY - System comprises preprocessing device that preprocesses biomass, a saccharification device that saccharifies the preprocessed biomass by using saccharification enzymes, and a saccharification enzyme production device that produces saccharification enzymes used in the saccharification device, first processing unit for transferring some of the preprocessed biomass as to the saccharification device, and second processing unit for transferring the remaining preprocessed biomass to the saccharification enzyme production device.    USE - The system or method is useful for processing the biomass (claimed) containing cellulose and hemicellulose e.g. rice straw and Panicum virgatum which is used as livestock feed.    ADVANTAGE - The system is cost-effectively produces many saccharification enzymes without using high-purity cellulose, monosaccharides, or disaccharides.    DETAILED DESCRIPTION - System comprises preprocessing device that preprocesses biomass, a saccharification device that saccharifies the preprocessed biomass by using saccharification enzymes, and a saccharification enzyme production device that produces saccharification enzymes used in the saccharification device, first processing unit for transferring some of the preprocessed biomass as to the saccharification device, second processing unit for transferring the remaining preprocessed biomass to the saccharification enzyme production device, where the saccharification enzyme-producing bacteria is cultured using the supplied preprocessed biomass as a culture medium, saccharification enzymes is produced, and the produced saccharification enzymes is transferred to the saccharification device. An INDEPENDENT CLAIM is included for method for processing the biomass, which involves using the above-mentioned system.
NOVELTY - Absorbent solution comprises water, and a nitrogen compound consisting of hindered 4-(aminoethyl)-tertiary morpholine (I).    USE - The absorbent solution is useful for removing acid compounds contained in a gaseous effluent such as natural gas, synthesis gas, combustion fumes, refinery gas, acidic gas obtained from an amine unit, Claus process tail gas obtained from a reduction unit, biomass fermentation gas, cement gas and incinerator fumes or removing hydrogen sulfide from gaseous effluent comprising carbon dioxide (all claimed).    ADVANTAGE - The absorbent solution enables energy-efficient removal of acid compounds contained in the gaseous effluent in an environmentally friendly manner.    DETAILED DESCRIPTION - Absorbent solution comprises water, and a nitrogen compound consisting of hindered 4-(aminoethyl)-tertiary morpholine of formula (I).    R1-R4 = H or 1-4C alkyl; either    R5 = 1-5C alkyl; and    R6 = 3-5C alkyl or 1-5C alkyl; or    R5R6 = 5-7 member ring, where the carbon atom is bonded to R6 of the nitrogen atom being either tertiary or quaternary.    An INDEPENDENT CLAIM is included for removing acid compounds contained in gaseous effluent, comprising absorbing acid compounds using the absorbent solution.
NOVELTY - Installation comprises a fermenter communicating with a source of air supply, a device for uniformly supplying an initial material to the fermenter, an air chamber having a lateral surface and a duct, front walls equipped with door, an inclined screw conveyor, and a scrape conveyor. The fermenter has chambers symmetrically installed relative to a longitudinal axis of the installation in an angle of 60-65 degrees to its base. An upper part of the chambers is provided with parallel grids. The air duct is communicated with an air extractor. A groove is positioned above the chambers.    USE - The installation is useful for preparing compost (claimed).
NOVELTY - Bio-organic fertilizer comprises 30-40 wt.% of livestock manure, 20-30 wt.% of kitchen waste, 15-25 wt.% of grass, 15-20 wt.% of straw powder, 1 wt.% of potassium dihydrogen phosphate, 1 wt.% of zeolite, 1 wt.% of lime powder, 3-5 wt.% of boric sludge and 1 wt.% of gypsum.    USE - The fertilizer is useful for grain, fruit, vegetable, forest and flower crop (claimed).    ADVANTAGE - The fertilizer improves soil fertility.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for: (1) preparing the bio-organic fertilizer comprising inoculating Bacillus megaterium in a culture medium at 30 degrees C for 24 hours to obtain a bacterial suspension, shaking the suspension in a shaking table at 28-30 degrees C and a rotating speed of 180 revolutions per minute for 48-72 hours, adding livestock manure in the suspension at 80 degrees C, where the livestock manure comprises chicken, duck excrement, cattle and sheep excrement, dehydrating the mixture, crushing kitchen waste, grass and straw powder into powder with 40-60-meshes and then adding potassium dihydrogen phosphate, zeolite, powder of lime, boric sludge and gypsum, primarily fermenting the mixture in a fermentation tank at 75 degrees C for 2 weeks and secondarily fermenting for 1-2 weeks, drying the fermented mixture until water content becomes 18-23%, sieving at 60-80 meshes and aging using agitator; and (2) use of the fertilizer for grain, fruit, vegetable, forest, flower crop, comprising applying fertilizer, after ditching the whole of the land or dig pits and then adding soil mix before planting, dressing by placing the soil mixed fertilizer on one side or trenching around the roots of crops and applying fertilizer into the soil few days before sowing.
NOVELTY - Nutritional soil comprises 15-30 wt.% of soil, 30-50 wt.% of fermented cow dung, 2-10 wt.% of perlite, 10-25 wt.% of straw, 2-8 wt.% of bacterial enzymes and 2-10 wt.% of water.    USE - The nutritional soil is useful for cultivating Artemisia arborescens (claimed) and preventing and treating plant insect pests.    ADVANTAGE - The nutritional soil cultivates Artemisia arborescens with good permeability, good heat-insulating property, high yield, less labor intensive and reduced water loss.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cultivating Artemisia arborescens comprising paving the nutrition soil and adding southernwood resveratrol and then fertilizing.
NOVELTY - Liquid fertilizer comprises 40-50 wt.% of lemon peel, 30-40 wt.% of Phellodendron, 10-20 wt.% of bone powder, 5-10 wt.% of brown sugar, 1-2 wt.% of pectin enzyme, 1-2 wt.% of ferment bacteria, 0.5-1.5 wt.% of efficient microbes and purified water in a ratio of 100:300.    USE - The liquid fertilizer is useful for crops.    ADVANTAGE - The liquid fertilizer is environmentally friendly and capable of improving soil environment and soil activity, releasing soil hardening, and improving growth and yield of the crop with resistance to drought.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the liquid fertilizer comprising adding the raw materials, carrying out enzymolysis process, inoculating 1-2% of ferment bacteria, stirring for 15 days, inoculating efficient microbes at 20-30 degrees C until a pH reaches 3.5-4, and carrying out ultrafiltration to obtain a lemon fermented liquid.
NOVELTY - Preparation of organic fertilizer, involves (a) crushing chicken manure, pig manure and P.eryngii by crusher, sieving mixture, and uniformly stirring the mixture, (b) adding 0.1-0.5 wt.% bentonite into the mixture, controlling ratio of the mixture to 25-35:1, and inoculating 0.1-5% microbial agent to the mixture, (c) piling a stack with length of 2-35 m, width of 0.25-3 m and height of 0.08-1.1 m by using a fork-lift truck, and (d) controlling initial moisture content to 55-60%.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is prepared into different fertilizers, e.g. bio-organic fertilizer, and biological organic and inorganic fertilizers. The method saves time and energy due to short fermentation period, and low nitrogen loss respectively. The pollution degree of odor to the environment is low during preparation of fertilizer.    DETAILED DESCRIPTION - Preparation of organic fertilizer, involves (a) selecting 25-35 wt.% chicken manure, 28-32 wt.% pig manure and 33-47 wt.% Pleurotus eryngii as active ingredient, crushing chicken manure, pig manure and P.eryngii by crusher, sieving mixture, and uniformly stirring the mixture, (b) adding 0.1-0.5 wt.% bentonite into the mixture, controlling ratio of the mixture to 25-35:1, and inoculating 0.1-5% microbial agent to the mixture, (c) piling a stack with length of 2-35 m, width of 0.25-3 m and height of 0.08-1.1 m by using a fork-lift truck, and (d) controlling initial moisture content to 55-60%. The microbial culture is Trichoderma strain (ACCC 30449), where strain is not less than 2 billion spores/g.
NOVELTY - Chicken manure type fermented organic fertilizer comprises 3000 pts. wt. chicken manure having water content of 60%, 450-600 pts. wt. edible fungus waste residue material having water content of 10%, 100-150 pts. wt. oil dreg having water content of 6%, 2-3 pts. wt. composite leavening agent, and 20-30 pts. wt. high protein nutritional yeast powder. The oil dreg is obtained by mechanically pressing the cottonseed or rapeseed.    USE - Chicken manure type fermented organic fertilizer.    ADVANTAGE - The chicken manure type fermented organic fertilizer is not added with any fertilizer except chicken manure and has sufficient fermentation and high heat yield. Water in the chicken manure can be quickly evaporated.    DETAILED DESCRIPTION - Chicken manure type fermented organic fertilizer comprises 3000 pts. wt. chicken manure having water content of 60%, 450-600 pts. wt. edible fungus waste residue material having water content of 10%, 100-150 pts. wt. oil dreg having water content of 6%, 2-3 pts. wt. composite leavening agent, and 20-30 pts. wt. high protein nutritional yeast powder. The oil dreg is obtained by mechanically pressing the cottonseed or rapeseed. The chicken manure type fermented organic fertilizer is prepared by mixing chicken manure, edible fungus waste residue material, oil dreg, composite leavening agent, and high protein nutritional yeast powder, stacking, and fermenting.
NOVELTY - Production of pollution-free biological agent comprises loosely stacking fresh livestock manure to maintain good ventilation.    USE - Production of pollution-free biological agent (claimed).    ADVANTAGE - The method can shorten the organic materials rotten time and reduces nitrogen loss.
NOVELTY - Dendrobium epiphytic planting fertilizer comprises glutinous rice paste and fermented cow dung.    USE - Dendrobium epiphytic planting fertilizer.    ADVANTAGE - The fertilizer improves survival rate of Dendrobium epiphytic growth by more than 98%, and provides Dendrobium that is not easy to rot when flooded, resistant to damage and conducive to imitation ofDendrobium wild cultivation. It has simple preparation, and simple and easy to use.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for (a) preparation of Dendrobium epiphytic planting fertilizer by uniformly mixing glutinous rice paste and fermented cow dung according proportion to obtain product; and (b) epiphytic planting of Dendrobium by applying fertilizer to Dendrobium epiphytic roots; and fixing Dendrobium epiphytic roots on tree bark to grow Dendrobium.
NOVELTY - An Agaricus blazei original seed culture material comprises 80-84 wt.% goat manure, 6-10 wt.% bagasse, 4-6 wt.% bran, 2 wt.% dry soil, 2 wt.% gypsum powder, and 1 wt.% lime powder.    USE - Agaricus blazei original seed culture material.    ADVANTAGE - The culture material has high working efficiency, kills Escherichia coli, parasitic ovum and weed seed, sanitizes environment of sheep farms, widens cultivating raw material, and reducing strain.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a preparation method of Agaricus blazei original seed culture material which comprises providing above raw materials and performing stacking fermentation.
NOVELTY - Producing organic fertilizer using recycled agricultural wastes, comprises carrying out anaerobic dry fermentation of the livestock and poultry waste and crops straw to produce biogas, biogas residue and biogas slurry, where the biogas is used for generating electricity, the biogas slurry is used as inoculum, mixing biogas residue and fresh livestock manure and placing in a dynamic fermenting and composting tank, fermenting and composting, transferring the material to the static composting sites, carrying out static fermentation and composting, completing sieving, extruding and granulating.    USE - The method is useful for producing organic fertilizer using recycled agricultural wastes (claimed).    ADVANTAGE - The method uses natural microorganisms and microbial inoculation material for deodorizing, reducing ferment speed; has short period; is easy to realize mechanized operation; uses energy recycling process; does not produce secondary pollution; achieves waste resource recycling; is safe and environmentally friendly; and can produce great social, ecological and economic benefit, and has strong popularization and application value.    DETAILED DESCRIPTION - Producing organic fertilizer using recycled agricultural wastes, comprises carrying out anaerobic dry fermentation of the livestock and poultry waste and crops straw to produce biogas, biogas residue and biogas slurry, where the biogas is used for generating electricity, the biogas slurry is used as inoculum, mixing biogas residue and fresh livestock manure and placing in a dynamic fermenting and composting tank, completing dynamic fermenting and composting, transferring the material to the static composting sites, carrying out static fermentation and composting, completing static fermenting and composting, sieving and extruding the material and granulating to obtain the standard organic fertilizer.
NOVELTY - Method for preparing biological nutrient, involves using 86% solid effective microorganism (EM) which is greater than or equal to 100 hundred million viable cells/g, 9% solid formulation of photosynthetic bacteria which is greater than or equal to 50 hundred million viable cells/g, 4% growth hormone and 1% trace elements.    USE - The method is useful for preparing biological nutrient (claimed) which is used in farming, livestock breeding, and water industry.    ADVANTAGE - The method is environmentally-friendly and cost-effective, and shortens the fermentation period.
NOVELTY - Preparing 2-(carbonyl-N-phenothiazine-yl)-benzoic acid, comprises adding phenothiazine and phthalic anhydride into a reaction container, adding acetonitrile and adding concentrated hydrochloric acid in a drop wise manner while stirring to obtain reaction solution, cooling, stirring and reacting to obtain a mixed solution, vacuum extracting and vaporizing to obtain concentrated solution, where the concentrated solution is 10-15% of the volume of mixed solution, cooling the concentrated liquid to room temperature, adding water, stirring uniformly, filtering, washing the filter cake and drying.    USE - The method is useful for preparing 2-(carbonyl-N-phenothiazine-yl)-benzoic acid (claimed).    ADVANTAGE - The method uses acetonitrile as a solvent, and concentrated hydrochloric acid as a catalyst; is simple, has short reaction time, mold reaction conditions, simple post-treatment process; utilizes easily available low cost raw materials; and has high productive rate.    DETAILED DESCRIPTION - Preparing 2-(carbonyl-N-phenothiazine-yl)-benzoic acid, comprises (a) adding phenothiazine and phthalic anhydride in a mol ratio of 2.5:(2.5-3.3) into a reaction container, adding acetonitrile, adding concentrated hydrochloric acid in a drop wise manner while stirring to obtain reaction solution, cooling to 45-85 degrees C, and stirring and reacting for 1-3 hours to obtain a mixed solution, and (b) vacuum extracting and vaporizing to obtain concentrated solution, where the concentrated solution is 10-15% of the volume of the mixed solution, cooling the concentrated liquid to room temperature, adding water, stirring uniformly, filtering, washing the filter cake with water, and drying.
NOVELTY - Preparing tilmicosin phosphate crystal comprises completely dissolving tilmicosin phosphate powder in ethyl acetate, slowly adding isopropyl ether in a drop wise manner, mixing under a stirring state at 5 degrees C, stirring continuously during addition for 30-60 minutes, carrying out solid-liquid separation, washing, and vacuum drying.    USE - The method is useful for preparing tilmicosin phosphate crystal (claimed).    ADVANTAGE - The method: provides crystal particles, which replaces powder, has high specific gravity; avoids dust pollution; and has easy solvent recycling step. The crystal: is easy to sink in water; has high dispersibility, high dissolution rate and high content; and can be directly added to animal feed or animal drinking water.
NOVELTY - An organic solid waste treatment method involves homogenizing and preheating organic solid waste, and carrying out thermal hydrolysis reaction. The material is placed in a depressurization tank and a buffer tank to carry out primary and secondary depressurization process. Heat exchange and anaerobic digestion is carried out with the material. Vacuum degassing treatment is carried out with the digested sludge. The treated sludge is mixed with flocculating agent and dehydrated to obtain dehydrated sludge. The dehydrated sludge is conveyed to a drying room to obtain dried biogas residue.    USE - Method for treating organic solid waste.    ADVANTAGE - The method enables treating organic solid waste with high digestive efficiency and sludge dehydration efficiency.    DETAILED DESCRIPTION - An organic solid waste treatment method involves homogenizing and preheating organic solid waste in a pre-heating tank, and carrying out thermal hydrolysis reaction by placing the preheated organic solid waste in a thermal hydrolysis reactor. The material is placed in a depressurization tank and a buffer tank to carry out primary and secondary depressurization process. Heat exchange and anaerobic digestion is carried out with the material. Vacuum degassing treatment is carried out with the digested sludge in a digested sludge tank. The treated sludge is mixed with flocculating agent and dehydrated to obtain dehydrated sludge. The dehydrated sludge is conveyed to a drying room to obtain dried biogas residue.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for treating organic solid waste.
NOVELTY - A straw rotten agent comprises 15-30 pts. wt. lignin decomposing fungi and 1-10 pts. wt.cellulase preparation, which comprises a mixture of Trichoderma and Aspergillus niger fermentation product.    USE - Straw rotten agent.    ADVANTAGE - The agent is inexpensive, and exhibits high production efficiency and better applicability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing straw rotten agent, which involves adding white rot fungi in a solid fermentation culture medium, adding adsorbent to a substrate for 10-15 times, drying and crushing the mixture to obtain white rot fungus powder, mixing Trichoderma and Aspergillus Niger, fermenting, drying and crushing the mixed product to obtain cellulase preparation, mixing the obtain product with powder to obtain straw rotten agent.
NOVELTY - A microbial fertilizer preparation method involves adding fermentation microbial inoculum to agricultural wastes, and selecting appropriate inorganic and organic inductors according to requirements of breeding enzyme of the inoculum. The fermentation microbial inoculum is triggered to ferment the agricultural wastes followed by thoroughly decomposing agricultural wastes, where the agricultural wastes comprise straw, bran, rice hull, soybean meal, wood powder, peel and weeds.    USE - Method for preparing microbial fertilizer.    DETAILED DESCRIPTION - A microbial fertilizer preparation method involves adding fermentation microbial inoculum to agricultural wastes, and selecting appropriate inorganic and organic inductors according to requirements of breeding enzyme of the inoculum. The fermentation microbial inoculum is triggered to ferment the agricultural wastes followed by thoroughly decomposing agricultural wastes, where the agricultural wastes comprise straw, bran, rice hull, soybean meal, wood powder, peel and weeds and the fermentation microbial inoculum comprises Cellulomonas fIavigena, Lactobacillus casei, Azotobacter vinelandii, Rhizobium leguminosarum, Aspergillus niger, Aspergillus oryzae and Humicola insolens.
NOVELTY - An organic fertilizer comprises 50-60 pts. wt. straw powder, 15-20 pts. wt. rapeseed cake powder, 6-8 pts. wt. alfalfa, 4-5 pts. wt. inverted grass powder, 2-4 pts. wt. soil, 5-6 pts. wt. flour, 8-10 pts. wt. vinegar residue, 6-10 pts. wt. soy sauce, 4-6 pts. wt. shell powder, 10-20 pts. wt. bran, 3-4 pts. wt. red root powder, 5-7 pts. wt. canal mud, 50-60 pts. wt. swill, 8-10 pts. wt. brown sugar and animal feces.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer has high organic matter content, active material content and high nutrition, and can improve soil quality and soil structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves adding flour with 6-8 times water, heating at 80-90 degrees C, stirring, adding the straw powder, rapeseed cake powder, soy sauce residue, stirring and dispersing for 20-30 minutes, drying and granulating the particle diameter to 2 mm. Sugar fermentation liquid is prepared by adding brown sugar in 1.8-2 times of clean water, adding 10-15 wt.% brown sugar fermenting agent and 1-2 wt.% alum, stirring and fermenting at 30-40 degrees C for 15-20 days, adding 1-2 wt.% borax, agitating to obtain fermentation liquid. EM bacteria fermentation soil is prepared by adding shell powder, bran, 0.5-0.8 wt.% EM bacteria liquid, water heating for 3-5 hours to obtain the product. Fermenting is carried out by stacking the material, mixing with raw material, adding 2-4 wt.% humic acid mixing material, 0.1-0.2 wt.% Chinese herbal medicine, stirring uniformly, piling the normal temperature fermenting for 10-12 h, turning, continuously stacking to ferment for 2-4 hours, drying to obtain the biological organic fertilizer, where the Chinese herbal medicines are 10-20 pts. wt. herba Houttuyniae, 10-12 pts. wt. fresh reed, 4-5 pts. wt./ unbracteolated Spurge Root, 2-4 pts. wt. folium Artemisiae argyi and 1-2 pts. wt. sunflower.
NOVELTY - A biological liquid fertilizer comprises 1 pts. wt. diluted waste water, 0.06-0.2 pts. wt. bran and 0.1-0.15 pts. wt. composite microbial agent, where the diluted waste water is prepared by diluting livestock and poultry excrement by water according to a weight ratio of 1:4 to 1:6, the composite microbial agent comprises strains and EM original liquid according to a weight ratio of 5:6 to 7:3, the strains include Trichoderma viride, Saccharomyces cerevisiae and Bacillus subtilis.    USE - Biological liquid fertilizer.    ADVANTAGE - The fertilizer has high fermentation degree, high efficiency and obvious yield increasing effect, and can be prepared in a quick and environment-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a biological liquid fertilizer, which involves diluting the livestock and poultry excrement by water, mixing the diluted waste water, the bran and the composite microbial agent to obtain a mixed material, sealing and fermenting the material for 5-7 days to obtain a fermentation liquid, filtering the liquid, mixing nitrogen, phosphorus and potassium nutrients with the obtained filtrate to obtain a finished product.
NOVELTY - An organic fertilizer preparing method involves collecting fresh horse manure, crushing wheat and rice waste, and tobacco leaf. The crushed materials are mixed in a fermentation tank. Water is added to the crushed material. The tank is covered with a plastic film. The crushed particles are stacked to obtain fermentation microbial inoculum. The wheat straw and waste of tobacco leaf are piled. Urea and magnesium sulfate are mixed in the fermentation microbial inoculum. The materials are stacked to obtain the organic fertilizer.    USE - Method for preparing organic fertilizer that is utilized for killing pathogenic microorganism and preventing wheat straw and tobacco leaf.    ADVANTAGE - The method enables preparing organic fertilizer with low cost and labor intensity, quick rotten and high fermentation temperature in a simple manner.    DETAILED DESCRIPTION - An organic fertilizer preparing method involves collecting fresh horse manure, crushing wheat and rice waste, and tobacco leaf to 3-5 mm. The crushed materials are mixed in a ratio 40: 50: 50: 1 in a fermentation tank. Water is added to the crushed material. The tank is covered with a plastic film. The crushed particles are stacked for 2-24 days to obtain the fermentation microbial inoculum. The wheat straw and waste of tobacco leaf are piled, where the straw and leaf weight is 100 kg. 500 g urea and 100 g magnesium sulfate are mixed in the fermentation microbial inoculum. The materials are stacked for 6-90 days till the wheat straw and waste tobacco leaf are turned in to brown to obtain the organic fertilizer.
NOVELTY - An organic fertilizer preparing method involves taking a fermentation tank with a light transmittance sunlight panel at lower and upper parts with a vent hole for an aeration pipe. Waste tobacco leaf and fresh horse manure are mixed and placed in the tank. The tank is covered with a plastic film. The stack is left for 2-28 days to obtain fermentation microbial inoculum. The crushed waste tobacco leaf, urea and magnesium sulfate are added to the fermentation microbial inoculum. The tank is stacked and fed once every 6 hours with an air compressor by an air pipe to obtain organic fertilizer.    USE - Method for preparing an organic fertilizer.    ADVANTAGE - The method enables preparing organic fertilizer with low cost, quick rotten, high fermentation temperature, effective killing of pathogenic microorganism disease, and in a simple manner.    DETAILED DESCRIPTION - An organic fertilizer preparing method involves taking a fermentation tank with light transmittance sunlight panel at bottom and upper part with vent hole for aeration pipe. Waste tobacco leaf is crushed and fresh horse manure is collected. The waste tobacco leaf and fresh horse manure are mixed in a ratio 100:25-30:2 and placed in tank. The tank is covered with plastic film and for every 7 days the stack is mixed. The stack is left for 2-28 days to obtain fermentation microbial inoculum. The crushed waste tobacco leaf, urea and magnesium sulfate are added to the fermentation microbial inoculum. The fermentation tank is stacked for 3 days and fed once every 6 hours with air compressor by air pipe air to obtain organic fertilizer, where each ton of waste tobacco leaf comprises 2.5 kg urea and 2.5 kg ammonium phosphate.
NOVELTY - A biological organic fertilizer comprises 60-65 pts. wt. rice bran, 6-7 pts. wt. sepiolite powder, 8-10 pts. wt. waste lees, 2-4 pts. wt. rice, 10-15 pts. wt. bone powder, 3-5 pts. wt. flour, 4-6 pts. wt. edible fungi slag, 4-6 pts. wt. grape fruit peel, 10-15 pts. wt. slag, 2-3 pts. wt. phosphogypsum, 2-3 pts. wt. Ryegrass, 4-5 pts. wt. Loquat leaf, 54-60 pts. wt. swill, 10-13 pts. wt. brown sugar and 74-80 pts. wt. animal.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer has high organic matter content, better soil quality and structure, and achieves better ecological balance and nutrition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biological organic fertilizer, which involves adding the flour with 6-8 pts. wt. water, heating at 80-90 degrees C, stirring the heated material and adding the rice bran, sepiolite powder, waste distilled grain, stirring and dispersing for 20-30 minutes, followed by drying and granulating into 2 mm, dissolving the brown sugar in 1.8-2 pts. Wt. clean water, adding 10-15% brown sugar fermenting agent, and stirring and fermenting for 15-20 days at 30-40 degrees C, and adding 1-2% ferrous sulfate and stirring uniformly to obtain fermentation liquid, adding the bone powder, loquat leaf, fruit residue with 0.5-0.8% EM bacteria liquid and 60-65% water content and heating for 3-5 hours to obtain material-A, stacking the material-A and added with remaining raw materials, followed by adding 2-4% humic acid with 0.1-0.2% Chinese herbal medicine and stirring uniformly for 10-12 hours, adding material-B and stirring, stacking for 2-4 hours, and drying to obtain the biological organic fertilizer, where the Chinese herbal medicine comprises 7-10 pts. wt. herba Houttuyniae, 10-15 pts. wt. Unbracteolated Spurge Root, 4-7 pts. wt. cotton root and 2-3 pts. wt. folium Artemisiae Argyi.
NOVELTY - A biological organic fertilizer comprises 63-73 pts. wt. grass, 14-19 pts. wt. ammonium chloride, 8-11 pts. wt. hydrolyzed feather powder, 2-3 pts. wt. Gnetum montanum, 3-4 pts. wt. watermelon, 5-10 pts. wt. bran, 9-15 pts. wt. flour, 2-3 pts. wt. perilla, 4-5 pts. wt. fly ash, 4-6 pts. wt. pear tree root powder, 2-3 pts. wt. towel gourd, 1-2 pts. wt. boric acid, 1-2 pts. wt. oil shale, 63-70 pts. wt. swill, 11-17 pts. wt. brown sugar and 75-80 pts. wt. animal feces.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer has high organic matter content and rich nutrition content, and improves quality and structure of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method preparing a biological organic fertilizer, which involves adding flour with water, heating the obtained mixture, adding grass, ammonium chloride, hydrolyzed feather powder with the mixture, stirring and dispersing the mixture for 20-30 minutes, drying and granulating the mixture, preparing brown sugar fermentation liquid by adding brown sugar with fermenting agent, wintergreen and alum, mixing bran, watermelon and pear tree root powder with EM bacteria liquid, adding water with the obtained material, mixing rest of raw materials, humic acid and Chinese herbal medicine with the obtained material, stirring the material, fermenting the material for 10-12 hours, and drying the fermented material to obtain a finished product.
NOVELTY - A biological organic fertilizer comprises 52-60 pts. wt. plant ash, 8-10 pts. wt. stone powder, 7-10 pts. wt. alum powder, 3-4 pts. wt. wolfberry leaves, 12-17 pts. wt. tea leaves, 3-5 pts. wt. flour, 3-6 pts. wt. borax, 3-4 pts. wt. sands vine, 8-15 pts. wt. peanut vine powder, 2-4 pts. wt. potassium chloride, 7-10 pts. wt. soy sauce residue, 3-5 pts. wt. sunflower seed, 55-60 pts. wt. swill, 10-12 pts. wt. brown sugar and 70-80 pts. wt. animal feces.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer improves soil quality, maintains ecological balance, and provides large active substances and high organic matters to improve fertility of soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a biological organic fertilizer, which involves adding flour with 6-8 times of water at 80-90 degrees C and stirring to obtain a mixture, adding plant ash, stone powder and soy sauce residue into the mixture, stirring and dispersing for 20-30 minutes, drying and granulating the dispersed mixture to obtain a granulated mixture A, adding the brown sugar with 1.8-2 times of clean water, wintergreen and alum, stirring and fermenting for 15-20 days at 30-40 degrees C, agitating 1-2 wt.% manganese sulfate to obtain a fermentation liquid B, adding soy sauce residue, sunflower seed, peanut vine powder, 0.5-0.8% EM bacteria liquid and 60-65 wt.% saliva at normal temperature for 3-5 hours to obtain a material C, mixing A and B mixtures with rest raw material, 2-4 humic acid mixed material and 0.1-0.2 wt.% Chinese herbal medicine uniformly, fermenting for 10-12 hours at normal temperature to obtain a fermented mixture, adding material B with the fermented mixture, followed by fermenting for 2-4 hours and drying to obtain a finished product.
NOVELTY - A biological organic fertilizer comprises 30-40 pts. wt. cassava slag, 15-20 pts. wt. ammonium hydrogen carbonate, 25pts. wt. dyers woad powder, 3-4 pts. wt. alum powder, 6-8 pts. wt. plant ash, 4-5 pts. wt. flour, 4-5 pts. wt. grass meal, 10-15 pts. wt. brown sugar, 1-2 pts. wt. vegetable oil, 6-8 pts. wt. bamboo leaves powder, 15-20 pts. wt. bran, 4-6 pts. wt. citric acid residue, 50-60 pts. wt. swill, 10-15 pts. wt. sawdust, 4-6 pts. wt. sweet clover powder and 60-80 pts. wt. animal/human feces.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer has rich nutrition, and improves soil quality with ecological balance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biological organic fertilizer, which involves mixing the flour and the grass meal with water, stirring the obtained mixture at 80-90 degrees C, adding the cassava slag, the ammonium hydrogen carbonate and the vegetable oil with the stirred mixture, dispersing the stirred mixture for 20-30 minutes, drying and granulating the dispersed mixture, adding the brown sugar and clean water into the granulated mixture, adding brown sugar fermenting agent and the alum into the dissolved solution, stirring and fermenting the solution at 30-40 degrees C for 15-20 days, adding the water, the plant ash, the bamboo powder, the bran, the citric acid residue and EM bacteria liquid into the obtained fermented liquid, mixing humic acid and Chinese medicinal herb with the obtained fermented liquid, stirring the liquid at normal temperature for 10-12 hours followed by turning, adding, drying the liquid to obtain a finished product, where the chinese herbal medicine comprises 10-20 pts. wt. Houttuynia cordata, 8-10 pts. wt. pepper straw, 6-8 pts. wt. cotton root, 4-6 pts. wt. Radix stemonae and 2-4 pts. wt. sunflower.
NOVELTY - An organic fertilizer comprises 10 pts. wt. sugar dregs, 32 pts. wt. humic acid, 10 pts. wt. amino acid, 10 pts. wt. plant ash, 10 pts. wt. lignin, 15 pts. wt. medical dregs, 8 pts. wt. bentonite and 5 pts. wt. biological germ.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer containing sugar dregs is simple and convenient to prepare, and the addition of sugar dregs after smashing and fermenting enables the forming effect in pelleting to be good. The addition of abundant humic acid promotes the sugar dregs to transfer into the components that the crop can absorb and being absorbed by the crop, so as to increase the sugar content of the crop, and enable the nutrition of the crop to be more comprehensive.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an organic fertilizer, which involves uniformly mixing and stirring 10 pts. wt. sugar dregs, 32 pts. wt. humic acid, 10 pts. wt. amino acid, 10 pts. wt. plant ash, 10 pts. wt. lignin, 15 pts. wt. medical dregs, 8 pts. wt. bentonite and 5 pts. wt. biological germ, crushing the obtained mixture to obtain the mixed material, fermenting the mixed material at a temperature of 71 degrees C for 9 days, controlling the pH value of the mixed material to 6-7.8, carrying out fermentation after granulating, drying and filtering to obtain the organic fertilizer.
NOVELTY - An organic fertilizer comprises 19 pts. wt. bean meal, 10 pts. wt. pulp powder, 23 pts. wt. cortex, 14 pts. wt. mushroom residue, 9 pts. wt. bone cement, 12 pts. wt. sugar slag, 8 pts. wt. bentonite and 5 pts. wt. biological bacteria.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer has high effect in promoting growth of crops, high content of yeast fermentation, promoted organic fertilizer in the organic matter and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves mixing 19 pts. wt. soybean meal, 10 pts. wt, 10 pts. wt. pulp powder, 23 pts. wt. cortex, 14 pts. wt. mushroom residue, 9 pts. wt. bone cement, 12 pts. wt. sugar slag, 8 pts. wt. bentonite and 5 pts. wt. biological bacteria, stirring uniformly, fermenting at 70 degrees C for 8 days, mixing everyday, controlling the pH value of the mixed material to 6-7, drying and filtering to obtain the biological nutrient content of organic fertilizer.
NOVELTY - An organic fertilizer comprises 15 pts. wt. prickly ash meal, 15 pts. wt. bean pulp, 10 pts. wt. plant ash, 15 pts. wt. medicine dregs, 20 pts. wt. corn slag, 15 pts. wt. bone powder, 10 pts. wt. bentonite, 10 pts. wt. biological bacteria, 4.5 pts. wt. trace element, 0.5 pts. wt. normal methylmorpholinenoxide.    USE - Organic fertilizer.    ADVANTAGE - The organic fertilizer has medical value and synergistic effect, reduces crop diseases and insect pests, preserves the ecological environment, improves yield of crops, and is low in cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves mixing 15 pts. wt. prickly ash meal, 15 pts. wt. bean pulp, 10 pts. wt. plant ash, 15 pts. wt. medicine dregs, 20 pts. wt. corn slag, 15 pts. wt. bone powder, 10 pts. wt. bentonite, 10 pts. wt. biological bacteria, 4.5 pts. wt. trace element, 0.5 pts. wt. normal methylmorpholinenoxide, stirring uniformly, fermenting mixed material, heating at 72 degrees C for 11 days, mixing material every day, controlling the pH value of the mixed material to 6-8, drying and filtering to obtain medicine slag.
NOVELTY - An organic fertilizer comprises 12 pts. wt. protein, 20 pts. wt. humic acid, 15 pts. wt. fungus mud, 8 pts. wt. bone powder, 10 pts. wt. cassava residue, 10 pts. wt. sugar dreg, 15 pts. wt. furfural dreg and 10 pts. wt. bentonite.    USE - Organic fertilizer for crops.    ADVANTAGE - The fertilizer reduces disease rate and improves yield of crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves utilizing the mentioned component as raw materials, mixing the materials, stirring, crushing the mixed material, granulating, fermenting the crushed material at 72 degrees C for 10 days, controlling pH value of the mixed material to 6.5-8, drying and filtering the fermented material to obtain the organic fertilizer.
NOVELTY - An organic fertilizer comprises 15 pts. wt. pepper meal, 15 pts. wt. humic acid, 10 pts. wt. amino acid, 5 pts. wt. cigarette foam, 30 pts. wt. bacterial sludge, 10 pts. wt. starch dreg, 10 pts. wt. bentonite and 5 pts. wt. biological germ.    USE - Organic fertilizer for crop.    ADVANTAGE - The fertilizer improves crop manufacturing efficiency, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a biological bacteria organic fertilizer, which involves weighing and mixing the above mentioned raw materials to obtain mixed material, carrying out fermentation process with the mixed material at 72 degrees C for 11 days, controlling the pH of the mixed material at 6-8, granulating, drying and filtering the obtained decoction to obtain hot pepper, and preparing organic fertilizer.
NOVELTY - An organic inorganic compound fertilizer comprises 23 pts. wt. urea, 15 pts. wt. ammonium dihydrogen phosphate, 18 pts. wt. potassium sulfate, 24 pts. wt. humic acid, 10 pts. wt. cigarette foam, 5 pts. wt. bentonite and 5 pts. wt. biological bacteria.    USE - Organic inorganic compound fertilizer.    ADVANTAGE - The fertilizer promotes growth of the crop, and is good in forming in pelleting, and the cigarette foam is turned into a valuable ingredient, so as to alleviate pollution to the environment of fertilizer fertilization.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic inorganic compound fertilizer, which involves weighing the components, mixing and stirring uniformly, and fermenting the mixture at 70 degrees C for 13 days, and the pH value in fermentation controlled to 6-7, and the mixture after fermentation, and drying.
NOVELTY - An organic fertilizer comprises 12 pts. wt. mycoprotein, 20 pts. wt. humic acid, 15 pts. wt. bacterial sludge, 8 pts. wt. bone meal, 10 pts. wt. manioc dreg, 10 pts. wt. sugar dreg, 10 pts. wt. furfural dreg, 10 pts. wt. bentonite and 5 pts. wt. biological bacteria.    USE - Organic fertilizer.    ADVANTAGE - The fertilizer reduces disease rate and improves yield rate of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic fertilizer, which involves weighing the mentioned raw materials, crushing and mixing the mentioned materials to obtain mixed material, fermenting the mixed material at 72 degrees C for 10 days, controlling pH value of the mixed material to 6.5-8 and granulating, filtering and drying the fermented material to obtain a finished product.
NOVELTY - An organic water soluble fertilizer is prepared by utilizing less than or equal to 50 billion/ml viable bacteria, less than or equal to 100 g/l amino acid, 4-150 g/l humic acid and less than or equal to 30 g/l calcium-magnesium element as raw material, adding microbial inoculum fertilizer, fermenting the fertilizer, extracting amino acid to obtain free amino acid solution, mixing the raw materials and evaporating and concentrating the mixed materials at less than or equal to 50 degrees C.    USE - Organic water soluble fertilizer for protecting root and soil.    ADVANTAGE - The fertilizer has balanced nutrition and simple and convenient preparation process, and saves labor and improves soil structure and crop resistance to pests and diseases.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing organic water soluble fertilizer.
NOVELTY - A soil improvement bactericide comprises 30-40 pts. wt. earthworm manure, 40-50 pts. wt. humic acid raw powder, 4-10 pts. wt. potassium hydroxide and 5-15 pts. wt. micro-organism strain as main materials and 1-5 pts. wt. wetting dispersant as an auxiliary material.    USE - Soil improvement bactericide.    ADVANTAGE - The bactericide has high organic content, strong biological activity, rich nutrition content and effects of increasing roots, strengthening seedling, resisting stress, resisting lodging, promoting precocity, resisting residue, preventing pollution, increasing yield and improving soil quality, and can be prepared in a simple, cost-effective and easy manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a soil improvement bactericide, which involves adding the potassium hydroxide added with the humic acid raw powder in a reaction kettle, adding water to the kettle, heating the kettle at 50-70o?C, and drying and crushing the obtained product to obtain potassium humate, crushing and sieving the earthworm manure, mixing the potassium humate, the obtained earthworm manure powder, the micro-organism strain, and the wetting dispersant, adding water with the obtained mixture, stirring the mixture, drying and crushing the mixture to obtain a finished product.
NOVELTY - A polylactide-loaded prodrugs (I)-(III) are new.    USE - Polylactide-loaded prodrug (claimed).    ADVANTAGE - The polylactide-loaded prodrug controls drug loading capacity, and is economically prepared with excellent hydrophilic property without polluting the environment, by a simple method.    DETAILED DESCRIPTION - A polylactide-loaded prodrugs of formula (I)-(III) are new.    x,x1=0-100;    y,y1+z1=1-100;    n=10-100;    R1=1-3C alkoxy;    R2=-(C(-H)2)m-;    m=1-5;    R3=-(C(-H)2)r-;    r=2-5;    R4=-(CH2-C(-OH)-CH2-OH), -(CH2-CH2-C(-OH)-CH2-OH), -(CH2-C(-OH)-CH2-CH2-OH), -(CH2-CH2-CH2-C(-OH)-CH2-OH), or -(CH2-C(-OH)-CH2-CH2-CH2-OH);    R5=-(CH2-C(-O-B')-CH2-OH) or -(CH2-C(-OH)-CH2-O-B'), -(CH2-CH2-C(-O-B')-CH2-OH) or -(CH2-CH2-C(-OH)-CH2-O-B'), -(CH2-C(-O-B')-CH2-CH2-OH) or -(CH2-C(-OH)-CH2-CH2-O-B'), -(CH2-CH2-CH2-C(-OH)-CH2-O-B') or -(CH2-CH2-CH2-C(-O-B')-CH2-OH), -(CH2-CH2-C(-OH)-CH2-CH2-O-B') or -(CH2-CH2-C(-O-B')-CH2-CH2-OH), or -(CH2-C(-OH)-CH2-CH2-CH2-O-B') or -(CH2-C(-O-B')-CH2-CH2-CH2-OH);    R6=-(CH2-C(-O-B')-CH2-O-B'), -(CH2-CH2-C(-O-B')-CH2-O-B'), -(CH2-C(-O-B')-CH2-CH2-O-B'), -(CH2-CH2-CH2-C(-O-B')-CH2-O-B'), -(CH2-CH2-C(-O-B')-CH2-CH2-O-B') or -(CH2-C(-O-B')-CH2-CH2-CH2-O-B');and    B',D'=hydroxy group-containing drug molecules or carboxy group-containing side polylactide after esterification reaction.    An INDEPENDENT CLAIM is included for preparation of polylactide-loaded prodrug.
NOVELTY - A sandy soil additive comprises 50-60 wt.% fungus chaff, 35-40 wt.% biogas and 5-10 wt.% horse dung.    USE - Sandy soil additive.    ADVANTAGE - The method enables preparing sandy soil additive with simple and easy manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for method for preparing sandy soil additive, which involves mixing fungus chaff, biogas and horse dung in a fermentation tank and covering air hole with a fermentation cover. The mixture is decayed for plastic greenhouses at temperature 25-30 degrees C in day time and 20-25 degrees C in night time for 50-80 days and decomposing period for turning every 4 days, adding proper amount of water, and fermenting for 50-80 days to obtain a finished product, where the horse dung is rich in microorganism bacteria bran corrosion solution.
NOVELTY - Extracting Boninic acid from Ramalina boninensis (Y. Asahina) involves crushing the plant leaves into coarse powder, putting in extraction tank containing CO2 and entrainer for supercritical fluid extraction and collecting extract; dissolving obtained extract in methanol, loading onto high pressure dry silica gel column chromatography, eluting by using methylene dichloride-acetone as solvent system, collecting the acid stream, decompressing and concentrating under reduced pressure, and drying to obtain crude product; and dissolving the crude product in ethyl acetate-ethanol.    USE - For extracting boninic acid (claimed) which is useful as anti-inflammatory drug and for inhibiting growth of Staphylococcus aureus.    ADVANTAGE - The present method is simple and rapid; has low energy consumption; is environment-friendly production technique which is suitable for mass production; and provides product in high yield and high purity.    DETAILED DESCRIPTION - Extracting Boninic acid from Ramalina boninensis (Y.Asahina) involves: crushing the leaves of the plant into coarse powder, putting in extraction tank containing CO2 and entrainer (preferably 90-99% ethanol solution) for supercritical fluid extraction at extracting pressure of 38-45 MPa, temperature of 35-50 degrees C, time of 1-2 hours, then purging at 30-40 degrees C and pressure of 6-8 MPa, and collecting the extract; dissolving the obtained extract in methanol, loading onto high pressure dry silica gel column chromatography, eluting by using methylene dichloride-acetone as solvent system, collecting the acid stream, decompressing and concentrating under reduced pressure, and drying to obtain crude product; and dissolving the crude product in ethyl acetate-ethanol, refluxing and crystallizing to obtain the product. The vol. ratio of methylene:acetone is 13-2:3; and ethyl acetate-ethanol is 6:1.
NOVELTY - Preparing confusarin involves crushing horse penis, dendrobe raw material into 20-80 meshes, putting into carbon dioxide supercritical extracting tank, extracting at 30-60 degrees C, dissolving the extract by chloroform, filtering, recycling reagent to obtain crude extract; serving stationary phase of crude extract as fixing phase and bottom phase as a mobile phase by taking trichloromethane, methanol and water as solvent system, performing purification via high-speed counter-current chromatography, collecting distillate; and drying the distillate under reduced pressure, to obtain confusarin.    USE - For preparation of confusarin (claimed), which is used in medicament.    ADVANTAGE - The process is simple and convenient to operate; avoids or minimizes pollution; prepares confusarin in high product purity, so that industrialized amplification is easy to realize.    DETAILED DESCRIPTION - Preparation of confusarin involves crushing horse penis, dendrobe raw material into 20-80 meshes, putting into carbon dioxide (CO2) supercritical extracting tank, extracting at 30-60 degrees C, and at a pressure of 20-30 Mpa for 1-4 hours, dissolving the extract by chloroform, filtering, recycling reagent to obtain crude extract; serving a stationary phase of the crude extract as a fixing phase and a bottom phase of the crude extract as a mobile phase by taking the trichloromethane, methanol and water as a solvent system, performing purification via high-speed counter-current chromatography, collecting a distillate; and drying the distillate under reduced pressure, to obtain confusarin.
NOVELTY - Method of using biological technique for processing household garbage comprises breaking and crushing household garbage, adding straw, stirring, adding composite microbial bactericide, adding deodorizer, fermenting, and synthetically sorting according to (i) metal for recovery processing, (ii) selected plastic materials, packaging, recycling or making wood boards, (iii) comprehensive object including brick stone whetstone piece which can be landfilled, un-recyclable combustible species; or (iv) rest organic matter garbage fermentation and/or sandy soil, which is an organic fertilizer.    USE - Method of using biological technique for processing household garbage (claimed).    ADVANTAGE - The method allows processing of 100-120 tons of garbage daily, provides garbage degradation of 80%, reduces labor by 60% for later period comprehensive sorting and reduces cost by 25%.    DETAILED DESCRIPTION - Method of using biological technique for processing household garbage comprises putting household garbage into storage tank, breaking and crushing in plate-type feeding machine feeding bag breaking machine, adding 5-15 wt.% straw, mixing and stirring, adding 0.5-2 wt.% composite microbial bactericide for aerobic composting and fermenting, adding 8-12 wt.% deodorizer, stacking, ventilating and fermenting at 45-65 degrees C, and humidity of 40%-50% 14-18 days, turning for 3-5 times, then synthetically sorting according to (i) metal for recovery processing, (ii) selected plastic materials, packaging, recycling or making wood boards, (iii) comprehensive object including brick stone whetstone piece which can be landfilled, un-recyclable combustible species; or (iv) rest organic matter garbage fermentation and/or sandy soil, which is an organic fertilizer.
NOVELTY - 60-85 wt.% 99.9% Refined methanol is added to a reaction kettle, and 5-20 wt.% octane number regulator, 1-35 wt.% cold start accelerant, and 0.06-0.09 wt.% cosolvent are added and stirred. 0.03-0.05 wt.% Antioxidant anticorrosion detergent and 0.001 wt.% coloring agent are then added to the resultant mixture, continuously stirred for 30-60 minutes, filtered, and depositing for 24 hours to obtain hydrocarbon oil.    USE - Preparation of hydrocarbon oil for spark-ignition engine.    ADVANTAGE - The method efficiently provides hydrocarbon oil which does not layered and emulsified in 180 days. Emission is reduced by 70-90%; using the hydrocarbon oil. The hydrocarbon oil is economical, and has octane number of 95-97.
NOVELTY - Nilotinib is obtained by carrying out one-step condensation reaction on 4-(3-pyridyl)-2-pyrimidone, methyl/ethyl/benzyl 3-amino-4-methyl benzoate, and 5-(4-methyl-1H-imidazol-1-yl)-3-trifluoromethyl phenylamine in the presence of an organic alkali and a condensing agent.    USE - Preparation of nilotinib for pharmaceuticals.    ADVANTAGE - The method enables simple, economical and environmentally-friendly industrial preparation of high-quality nilotinib by using easily available raw materials, under mild conditions.
NOVELTY - A cordyceps sinensis absorption and production method utilization rate improving method involves selecting cordyceps sinensis stock material and removing impurities to obtain clean raw material. The cleaned raw material is crushed into cordyceps sinensis powder. Impurities of the cordyceps sinensis powder are discharged and extracted. The liquid is extracted by filtering, and absorbing clear liquid part is condensed into a paste. The concentrated paste is dried under vacuum condition. The dried paste is crushed into cordyceps sinensis extract dry powder.    USE - Method for improving cordyceps sinensis absorption and production method utilization rate.    ADVANTAGE - The method enables improving cordyceps sinensis absorption and production method utilization rate without toxic substance and with improved cordyceps sinensis solubility and increased functional component content in simple and efficient manner.    DETAILED DESCRIPTION - A cordyceps sinensis absorption and production method utilization rate improving method involves selecting cordyceps sinensis stock material and removing impurities to obtain clean raw material. The cleaned raw material is crushed into 20-600 mesh cordyceps sinensis powder. Impurities of the cordyceps sinensis powder are discharged and extracted at 30-85 degrees C for 0.5-6 hours. The liquid is extracted by filtering, and absorbing clear liquid part is condensed into a paste by low temperature heating at 40-65 degrees C. The concentrated paste is dried for 0.5-5 hours under vacuum condition at 50-90 degrees C. The dried paste is crushed into 40-120 meshes cordyceps sinensis extract dry powder.
NOVELTY - This utility model claims a kind of low temperature pyrolysis biomass steam production system for active carbon and hydrogen, comprising a biomass pre-processing drying unit (1), water vapour and low temperature pyrolysis unit (2), a high temperature cyclone separating unit (3), a catalytic reforming unit (4), cooling and purifying the hydrogen separating unit (5), wherein the biomass pre-processing drying unit (1) are connected with the low temperature pyrolysis steam unit (2), a high temperature cyclone separating unit (3), a catalytic reforming unit (4), a hydrogen cooling purifying and separating unit (5) is the gas outlet of the biomass drying pre-processing unit (1) and the high temperature cyclone separating unit (3). The utility model not only improves the heat utilization rate in the pyrolysis process, reduces the subsequent pyrolysis section of the dust and tar content in the air, and simplifies the active carbon and production technique, low investment of the hydrogen and low energy consumption.
NOVELTY - A kind of sediment cleaning device, comprising a draining pipe (2), the outlet pipe (2) of the outer side is provided with an air inlet pipe (1) and a water inlet pipe (3) (5), wherein the air inlet pipe (1) and outlet (17) is connected with the outlet of the water pump inlet pipe ((6, 3) are connected the pipe inlet (7) of the shell (2), a feeding pool end of the draining pipe (2) is connected with the residue pumping car, sewage inlet connected with the air inlet pipe (1) is connected with the air pump air outlet is connected with the water inlet of the water inlet pipe (3) is connected with the external water pipe is connected with the discharging pipe (2) in the left and right, front and back directions of the tank are respectively provided with a left pull rope (11) and the right pull rope (12), a front pull rope (13) and the pull rope (14). The structure is simple, the cost is low, it is convenient to use with good effect, capable of completely removing all sediment.
NOVELTY - Preparation of pantoprazole sodium involves reacting chlorine with 2-hydroxymethyl-3,4-dimethoxy pyridine (II) as raw material and obtaining generating 2-chloromethyl-3,4-dimethoxy pyridine hydrochloride (III), carrying out condensation of the obtained compound (III) and 5-difluoromethoxy-2-sulfydryl-1H-benzimidazole in presence of inorganic base and obtaining 5-difluoromethoxy-2-((3,4-dimethoxy-2-pyridyl)methyl) sulfenyl-1H-benzimidazole, oxidizing the obtained compound (IV) by using oxidant and obtaining 5-difluoromethoxy-2-((3,4-dimethoxy-2-pyridyl)methyl)sulfinyl-1H-benzimidazole.    USE - Preparation of pantoprazole sodium (claimed).    ADVANTAGE - The method efficiently and economically provides pantoprazole sodium having high purity.    DETAILED DESCRIPTION - Preparation of pantoprazole sodium involves reacting chlorine with 2-hydroxymethyl-3,4-dimethoxy pyridine (II) as raw material and obtaining generating 2-chloromethyl-3,4-dimethoxy pyridine hydrochloride (III), carrying out condensation of the obtained compound (III) and 5-difluoromethoxy-2-sulfydryl-1H-benzimidazole in presence of inorganic base and obtaining 5-difluoromethoxy-2-((3,4-dimethoxy-2-pyridyl)methyl) sulfenyl-1H-benzimidazole, oxidizing the obtained compound (IV) by using oxidant and obtaining 5-difluoromethoxy-2-((3,4-dimethoxy-2-pyridyl)methyl)sulfinyl-1H-benzimidazole, reacting 5-difluoromethoxy-2-((3,4-dimethoxy-2-pyridyl)methyl)sulfinyl-1H-benzimidazole with sodium hydroxide, and purifying product.
NOVELTY - This utility model claims a joint method for restaurant and kitchen rubbish ethanol and lactic acid. The device comprises a hydro-thermal reactor, which is used for separating the solid phase of the kitchen garbage conveying to the fermentation tank from the hydro-thermal reactor of the spiral conveyor and the fermentation tank for the solid phase of the kitchen garbage to the spiral conveyer of the fermentation tank from the hydro-thermal reactor is set in a hydrothermal reactor and the fermentation tank and fermentation tank comprises a fermentation chamber and a lactic acid fermentation. The utility model coupling kitchen garbage hydro-thermal treatment, three-phase separation, fermentation device, which greatly reduces the consumption of the energy, at the same time can realize continuous feeding, the kitchen waste processing efficiency. By the utility model, the kitchen garbage and hydro-thermal treatment, the oil, water and slag layering, easy three-phase separation, the waste oil after separating can be deeply processed into biological diesel oil, organic matter of microorganism fermenting fuel ethanol and/or lactic acid, the fermentation residue is used to produce derived fuel or fertilizer.
NOVELTY - This utility model claims a kind of injector air power device, a common battery supplies direct current electricity, the electrolytic cell principle electrolytic chamber under a certain current and voltage of the cathode plate and the anode plate in the electrolyte to generate hydrogen and oxygen respectively enter into electrolytic compensating chamber through pipeline, the electrolytic compensation solution into electrolytic chamber compensation electrolyte loss in gas pressure, so as to separate hydrogen and oxygen output, which can be used as the power source of the gas injector to push the injector, this utility model has simple structure, and the safety factor is high, which greatly reduces the volume of the injection pump, it is convenient to carry, easy to replace and maintain, long service life, low cost, and the electrolytic water generated by the gas without environment pollution.
NOVELTY - The bio-toilet has a solid-liquid separator whose outlet is connected with a fermentation device of a fermentation tank that is provided with a stirring device, where one end of the fermentation tank is provided with a feeding port and another end of the fermentation tank is equipped with a discharging port. The stirring device is provided with a support frame that is arranged on front of the fermentation device. A stirring shaft is provided with a spiral belt, where the stirring shaft corresponding to spiral screws is arranged with a stirring rod.    USE - Resource type bio-toilet.    ADVANTAGE - The bio-toilet allows excrement to be conveniently and effectively processed without consumption of energy resources and electricity or natural gas for heating in fermentation process so as to save energy resources.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for processing dispose excrement.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a resource type bio-toilet.
NOVELTY - A matrine agent production method involves carrying out enzymolysis on crushed radix Sophora flavescens raw material by using a composite bio-enzyme, and extracting enzymolysis liquid. The liquid is filtered and concentrated to obtain a radix Sophora flavescens concentrated liquid. The concentrated liquid is compounded with phytoextraction intermediates. Agents and surfactants are stabilized to obtain matrine agent.    USE - Method for producing a matrine agent.    ADVANTAGE - The method enables producing a matrine agent with high insecticidal performance, high storage stability, low toxicity and no pesticide residue in a convenient and environment-friendly manner.
NOVELTY - An organic fertilizer preparing method involves taking 65-75 wt.% straw, 15-25 wt.% sawdust, 5-15 wt.% shell skin, 0.5-2 wt.% calcium oxide, performing pyrolysis of potassium carbonate and calcium, magnesium, sulfur, phosphorus, iron, small amounts of boron, aluminum, manganese and other trace raw materials, such as animal manure, garbage, litter rotten leaves, biogas, waste bacteria and other organic fertilizer materials. The materials are stacked for fermentation. The materials are crushed and mixed. The crushed materials are dried. The dried materials are packed and stored.    USE - Method for preparing biomass boiler ash organic fertilizer.    ADVANTAGE - The method enables preparing organic fertilizer that has low cost, anti-pollution effect, outstanding economic benefit and recyclable property.
NOVELTY - A biological expanded graphite preparation method involves adding composite strain liquid to a dispersing medium containing persistent organic pollutant. The mixture is stirred, and incubation is carried out to obtain fixed bacteria degrade biological expanded graphite, where incubation is performed by Bacillus licheniformis, Bacillus pumilus, Bacillus subtilis and Alcaligenes. The persistent organic pollutant kept in a culture medium to obtain the mixed strain liquid and biological expanded graphite is added to the aerobic composting.    USE - Method for preparing a biological expanded graphite that is utilized for removing persistent organic pollutants out of composting sludge.    ADVANTAGE - The method enables preparing the biological expanded graphite with better hydrophobicity, better adsorptivity and better biodegradability, and avoids secondary pollution.    DETAILED DESCRIPTION - A biological expanded graphite preparation method involves adding 10-30 ml composite strain liquid to a dispersing medium containing persistent organic pollutant. The mixture is stirred, and incubation is carried out for 3-5 days to obtain fixed bacteria degrade biological expanded graphite, where incubation is performed by ray fungi, Chrysosporium fungus, Bacillus licheniformis, Bacillus pumilus, Bacillus subtilis and Alcaligenes. The persistent organic pollutant kept in a culture medium for 5-7 days to obtain the mixed strain liquid and biological expanded graphite is added to the aerobic composting.
NOVELTY - A combustion gas preparation method involves subjecting kitchen rubbish and/or organic waste to biochemical fermentation in presence of acid-producing bacteria and hydrogen-producing acetogenic bacteria. The fermented product is subjected to methane gas purification and compression.    USE - Method for preparing combustion gas for vehicle and ship engine.    ADVANTAGE - The method enables accelerating fermentation speed, realizing effective recycling of hydrogen and meeting quality standards of fuels.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for preparing combustion gas. '(Drawing includes non-English language text)'
NOVELTY - An amino-sugar compound (I) is new.    USE - Amino-sugar compound for use as plant immune activator.    ADVANTAGE - The amino sugar compound effectively activates plant cells, induces plant immune system, improves disease-resistant and virus-resistant capability in plants, strengthens plant stress resistance against dry and cold weathers, promotes crop growth and improves yield and quality of crops, and is non-toxic, pollution-free and safe.    DETAILED DESCRIPTION - An amino-sugar compound of formula (I) is new.    R1 = H or CH3;    R2 = 2-16C, 3-16C, 1-18C, 3-18C, 4-18C, 3-20C or 4-20C;    R3, R4 = H or Cb;    b = not defined;    R5 = H or acetate;    R6 = H, acetate, sulfate, Fuc, AcFuc or MeFuc;    R7 = H or CH2OHCHOHCH2OH; and    n = 1-4.
NOVELTY - Rooting liquid fertilizer comprises 20-80 pts. wt. concentrated amino acid fermentation broth, 15-30 pts. wt. urea, 5-20 pts. wt. potassium fulvate, 10-20 pts. wt. alginic acid, 5-15 pts. wt. chitosan, 10-30 pts. wt. Bacillus subtilis, 5-20 pts. wt. alpha -naphthalene acetic acid, 10-35 pts. wt. sodium nitrophenolate, 1-4 pts. wt. indole butyric acid potassium salt, 5-15 pts. wt. nitric acid and 10-20 pts. wt. calcium nitrate.    USE - Rooting liquid fertilizer.    ADVANTAGE - The rooting liquid fertilizer has high purity nutrients, and provides superior activity after application in site and crop nutrient to quickly restore crop health. It has good water solubility and absorption, environment friendly, does not produce residue, and does not cause greenhouse crop damage.
NOVELTY - Liquid microbial fertilizer comprises polyglutamic acid composition comprising microbial fermentation broth, complex nutrient, and gamma -polyglutamic acid are in a ratio of 1:1:0.05-0.1, where the microbial fermentation broth comprises Bacillus thuringiensis, B.amyloliquefaciens, and B.megaterium in a mass ratio of 1:1:1, and complex nutrients comprises nitrogen, phosphorus, potassium, trace element, organic matter, amino acid composition, and wheat grass powder.    USE - The liquid microbial fertilizer is useful for resisting insects, and degrading organic matter.    ADVANTAGE - The liquid microbial fertilizer consumes minimal water, is environmentally-friendly, and exhibits minimal water retention property.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the liquid microbial fertilizer, which involves (a) activating the above-mentioned strain and inoculating the strain, (b) preparing seed liquid of the above-mentioned strain, (c) preparing fermentation liquid medium and fermenting and culturing strain, (d) collecting the fermented bacterial strain, (e) adding complex nutrients and polyglutamic acid and uniformly blending the mixture, and (f) adding the mixture in plastic bottle, and sterilizing the bottle using ultraviolet.
NOVELTY - Method for separating and preparing salvianolic acid B involves adding Salvia miltrorrhiza medicinal material in an amount of 5-20 times of amount of water, extracting, filtering, obtaining crude extract of Salvia miltrorrhiza, subjecting the obtained product to high-performance hydrophobic interaction chromatography, separating silicon-containing compound (I), collecting chromatographic fractions, and freeze-drying to obtain salvianolic acid B. The matrix blank diameter is 80-90 Angstrom . The silica microspheres have a particle size of 5-10 mu m.    USE - Method for separating and preparing salvianolic acid B (claimed).    ADVANTAGE - The method enables easy and environmentally-friendly separation and preparation of salvianolic acid B having purity of more than 95%, with quality recovery rate is more than 90%, and without using high-concentration organic solvent.    DETAILED DESCRIPTION - Method for separating and preparing salvianolic acid B involves adding Salvia miltrorrhiza medicinal material in an amount of 5-20 times of amount of water, extracting, filtering, obtaining crude extract of Salvia miltrorrhiza, subjecting the obtained product to high-performance hydrophobic interaction chromatography, separating silicon-containing compound of formula (I), collecting chromatographic fractions, and freeze-drying to obtain salvianolic acid B. The matrix blank diameter is 80-90 Angstrom . The silica microspheres have a particle size of 5-10 mu m. The high-performance hydrophobic interaction chromatography is carried out using mobile phase (A) solution with 0.5-3 mol/L ammonium sulfate, 0-50 mmol/L potassium phosphate, and pH of 5-8, and solution as mobile phase (B) solution with 0-50 mmol/L potassium phosphate and pH of 5-8, flow rate of 0.5-2 mL/minute, linear gradient of mobile phase (B) solution of 0-100%, and detection wavelength of 280-290 nm.    R=group of formula (i) or (ii) or group of formula: -(-CH2-CH2-O-)n-H (iii);and    n=10-25.
NOVELTY - C-(6,11-Dihydro-5H-dibenzo(b,e)azepin-6-yl)-methylamine is reacted with tert-butyl N-((1Z)-(((tert-butoxy)carbonyl)amino)(methylsulfanyl)methylidene)carbamate to obtain a condensed product. The obtained condensate is cyclized in organic solvent in the presence of p-toluene sulfonic acid, to obtain tert-butyl N-(2,4-diazatetracyclo(12.4.0.02,6.07,12)octadeca-1(18),3,7,9,11,14,16-heptaen-3-yl)carbamate. The obtained compound is salified to obtain epinastine hydrochloride.    USE - Manufacture of epinastine hydrochloride used in medicine field.    ADVANTAGE - The epinastine hydrochloride with reduced toxicity is manufactured by a safe and environmentally-friendly process.    DETAILED DESCRIPTION - C-(6,11-Dihydro-5H-dibenzo(b,e)azepin-6-yl)-methylamine is reacted with tert-butyl N-((1Z)-(((tert-butoxy)carbonyl)amino)(methylsulfanyl)methylidene)carbamate to obtain tert-butyl N-((1Z)-((9-azatricyclo(9.4.0.03,8)pentadeca-1(15),3,5,7,11,13-hexaen-10-ylmethyl)amino)((((tert-butoxy)carbonyl)imino))methyl)carbamate. The carbamate is cyclized in organic solvent in the presence of p-toluene sulfonic acid, to obtain tert-butyl N-(2,4-diazatetracyclo(12.4.0.02,6.07,12)octadeca-1(18),3,7,9,11,14,16-heptaen-3-yl)carbamate. The obtained compound is salified to obtain epinastine hydrochloride.
NOVELTY - Method of saccharification of lignocellulosic biomass involves mixing and reacting electrolyzed reduced water having pH of 12.8-14 to lignocellulosic biomass at 130-200 degrees C for 30-90 minutes, adjusting water pressure to 3-10 bar, subjecting mixture to solid-liquid phase separation, treating using solid biomass saccharification enzymes and pre-treating using aqueous solution of citric acid having pH of 4-5.5.    USE - Method of saccharification of lignocellulosic biomass (claimed).    ADVANTAGE - The method is carried out efficiently and economically by consuming reduced amount of energy.
NOVELTY - A composition comprises a cavitand compound (I). The composition is in a crystalline form and has void spaces of 15 A3 or more, where the void spaces are free of other atoms and molecules.    USE - Composition is used for gas separation and gas storage (all claimed).    ADVANTAGE - The composition has high crystallinity.    DETAILED DESCRIPTION - A composition comprises a cavitand compound of formula (I) and/or its stereoisomers. The composition is in a crystalline form and has void spaces of 15 A3 or more, where the void spaces are free of other atoms and molecules.    R=H, 1-6C alkyl, halo, or NO2;    R1=H, 1-6C alkyl, Ph, (1-6C alkyl)xPh, (C(halo)3)xPh, or (halo)xPh;    Y'=-CH2-, C(1-6C alkyl)2, or Si(1-6C alkyl)2;and    x=1-3.    INDEPENDENT CLAIMS are included for the following:    (1) cavitand compound of formulae (IIa)-(IIc) and/or its stereoisomers;    (2) method for gas separation, which involves exposing a sample comprising two or more gases to the composition and selectively forming a host-guest complex between the composition and one or more gases from the sample; and    (3) method for gas storage, which involves exposing a sample comprising one or more gases (a) to the composition, and forming a host-guest complex between the composition and one or more gases (a), where the complex is capable of retaining 95% or more gas at an ambient temperature which 10 degrees C or more than the boiling point of the gas.    R4=H, CH3, i-Bu, Ph, 4-CF3Ph, 3,5-(CF3)2Ph, or 3,5-F2Ph;    Z=-CH2-, -Si(CH3)2-, -Si(CH2CH3)2-, or -Si(i-Pr)2-;    R5=H, CH3, CH2CH3, i-Bu or 3,5-(CF3)2Ph;    R6=H, 1-6C alkyl, Ph, (1-6C alkyl)xPh, (C(halo)3)xPh, or (halo)xPh, preferably H;and    Z'=-CH2-, C(1-6C alkyl)2, or Si(1-6C alkyl)2, preferably CH2.    (i) R4 is not CH3, when Z is -CH2-, -Si(CH3)2- or -Si(CH3CH2)2-, and R4 is not Ph, when Z is -CH2-; and (ii) R5 is not H, when Z is -CH2- or -Si(CH3)2-, and R5 is not CH3, when Z is -CH2-.
NOVELTY - Unit (1) comprises: an electrolyzer (2) designed to carry out electrolysis of water to produce hydrogen and oxygen; and a methanation reactor (3) designed to produce methane by causing the hydrogen produced by the electrolyzer to react with carbon dioxide. The unit comprises a direct conduction line for the hydrogen from the electrolyzer to the methanation reactor and a thermostatic safety valve arranged on a line which is designed to draw off the methane produced by the methanation reactor, and the electrolyzer comprises an electrolytic cell (6) and a tank (7) for supply of water.    USE - The unit is for accumulation of energy (claimed).    ADVANTAGE - The unit enables efficient and intrinsically safe way low-cost electrical energy to convert it and accumulate it in the chemical energy of methane, which in turn may be used as such or for producing energy in a closed system when required by the grid.    DETAILED DESCRIPTION - Unit (1) comprises: an electrolyzer (2) designed to carry out electrolysis of water to produce hydrogen and oxygen; and a methanation reactor (3) designed to produce methane by causing the hydrogen produced by the electrolyzer to react with carbon dioxide. The unit comprises a direct conduction line for the hydrogen from the electrolyzer to the methanation reactor and a thermostatic safety valve arranged on a line which is designed to draw off the methane produced by the methanation reactor, and the electrolyzer comprises an electrolytic cell (6) and a tank (7) for supply of water hydraulically connected to the electrolytic cell for supplying it with water as electrolyte.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of the unit for accumulation of energy.    Unit (1)    Electrolyzer (2)    Methanation reactor (3)    Electrolytic cell (6)    Tank (7)
NOVELTY - A hydrogen-generation device (100) is provided with a reformer (130) for carrying out reforming reaction using raw material (BB) and water vapor, and generating hydrogen-containing gas, a transformer (140) for decreasing the carbon monoxide in the hydrogen-containing gas by shift reaction, an evaporator (120) for evaporating water (AA) and adjacently provided on an upstream side of the transformer, and a hydrodesulfurizer (110) for removing the sulfur compounds in the raw material by hydrodesulfurization reaction and adjacently provided on a downstream side of the transformer.    USE - Device is used for generating hydrogen for fuel cell system (claimed).    ADVANTAGE - The hydrogen-generation device has excellent durability. The hydrogen is efficiently produced by the device, by a simple process.    DETAILED DESCRIPTION - A hydrogen-generation device is provided with a reformer for carrying out reforming reaction using raw material and water vapor, and generating hydrogen-containing gas, a transformer for decreasing the carbon monoxide in the hydrogen-containing gas by shift reaction, an evaporator for evaporating water and adjacently provided on an upstream side of the transformer to exchange heat and a hydrodesulfurizer for removing the sulfur compounds in the raw material by hydrodesulfurization reaction and adjacently provided on a downstream side of the transformer to exchange heat. An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen generation device. (Drawing includes non-English language text)    Hydrogen-generation device (100)    Hydrodesulfurizer (110)    Evaporator (120)    Reformer (130)    Transformer (140)    Water (AA)    Raw material (BB)
NOVELTY - A Bipolar alkaline water electrolysis unit (12) consists of anode (18) consisting of porous material for oxygen generation, cathode (19) for hydrogen production, electroconductive partition (22) which divides the anode and the cathode, and outer frame (16) which surrounds the electroconductive partition. The upper portion of the electroconductive partition and/or the outer frame is provided with passage portion for gas and electrolyte solution. The lower portion of electroconductive partition and/or outer frame is provided with the passage portion for electrolyte solution.    USE - Bipolar alkaline water electrolysis unit used in electrolytic cell for electrolyzing electrolyte solution containing alkaline water (claimed).    ADVANTAGE - The electrolysis unit enables to perform electrolysis at low voltage. The assembly of electrolytic cell is simple and economical.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the arrangement of each component in the bipolar alkaline water electrolysis unit.    Bipolar alkaline water electrolysis unit (12)    Outer frame (16)    Anode (18)    Cathode (19)    Electroconductive partition (22)    Electrolytic cell (100)
NOVELTY - A recombinant cell expressing at least one heterologous alkane exporter protein comprising an ATP binding cassette (ABC) comprising amino acid sequence of SEQ ID NO: 1, is new. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication.    USE - The recombinant cell is useful for producing biofuel comprising 6-16C alkanes, decane or undecane (all claimed).    ADVANTAGE - The recombinant cell consumes minimal time to generate tolerance strains through heterologous expression of transporters as compared to existing conventional evolutionary strategies, simply prepares biofuel, and has improved cell tolerance.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for producing biofuel, involves culturing the recombinant cell which allows the expression of at least one heterologous alkane exporter protein; and    (2) method of increasing resistance towards biofuel toxicity in a cell, involves introducing a nucleic acid molecule encoding for a heterologous alkane exporter protein comprising the above-mentioned ABC, and culturing the cell under conditions that allow expression of heterologous alkane exporter protein.
NOVELTY - Catalyst for hydrodeoxygenation of biomass pyrolysis oil, comprises a noble metal as active phase on a solid support, where the noble metal is doped with at least one catalyst promoter selected from phosphorus, boron, sulfur and nitrogen.    USE - The catalyst is useful for hydrodeoxygenation of biomass pyrolysis oil (claimed).    ADVANTAGE - Doping noble metal catalysts such as catalysts containing ruthenium, with low amounts of a catalyst promoter such as phosphorus, results in an improvement of catalyst performance, activity, selectivity, and stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of forming a catalyst for the hydrodeoxygenation of biomass pyrolysis oil, involving: (a) impregnating a solid support with a solution or suspension comprising a noble metal precursor; (b) impregnating the solid support with a solution or suspension comprising a catalyst promoter precursor, where the catalyst promoter is selected from phosphorus, boron, sulfur and nitrogen; (c) drying the impregnated solid support; and (d) calcining the dried impregnated solid support; and    (2) a method for hydrodeoxygenation of a biomass pyrolysis oil, involving: (i) providing the catalyst; and (ii) contacting the biomass pyrolysis oil with the catalyst under conditions that allow hydrodeoxygenation of the biomass pyrolysis oil.
NOVELTY - Invention relates to a method for comprehensive treatment of hydrocarbon gases for one or more oil refineries wherein the starting gases used are mixtures of same-type refinery gases from different processing equipment, which are an ethane-containing hydrocarbon fraction, a hydrocarbon fraction with high content of hydrogen and a reflux fraction, taken for further treatment at the next steps: compressing the starting gases, removal of hydrogen sulphide and carbon dioxide from said gases, subsequent splitting of the reflux fraction into a deethanisation gas, a light ethane-containing hydrocarbon fraction, a propane-propylene fraction, a butane-butylene fraction and a fraction of C5 or higher hydrocarbons, obtaining hydrogen using a hydrocarbon fraction with high content of hydrogen, compressing, drying, removing O2, As, Hg, NOx and other impurities, which are toxic for catalysts and equipment, from the ethane-containing fraction and splitting said fraction into a deethanised gas, an ethane fraction and a fraction of C3 or higher hydrocarbons, chemical conversion of the ethane fraction to obtain pyrolysis products in a pyrolysis furnace, splitting pyrolysis products with separation of ethylene and using the propane-propylene and butane-butylene fractions to obtain high-octane motor petrol components by alkylation and/or oligomerisation, petrochemical synthesis products, and obtaining a liquefied propane-butane mixture as fuel for car engines.    USE - Chemistry.    ADVANTAGE - High quality of end products.16 cl, 1 dwg, 4 ex
NOVELTY - The method involves applying electromagnetic radiation to a hydrate deposit by using an electromagnetic spectrum power source e.g. carbon dioxide laser. The electromagnetic radiation is delivered to the hydrate deposit in infrared region of electromagnetic spectrum. A control system is provided for controlling the spectrum power source and for automatically shutting off the spectrum power source in the event of certain pre-defined conditions e.g. inappropriate power level, excessive reflected power or unsuitable power duration.    USE - Method for dissociating methane from hydrate deposits in ocean's floor, well bore, deep water flow line and leak containment system (all claimed).    ADVANTAGE - The method enables the application of the electromagnetic radiation to the hydrate deposit by using the electromagnetic spectrum power source e.g. carbon dioxide laser, thus ensuring safe, reliable, economical and environment-friendly dissociating of the methane from the hydrate deposits, without causing hydrate formation during deep water drilling activities.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for recovering methane from methane hydrate located beneath ocean's floor    (2) an apparatus for dissociating methane from hydrate deposits.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram illustrating a method for dissociating methane from hydrate deposits.
NOVELTY - Amperometric gas sensor (10) for measuring a concentration of an analyte, comprises: a solid support (22); and a working electrode (24A) in contact with the solid support, where the analyte comprises a dopant which when in contact with the solid support increases the electrical conductivity of the solid support.    USE - The amperometric gas sensor is useful for measuring a concentration of an analyte, which is gaseous analyte or sterilant gas (all claimed).    ADVANTAGE - The amperometric gas sensor: is relatively small so that uncompensated resistance is negligible, hence it has simplified design and minimizes stray current pickup; and increases the sterilization process and/or provides greater assurance of effective sterilization over a given period.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) a method (M1) for determining a concentration of a gaseous analyte in an enclosed space, comprising placing the amperometric gas sensor in the enclosed space, flowing the analyte in the enclosed space in contact with the sensor, and determining the concentration of the analyte in the enclosed space using the amperometric gas sensor; and    (2) a method (M2) for determining a concentration of a sterilant gas in a vacuum chamber during a sterilization process, comprising placing the amperometric gas sensor in the vacuum chamber, conducting the sterilization process in the vacuum chamber under a vacuum using the sterilant gas, and determining the concentration of the sterilant gas in the vacuum chamber using the amperometric gas sensor.    DESCRIPTION OF DRAWING(S) - The figure shows a perspective view of the amperometric gas sensor.    Amperometric gas sensor (10)    Solid support (22)    Working electrode (24A)    Working electrode (24B)    Space or gap (26)
NOVELTY - Recombinant host cell comprising a mutant ketol-acid reductoisomerase enzyme is new. The enzyme has a ketol-acid reductoisomerase hidden Markov model (HMM) search profile E value of less than 10-3 using the HMM search program and comprises at least one mutation within the phosphate binding loop of the enzyme. The mutation comprises a substitution at the residue corresponding to Thr-52 of SEQ ID NO: 17 (comprising fully defined 338 amino acids as given in the specification), where the substitution is a substitution to a polar, negatively charged amino acid.    USE - The recombinant host cell is useful for converting acetolactate to 2,3-dihydroxyisovalerate, and producing isobutanol (all claimed), where the isobutanol is useful as a fuel or fuel additive.    ADVANTAGE - The recombinant host cell acquires NADH specificity and provides isobutanol having the energy content similar to that of gasoline and blended with any fossil fuel, where the isobutanol yields only carbon dioxide and little or no sulfur oxide (SOx) or nitrogen oxide (NOx) when burned in the standard internal combustion engine, and is less corrosive than ethanol.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) converting acetolactate to 2,3-dihydroxyisovalerate, comprising providing the recombinant host cell and contacting the recombinant host cell with acetolactate, where the recombinant host cell converts acetolactate to 2,3-dihydroxyisovalerate; and    (2) producing isobutanol, comprising providing a recombinant host cell comprising an isobutanol biosynthetic pathway that comprises the mutant ketol-acid reductoisomerase enzyme, and contacting the recombinant host cell with a fermentable carbon substrate, where the recombinant host cell produces isobutanol.
NOVELTY - Cosmetic composition comprises an aqueous dispersion of hydrophobic silica aerogel particles and an alcohol compound, its optical isomers and its solvates i.e. hydrates.    USE - The cosmetic composition is useful for treating keratinous fibers of hair of a human to maintain the shape of the hair (all claimed).    ADVANTAGE - The composition provides excellent capping properties, is homogeneous and opalescent mixture with a pleasant touch, avoids the dryness of the hair, and avoids the visibility of the residues.    DETAILED DESCRIPTION - Cosmetic composition comprises an aqueous dispersion of hydrophobic silica aerogel particles and an alcohol compound of formula (R3-CH2-CH(R2)-R1) (I) and/or its optical isomers, solvates or hydrates.    R1 = OH, CH2OH or CH3;    R2 = H or OH; and    R3 = H, CHOH, -(O-CH2-CH2)(n-OH) in which n is 1-10, (CH2-CH2)(n-OH) in which n is 1-5, CH(OH)-CH3 or hydroxy group.
NOVELTY - Genetically engineered carboxydotrophic acetogenic bacterium comprising an exogenous nucleic acid encoding a nonspecific acetyltransferase (wax ester synthase/acyl coenzyme-A: diacylglycerol acyltransferase), is new.    USE - The genetically engineered bacterium is useful for converting carbon monoxide and/or carbon dioxide into biodiesel, where the biodiesel comprises fatty acid ethyl esters, or fatty acid butyl esters (all claimed).    ADVANTAGE - The genetically engineered bacterium produces a greater amount of biodiesel than a parental microorganism, by reducing the cost of feedstock, reducing complexity of the equipment and parameter control, and utilizing limited handling and separation steps.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) converting carbon monoxide and/or carbon dioxide into biodiesel, comprising: passing a gaseous carbon monoxide-containing and/or carbon dioxide-containing substrate to a bioreactor containing a culture of the genetically engineered carboxydotrophic acetogenic bacterium in a culture medium so that the bacterium convert the carbon monoxide and/or carbon dioxide to biodiesel; and recovering the biodiesel from the bioreactor; and    (2) a plasmid which replicates in a carboxydotrophic acetogenic bacterium, comprising an exogenous nucleic acid encoding a nonspecific acetyltransferase (wax ester synthase/acyl coenzyme-A: diacylglycerol acyltransferase).
NOVELTY - The method involves introducing water into a humidified oxygen stream, where the water comprises droplets that are suspended in the oxygen stream to form a super-humidified oxygen stream. The water is introduced into a humidified hydrogen stream, where the hydrogen stream water comprises droplets that are suspended in the humidified oxygen stream to form a super-humidified hydrogen stream. The super-humidified oxygen stream is introduced to a cathode. The super-humidified hydrogen stream is introduced to an anode such that a polymer exchange membrane (PEM) fuel cell provides power to a load.    USE - Method for humidifying a fuel stream e.g. reactant gas stream such as oxygen or hydrogen stream, in a hybrid humidifier PEM fuel cell stack.    ADVANTAGE - The method enables increasing humidity of gas feed streams to a point above saturation humidity so as to improve efficiency of the PEM fuel cell. The method enables a humidification system to cover whole range of flow rates and to have shorter response time for changing fuel cell conditions during start-ups and transient operation so as to achieve desired humidity in the fuel cell stack. The method enables providing improved performance through use of primary humidification and secondary humidification.    DETAILED DESCRIPTION - The water droplets are micro-droplets.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a hybrid humidifier PEM fuel cell.
NOVELTY - Method for preparing concentrated sugar solution using cellulose containing biomass as raw material, involves hydrolyzing the cellulose containing biomass, filtering sugar solution through microfiltration membrane and/or ultrafiltration membrane, collecting refined-sugar aqueous solution from permeation side, collecting permeated water from permeation side and collecting concentrated sugar solution from imperviousness side by filtering refined-sugar aqueous solution by nano membrane filter, and washing microfiltration membrane and/or ultrafiltration membrane.    USE - The method is useful for preparing concentrated sugar solution for manufacturing ethanol using yeast (all claimed).    ADVANTAGE - The method is environmentally-friendly and recycles water.    DETAILED DESCRIPTION - Method for preparing concentrated sugar solution using cellulose containing biomass as raw material, involves hydrolyzing the cellulose containing biomass to prepare sugar solution, filtering sugar solution through microfiltration membrane and/or ultrafiltration membrane, collecting refined-sugar aqueous solution from permeation side, collecting permeated water from permeation side and collecting concentrated sugar solution from imperviousness side by filtering refined-sugar aqueous solution by nano membrane filter, and washing microfiltration membrane and/or ultrafiltration membrane, where the method involves suspending biomass in water, hydrolyzing the biomass by at least one process chosen from hydrothermal treatment, acid treatment, alkali treatment, and enzyme treatment and further involves utilizing the permeated water.
NOVELTY - Environmental improvement material comprises carrier comprising ferrihydrite.    USE - The environmental improvement material is useful for processing contaminant (claimed).    ADVANTAGE - The environmental improvement removes heavy metal and radioactive substance by absorption from polluted water or contamination soil, or improves various environments, such as growth promotion of seaweed, adsorption removal of hydrogen sulfide, methane gas and ammonia, and promotes decomposition promotion of raw food waste material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for removal processing method of contaminant, which involves positioning environmental improvement material on surface and/or inside contaminated material, and removing contaminant, or preventing outflow and inflow of contaminant.
NOVELTY - Producing methane and hydrogen from biogas, comprises (i) separating and recovering methane from biogas by gas separation membrane, (ii) injecting the mixed gas of carbon dioxide and methane, which is not separated in the previous step into a reactor equipped with the gas separation membrane and filled with a catalyst, and (iii) generating hydrogen by reforming catalyst and reacting mixed gas of methane and carbon dioxide injected into the reactor and simultaneously separating and recovering hydrogen by gas separation membrane.    USE - The method is useful for producing methane and hydrogen from biogas (claimed).    ADVANTAGE - The method: results in production of the high purity methane, which can be utilize as fuel; prevents deactivation and extends life span of the catalyst; and improves hydrogen yield.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for producing methane and hydrogen from biogas. (Drawing includes non-English language text).
NOVELTY - The sludge treating equipment has an inlet port (110) through which the sludge is flowed in. A pulverizing device (120) is provided for rotatively shattering the sludge to pieces. A blower (130) is provided for supplying the jet of fluid to the pulverizing device. An outlet portion is provided for ejecting the pulverized solid content to outside. A collector (160) is provided for collecting the sludge of solid content pulverized from the pulverizing device.    USE - Sludge treating equipment for treating sludge such as livestock excretions and sewage mixture generated in stockbreeding farmhouse.    ADVANTAGE - The efficiency and simplification of sludge treating equipment can be improved. The environmental pollution can be minimized.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for sludge treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the sludge treating equipment. (Drawing includes non-English language text)    Inlet port (110)    Pulverizing device (120)    Blower (130)    Heater (150)    Collector (160)
NOVELTY - Invention relates to a method of extracting methane from gas mixtures by bringing the mixture into contact with an aqueous solution of a cyclic ether with concentration of not more than 20 mol % at temperature not higher than 20 degrees C and pressure of up to 3.0 MPa to obtain a condensed phase containing mixed hydrates of methane and the cyclic ether and a gas phase, separating the gas phase, extracting methane from the condensed phase and recycling the aqueous solution of the cyclic ether for extraction.    USE - Chemistry.    ADVANTAGE - Method enables to efficiently extract methane from gas mixtures by simplifying the process, particularly lowering the separation pressure.2 cl, 8 tbl, 8 ex, 1 dwg
NOVELTY - Humic acid-containing water soluble liquid fertilizer comprises 28-40 wt.% of biogas residue, 15-25 wt.% of urea, 6-12 wt.% of phosphoric acid, 7-15 wt.% of potassium hydroxide and balance amount of marsh gas waste water.    USE - Used as humic acid-containing water soluble liquid fertilizer.    ADVANTAGE - The humic acid-containing water soluble liquid fertilizer reduces the excrement sewage treatment cost and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the humic acid-containing water soluble liquid fertilizer comprising: (1) wet and dry separation of sewage containing fecal, introducing the resulting liquid into biogas anaerobic fermentation tank to obtain marsh gas and marsh gas wastewater and then carrying out solid-liquid separation to obtain marsh gas wastewater of supernatant and non-fossil sources of humic acid supernatant, where the solid content of the marsh gas residue is 10-30 wt.%; and (2) adding urea, phosphoric acid with the obtained supernatant and uniformly stirring and then adding potassium hydroxide and stirring.
NOVELTY - Residue of monoammonium phosphate is dissolved in concentrated phosphoric acid having concentration of 35-46%, to obtain slurry. The slurry is added to a tube reactor,and sulfuric acid having concentration of 98%, and ammonia having purity of 99.6% are added. Reaction is carried at 115-140 degrees C and under pressure of 0.3 MPa for 1-2 seconds, to obtain monoammonium phosphare crystal having moisture of 10%.    USE - Manufacture of monoammonium phosphate crystals (claimed).    ADVANTAGE - The method enables manufacture of monoammonium phosphate crystals economically, and is environmentally-friendly.
NOVELTY - A 1,3-butanediol is condensed using 1-50 %mass solid super-acid or molecular sieve as catalyst at 50-190 degrees C for 10 hours, to obtain a solution. The obtained solution is cooled, filtered, decompressed, and distilled, to obtain the 2-hydroxydiphenyl ether with yield of 95% or more.    USE - Preparation of 2-hydroxydiphenyl ether used as raw material for manufacture of medicines.    ADVANTAGE - The 2-hydroxydiphenyl ether has high efficiency, and is environmentally-friendly and economical, and prepared efficiently by simple method.
NOVELTY - Synthesis of vinpocetine involves adding ethanol solution into the solid vincamine, alkaline-hydrolyzing, dehydrating in molecular sieve dehydration column, and esterifying in solid acid esterification column.    USE - Synthesis of vinpocetine (claimed).    ADVANTAGE - The method efficiently and economically provides vinpocetine, using simple process without generating wastewater.
NOVELTY - Preparation of a complex of sulforaphane and cyclodextrin, comprises: (i) reacting, in an aqueous solvent, a 1-isothiocyanato-4-methylsulfanyl-butane (A) with an oxidizing agent and in the presence of a catalyst to form sulforaphane; and (ii) mixing the sulforaphane from step (i) with cyclodextrin in an aqueous solvent to form a precipitate of the sulforaphane-cyclodextrin complex.    USE - The method is useful for synthesizing sulforaphane-cyclodextrin complex, which is useful for treating and/or preventing cancer and microbial infections (all claimed). No biological data given.    ADVANTAGE - The method provides complex with high yield and purity by utilizing less number of steps in an industrial, cost-effective and environmentally-friendly manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a sulforaphane-cyclodextrin complex obtainable by the process.
NOVELTY - Preparing a dihalopyridine compound (IA) comprises (a) adding a first liquid mixture comprising a metal nitrite salt to a second liquid mixture comprising a pyridin-3-amine compound (IB), a hydrohalic acid and an iron(III) compound.    USE - The process is useful for preparing (IA) (claimed), which is useful as intermediates for preparing crop protection agents, pharmaceuticals and other fine chemicals.    ADVANTAGE - The process prepares (IA) with high yield while avoiding the use of expensive and potentially environmentally harmful copper salts, multiple reaction vessels and additional solvents.    DETAILED DESCRIPTION - Preparing a dihalopyridine compound of formula (IA) comprises (a) adding a first liquid mixture comprising a metal nitrite salt to a second liquid mixture comprising a pyridin-3-amine compound of formula (IB), a hydrohalic acid and an iron(III) compound.    X1, X2 = Cl or Br; and    Y1 = 0-3 substituents comprising alkyl, aryl, heteroaryl (all optionally substituted), halide, CN, NO2 or OH.
NOVELTY - Modified matrix, solid fertilizer and liquid fertilizer composition comprises slag, sawdust, sand and multi-micro composite mineral as matrix; solid fat, nitrogen, phosphorus, potassium, organic matter and effective viable bacteria as solid fertilizer; and biogas, nitrogen, potassium, phosphorus, carbon dioxide, fluorine, bromine, iron, strontium, lithium, boron, silicon, zinc and selenium as liquid fertilizer.    USE - Modified matrix, solid fertilizer and liquid fertilizer composition used for cultivating melon (claimed).    ADVANTAGE - The composition increases internal gas diffusion characteristics, improves oxygen matrix, increases temperature of base system, prompts strong decomposition of organic matter, improves melon root respiration and promotes plant growth and development.    DETAILED DESCRIPTION - A modified matrix, solid fertilizer and liquid fertilizer composition comprises 15-35 wt.% slag, 35-45 wt.% sawdust, 15-25 wt.% sand and 15-25 wt.% multi-micro composite mineral as matrix; 45-55 wt.% solid fat, 2-8 wt.% nitrogen, 2-8 wt.% phosphorus, 2-8 wt.% potassium, 20-30 wt.% organic matter and 5-10 wt.% effective viable bacteria as solid fertilizer; and 85-94 wt.% biogas, 0.02-0.8 wt.% nitrogen, 0.5-0.13 wt.% potassium, 0.4-10 wt.% phosphorus, 0.2-0.6 wt.% carbon dioxide, 0.3-0.8 wt.% fluorine, 0.002-0.006 wt.% bromine, 0.001-0.005 wt.% iron, 0.28-0.68 wt.% strontium, 0.0463-0.863 wt.% lithium, 0.125-0.325 wt.% boron, 2.465-9.465 wt.% silicon, 0.001-0.009 wt.% zinc and 0.002-0.01 wt.% selenium as liquid fertilizer. An INDEPENDENT CLAIM is included for the cultivation of melon comprising preparing substrate in bag, connecting and fastening bags, laying bags, digging holes for surface cultivation, adding solid fertilizer at 5-10 cm away from roots, emerging plant, dissolving liquid fertilizer in water and irrigating liquid fertilizer for 1-6 times everyday.
NOVELTY - Preparation of ternary compound solid base catalyst involves adding alkaline earth metal oxide (MO) and sodium montmorillonite (MMT) with potassium fluoride (KF) with concentration of 5-70 %mass, stirring in water, placing for 2 hours, obtaining x-KF/MO-MMT precursor, providing obtained precursor to the oven, drying at 80 degrees C for 12 hours, grinding, sieving through sieve of 100 meshes, reserving sieve samples and roasting.    USE - Preparation of ternary compound solid base catalyst used for producing biodiesel.    ADVANTAGE - The ternary compound solid base catalyst is efficiently prepared with high reaction activity.    DETAILED DESCRIPTION - Preparation of ternary compound solid base catalyst involves adding alkaline earth metal oxide (MO) and sodium montmorillonite (MMT) in the mass ratio of 1:1 with potassium fluoride (KF) with concentration of 5-70 %mass, stirring in water, controlling at stirring speed of 100-120 rpm, placing for 2 hours, obtaining x-KF/MO-MMT precursor, providing obtained precursor to the oven, drying at 80 degrees C for 12 hours, grinding, sieving through sieve of 100 meshes, reserving sieve samples, and roasting at 400-600 degrees C in air atmosphere for 4 hours. The volume ratio of aqueous solution and potassium fluoride is 1 g:1 mL.
NOVELTY - The device has a high temperature furnace chamber (1) whose top portion is provided with a substrate outlet. The bottom surface of the high temperature furnace chamber is provided with a supporting grid plate (4). The side surface of the high temperature furnace chamber is provided with air inlet. The side top portion of high temperature furnace chamber is provided with an air outlet. The air outlet is connected with a separate air flow combustion engine fuel inlet.    USE - Epidemic disease dead poultry treatment device.    ADVANTAGE - The fuel consumption and cost of the device are reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the epidemic disease dead poultry treatment device.    High temperature furnace chamber (1)    Died pig inlet (2)    Drying chamber (3)    Supporting grid plate (4)    Multilayer grinder (6)
NOVELTY - An organic-inorganic biofertilizer comprises 20-25 pts. wt. nitrogen fertilizer, 7-9 pts. wt. phosphate fertilizer, 7-9 pts. wt. potassium fertilizer, 50-60 pts. wt. chicken manure fermentation lees powder fertilizer, 4-6 pts. wt. adsorbent, 3-5 pts. wt. coating agent, and 1-1.5 pts. wt. microbial agent.    USE - Organic-inorganic biofertilizer.    ADVANTAGE - The organic-inorganic biofertilizer has long-term effect and quick action, and can increase crop yield by 12-30%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the organic-inorganic biofertilizer, comprising mixing and granulating urea, monoammonium phosphate and potassium sulfate, then rolling, sieving to obtain particles to particle size of 1.5-2.5 mm, spraying coating agent on surface of the particles, rolling the coated particles into the chicken manure fermentation lees powder fertilizer and granulating to cover the chicken manure fermentation lees fertilizer on the particle surface, then sieving the particles to particle size of 2.5-3.5 mm, spraying solid microbial inoculum, then uniformly spraying 60% coating agent on the coated particle surface, and drying with hot air at 60-80 degrees C to water content of less than 8%.
NOVELTY - The method involves mixing low pressure steam material into synthesis reaction area using methylamine reaction heat. The urea synthesis tower (2) is divided into paths. The excess ammonia in gas-liquid mixture is supplied to top of a stripping tower (3). A disc liquid distributor distributes liquid along tube wall through groove. A high pressure decomposing separation unit separates methylamine non-transformed urea and excess amine. A high efficiency mixer mixes methylamine in material mixing area with heat material. The methylamine reaction is heated to low pressure steam.    USE - Energy-saving method for producing urea circulating aqueous solution.    ADVANTAGE - The convenient and simple operation of energy-saving method can be performed reliably. The urea consumption of energy-saving method can be reduced effectively. The operation stability and operation period of energy-saving method can be improved efficiently.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the Energy-saving method.    Reactor (1)    Urea synthesis tower (2)    Stripping tower (3)    Energy-saving reactor (4)    Pipe hole (6)
NOVELTY - Preparing methane and bio-fertilizer comprises selecting cassava slag having a total solid content of 4-10%, feeding and reacting the cassava slag into an anaerobic reactor and discharging, and adding the anaerobic bacteria into the anaerobic reactor and reacting to obtain methane having 55-65% of crude product and squeezing cassava slag to obtain bio-fertilizer residue and collecting the obtained crude product of methane into the wet-type gas storage tank and passing the crude product into a gas compression plant for purifying to obtain more than 97% of the product.    USE - The methane is useful in a boiler room of the factory for combustion gas and as gasoline for automotive fuel (claimed).    ADVANTAGE - The method prepares methane and bio-fertilizer with excellent biodegradable performance in cost-effective and environmental-friendly manner.
NOVELTY - Promoting fruiting and flowering of morning glory comprises soaking morning glory seed, disinfecting with potassium permanganate solution, repeatedly washing with clean water, draining water, cutting with a blade, spreading on a base, seeding, watering, allowing to sprout for 3-6 days, covering a frame on the seedlings after the seedling has 4 true leaves, covering a sun-shading cloth for shading for 7-15 days, controlling the seedling bed temperature at 18-28 degrees C, illuminating 8-10 hours per day, planting in a field, fertilizing with fertilizer and performing water management until flowering.    USE - The method is useful for promoting fruiting and flowering of morning glory (claimed).    ADVANTAGE - The method is simple, easy and economical; promotes early flowering of a variety of morning glory seed with high yield; and is suitable for large scale production.
NOVELTY - Method for preparing special organic and inorganic compound fertilizer using sugarcane refinery filtered mud, involves (a) obtaining urea, calcium superphosphate or calcium magnesium phosphate, potassium chloride and dry filter mud, (b) stacking sludge and naturally fermenting the filter mud, spreading the fermented filter mud, naturally drying the filter mud in sun, and crushing the filter mud, and (c) adding nitrogen, phosphorus and potassium fertilizer to the crushed filter mud, mixing and crushing the mixture by existing method, and processing the product.    USE - The method is useful for preparing special organic and inorganic compound fertilizer (claimed).    ADVANTAGE - The method improves soil, soil fertility, yield of sugarcane to 0.5-1 ton, cane sugar to 0.5-1% and utilization rate of the fertilizer to 3-5%, and avoids hardening of the soil.    DETAILED DESCRIPTION - Method for preparing special organic and inorganic compound fertilizer using sugarcane refinery filtered mud, involves (a) obtaining 4.17-42.87 wt.% urea, 11.52-60.87 wt.% calcium superphosphate or calcium magnesium phosphate, 3.33-16.66 wt.% potassium chloride and 25-37.5 wt.% dry filter mud, (b) stacking sludge and naturally fermenting the filter mud for 30-40 days, where the water content of the filter mud is maintained at 25-35%, spreading the fermented filter mud to a thickness of 10-15 cm, naturally drying the filter mud in sun for 2-3 days, where the water content of the filter mud is 15-25%, and crushing the filter mud using crusher to obtain particles having size of 40-50 meshes, and (c) adding nitrogen, phosphorus and potassium fertilizer to the crushed filter mud, mixing and crushing the mixture by existing method, and granulating, drying, cooling, sieving and packaging the obtained product.
NOVELTY - Preparing nicarbazin comprises (i) reacting p-nitroaniline, solid phosgene and a reaction solvent and monitoring the reaction by thin layer chromatography for complete conversion of p-nitroaniline to 1,3-bis(4-nitrophenyl)urea; (ii) reducing temperature, adding methanol, stirring uniformly, adding acetylacetone, urea and an inorganic acid, heating and reacting for 9-15 hours, adjusting pH to 6, stirring continuously, cooling, centrifuging and washing the filter cake with water and drying to obtain nicarbazin; and (iii) recycling nicarbazin mother liquor and recycling the solvent.    USE - The method is useful for preparing nicarbazin (claimed).    ADVANTAGE - The method: ensures the production in a single resection kettle (claimed); realizes clean production and reduces energy consumption; reduces the operation time and steps; and reduces the use of production equipments.    DETAILED DESCRIPTION - Preparing nicarbazin comprises (i) adding p-nitroaniline, solid phosgene and a reaction solvent into a reaction kettle, reacting for 16-30 hours at 75-135 degrees C and monitoring the reaction by thin layer chromatography for complete conversion of p-nitroaniline to 1,3-bis(4-nitrophenyl)urea; (ii) reducing temperature of the reaction system to 50 degrees C, adding methanol, stirring uniformly, adding acetylacetone, urea and an inorganic acid, heating to 70 degrees C and reacting for 9-15 hours, adjusting pH to 6 using an alkali, stirring continuously for 3-10 hours, cooling to 20-25 degrees C, centrifuging, collecting the centrifugal mother liquor for recycling, washing the filter cake with water and drying to obtain nicarbazin; and (iii) recycling nicarbazin mother liquor and recycling the solvent.
NOVELTY - Conversion and synthesis of ellagic acid from galla chinensis tannic acid production waste comprises preparing tannic acid production waste solution with total solid content accounting for 15-25%, adjusting concentration of tannic acid in the solution to 0.7-0.9 mg/ml and gallic acid to 0.1-0.3 mg/ml, adjusting pH to 8-10 with alkali solution, continuously introducing air or oxygen for 4-6 hours, filtering, washing the precipitate, suspending the precipitate in hydrochloric acid solution of pH 1-3, stirring for 1-3 hours, filtering, washing the precipitate, and vacuum freeze-drying.    USE - The method is useful for conversion and synthesis of ellagic acid from galla chinensis tannic acid production waste (claimed).    ADVANTAGE - The method converts waste into treasure, ensures comprehensive utilization of galla chinensis, produces high-purity ellagic acid which provides basis for research on the pharmacology and drug efficacy of the ellagic acid and to the development of a functional terminal product, and ensures comprehensive utilization of circular economy strategy.
NOVELTY - The method involves arranging a spray drying drum (1) in a slurry pump (3) for scraping a material screen. A grading cone (4) is provided with a sieve. The sieve is provided with a spiral returning plate (6). The spiral returning plate is provided with a high pressure spray gun (2) and an inclined guide plate (7).    USE - Calcium super phosphate spray granulation method.    ADVANTAGE - The method enables achieving uniform granularity, high integral intensity, energy-saving and environment-friendly effect, and low labor intensity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a calcium super phosphate spray granulation device.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view illustrating a calcium super phosphate spray granulation method.    Injecting spray drying drum (1)    High pressure spray gun (2)    Slurry pump (3)    Grading cone (4)    Spiral returning plate (6)    Inclined guide plate (7)
NOVELTY - A peptide -microbial organic fertilizer preparation method involves mixing slaughter blood organic waste water mixture and animal bone in a colloid mill. The mixture is pulped, and added with sugar. The mixture is pumped into a tubular sterilizer for sterilizing. The sterilized mixture is fermented, and cooled. Animal protein hydrolase and lipase are added. Enzymolysis reaction is performed. Mixed strain is added into an anaerobic fermentation tank, and fermented. Supernatant liquid is removed, and the clear liquid filtered to obtain peptide microorganism organic fertilizer.    USE - Method for preparing peptide-microbial organic fertilizer.    ADVANTAGE - The method enables preparing peptide-microbial organic fertilizer in simple and environment-friendly manner.    DETAILED DESCRIPTION - A peptide -microbial organic fertilizer preparation method involves mixing 85-90 mass% slaughter blood organic waste water mixture and 10-15 mass% animal bone in a colloid mill. The mixture is pulped into 160-200 meshes. 5-15 wt.% sugar is added with the mixture, and stirred for 15-20 minutes. The mixture is pumped into a tubular sterilizer for sterilizing at 90-140 degrees C. The sterilized mixture is added into a fermenting tank, and fermented. The fermented material is cooled at 40-50 degrees C. 0.1-0.5 wt.% animal protein hydrolase and lipase are added. Enzymolysis reaction is performed at 40-50 degrees C for 2-4 hours, and cooled at 37 plus minus 2 degrees C. 0.2-0.5 wt.% mixed strain is added in to an anaerobic fermentation tank, and fermented at 28 plus minus 2 degrees C for 20-24 hours. The strain is cooled at room temperature, and pH value is adjusted to 5-6. Supernatant liquid is removed, and the clear liquid filtered to obtain peptide microorganism organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for preparing peptide-microbial organic fertilizer. '(Drawing includes non-English language text)'
NOVELTY - A water-retaining soilless culture substrate production method involves utilizing cow manure and pig manure as organic matters, smashing the cow manure and the pig manure to the diameter of less than 5 mm, mixing at a weight ratio of 1:1, adding clear water to enable water content of the mixture to reach 45%, adding 0.2% organic fertilizer for fermenting special micro-ecological active microbial agents, controlling the temperature at 15-35 degrees C for piling fermentation after sufficient and stirring, raking completely from top to bottom once every five days, and drying for standby after 20 days.    USE - Method for producing water-retaining soilless culture substrate.    DETAILED DESCRIPTION - A water-retaining soilless culture substrate production method involves utilizing cow manure and pig manure as organic matters, smashing the cow manure and the pig manure to the diameter of less than 5 mm, mixing at a weight ratio of 1:1, adding clear water to enable water content of the mixture to reach 45%, adding 0.2% organic fertilizer for fermenting special micro-ecological active microbial agents, controlling the environmental temperature at 15-35 degrees C for piling fermentation after sufficient and even stirring, raking completely from top to bottom once every five days, and drying for standby after 20 days, where the culture substrate comprises 30-50 wt.% biological organic fertilizer, 5-10 wt.% peat, 10-15 wt.% fine sand, 5-8 wt.% coarse sand, 8-20 wt.% weathered coal, 1-3 wt.% ground phosphate rock, 2-8 wt.% vermiculite, 1-5 wt.% perlite, 2-5 wt.% calcium magnesium potassium mineral powder, 1-7 wt.% medical stone and 0.1-0.5 wt.% water-retaining agent
NOVELTY - Preparation of erlotinib involves performing condensation reaction of 6,7-bis(2-methoxyethoxy)-3,4-dihydroquinazolin-4-one and 3-aminophenylacetylene under effect of organic base and condensing agent.    USE - Preparation of erlotinib (claimed).    ADVANTAGE - The method economically provides erlotinib with high quality under mild reaction condition by a simple process. The erlotinib is environmentally-friendly.
NOVELTY - Method for recycling magnesium ions from magnesium sulfate solution involves mixing the magnesium sulfate solution and potassium chloride, such that magnesium sulfate in the magnesium sulfate solution reacts with the potassium chloride to obtain a mixture containing sulfate-potassium magnesium, cooling the mixture containing sulfate-potassium magnesium, forming sulfate-potassium magnesium crystals, separating the generated sulfate-potassium magnesium crystals, and obtaining a liquid produced after magnesium precipitation.    USE - Method for recycling magnesium ions from magnesium sulfate solution used for magnesium potassium sulfate product (claimed).    ADVANTAGE - The method enables environmentally-friendly recycling of magnesium ions from magnesium sulfate solution by a simple process with reduced energy consumption, and provides magnesium potassium sulfate product with high purity and high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for magnesium potassium sulfate product, which is obtained using the recycling of magnesium ions from magnesium sulfate solution.
NOVELTY - A microorganism potassium fertilizer preparation method involves mixing 35-55 wt.% sylvite powder, 10-15 wt.% peat powder, 15-25 wt.% bean pulp powder and 15-30 wt.% water to obtain a fermentation raw material. 85-95 wt.% fermentation raw material and 5-15 wt.% potassium bacteria liquid are uniformly mixed, and the pH value is adjusted to be 7-8.6. A fermentation liquid is prepared and placed into a fermentation tank at 20-75 degrees C. Primary fermentation is performed on the liquid for 4-6 days and secondary fermentation is performed on the liquid for 5-7 days to obtain finished product.    USE - Process for preparing a microorganism potassium fertilizer for trickle irrigation, liquid sprinkling, flushing and basal applications.    ADVANTAGE - The process enables improving the utilization rate and efficiency of the potassium fertilizer and reducing pollution of residual substances of chemical potassium to soil and fruits.
NOVELTY - A ground vine tea is extracted using hot water at 90-100 degrees C, and filtered. The concentrated filter liquor is cooled to 0-5 degrees C, to separate out sediments. A suction filtration is carried out, and the sedimented residue is dissolved in ethyl alcohol and filtered. The obtained ethyl alcohol solution is concentrated, to prepare ethyl alcohol extract. The prepared ethyl alcohol extract is added into pyrosulfite solution, and reacted. The reacted liquid is poured into an ice-water mixture, crystallized, filtered, washed, and dried, to obtain the myricetin.    USE - Preparation of myricetin (claimed).    ADVANTAGE - The myricetin has excellent transformation efficiency, high yield and purity, and is prepared by simple and environmentally-friendly method.    DETAILED DESCRIPTION - A ground vine tea is extracted using hot water at 90-100 degrees C, and filtered. The concentrated filter liquor is cooled to 0-5 degrees C, to separate out sediments. A suction filtration is carried out, and the sediment residue is dissolved in an absolute ethyl alcohol and filtered, to remove the undissolved substances. The obtained ethyl alcohol solution is concentrated, to prepare ethyl alcohol extract. The prepared ethyl alcohol extract is added into 10-40 %mass pyrosulfite solution, and reacted at 80-100 degrees C. The amount of pyrosulfite solution added is 1-3 times the amount of the ethyl alcohol extract. The reacted liquid is poured into an ice-water mixture, crystallized, filtered, washed, and dried, to obtain the myricetin.
NOVELTY - Preparing 4-amino-3-methyl quinoline nitrile derivative (I) involves cyclizing 3,4-di-substituted aniline (IIa) to a condensation reaction with 3,3-dimethoxy-2-formyl propionitrile (IIb) to obtain 6,7-3-methyl quinoline (III), intermediate (III) to generate 6,7 via oxidation and nitrification-di-substituted -4-nitro-3-methyl quinoline nitrile N-oxide (IV), intermediate (IV) to obtain 4 reduction amino-3-methyl quinoline derivatives (I).    USE - For preparing 4-amino-3-methyl quinoline nitrile derivative used as anti-tumor medicine.    ADVANTAGE - The preparation method is featured with easily obtained material, and has simple technique The method is economical and environment-friendly.    DETAILED DESCRIPTION - Preparing 4-amino-3-methyl quinoline nitrile derivative of formula (I) involves cyclizing 3,4-di-substituted aniline (IIa) to a condensation reaction with 3,3-dimethoxy-2-formyl propionitrile (IIb) to obtain 6,7-3-methyl quinoline (III), intermediate (III) to generate 6,7 via oxidation and nitrification-di-substituted -4-nitro-3-methyl quinoline nitrile N-oxide (IV), intermediate (IV) to obtain 4 reduction amino-3-methyl quinoline derivatives (I).    Y1=H, F, Cl, Br, I, OH, NO, -NO2, -NH2, -COOH, -CN, -CF3, -OCF3, alkyl, ether, -NHR1, -NR1R1, ester, -SO3R1, -R2OH, -R2OR1, alkyl (-R2NH2), alkyl (-R2NHR1K) alkyl tertiary amine (-R2NR1R1), -NHR3OH, -NR1R3OHh, -NHR3OR1K, -NR1R3OR1), -OR3OH, -OR3OR1K, -OR3NH2, -OR3NHR1, -OR3NHR1R1), -OCOR1, -NHCOR1, -NHCONHri, acyl group -OR3COR1, amino group alkyl, -NHR3COR1, -COR1, -COOR1, -CONHR1, -CONR1R1K, -R2COR1, -R2COOH, -R2COOR1, -R2CONH2, -R2CONHR1, -R2CONR1R1K, -R2OCOR1K, -R2OCONH2, -R2OCONHR1 or -R2OCONR1R1;    X and K=not defined.
NOVELTY - The storage tank has main structure that is provided with several working chambers. The working chambers are filled with garbage. The garbage is dried, after completing the production in the drying rack. The fermentation methane gas is pulverized with granule fuel in the pulverizing device.    USE - Garbage storage tank used in house, factory, heat power plant, farming village and forest area.    ADVANTAGE - The storing of the garbage can be made effectively, thus the environment can be protected from contaminants. The economical benefits of the storage tank can be improved. The cost of the storage tank can be lowered. The economic efficiency of the storage tank can be enhanced.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the garbage storage tank.
NOVELTY - Urea is reacted with methanol in a reaction kettle to generate a reaction product containing methyl carbamate and ammonia. Ammonia is led out of kettle in batches, and the ammonia is supplied into a urea synthesis device as raw material to react with carbon dioxide, and urea is again generated. The reaction kettle is connected with a condensing device, and the condensing device is selectively connected with the gas recycling device. The reaction kettle is connected with ammonia gas recovery device to recover ammonia gas, and recovery device is connected with urea synthesis device.    USE - Manufacture of methyl carbamate (claimed).    ADVANTAGE - The methyl carbamate is economically manufactured under intermediate temperature and pressure without catalyst, and the rate of conversion from urea to methyl carbamate is improved. By reaction converting the exported ammonia into urea, the greenhouse gas carbon dioxide is consumed, thus environmentally-friendly.
NOVELTY - Preparation of soil conditioner, involves collecting ultrafiltrated protein residue as active ingredient, adjusting pH of protein residue to 6 by adding alkali, adding 1-3 wt.% urea, 2-5 wt.% potassium dihydrogen phosphate and 1-3 wt.% magnesium sulfate to mixture, and performing anaerobic fermentation at room temperature for 4-15 days by using growth-promoting microbial inoculum or effective microorganism (EM) raw liquid.    USE - The method is useful for preparing soil conditioner (claimed).    ADVANTAGE - The method is convenient to operate, low in cost, and environmentally-friendly, has no secondary contamination in the production process, and saves energy. The prepared soil conditioner has excellent effect and agricultural product produced by the soil conditioner has excellent quality.    DETAILED DESCRIPTION - Preparation of soil conditioner, involves collecting ultrafiltrated protein residue as active ingredient, adjusting pH of protein residue to 6 by adding alkali, adding 1-3 wt.% urea, 2-5 wt.% potassium dihydrogen phosphate and 1-3 wt.% magnesium sulfate to mixture, and performing anaerobic fermentation at room temperature for 4-15 days in isolated air under the condition of pH 4-7, by using growth-promoting microbial inoculum or effective microorganism (EM) raw liquid, where mass ratio of microbial inoculum and protein residue is 1:400-800, and soil conditioner is greater than or equal to 4% fulvic acid, greater than or equal to 3% free amino acids, greater than or equal to 6% nitrogen (N), phosphorus pentoxide (P2O5), and potassium (K), and greater than or equal to 3% trace element.
NOVELTY - Preparing 4-((3-chloro-4-fluorophenyl)amino)-6-((4-(N,N-dimethylamino)-1-oxo-2-butene-1-yl)amino)-7-((S)-(tetrahydrofuran-3-yl)oxyyl)quinazoline (Afatinib) involves: etherification of 4-chloro-6-amino-7-hydroxy-quinazoline (II) and (S)-3-hydroxy tetrahydrofuran to obtain 4-chloro-6-amino-7-((S)-(-3-yl)oxy)quinazoline (III); acylation reaction of compound (III) with 4-(N, N-dimethylamino)-2-enebutyl chloride to obtain 4-6-((4-(N, N-dimethylamino)-1-oxo-2-butene-1-yl)amino)-7-((S)-(-3) oxy) quinazoline (IV); and condensation reaction of compound (IV) and 4-fluoro-3-chloroaniline.    USE - In preparing 4-((3-chloro-4-fluorophenyl)amino)-6-((4-(N,N-dimethylamino)-1-oxo-2-butene-1-yl)amino)-7-((S)-(tetrahydrofuran-3-yl)oxyyl)quinazoline (Afatinib) (claimed) for treating late stage non-small cell lung and advanced breast cancer.    ADVANTAGE - The method is simple, economical and environment-friendly, and is suitable for industrial amplification.
NOVELTY - Apparatus for producing biological energy source by organic waste and sludge comprises a biological reaction tower, the inner cavity of the reaction tower is divided into separate functional spaces vertically by separation plates; the inner cavity of the reaction tower is provided with a vertical stirring shaft provided with stirring blades which are respectively disposed in the separate functional spaces; the separation plates are fixed on the inner cavity of the reaction tower; and the separation plates are provided with through holes.    USE - The apparatus or process is useful for producing biological energy source by organic waste and sludge (claimed).    ADVANTAGE - The apparatus and process are short in gas production time, high in efficiency, high in gas production rate and good in solid-gas separation effect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is a process for producing the biological energy source comprising: (1) hydrolysis reaction: polysaccharides are decomposed into soluble monosaccharides under the effect of anaerobic bacteria; (2) acidification reaction: the soluble monosaccharides are absorbed and acidified into organic acids, alcohols, hydrogen and carbon dioxide by fermentation bacteria in the sludge; (3) gasification reaction: organic acids, hydrogen and carbon dioxide are subjected to the biochemical treatment by methane bacteria to generate methane; and (4) gas-residue separation: methane gas in solid residue rises and is discharged, and the solid residue is discharged downward, under extrusion of horizontal spiral vanes.
NOVELTY - Biomass preparing aromatic hydrocarbon device, especially biomass is lignocellulosic making device of an aromatic hydrocarbon by grinding device and the hydrogen production device. It is feeding port on the upper part of the shell, the lower part of the feeding port is grinding device, grinding material into the first mixing chamber, the mixing chamber is added aromatic hydrocarbon diluting device, a hydrogen pressure device, connected to the first mixing chamber and grinding device in the second mixing chamber is rich in aromatic hydrocarbon slurry with the grinding material catalytic continuously mixing a catalytic agent in the mixing chamber to form a second rich in aromatic hydrocarbon, the discharge hole at the bottom of the shell body, so as to grind the biomass catalytic form aromatic hydrocarbon, realizes the recycle use of biomass.
NOVELTY - This utility model claims a kind of marsh gas cooling and drying device, comprising a biogas fermentation tank (1) and biogas condensing conduit (5), a methane condensing conduit (5) is connected with the marsh gas fermentation tank (1) of the air outlet pipe (2) and the other end is connected with gas pipeline set on the ground surface (3) of the (4), the marsh gas condensation pipe (5) is set on the ground surface (3), the marsh gas condensing conduit (5) of the pipe body is connected with a condensed water collecting pipe (13), a condensed water collecting pipe (13) is set at the lower end of the condenser (6), the top of the condensing chamber (6) is set on the ground surface (3), and the top of the condensing chamber (6) is provided with a well cover (7). This utility model can make use of temperature to cool, dry methane, the methane reaches the needed temperature, it has simple structure, low production cost and convenient for maintenance.
NOVELTY - A thermal insulation biological medium oxidation treatment method involves removing solid impurities in the domestic sewage. Oxidation and nitrogen and phosphorus removal treatment are performed on the treated domestic sewage by virtue of microorganism medium, to remove organic matters. The domestic sewage is fed into a denitrification tank added with a carbon source to be denitrified, where temperature of the microorganism medium is maintained to be 10-50 degrees C.    USE - Method for thermal insulation biological medium oxidation treatment of domestic sewage.    ADVANTAGE - The method enables thermal insulation biological medium oxidation treatment with low investment on treatment of the domestic sewage, low operating cost, simple maintenance and management, stable operation, without no secondary pollution, influenced by regions and seasons and effluent quality can meet water quality standard of landscape surface water.
NOVELTY - A tubers vinasse high-value conversion method involves removing impurities from cassava powder, mixing the powder with tap water or decarburized biogas slurry to obtain mixed liquid. Liquefication and saccharification processes are carried out. A fermentation process is carried out by inoculating well-cultured wine-brewing yeast starter liquid into a fermentation medium and controlling fermentation temperature. Fermentation broth is distilled to obtain a finished product comprising ethanol and waste distillation liquid. The liquid is centrifugalized to obtain supernatant and wet cassava slag.    USE - Recycling method for high-value conversion of tubers vinasse.    ADVANTAGE - The method enables providing zero emission of organic waste water and high efficiency, and increasing production rate and output of biogas.    DETAILED DESCRIPTION - A tubers vinasse high-value conversion method involves removing impurities from cassava powder, mixing the cassava powder with tap water or decarburized biogas slurry to obtain mixed liquid. pH of the mixed liquid is adjusted. Liquefication and saccharification processes are carried out with the mixed liquid by using alpha-amylase and saccharifying enzyme. A fermentation process is carried out by inoculating well-cultured wine-brewing yeast starter liquid into a fermentation medium and controlling fermentation temperature at 28-34 degrees C. Fermentation broth is distilled to obtain a finished product comprising ethanol and waste distillation liquid. The waste distillation liquid is centrifugalized to obtain supernatant and wet cassava slag.
NOVELTY - A carbon source preparing method involves pre-processing kitchen rubbish by removing impurity and crushing. The pre-processed kitchen rubbish is placed in anaerobic acid reactor to carry-out fermentation. The mixture is stirred for producing acetic acid and ethanol product to produce hydrogen. The kitchen rubbish is fermented to obtain slurry with rich organic acid through centrifugal separation device. The slurry is introduced into a denitrification and dephosphorization system. Final treatment is carried-out on the kitchen waste residues generated through centrifugalization.    USE - Method for preparing carbon source.    ADVANTAGE - The method enables preparing carbon source with low cost, no toxicity, less kitchen waste, reusability and no harm.    DETAILED DESCRIPTION - A carbon source preparing method involves pre-processing kitchen rubbish by removing impurity and crushing. Not fermented materials such as paper, plastic and mineral, are removed. The pre-processed kitchen rubbish is placed in an anaerobic acid reactor to carry-out fermentation, where pH of the reactor is controlled by adding sodium hydroxide or hydrochloric acid and temperature is 45-50 degrees C. The mixture is stirred for producing acetic acid, propionic acid, butyric acid, valeric acid and ethanol product to produce hydrogen. The kitchen rubbish is fermented to obtain slurry with rich organic acid through centrifugal separation device. The slurry is introduced into a denitrification and dephosphorization system. Final treatment is carried-out on the kitchen waste residues generated through centrifugalization. The generated hydrogen is used as clean energy.
NOVELTY - A method for improving enzymolysis saccharification efficiency of lignocellulose involves crushing a lignocellulose raw material with 30-75% water mass, and storing the material in a sealing device. The material is added and heated into a steam explosion reactor using steam, where pressure is released to obtain a solid-liquid mixture. Solid-liquid separation, washing and drying processes are carried on the mixture. Cellulase and water are added into the dried mixture, and followed by solid-liquid separation to obtain liquid glucose and xylose.    USE - Method for improving enzymolysis saccharification efficiency of lignocellulose.    ADVANTAGE - The method enables reducing biomass loss, maintaining flexibility of the biomass and porous structure. The method enables realizing high sugar recovery rate and less degradation product, and improving enzymolysis saccharification rate.    DETAILED DESCRIPTION - A method for improving enzymolysis saccharification efficiency of lignocellulose involves crushing a lignocellulose raw material with 30-75% water mass, and storing the material in a sealing device. The material is added and heated into a steam explosion reactor using steam, where pressure is released to obtain a solid-liquid mixture. Solid-liquid separation, washing and drying processes are carried on the mixture. Cellulase and water are added into the dried mixture, and pH value of the mixture is adjusted in the range of 4.5-5.5, followed by solid-liquid separation to obtain liquid glucose and xylose.
NOVELTY - Preserving cherry tomato comprises harvesting eight mature cherry tomatoes; preserving, and adding 0.0015-0.003% eugenol, 0.5-1.5% chitosan, 1.5-3% citric acid and balance water; dissolving citric acid in hot water at 50-60 degrees C, and stirring the chitosan solution, cooling the fluid at room temperature, and dissolving; soaking the fruit for 2-5 minutes and picking; and drying the fruit at 20 degrees C, and storing.    USE - Method for preserving cherry tomato (claimed).    ADVANTAGE - The method can provide cherry tomato that uses preservative components which are pure natural, non-toxic, safe and environment-friendly.
NOVELTY - And the utility model claims a packing auger conveyor, a packing auger conveyor comprising a shell (11) and is set in the first push rod (12) of the shell, the upper part of the shell (11) is provided with a feed inlet (11a), the lower part is provided with a discharging port (11b), the first push rod (12) comprises a rotating shaft (12a) and the rotating shaft (12a) is set on the upper part of the first spiral blade (12b), wherein the housing (11) is set on the inner surface (13), the scraping component (13) is located between said first spiral blade (12b) is connected with the edge of the shell (11) inner surface. This utility model also claims a cellulose ethanol raw material pre-processing system. Provided with a scraper capable of the spiral blade and the scattering material and the inner surface of the shell so as to prevent the bulk material blocking between the spiral blade and the shell body, the shell body of the packing auger conveyor.
NOVELTY - This utility model claims a kind of organic waste integrated tank with fermentation and gas processor, comprising a containing the organic matter adsorption filler of bio-reaction device, the reaction device is provided with a spray head of atomizing fumigator for constant temperature liquid from a spraying filling nutrient solution to the upper part in turn is provided with a stuffing filter layer is at least two stages, the filler filter layer is provided with a spraying device, the spraying device. This utility model realizes integrated design, the pre-wet gas and purifying the same time, to form a wet environment more balanced, which is more helpful for the growth and propagation of the absorbing and degrading the pollutant, and the gas capable of back-flow, the exhaust gas residence time, improve the purifying effect of the organic bio-filler.
NOVELTY - This utility model claims a rotating tube reactor, comprising a horizontal cylinder, comprising an inner cylinder and an outer cylinder, wherein the two ends of the front end is provided with a detachable and a detachable back end, of the outer peripheral wall is provided with a sliding matched with the cylinder supporting rod and the cylinder is rotatably connected with an inner cylinder, an outer cylinder on the outer peripheral wall is fixedly provided with a cylinder supporting rod, the inner surface of the inner cylinder is provided with a used for realizing mixed with spiral propeller is pushed forwards to the material, the bottom and the bottom of the back end of the front end are respectively fixed with end support rod, a front end head is provided with a first sealing device is connected with the inner cylinder, and the end head is provided with a second sealing device is connected with the inner cylinder and has the advantages of simple structure, convenient operation, and it can realize the continuous feeding and discharging, and it can effectively control each point in the reactor temperature.
NOVELTY - This utility model claims a kind of fast enrichment nitrite-oxidizing bacteria of the culture device, relates to a sewage treatment and biological technology combined with the cross technical field, comprising a microorganism culture reactor is connected with a water inlet pipe, a water outlet pipe, a return pipe, an aeration pipe, aeration pipe is connected with the air inlet of the compressor, culture liquid microorganism culture tank is connected by the water pipe, the middle water tank is connected with the microorganism culture reactor through a return pipe, stirrer, aeration pipe, an aeration head, a microorganism culture reactor, the dissolved oxygen concentration DO sensor, a pH sensor, a temperature sensor and a heater; This utility model can make the growth of heterotrophic bacteria and ammonia-oxidizing bacteria in the sludge with obviously inhibit, promote enrichment nitrite-oxidizing bacteria of the microorganism bacteria total number in the active sludge is 85-90%, and tolerance is higher the nitrite concentration in high concentration nitrite waste water is reduced to less than 0.2mg/L.
NOVELTY - This utility model belongs to the control field, especially relates to a kind of anaerobic ammonia oxidation bacteria (Anammox) enriched reaction device. The reaction device comprises a reactor, a peristaltic pump and a water inlet box, a reactor is a continuous stirred tank reactor, the bottom of the reactor is provided with a water inlet and a mud discharge pipe, a water inlet box by a peristaltic pump and the water inlet are connected with the top of the reactor to ensure strict sealing anaerobic environment, is provided with a thermometer probe and a gas collecting pipe, a stirrer on the top part, the reactor is provided with a gas-liquid-solid three-phase separator. The device can be anaerobic ammonia oxidation water treatment process fast enriched anaerobic ammonia oxidizing bacteria, which can reduce the substrate concentration in the reactor, so as to effectively improve the product yield and reactor operation.
NOVELTY - Synthesizing nifuratel, comprises (i) substituting methylthio propylene oxide with 80% hydrazine hydrate to obtain 3-methylthio-2-hydroxypropyl hydrazide, (ii) subjecting 3-methylthio-2-hydroxypropyl hydrazide and diethyl carbonate to cyclization reaction to obtain 3-amino-5-(methylthio)oxazolidin-2-one, (iii) subjecting 2-(bis-methoxymethoxy-methyl)-5-nitro-furan and 10% sulfuric acid to hydrolysis reaction to obtain 5-nitro-furan-2-carbaldehyde and reacting directly with 3-amino-5-(methylthio)oxazolidin-2-one to obtain crude product, and (iv) recrystallizing the crude product.    USE - The method is useful for synthesizing nifuratel.    ADVANTAGE - The method: is carried out in a simple, easy and environmental friendly manner; is easy to control; and uses readily available raw materials.    DETAILED DESCRIPTION - Synthesizing nifuratel, comprises (i) substituting methylthio propylene oxide with 80% hydrazine hydrate at 80-85 degrees C and distilling off the reaction water under reduced pressure to obtain 3-methylthio-2-hydroxypropyl hydrazide, (ii) subjecting 3-methylthio-2-hydroxypropyl hydrazide and diethyl carbonate in a solution of sodium methoxide in methanol to cyclization reaction at 60-70 degrees C, and adding ethanol after completion of the reaction to obtain 3-amino-5-(methylthio)oxazolidin-2-one, (iii) subjecting 2-(bis-methoxymethoxy-methyl)-5-nitro-furan and 10% sulfuric acid in 95% ethanol to hydrolysis reaction to obtain 5-nitro-furan-2-carbaldehyde and reacting 5-nitro-furan-2-carbaldehyde directly with 3-amino-5-(methylthio)oxazolidin-2-one obtained in the step (ii) at 20-25 degrees C to obtain a nifuratel crude product, and (iv) recrystallizing the crude product and purifying.
NOVELTY - Manufacture of fatty acid involves thermally cracking and gasifying biomass to produce synthesis gas, contacting synthesis gas with hollow fiber film, supplying synthesis gas to in-situ attaching medium supply device, and performing anaerobic microorganism fermentation.    USE - Manufacture of fatty acid e.g. long-chain fatty acid.    ADVANTAGE - The fatty acid is manufactured efficiently by simple method.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacturing apparatus of fatty acid.
NOVELTY - This utility model claims a kind of environment-friendly livestock manure turning pulling machine, comprising a track frame, a travelling crane, a button switch and a wireless signal receiver and a wireless remote controller, a linkage mechanism comprises a direct current motor, a speed reducer, a driving gear and the output gear of the speed reducer is engaged with a direct current control circuit control and a chain wheel transmission mechanism, a direct current control circuit control the charging energy source or connected with the wireless signal receiver. A control button switch and remote wireless signal, core controller controls the direct current motor of direct current program-controlled circuit the positive and negative rotation driving reciprocating travel along the rail frame, at the same time, the thumb wheel rotating mixing livestock excrement and filler and uniformly stirring to make it through the linkage mechanism, an automatic return, the fermentation process and apparatus for the automatic production process. Compact structure, reduces the difficulty and cost of the breeding farm pollution. The operation is simple, convenient installation and maintenance, a wireless operation, safe environment-friendly and energy-saving.
NOVELTY - This utility model claims a sewage treatment of biological contact oxidation pond, the sewage treatment of biological contact oxidation tank comprises a tank body, a water inlet pipe, an aeration pipe, a water outlet pipe, the tank body is provided with a longitudinal unit grid, cell groove are connected with each other, and each unit grid is filled with filler and immobilized microorganism particles, the lower part of each unit grid is provided with a aeration pipe, the aeration pipe are located on the same horizontal plane and are parallel to each other, each aeration tube is connected with air inlet pipe, a gas inlet pipe is provided with an electric valve, the water pipe is set on the aeration pipe, the upper part of each unit grid are arranged with a groove and a convex rib, two adjacent cells is connected with the groove and convex edge. This utility model uniform aeration, filler is not easy to be blocked, it solves the high concentration ammonia-nitrogen, sulphide, phenol and so on for treating sewage of high concentration ammonia-nitrogen, sulphide, phenol and so on of good sewage treatment effect, convenient to install.
NOVELTY - This utility model claims a kind of thick bamboo fibre sewage treatment, the sewage treatment filler is thick bamboo fibre as base materials. The sewage treatment filler is elastic or composite filler is thick bamboo fibre as base materials are fixed to the central rope or embedded to obtain the fixed disc surface of the thick bamboo fibre is three-dimensional uniformly arranged radial structure. Using this utility model of sewage treatment filler treating sewage: bioreactor starting time is shortened for 7 days compared with the traditional organic elastic. Compared with traditional organic elastic filler, chemical oxygen demand and ammonium nitrogen average removing effect is obviously improved. As thick bamboo fibre flexibility of the difference, and the film is uniformly distributed, fully stretching the biochemical reactor and cohesion structure, makes full use of the space, enhance microorganism contact chance with the sewage and mass transfer effect.
NOVELTY - This utility model claims a kind of kitchen garbage joint alcohol and lactic acid of the integrated device. The main body of the device is water-separating-coupling fermentation reactor, comprising a tank body, a sight glass, a bracket, a U-shaped jacket, a pressure gauge, a screen, used for solid-liquid separation of the stirrer, which is used for testing the tank body inner part temperature of the reaction electrode, pH electrode for testing tank body material pH value and dissolved oxygen electrode for testing tank body material dissolved oxygen, sight glass, a pressure gauge, a temperature electrode, pH electrode and a dissolved oxygen electrode is set on the upper part of the tank body, the bracket is set at the bottom of the U shape jacket of the tank body is provided with a tank body, a screen in the bottom of the tank body, a stirrer comprises a motor, a stirring shaft and a blade, a motor and a stirring shaft, the fan blade is set on the stirring shaft, a motor is set on the outer top part of the tank body, a stirring shaft and a fan blade is suspended in the interior of the tank body. A coupling device for kitchen garbage hydro-thermal treatment, three-phase separation, fermentation device, greatly reduces the consumption of the energy.
NOVELTY - The method involves providing a base metal used as a reference point of plating formation to one surface of a porous structure or inner wall face of a pore (17) from one surface of porous structure. The plating solution is supplied to other surface side of porous structure while supplying electrolyte solution to one surface side. An electron is supplied to base metal through electrolyte solution which is infiltrated into the pore from one surface side. A plating film is deposited on base metal with plating solution, such that a hydrogen separation metal layer is formed.    USE - Manufacturing method of hydrogen separator.    ADVANTAGE - The generation of the gas leak by the damage of surface membrane can be prevented. The hydrogen separator can be manufactured easily, without damaging the apparatus.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the hydrogen separator.    DESCRIPTION OF DRAWING(S) - The drawing shows an explanatory view explaining the manufacture of hydrogen separator. (Drawing includes non-English language text)    Center hole (7)    Porous support (9)    Pore (17)    Electroless-plating layer (71)    Electroplating layer (77)
NOVELTY - A compost tea micro-fermentation package preparing method involves selecting raw materials. Animal manure is added to the raw materials and fermented for 60 days. The fermented materials are packed in polyethylene pours bags to obtain compost tea packaging materials, where the polyethylene bags are punched with marked microspores forming micro compost tea and the compost tea is maintained in high temperature aerobic fermentation for decomposing compost.    USE - Method for preparing a compost tea micro-fermentation package that is utilized for leaching compost tea.    ADVANTAGE - The compost tea micro-fermentation package has reduced labor intensity and labor investment, high disease-prevention effect and biological effect, and is simple to prepare.
NOVELTY - A diphenyl oxide derivative (I), is new. The diphenyl oxide derivative (I) is prepared by culturing Aspergillus sp. (HM535361), performing fermentation, immersing the fermentation product in methanol, decompressing and concentrating the product to obtain crude extract, suspending the extract in water, performing extraction, decompressing and concentrating extract, performing chromatographic separation, and concentrating the obtained eluate to obtain compounds including 4-methoxycarbonyl-diorcinol, 3,3'-O-dimethyl-violaceol-I, cordyol C and diorcinol.    USE - The diphenyl oxide derivative is useful as natural marine antifouling agent for preventing and controlling attachment of Balanus amphitrite larva (all claimed).    ADVANTAGE - The diphenyl oxide derivative is environmentally-friendly and has minimal toxicity.    DETAILED DESCRIPTION - A diphenyl oxide derivative of formula (I), is new. The diphenyl oxide derivative (I) is prepared by culturing Aspergillus sp. (HM535361), preparing fermentation culture medium and performing fermentation, immersing the obtained fermentation product in methanol, decompressing and concentrating the product to obtain crude extract, suspending the extract in water, performing extraction using ethyl acetate, decompressing and concentrating ethyl acetate extract, performing chromatographic separation, and concentrating the obtained eluate to obtain colorless or light red color oily compounds including 4-methoxycarbonyl-diorcinol, 3,3'-O-dimethyl-violaceol-I, cordyol C and diorcinol.    R1,R4=H or OH;    R2,R5=OH or OCH3;    R3=COOCH3 or H;    R1,R2,R5=OH;and    R1,R3,R4=H.
NOVELTY - Nitro compound (I), and aldehyde compound (II), (III) or phthalic acid are reacted in presence of zinc dust as catalyst and reducing agent. Acetic acid or ammonium chloride as reaction medium is added to resulting mixture and reacted in presence of solvents chosen from methanol, ethanol, acetonitrile, water, methanol/water, ethanol/water and acetonitrile/water, to obtain amide compound (V), (VI) or (VII).    USE - Synthesis of amide compound used for synthesizing pesticide.    ADVANTAGE - The method environmentally-friendly provides amide compound, under mild reaction condition within a short period of time, by a simple process.    DETAILED DESCRIPTION - Nitro compound of formula (I), and aldehyde compounds of formula: R2-CHO (II), (III) or phthalic acid are reacted in presence of zinc dust as catalyst and reducing agent. Acetic acid or ammonium chloride as reaction medium is added to resulting mixture and reacted in presence of solvents chosen from methanol, ethanol, acetonitrile, water, methanol/water, ethanol/water and acetonitrile/water, to obtain amide compounds of formula (V), (VI) or (VII).    R=o-, m-, p-(H, F, Cl, Br, -CH3, -OCH3, -COCH3, -COOCH3, or -COOC2H5);    R1=o-, m-, p-(H, F, Cl, Br, -OH , or -CH3);and    R2=-CH3, or -CH2CH2CH3 .
NOVELTY - A biodegradation bin comprises a biodegradation chamber (1) having an inner sleeve (11) and an outer sleeve cylinder (12), a cavity (13) installed inside a thermally conductive medium (17), end caps (14, 15) in the inner sleeve ends, a feeding inlet (141), an end cover (15), a discharging port (151), a discharging packing auger (16), and a jacket (42) having a thermal medium inlet (171) and a thermal medium inlet (172).    USE - A biodegradation bin used for an animal waste harmless treatment device (claimed).    ADVANTAGE - The device can completely inactivate common pathogenic microorganisms and thoroughly achieve harmless treatment.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic diagram of the device.    Biodegradation chamber (1)    Inner sleeve (11)    Outer sleeve cylinder (12)    Cavity (13)    End caps (14, 15)    End cover (15)    Discharging packing auger (16)    Thermally conductive medium (17)    Jacket (42)    Feeding inlet (141)    Discharging port (151)    Thermal medium inlet (171)    Thermal medium inlet (172)
NOVELTY - Production of biodegradable resin coated controlled-release fertilizer comprises (A) adding tung oil to reactor, heating, adding cold water insoluble urea-formaldehyde resin, acrylic thermoplastic resin, phenolic thermosetting resin, polyacrylamide, modified starch, and polyvinyl alcohol while stirring, heating, continuously stirring, cooling, and adding n-butyl acetate to obtain coating material; (B) granulating base material, and heating; and (C) drying granules, putting into coating machine, controlling temperature, spraying with coating material, cooling, and screening.    USE - Method for production of biodegradable resin coated controlled-release fertilizer (claimed).    ADVANTAGE - The method is simple in process and environment-friendly, completely and biologically degrades polymer resin material, envelops granular urea or granular composite fertilizer, controls release of nutrients according to temperature of soil and requirement of crops, improves utilization rate of fertilizer, and degrades envelop shell in the soil after releasing nutrients.    DETAILED DESCRIPTION - Production of biodegradable resin coated controlled-release fertilizer comprises (A) adding 30-50 pts. wt. tung oil to reactor, heating to 50-65 degrees C, adding 50-65 pts. wt. cold water insoluble urea-formaldehyde resin, 5-15 pts. wt. acrylic thermoplastic resin, 5-15 pts. wt. phenolic thermosetting resin, 3-5 pts. wt. polyacrylamide, 5 pts. wt. modified starch, and 5 pts. wt. polyvinyl alcohol while stirring, heating to 90-95 degrees C, continuously stirring for 30-40 minutes, cooling to 40-50 degrees C, and adding 10-40 pts. wt. n-butyl acetate to obtain coating material; (B) granulating base material, and heating to 50-60 degrees C; and (C) drying granules to 80-95 degrees C until moisture content is 1-2%, putting into coating machine, controlling temperature to 50-80 degrees C, spraying with 2-3 wt.% coating material, cooling, and screening.
NOVELTY - Preparing 3-(3,5-dihydroxy-4-isopropylphenyl)acrylic acid (I), comprises e.g. methylating 3,5-dihydroxybenzoic acid with dimethyl sulfate to obtain methyl 3,5-dimethoxybenzoate, then reacting with isopropanol to obtain 3,5-dimethoxy-4-isopropylbenzoic acid (III), reducing (III) to obtain 3,5-dimethoxy-4-isopropylbenzyl alcohol (IV), performing Pfitzner-moffatt oxidation of (IV) to obtain 3,5-dimethoxy-4-isopropylbenzaldehyde (V), performing Knoevenagel condensation of (V) with malonic acid to obtain 3-(3,5-dimethoxy-4-isopropylphenyl)acrylic acid (VI), and reacting (VI) with boron tribromide.    USE - The method is useful for preparing 3-(3,5-dihydroxy-4-isopropylphenyl)acrylic acid.    ADVANTAGE - The method: avoids use of environmentally hazardous reagents; improves production yield; and solves problem of impurities in drug substance raw materials, and thus it ensures quality standard of raw materials for clinical use.    DETAILED DESCRIPTION - Preparing 3-(3,5-dihydroxy-4-isopropylphenyl)acrylic acid (I), comprises (i) carrying out methylation reaction of 3,5-dihydroxybenzoic acid with dimethyl sulfate to obtain methyl 3,5-dimethoxybenzoate (II), (ii) reacting (II) with isopropanol at 0-100 degrees C in aqueous sulfuric acid solution, and processing to obtain 3,5-dimethoxy-4-isopropylbenzoic acid (III), (iii) carrying out reduction reaction of (III) with diborane reducing agent at 0-100 degrees C in ether solvent, and then post-processing to obtain 3,5-dimethoxy-4-isopropylbenzyl alcohol (IV), (iv) carrying out Pfitzner-moffatt oxidation reaction of (IV) with dimethyl sulfoxide and acetic anhydride at 0-50 degrees C to obtain 3,5-dimethoxy-4-isopropylbenzaldehyde (V), (v) carrying out Knoevenagel condensation reaction of (V) by heating with malonic acid and pyridine in presence of piperidine catalyst to obtain 3-(3,5-dimethoxy-4-isopropylphenyl)acrylic acid (VI), and (vi) reacting (VI) with boron tribromide to obtain final product.
NOVELTY - Triple-component eutectic ionic liquid comprises chloride anion ionic liquids (ILC), rare earth chlorinated salt (REC) and multi-hydrogen compound (HBD). The molar ratio of ILC, REC and HBD is 1:1:0.5-4.    USE - The ionic liquid is useful in an electrochemical cell and a super capacitor, for synthesizing nanomaterials, mesoporous materials, dissolving synthetic and natural fiber, and for catalytic gas adsorption (claimed).    ADVANTAGE - The ionic liquid: exhibits low melting point, low viscosity, high conductivity, good dissolving performance; can be produced in a simple and cost efficient manner without discharging toxic substance and by-products; uses readily available raw materials for its production; does not use the organic solvent in the reaction process; and is biodegradable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the triple-component eutectic ionic liquid, comprising uniformly mixing ILC, REC and HBD, heating to 100-140 degrees C and maintaining the temperature for 2-4 hours.
NOVELTY - The aerobic tank to dissolve the utility model claims a capable of maintaining the aerobic state is suitable for the organic waste dissolved. The used organic waste will dissolve the dissolving tank (1), is stored in the tank, ratio of the organic waste to liquid level (S1) is provided with at least one opening and the atmosphere (15) close to the upper part. The opening part (15) is provided for introducing air into the tank, a leading-in opening and used for making the gas in the tank is discharged to the outside of the discharge opening.
NOVELTY - A 6 alpha -amide penicillanate sulfoxide compound is prepared by reacting 6 beta -amido penicillanate sulfoxide compound, trimethylchlorosilane, organic base, and solvent, finishing reaction, and removing trimethyl.    USE - Preparation of 6alpha-amide penicillanate sulfoxide compound (claimed).    ADVANTAGE - Raw is cheap and easy to obtain, preparation process is safe and environment-friendly and has easy separation, production cost is reduced, reaction condition is mild and easy to control, and yield is high.    DETAILED DESCRIPTION - A 6 alpha -amide penicillanate sulfoxide compound of formula (II) is prepared by reacting 6 beta -amido penicillanate sulfoxide compound of formula (I), trimethylchlorosilane, organic base, and solvent, finishing reaction, and removing trimethyl.    R1=arylmethyl, aryloxy or aryl, and    R2=benzyl, benzhydryl, or optionally substituted benzyl on benzene ring or heterocycle with substituent on benzene ring.
NOVELTY - This utility model is a kind of organic compound fertilizer production system, comprising a high pressure hydrolysis system, high temperature hydrolysis system, solid-liquid separation system, solid crushing system and a cooling system is composed of a high pressure hydrolysis system comprises a pressure detecting device, a high temperature hydrolyzing system comprises a temperature detector, solid-liquid separation system comprises a consistency analyzer, cooling system comprises a cooling temperature testing device, and passes through the technical solution is as follows: the production efficiency, and improve the utilization ratio and scientific and the raw material has no pollution to the environment.
NOVELTY - This utility model claims a kind of used for organic fertilizer production of vertical open fermentation tank, belonging to the field of organic fertilizer processing technology field. The vertical open fermentation tank comprises a tank opening, a tank body, a tank with an insulating layer of the bottom, a bracket and a rotating electrical machine, wherein the tank body is set on the supporting column, wherein the outer wall of the tank body wall is provided with a snake-shaped heating pipe, the rotary motor is connected with a stirring frame cross, wherein the rotating motor is fixed on the tank by the supporting frame, the stirring of the cross bracket is fixed on the bracket through the rotating roller, the upper cross stirring frame is provided with a stirring rod, the upper insulating layer is further provided with a charging pipe, the charging pipe is provided with a charging nozzle, a plurality of the tank body. This utility model small floor area, raising the temperature time is short, the fermentation temperature, fermentation time is short, the total fermentation, high degree of mechanization, labour cost and basically does not pollute the environment.
NOVELTY - This utility model is a kind of compound organic fertilizer production system, comprising a sieving system, a mixing system, a sampling system, a mixing system and a moulding system, wherein the sampling system comprises a level sampling system, screening system comprises a sorting device, a magnetic device and a crushing device, mixing system comprises a screening device, a magnetic separation device and mixing device, the two level sampling system is the first level sampling system and sampling system, wherein the sampling system is connected with the secondary sampling system by the technical solution and can reduce the production cost and improve the production efficiency and no pollution to the environment.
NOVELTY - This utility model is a kind of organic compound fertilizer production system, comprising a crushing device, mixing device, granulating device, a drying device and a sieving device, wherein the crushing device is connected with the mixing device, mixing device is connected with the granulating device, granulating device is connected with the drying device, the drying device is connected with the screening device, crushing device comprises a crushing machine, mixing device comprises a mixing module, wherein the mixing module is connected with the secondary mixing a drying device comprises a humidity detector and a temperature detector by the technique solution comprises macro-element, organic nutrient, mass production can be effectively and no pollution to the environment.
NOVELTY - This utility model is a kind of organic compound fertilizer production system, comprising a crushing device, a mixing device, granulating device, a drying device, a screening device and a magnetizing device, wherein the crushing device is connected with the mixing device, mixing device is connected with the granulating device, granulating device is connected with the drying device, the drying device is connected with the screening device, screening device is connected with the magnetizing device, crushing device comprises a crushing machine, mixing device comprises a mixing module, wherein the mixing module is connected with the secondary mixing a drying device comprises a humidity detector and a temperature detector, magnetic device comprises a magnetic induction module, a magnetic sensing module comprises a magnetic induction line generating device, by the technical solution is as follows: scientific and sanitary, has no pollution to the environment, and improves the production efficiency.
NOVELTY - This utility model is a kind of fruit tree with spherical composite fertilizer, which is composed of fertilizer core, layer and layer, wherein from inside to outside in turn into fertilizer core, layer and layer, enzyme layer thickness is 4-5 mm, hydrolyzing is 0.02-0.028 mm, enzymolysis movable layer is set with 1-3 fertilizer core by the technique solution comprises major elements, trace elements, increasing crop resistance, no pollution to the environment.
NOVELTY - This utility model claims a kind of active carbon, caffeine isolated cracking device, the active carbon, caffeine isolated cracking device comprises a feeder, a cracker, a cracker, a condenser and a discharging device. This utility model is used for producing caffeine special device, main improvement is that the host device is changed from the original vertical structure is a horizontal structure, which can absorb a processing water drying and impurity destruction and caffeine separation in the water, impurity and caffeine in the active carbon, extracting, at the same time, the active carbon can be recycled, the whole production process automation, capable of continuously working and improve the production capacity and is safe and environment-friendly.
NOVELTY - This utility model claims a marsh gas collecting and utilizing system, wherein a kitchen waste water treatment system is provided with a middle-temperature reactor, the temperature of the top of the reactor is provided with a marsh gas outlet, a marsh gas storage tank is connected with the biogas outlet connected with the lower part of the marsh gas tank is provided with a cold spraying tank. This utility model is a kind of marsh gas collecting and utilizing system solves the problem that the kitchen waste processing system in current technology is not suitable for Chinese situation, processing effect is not ideal, is easy to cause waste, effectively treating waste water, and collecting and processing the marsh gas to obtain the good waste water treatment effect.
NOVELTY - A kind of film slot combined dry fermentation marsh gas device, belonging to the field of organic solid waste resource utilization field, especially relates to a kind of use, film, a composite structure of dovetail groove, which is suitable for dry fermentation for preparing biogas device. A fermentation tank, a flexible, top, a sealing door, a hydraulic drive system, pneumatic sealing system, an auxiliary heating system, spraying system, a gas circulation system and so on, the fermentation material containing groove, a soft gas collecting heat, solar heat-collecting shed top, a sealing door seal block inlet and outlet, a hydraulic driving system drives the sealing door is opened, pneumatic sealing system for sealing a sealing door, an auxiliary heating system for inoculating material, the gas circulating system for promoting heat transfer material is a material, biogas slurry spraying system. The utility model is provided with engineering construction cost, low operation cost, single reactor process ability, material heat transmission and mass transfer effect is good, the yield is high.
NOVELTY - This utility model claims a fermentation tank and the marsh gas pool combined device, comprising a fermentation tank and the marsh gas tank, the fermentation tank is provided with a hot air device and a waste heat heating circulation device, wherein the marsh gas tank is provided with a hot water circulator and waste heat heating circulating device connected with, a circulator according to waste heat heating is provided with a hot water outlet and a cold water inlet, a hot water circulator is provided with a hot water inlet and a cold water outlet, a hot water inlet through the pipeline is connected with a hot water outlet, a cold water outlet is connected with the cold water inlet through the pipeline. The hot water circulation device of the utility model is provided with waste heat heating circulator with the marsh gas tank, the tank body of the fermentation tank is connected with the water in the fermentation tank by using the heat produced in the process of heating waste heat heating circulation pipe, the generated hot water but also can be hot water circulator using a heating device of small biogas tank to form a virtuous circle, at the same time, solves the problem that the low temperature below a marsh gas pool gas at least;
NOVELTY - Production of microorganism nutrient solution comprises adding 3 L oilfield sewage to microorganism of active sludge comprising water activated sludge microbial strains, performing aeration test oil removal effect in laboratory using scale experiment device for 4 hours, settling for 2 hours, and taking upper part as first test microaerated oil; repeating procedure, recording each test effluent oil content, determining nutrient component according to crude oil degradation rate, detecting, and analyzing main nutrients of chemical agents.    USE - Method for production of microorganism nutrient solution (claimed).    ADVANTAGE - The method has simple operation and reduces microbial sewage system operating costs.
NOVELTY - The utility model claims a method for screening animal excrement organic fertilizer sieving machine, which is suitable for livestock excrement, plant ash, humus and so on fermenting organic fertilizer. A machine frame, a feeding hopper, a feeding hopper bracket, a bearing base, a bearing base, a screen, a screen supporting rod, a screen hoop ring, a screen roller shaft, a coupler, a speed reducer, a belt, a motor, a funnel, mixed material funnel, a motor base, transmission belt and a screen. This utility model is new organic fertilizer sieving machine has novel design, simple structure, can quickly process large scale screening animal excrement, reduce the environmental pollution and the recycled animal excrement, and capable of reducing the labour intensity of the worker, social and efficient development requirement of environment-friendly.
NOVELTY - The method involves discharging food waste injected to first collector (53) to first inlet of the dispersion conveyor (10). The food waste injected to second collector is discharged to the second inlet. The food waste flowed into dispersion conveyor is distributed to the outlet selected between the outlets of the dispersion conveyor. The food waste discharged through outlets is crushed using crushers (15,17). The food waste discharged from the crushers is induced into the dehydrators (18,19), so as to remove foreign substances from food waste.    USE - Method for processing food waste from kitchen.    ADVANTAGE - The food waste can be processed effectively and easily, thus the generation of bad smell caused due to decaying of food can be prevented. The odor removal effect can be enhanced and the neighboring environment can be improved. The economical efficiency can be improved. The high-quality food can be obtained. The moisture of the food waste can be remarkably decreased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an apparatus for processing food waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the processing of food waste. (Drawing includes non-English language text)    Dispersion conveyor (10)    Crushers (15,17)    Dehydrators (18,19)    First collector (53)    Second collector (80)
NOVELTY - Preparation of mesotrione comprises reacting 2-nitro-4-methylsulfonylbenzaldehyde and 1,3-cyclohexanedione mixed solution at 5-45 degrees C, adding alkali solution dropwise, maintaining the reaction temperature for 0.5-2 hours and obtaining 2-(2-nitro-4-(methylsulfonyl)hydroxybenzyl)cyclohexane-1,3-dione as intermediate, reacting obtained compound with oxidizing agent at 35-60 degrees C for 1-3.5 hours, heating, cooling in an ice bath, filtering, washing product with water until neutral and purifying.    USE - Preparation of mesotrione (claimed).    ADVANTAGE - The method efficiently and economically provides mesotrione using simple process without causing pollution to environment.
NOVELTY - Preparation of albendazole involves reacting dichlorobenzene raw material with concentrated sulfuric acid and nitric acid, soda and water and processing organic layer and obtaining 2,4-dichloro-nitrobenzene, reacting obtained compound with amination reaction in organic solvent or water and obtaining 2-nitro-5-chloro aniline, reacting obtained compound with propanethiol in organic solvent or water and obtaining 2-nitro-5-propylthio aniline, reducing obtained compound in organic solvent in presence of catalyst and obtaining 4-propylthio-o-phenylenediamine.    USE - Preparation of albendazole used as insect repellent.    ADVANTAGE - The method efficiently and economically provides albendazole, with high yield.    DETAILED DESCRIPTION - Preparation of albendazole involves reacting dichlorobenzene raw material with concentrated sulfuric acid and nitric acid, soda and water and processing organic layer and obtaining 2,4-dichloro-nitrobenzene, reacting obtained compound with amination reaction in organic solvent or water and obtaining 2-nitro-5-chloro aniline, reacting obtained compound with propanethiol in organic solvent or water and obtaining 2-nitro-5-propylthio aniline, reducing obtained compound in organic solvent in presence of catalyst and obtaining 4-propylthio-o-phenylenediamine and cyclizing obtained product in organic solvent using o-phenylenediamine reagent.
NOVELTY - Method for pretreating solid anaerobic fermentation residues, involves treating the residues using water in a ratio of 1:2.5 for 10-15 minutes, packing treated product, extruding the product for 1-2 minutes to squeeze out excess water, and adjusting the moisture content to 65%.    USE - The method is useful for pretreating solid anaerobic fermentation residues which is useful for producing culture medium of edible mushrooms, and in agriculture and food industry (claimed).    ADVANTAGE - The method utilizes waste material and solves the problem of environmental pollution, saves resources, and provides high social and economic benefits.
NOVELTY - Fruit and vegetable seedling culturing substrate utilizing agricultural wastes, is prepared by processing cassava residues, fungus residues, vinegar residues, gardening vermiculite and gardening perlite in ratio of 4.5:3.5:1:0.5:0.5, and adding 37.5 kg decomposed livestock excrements and mixing thoroughly and evenly.    USE - As fruit and vegetable seedling culturing substrate (claimed).    ADVANTAGE - The substrate is capable of improving quality of the seedlings, reduces consumption of the turf resources, reduces pollution of the agricultural wastes, protects ecological environment, lowers the seedling culturing cost, and realizes cost saving and synergism of vegetable industrialized seedling culturing and sustainable development.
NOVELTY - A cefuroxime lysine compound comprises 98-99.99 wt.% cefuroxime lysine and 0.01-2 wt.% bisdehydro-descarbamoyloxy cefuroxime diacid.    USE - Cefuroxime lysine compound is used as sterile powder injection, frozen dry powder injection and aqueous needle injection (all claimed).    ADVANTAGE - The cefuroxime lysine compound is efficiently prepared with high stability, and reduced impurity content and polymer content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cefuroxime lysine compound, which involves mixing and reacting 7-amino-3-(ethoxymethyl)-8-oxo-5-thia-1-azabicyclo(4.2.0)oct-2-ene-2-carboxylic acid and 2-(furan-2-yl)prop-2-enoyl chloride in the presence of sodium hydroxide, obtaining 3-(ethoxymethyl)-7-(2-(furan-2-yl)prop-2-en-1-yl)-8-oxo-5-thia-1-azabicyclo(4.2.0)oct-2-ene-2-carboxylate, reacting obtained compound with sodium hydroxide and hydrochloric acid, obtaining 7-(2-(furan-2-yl)prop-2-en-1-yl)-3-methyl-8-oxo-5-thia-1-azabicyclo(4.2.0)oct-2-ene-2-carboxylic acid, reacting obtained compound with caesium iodide, obtaining 3-((aminomethoxy)methyl)-7-(2-(furan-2-yl)prop-2-en-1-yl)-8-oxo-5-thia-1-azabicyclo(4.2.0)oct-2-ene-2-carboxylic acid, reacting obtained compound with sodium, obtaining 3-((aminomethoxy)methyl)-7-(2-(furan-2-yl)prop-2-en-1-yl)-8-oxo-5-thia-1-azabicyclo(4.2.0)oct-2-ene-2-carboxylate, reacting obtained compound, obtaining 3-((aminomethoxy)methyl)-7-(2-(furan-2-yl)prop-2-en-1-yl)-8-oxo-5-thia-1-azabicyclo(4.2.0)oct-2-ene-2-carboxylic acid and reacting obtained compound.
NOVELTY - Allylamine is acidified with hydrochloric acid to obtain allylamine hydrochloride. Allylamine hydrochloride is addition-polymerized polymer and alkalized to obtain an allylamine polymer. The polymer is reacted with epoxy chloropropane to obtain sevelamer hydrochloride, which is neutralized and reacted with carbonic acid to obtain sevelamer carbonate.    USE - Preparation of sevelamer carbonate (claimed).    ADVANTAGE - The method enables stable reactions, is environmentally-friendly, suitable for industrial production, and short in cycle, uses economical raw materials, and provides high yield.    DETAILED DESCRIPTION - Allylamine is acidified with hydrochloric acid to obtain allylamine hydrochloride. Allylamine hydrochloride is addition-polymerized polymer and alkalized to obtain an allylamine polymer. The polymer is reacted with epoxy chloropropane to obtain sevelamer hydrochloride, which is neutralized and reacted with carbonic acid to obtain sevelamer carbonate. The allylamine polymer is of formula: -(-CH2-CH(-CH2-NH2)-)n-.    n=not defined.    N.B: n is not defined.
NOVELTY - The device has a first mixing shaft that is provided in the first containing space (10) of the first groove chamber (1). Each chamber is respectively provided with an opening (11). A material-mixing roller is connected with a drive motor and the mixing shaft is provided with a spiral blade. The first and second material-mixing rollers are connected with a driving motor. The mixed materials are transferred from the first and second groove chambers to the second material-mixing roller.    USE - Tandem type heat conveying reaction device used for producing organic fertilizer.    ADVANTAGE - The organic fertilizer can be produced according to characteristics of different organic matter raw materials with different reaction in the different stages of the production process.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of tandem type heat conveying reaction device.    First groove chamber (1)    Third opening (3)    First containing space (10)    Opening (11)    Concave internal tooth (12)
NOVELTY - Plant growth promoting liquid fertilizer prepared by mixing amino acid liquid fertilizer prepared as by-products of food industries, crab shell, bone meal and palm ash in a ratio of 70:10:10:10 to obtain a liquid fertilizer mixture and inoculating a culture medium containing Lysobacter antibioticus, Bacillus thuringiensis and Paenibacillus ehimensis of 1 pts. wt. relative to 100 pts. wt. of the liquid fertilizer mixture, is claimed.    USE - Used as a plant growth promoting liquid fertilizer.    ADVANTAGE - The fertilizer is an environmental friendly and made from natural raw materials, and maximizes the availability of nitrogen-phosphate-potassium to plants. There is no nozzle clogging of liquid fertilizer while irrigating together with increased accessibility of the substrate to the microorganisms. The fertilizer also prevents damage from pest and negative effect of microorganism.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for preparing the plant growth promoting liquid fertilizer by preparing the liquid fertilizer mixture as above, inoculating the culture medium in the liquid fertilizer mixture, and composting by aerating in the inoculated liquid fertilizer mixture.
NOVELTY - The apparatus comprises two bio-chips arranged in a fermenter to purify the organic waste water filled in the fermenter, and a sensor mounted in the fermenter for sensing and controlling an amount of moisture.    USE - The apparatus is useful for treating an organic waste water (claimed), food sewage, livestock excretions and human excrement.    ADVANTAGE - The waste water is treated in a simple and cost-effective manner without pollution.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) treating an organic waste water; and    (2) a bio-chip.
NOVELTY - The apparatus has a livestock excretion reservoir (10) for storing livestock excretion and a supplementary material reservoir (20) for storing rice straw. A supplementary material pre processor (30) crushes supplementary material mixed with livestock excretion in a mixed unit (40). A solid/liquid separator (60) separates crushed material into solid/liquid material, using inflow water from an acid formation tank (50). A liquefied fertilizer fermenter produces the liquefied fertilizer from the separated material using methane gas in methane generating bath (80).    USE - Apparatus for performing anaerobic digestion using livestock wastewater and subsidiary materials.    ADVANTAGE - Since the crushed material is separated into solid/liquid material using inflow water from acid formation tank, the stirring efficiency of the anaerobic digestion apparatus can be increased. The impact load generation in the anaerobic digestion apparatus can be reduced, so as to maximize the methane fermentation efficiency of the anaerobic digestion apparatus. The degradation problem due to the generated organic acid accumulation phenomenon in the supplementary material can be eliminated.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion apparatus.    Livestock excretion reservoir (10)    Supplementary material reservoir (20)    Supplementary material pre processor (30)    Mixed unit (40)    Acid formation tank (50)    Methane generating bath (80)
NOVELTY - The system has a gas generating assembly that is positioned at pressure within the polar molecular fluid. A gas conduit bundle assembly is extended from the gas generating assembly positioned at or near atmospheric pressure. The electrical potential is generated between the first and second electrodes results in an electrolytic breakdown of the polar molecular fluid into constituent gas components. The gas components are generated at a pressure above atmospheric pressure dependent upon the pressure of the operation of the system.    USE - System for producing pressurized gas from polar molecular fluid.    ADVANTAGE - The electrolysis system can be operable by simple geometric structures positioned in conjunction with the respective electrodes. The gas filtration bells can permit the discrimination between hydrogen gas molecules and oxygen gas molecules.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the electrode bell pressurized gas generator apparatus.    Deep water electrolysis system (10)    Long outer tube (12)    Inner tube (14)    Cap (16)    Collection bell (18)
NOVELTY - A fuel generator comprises fuel generating agent (1) of porous body which generates fuel gas by oxidation reaction, volume expansion agent (2) of porous body which expands in volume by oxidation reaction, and container (3) which accommodates fuel generating agent and volume expansion agent. Filling rate of volume expansion agent in unoxidized state is higher than filling rate of fuel generating agent in unoxidized state. Volume expansion agent is interposed between fuel generating agent and inner wall of container.    USE - A fuel generator for fuel cell system (claimed).    ADVANTAGE - Danger due to high temperature increase in generator is prevented, therefore improving safety.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the fuel generator.    Fuel generating agent (1)    Volume expansion agent (2)    Container (3)    Gas distribution opening (4)    Piping (5)
NOVELTY - Method of collecting methane gas from natural gas hydrate involves substituting replacement gas and methane gas by using electrolyte.    USE - Method of collecting methane gas from natural gas hydrate (claimed).    ADVANTAGE - The method efficiently and economically collects methane gas from natural gas hydrate.
NOVELTY - Proposed device comprises casing to accommodate cells connected in series and composed of cathode, anode, gastight membrane arranged there between, pump to circulate alkaline electrolyte, tanks with alkaline electrolyte, water feed system, device to separate oxygen from water and alkali vapors and device to separate hydrogen from water and alkaline vapors. Anode of every cell is composed of screen tube while cathode is composed of hollow cylinder made from porous water-repellant material. Note here that anode and cathode are located close to gastight membrane to form cathode gas chamber between outer side of cathodes and casing connected with hydroseal chamber, alkaline electrolyte tank and device separating hydrogen from water and alkali vapors. Cell anode chambers are connected with heat exchanger and alkaline electrolyte tank communicated with device separating oxygen from water and alkali vapors and water feed system.    USE - Metallurgy.    ADVANTAGE - Power savings, higher efficiency, reliability and safety.5 cl, 2 dwg
NOVELTY - Usage method of caustic scrubber (320) involves receiving a process gas (310) stream from anaerobic digestion system or landfill gas system, flowing the process gas stream up vertically through a vertical column (330), flowing a caustic liquid solution downward through the vertical column (340) such that the caustic liquid solution removes acid(s) from the gas stream, bubbling out treated gas which is free of acids through an opening at the top of the vertical column, and flowing the treated gas (350) into an anaerobic digestion cleanup system or a landfill gas cleanup system.    USE - Usage method of caustic scrubber for treatment of process gas e.g. biogas used as cooking fuel and boiler fuel for generating electricity, and for combined heat and power engines.    ADVANTAGE - The process gas from stream from anaerobic digestion system or landfill gas system is efficiently processed using the caustic scrubber.    DETAILED DESCRIPTION - Usage method of caustic scrubber for treatment of process gas from anaerobic digestion system or landfill gas system, involves receiving a process gas stream from the anaerobic digestion system or a landfill gas system, flowing the process gas stream up vertically through a vertical column, flowing a caustic liquid solution downward through the vertical column such that the caustic liquid solution removes at least one acid from the process gas stream, bubbling out treated gas which is free of acids through an opening at the top of the vertical column, and flowing the treated gas into an anaerobic digestion cleanup system or a landfill gas cleanup system.    DESCRIPTION OF DRAWING(S) - The drawing shows a view explaining the usage method of caustic scrubber.    Caustic scrubber system (300)    Process gas (310)    Caustic scrubber (320)    Columns (330,340)    Treated gas (350)
NOVELTY - Preparing intercalated and/or exfoliated organophilic clay comprises: producing microalgae comprising 0.2-20%, preferably 6-20% of dry material; grinding the macroalgae; and shear mixing the macroalgae with a mass of clay that is 0.25-1.6 times the mass of the macroalgae for 1 hour to permit the intercalation and/or exfoliation of the proper clay.    USE - The method is useful for preparing intercalated and/or exfoliated organophilic clay such as sodium activated bentonite clay that is used in a fertilizer product, in dietary supplement for animals such as farmed fish and in a ceramic filler (all claimed), where the clay is used for effluent treatment and as a filler in polymer matrices to produce clay-polymer nanocomposites.    ADVANTAGE - The method is useful for preparing efficient and reliable intercalated and/or exfoliated organophilic clay only from natural materials without intermediate chemical transfer and pollution load in a simple and cost-effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an intercalated and/or exfoliated organophilic clay spacing sheet of 10 Angstrom , preferably 30 Angstrom and 10% of exfoliated platelets.
NOVELTY - A recycle soil comprises water-retentive raw material (A) containing dry aggregates, molten slag and dewatering cake obtained by dehydrating incinerated ash and water-supply-and-sewerage sludge produced from general waste, industrial waste or water-supply-and-sewerage sludge, and silt raw material (B) containing gypsum waste material, chippings powder and screenings.    USE - Recycle soil is used as planting soil.    ADVANTAGE - The recycle soil has excellent stability, water permeability and water-retention property, and is economically prepared.
NOVELTY - Producing oil in a form of triglyceride comprises providing a carbon source and a nitrogen source, and culturing a yeast strain of Pseudozyma prune with the carbon source and the nitrogen source to produce the oil.    USE - The method is useful for producing oil (preferably bio-diesel oil) in a form of triglyceride, where the oil includes 14-20C-medium-chain fatty acid, saturated fatty acids and unsaturated fatty acids for manufacturing biodiesel oil (all claimed).    ADVANTAGE - The method simply produces the oil with high yield and potential.
NOVELTY - Preparation of biodiesel involves pre-treating waste oils and fats, esterifying raw materials chosen from oil, methanol and cosolvent pretreated and measured by metering pump and supplying materials into a buffer, pumping raw materials into a continuous tubular reactor, reacting materials for 1-3 hours, separating, decoloring without heating, supplying crude methyl ester into decoloring tank to undergo filtering and decoloring with white clay and obtaining product (A), decoloring and degassing with heating, sending crude methyl esters into decoloring tank to react with white clay.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The method efficiently and economically provides biodiesel, using simple process in short period of time.    DETAILED DESCRIPTION - Preparation of biodiesel involves pre-treating waste oils and fats, esterifying raw materials chosen from oil, methanol and cosolvent pretreated and measured by metering pump and supplying materials into a buffer, pumping raw materials into a continuous tubular reactor, reacting the materials for 1-3 hours, separating, decoloring without heating, supplying crude methyl ester into decoloring tank to undergo filtering and decoloring with white clay and obtaining product (A), decoloring and degassing with heating, sending crude methyl esters into decoloring tank to react with white clay, heating the decoloring tank by the use of steam at 70-80 degrees C for 1-3 hours and obtaining product (B).
NOVELTY - An herbicidal composition comprises 5-10 wt.% fenoxaprop, 10-50 wt.% benazolin, 3-5 wt.% cloquintocet-mexyl, 8 wt.% Pluronic 125 (RTM: 2-methyloxirane), 5 wt.% propylene glycol, 8 wt.% xanthan gum, 1 wt.% methylated vegetable water and less than 100 wt.% water.    USE - Herbicidal composition i.e. water suspension used for treating and controlling weeds in wheatland.    ADVANTAGE - The composition is environment-friendly and has low cost.
NOVELTY - Seaweed extract fertilizer is prepared by adding seaweed with water, stirring, extracting for 2-15 hours, centrifugally separating the clear liquid to obtain seaweed extract, preparing fermentation culture medium by adding 1000 pts. wt. seaweed extract with 6-10 pts. wt. peptone, 1-5 pts. wt. yeast extract, 5-10 pts. wt. sodium chloride, 0.5-1 pt. wt. potassium dihydrogen phosphate (KH2PO4), and 0.1-0.5 pt. wt. magnesium sulfate (MgSO4), adjusting the pH at 7-8 to obtain the fermentation culture medium, inoculating Bacillus subtilis (CGMCC 6616), and fermenting.    USE - Seaweed extract fertilizer.    ADVANTAGE - The seaweed extract fertilizer has viable count of greater than or equal to 2.0x 109 colony forming units/ml, fast fertilizer efficiency, and high quality, is rich in plant growth-regulating substances such as alginic acid, seaweed oligosaccharide, gibberellin, and indoleacetic acid, can be directly and conveniently absorbed by root systems of crops, accelerates high yield and early-ripe of plants, enhances the disease-resistance, and improves the quality of crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of seaweed extract fertilizer.
NOVELTY - Production of organic fertilizer comprises adding cattle manure into anaerobic fermenting tank, continuously fermenting, separating by extrusion separating device to obtain dry cattle manure and wastewater, adding wastewater into marsh gas tank, uniformly mixing dry cattle manure, marsh mud, chicken manure, microbial inoculum, and straw powder, adding into fermentation tank, controlling the fermentation temperature, stacking, conducting secondary fermentation at normal temperature, drying, crushing, screening, and packing.    USE - Production of organic fertilizer (claimed).    ADVANTAGE - The method solves the pollution problem and improves the economic value.    DETAILED DESCRIPTION - Production of organic fertilizer comprises adding cattle manure into anaerobic fermenting tank, continuously fermenting for 48 hours, separating by extrusion separating device to obtain dry cattle manure having water content of 55-60% and wastewater, adding wastewater into marsh gas tank, uniformly mixing dry cattle manure, marsh mud, chicken manure, microbial inoculum, and straw powder at 6.5:1:1:0.0000105:1.5 weight ratio, adding into fermentation tank, controlling the fermentation temperature at 55-65 degrees C for greater than or equal to 72 hours, stacking, conducting secondary fermentation at normal temperature, where fermentation time is 15-20 days during summer and autumn and 20-25 days during winter and spring, drying, crushing, screening, and packing.
NOVELTY - Biological bacterium organic fertilizer comprises 19 pts. wt. soybean meal, 10 pts. wt. hide powder, 23 pts. wt. cotton seed meal, 14 pts. wt. mushroom residue, 9 pts. wt. bone cement, 12 pts. wt. sugar residue, 8 pts. wt. bentonite, 4.5 pts. wt. biological bacteria, and 0.5 pts. wt. trace element fertilizer.    USE - Biological bacterium organic fertilizer.    ADVANTAGE - The biological bacterium organic fertilizer contains nitrogen, phosphorus, and potassium nutrients of higher than 8%, thus providing quick effect for promoting crop growths. It has short fermentation period and low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological bacterium organic fertilizer by weighing components according to proportions; uniformly mixing and stirring to obtain mixture; adding fermentation yeast; fermenting mixture at 70 degrees C for 8 days with turning every other day; controlling pH of mixed material at 6-7; granulating; drying; and filtering to biological bacterium organic fertilizer.
NOVELTY - A straw mushroom stock seed culture material comprises 80-90 wt.% rabbit manure, 7-17 wt.% straw mushroom slag, 2 wt.% gypsum powder and 1 wt.% lime powder.    USE - Straw mushroom stock seed culture material.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of straw mushroom stock seed culture material comprising exposing raw materials for 1-2 days, killing bacteria; wetting rabbit manure with water; stacking rabbit manure, inserting stick, covering upper part with tarpaulin to naturally ferment, turning material when temperature reaches 60 degrees C, keeping for 24 hours, uniformly adding straw mushroom slag, lime powder and gypsum powder, turning once/3 days; covering upper part with ventilating sponge, sterilizing, cooling, incubating at 100 degrees C, heating to 121 degrees C for 2 hours; and cooling to less than 25 degrees C.
NOVELTY - An organic ecological fertilizer comprises 100 pts. wt. tobacco stalk ash and 800-900 pts. wt. sesame cake. The fertilizer is prepared by mixing sesame cake and tobacco stalk ash in a fermentation tank, adjusting pH value of the mixture to 7-8, adding microbial strain and uniformly stirring; heating the mixture for high temperature sterilization by using interlayer heat conducting oil at 90-110 degrees C for 2 hours; and keeping temperature at 70-80 degrees C after sterilizing, and then continuously stirring and fermenting.    USE - Organic ecological fertilizer.    ADVANTAGE - The fertilizer can fully utilize mineral nutrient in tobacco.    DETAILED DESCRIPTION - An organic ecological fertilizer comprises 100 pts. wt. tobacco stalk ash and 800-900 pts. wt. sesame cake. The fertilizer is prepared by mixing sesame cake and 70 pts. wt. tobacco stalk ash in a fermentation tank, adjusting pH value of the mixture to 7-8, adding microbial strain and uniformly stirring; heating the mixture for high temperature sterilization by using interlayer heat conducting oil at 90-110 degrees C for 2 hours; keeping temperature at 70-80 degrees C after sterilizing, then continuously stirring and fermenting for 12 hours; cooling the fermented material to 50 degrees C; adding the cooled material with 30 pts. wt. tobacco stalk ash, adjusting pH value of the material to 8-9, then adding composite strain and wheat bran, and uniformly stirring; uniformly stirring the mixed material, and fermenting for second time at 35-45 degrees C, turning the stack every 12 hours for one time, and continuously fermenting for 4-5 days.
NOVELTY - Manufacture of synthetic natural gas involves reacting coal or biomass, and oxygen, hydrogen or mixed gas with carbon monooxide to obtain synthetic gas of carbon dioxide and hydrogen, recovering heat of obtained gas, removing impurities and hydrogen sulfide, passing crude synthetic gas to isothermal reactor, performing water gas shift process with steam to synthesize methane, cooling gas emitted from the reactor, removing water and carbon dioxide, passing obtained product to primary adiabatic reactor, and passing gas emitted from primary adiabatic reactor to secondary adiabatic reactor.    USE - Manufacture of synthetic natural gas (claimed).    ADVANTAGE - The synthetic natural gas is economically, effectively and efficiently manufactured with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthetic natural gas-manufacturing device.
NOVELTY - Preparing a composition comprises (1) slowly adding the aqueous ammonia with pH value of 3 with waste acid in a controlled manner at temperature of less than 90 degrees C to obtain a solution having pH value of 4.8-5.5, (2) filtering the obtained product to generate a filter cake and filtrate, (3) dissolving the filter cake in aqueous ammonia to adjust the pH value of the precipitation to 8-9, (4) removing insoluble impurities by filtration, (5) centrifuging the obtained product to obtain acid precipitation and (6) carrying out ion exchange/ammonia desorbing process using anion exchange resin.    USE - The method is useful for preparing a composition (claimed), which is useful as a fertilizer product.    ADVANTAGE - The method prepares the composition without pollution.    DETAILED DESCRIPTION - Preparing a composition comprises (1) slowly adding the aqueous ammonia with pH value of 3 with waste acid in a controlled manner at temperature of less than 90 degrees C to obtain a solution having pH value of 4.8-5.5, (2) filtering the obtained product to generate a filter cake and filtrate, (3) dissolving the filter cake in aqueous ammonia to adjust the pH value of the precipitation to 8-9, (4) removing insoluble impurities by filtration, (5) centrifuging the obtained product to obtain acid precipitation and (6) carrying out ion exchange/ammonia desorbing process using anion exchange resin to obtain desorption liquid and (7) evaporating and crystallizing the ion exchange liquid using an evaporator to obtain ammonium molybdate containing mixture of ammonium sulfate and ammonium nitrate mixture fertilizer product.
NOVELTY - The device has a grinder (1) for crushing straws. An auger drying and conveying mechanism (2) is provided with crushed straws for carrying out a conveying process. A carbonization furnace (3) dries the processed straws for improving carbonization efficiency. A coke and dust removal equipment (4) and a gas collecting device (5) respectively collect and processes dust and gas that are generated during the carbonization process for realizing zero-pollution emission.    USE - Straw carbonization device.    ADVANTAGE - The device has high carbonization efficiency, zero-pollution emission and reasonable structure.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a straw carbonization device.    Grinder (1)    Auger drying and conveying mechanism (2)    Carbonization furnace (3)    Coke and dust removal equipment (4)    Gas collecting device (5)
NOVELTY - A high-proportion methanol petrol comprises 0-15 vol.% petrol, 85-99 vol.% car fuel methanol and 0.5-2.0 vol.% high-proportion methanol car fuel additive-TP, where the high-proportion methanol car fuel additive-TP comprises isobutyl alcohol, isoamyl alcohol, ethanol, ethyl toluene, diethyl ether and solvent oil-120.    USE - High-proportion methanol petrol for a car.    ADVANTAGE - The petrol has strong power performance, and reduces pollutant emission.
NOVELTY - Preparation of microorganism nitrogen fertilizer comprises mixing 1.86-5.73 wt.% trace element, 0.02-0.06 wt.% calcium carbonate, 30-60 wt.% carbon source, 6-12 wt.% nitrogen source, and 20-40 wt.% water, sealing for 24-48 hours to do advanced ammoniation treatment, and degrading; adding mixture of 85-95% raw material yeast and 5-15% bacteria, adjusting fermentation liquid pH value to 7.1-7.8, first level fermenting at 25-50 degrees C for 4-6 days, then second level fermenting for 5-7 days to obtain microorganism nitrogen fertilizer; and crushing or granulating, and packaging.    USE - Preparation method of microorganism nitrogen fertilizer (claimed).    ADVANTAGE - The prepared fertilizer has comprehensive nutrition, high utilization rate, no burning, capable of activating loosen soil and improving physical property of the soil, solves the problem that the effect of urea is short, improves the fruit quality and reduces agrochemical medicine residue.    DETAILED DESCRIPTION - Preparation of a microorganism nitrogen fertilizer comprises:    (A) mixing 1.86-5.73 wt.% trace element, 0.02-0.06 wt.% calcium carbonate, 30-60 wt.% carbon source, 6-12 wt.% nitrogen source, and 20-40 wt.% water, stirring and mixing uniformly, sealing for 24-48 hours to do advanced ammoniation treatment, and degrading to obtain fermentation raw material;    (B) adding mixture of 85-95% raw material yeast and 5-15% bacteria, adjusting fermentation liquid pH value to 7.1-7.8, putting into a fermenting tank, turning once the fermentation liquid every 3-6 hours, first level fermenting at 25-50 degrees C for 4-6 days, then second level fermenting for 5-7 days to obtain microorganism nitrogen fertilizer; and    (C) crushing or granulating, packaging and obtaining the microorganism-containing nitrogen fertilizer product.
NOVELTY - Organic-inorganic complex fertilizer containing biological bacterium and microelement comprises 23 pts. wt. urea, 15 pts. wt. monoammonium phosphate, 18 pts. wt. potassium sulfate, 24 pts. wt. humic acid, 10 pts. wt. tobacco powder, 5 pts. wt. bentonite, 4.5 pts. wt. biological bacteria, and 0.5 pt. wt. microelement fertilizer.    USE - Organic-inorganic complex fertilizer.    ADVANTAGE - The released nutrients and crop growth needs are coordinated. The utilization rate of effective components in the organic-inorganic complex fertilizer is above 55%. The organic-inorganic complex fertilizer promotes crop yield increase. Due to the addition of bentonite, the forming effect while granulating the organic-inorganic complex fertilizer is good.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic-inorganic complex fertilizer containing biological bacterium and trace element comprising weighing the raw materials, mixing and stirring uniformly, fermenting the mixed material at 70 degrees C for 13 days, turning the mixed material every other day during the fermentation period, controlling the pH of the mixed material at 6-7, granulating, drying, and filtering to obtain the product.
NOVELTY - Extraction of macranthoides saponin B comprises soaking honeysuckle in 5-8 times saturated lime, extracting, neutralizing extract, filtering using ultrafiltration membrane, keeping liquid in nanofiltration membrane, concentrating, precipitating with ethanol, centrifuging, and concentrating liquid under reduced pressure to obtain extract; and subjecting to high-speed countercurrent chromatography, monitoring through UV detector, collecting target component, recovering agent, and vacuum drying.    USE - Method for extraction of macranthoides saponin B (claimed).    ADVANTAGE - The method is easy to industrialize, and has simple process, high yield, and low pollution.
NOVELTY - Separation of Akebia saponin D comprises crushing raw material, adding 3-5 times 30-80% methanol, microwave extracting for 5-20 minutes, extracting for 2-3 times, recovering reagents, filtering through ultrafiltration membrane and concentrating nanofiltration permeate; and purifying by high-speed countercurrent chromatography, monitoring using UV detector, collecting target components, recycling reagent and vacuum drying.    USE - Method for separating Akebia saponin D (claimed).    ADVANTAGE - The method is simple, easy and environment-friendly and has high yield.
NOVELTY - Preparation of Liriope spicata saponin B comprises crushing dwarf lilyturf root raw material, adding 3-8 times of 30-90% methanol solution, microwave extracting for 5-10 minutes, extracting for 2-3 times, decompressing and recycling extracting agent, carrying out ultrafiltration and nanofiltration, film concentrating, drying concentrated solution to obtain crude extract, purifying by high speed counter-current chromatography, monitoring by evaporation light scattering detector using spectrum collecting target component, recycling reagent, decompressing and drying.    USE - Method for preparing L. spicata saponin B (claimed).
NOVELTY - Poly- epsilon -caprolactone compound (I) or (II) is new.    USE - Poly- epsilon -caprolactone compound used for treating tumors (claimed).    ADVANTAGE - The compound is pure, water-soluble and biodegradable. The method is economical, efficient and non-toxic.    DETAILED DESCRIPTION - Poly- epsilon -caprolactone compound of formulae (I) or (II) is new.    M=alkali metals;    D=molecular anti-tumor drug group;    R=1-6C alkoxy;    x=1-100;    y=1-100;    z=3-300; and    n=100-300.    An INDEPENDENT CLAIM is included for preparation of compound (I) or (II).
NOVELTY - An organic vegetable soilless culture substrate comprises organic substrate using organic waste in the compost rotten fermenting process, where ratio of base slag and vermiculite or perlite is 1-4: 1.    USE - An organic vegetable soilless culture substrate.    ADVANTAGE - The substrate uses solid organic waste, and recycles natural resource to provide a low cost soilless culture substrate, and has high economic and social benefit.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the soilless substrate comprising:    (A) adding 200-400 kg licorice residue to 1000 kg fresh chicken manure, each 20 cm thickness, spraying mixed aqueous solution to make 60-70% licorice residue moisture content;    (B) composting such that licorice dreg stack central temperature is more than 65 degrees C when carrying out, at the same time adding water; and    (C) when the slag temperature and the environment temperature are not the same, substrate color is brown, and has no peculiar smell.
NOVELTY - Preparation of N-alkyl substituted sulfonamide compound involves: mixing sulfonamide compound and alcohol compound in organic solvent, under the action of organic acid catalyst at 30-200 degrees C, TLC tracking and detecting until the reaction is finished, where the reaction liquid contains the sulfonamide compound after the treatment, where organic solvent is toluene, xylene, acetonitrile, dimethyl sulfoxide, dimethyl formamide or dioxane.    USE - For the preparation of N-alkyl substituted sulfonamide compound (claimed) used as important organic synthesis intermediate in medicine, pesticide and so on; as important organic intermediate, pharmaceutical intermediate, and as raw material for pesticide and chemical products.    ADVANTAGE - The method is featured with mild reaction condition, uses easily available raw material sources, has low cost, and convenient operation, provides product in high yield, is green and environment-friendly. The method has good selectivity and simple operation step, and mild condition thereby allowing industrial application.    DETAILED DESCRIPTION - Preparation of N-alkyl substituted sulfonamide compound of formula R1-SO2-NH-R2 (I) involves: mixing sulfonamide compound of formula R1-SO2-NH2 (III) and alcohol compound of formula R2OH (II) in organic solvent, under the action of organic acid catalyst at 30-200 degrees C, TLC tracking and detecting until the reaction is finished, where the reaction liquid contains sulfonamide compound (I) after the treatment, where the organic solvent is toluene, xylene, acetonitrile, dimethyl sulfoxide, dimethyl formamide or dioxane. The compound (III), compound (II), and acid catalyst are in a ratio of 1:1-25:0.01-10.    R1=3-10C alkyl or phenyl (optionally substituted by substituent selected from 1-6C alkyl or halo) (preferably phenyl, para-methyl-phenyl, methyl-phenyl, chlorophenyl, or bromophenyl);    R2=1-10C alkyl or benzyl (preferably benzyl, methyl, butyl, isopropyl or cyclohexyl).
NOVELTY - Method for preparation of imatinib involves: reacting 4-(3-pyridyl)-2-pyrimidinone, N-((4-methyl-3-amino)phenyl)-4-(chloromethyl)benzamide and 4-methyl-piperazine in presence of organic base and condensing agent, by condensation reaction to form imatinib.    USE - For preparation of imatinib (claimed) useful for treating chronic myeloid leukemia and gastrointestinal stromal tumor.    ADVANTAGE - Compared with existing technology, preparation method is easy to perform, is simple, requires mild reaction conditions, controls quality of imatinib such that imatinib has improved quality, is environment friendly, is suitable for industrialized production, and has improved economical efficiency, selectivity and controllability of reaction operation.
NOVELTY - Manufacture of coal briquet involves smashing waste of empty fruit bunch, pulverizing the smashed waste, drying, charring at high temperature, cooling, carbonizing with carbide at high temperature, pulverizing, mixing with binder, supplying into a mold, molding, separating the molded product, and storing.    USE - Manufacture of coal briquet (claimed).
NOVELTY - A resorcinol is prepared by performing catechol isomerization in reactor under action of catalyst.    USE - Preparation of resorcinol (claimed).    ADVANTAGE - Preparation process is environment-friendly and has low waste discharge and mild reaction condition.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of catalyst which involves performing ion exchange to obtain catalyst carrier and adhesive, uniformly mixing auxiliary extrusion agent, adding nitric acid solution and kneading to obtain formed catalyst carrier, drying and roasting, impregnating catalyst active component by loading and baking amount of auxiliary extrusion agent is 2-4 wt.% total weight of catalyst.
NOVELTY - Ecological organic fertilizer comprises 85-93 wt.% ammonium humate, 5-10 wt.% xylose and 2-5 wt.% triple superphosphate.    USE - As ecological organic fertilizer.    ADVANTAGE - The ecological organic fertilizer improves physical and chemical properties of soil and viability of ecological vegetation crops. The preparation method is simple and convenient and requires low production cost, and has good economic benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) preparing ammonium humate by (i) crushing coal into fine powder of 80-300 mesh sieve, (ii) mixing 50-70 wt.% coal powder, 5-10 wt.% urea, 10-20 wt.% ammonium hydrogen carbonate and 5-20 wt.% clean water to obtain mixture, (iii) heating the mixture at 50-80 degrees C for 2-3 hours, (iv) drying the mixture obtained in step (iii) for 3-10 hours, (v) sealing the dried mixture for 5-10 days, and (vi) drying the sealed mixture at 50-80 degrees C for 2-3 hours, until the moisture content reaches 15% or less to obtain ammonium humate, and (b) mixing 85-93 wt.% ammonium humate, 5-10 wt.% xylose and 2-5 wt.% triple superphosphate and crushing the mixture to fineness of 70-90 mesh.
NOVELTY - This utility model claims a kind of domestic marsh gas generating device, comprising a vertical shaft of the lower plane, the underground fermentation, fermentation room is connected with the connected with the collecting tank, the technical solution is as follows: the domestic marsh gas generating device further comprises a well for a heat preservation tube providing heat circulation water of the solar water heater, fermentation time can drive the lifting of the lifting mechanism in the vertical well, the fermentation chamber is provided with a discharging port, a feeding port, a marsh gas pipe, is arranged between the heat preservation layer in the fermentation, and the fermentation heat preservation layer is set between the heat circulation water with a heat preservation pipe. Solves the problem that the existing technology is retained a bad effect, high energy consumption, low yield and so on. Making full use of the solar energy to a fermentation material liquid, using the most efficient heating heat preservation technical measures, the northern winter for need of marsh gas.
NOVELTY - The method involves providing flocculent sludge biological phosphorus removal functional discharge for a sewage treatment plant. The phrosphorus sludge is inoculated in a SBR reactor, where inoculation quantity of the phosphorus sludge is 3000-3200 mg/l. The sludge is cultured by adopting anaerobic operation mode, anaerobic running mode and anoxic running mode, where total phosphorus concentration of the sludge is 300 -400 mg/l.    USE - Denitrification phosphorus accumulating bacteria granular sludge preparation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a photographic view illustrating a denitrification phosphorus accumulating bacteria granular sludge preparation method.
NOVELTY - A trough-type aerobic composting odors emission reduction, collection and processing method involves adding composting raw material into a composting tank for generating odor, which is collected by a shutter under a hood collection. The generated odor is mixed with air by a draught fan and entered into a cyclone dust collector and a deodorization tower to remove dust.    USE - Emission reduction, collection and processing method for trough-type aerobic composting odors.    ADVANTAGE - The method enables reducing odor releasing, improving compost efficiency and aerobic composting open environment condition and collecting the deodorizing and gas composition.
NOVELTY - A biodiesel production method involves pre-processing the kitchen waste by sorting, crushing and dehydrating in vacuum to obtain hogwash oil. Methanol, hogwash oil and a catalyst are weighed. The catalyst is dissolved in methanol, and the hogwash oil and methanol are dissolved with catalyst into a reaction kettle, stirred and heated at 80-350 degrees C for 3-60 minutes. Decompressing and distilling is carried out after the reaction is finished. The methanol is recycled, and the product is kept for dividing into layers, where lower layer is glycerol and upper layer is biodiesel.    USE - Method for producing biodiesel from kitchen rubbish.    ADVANTAGE - The method enables producing biodiesel with short reaction time, mild reaction conditions and simple post-treatment product, in a simple and efficient manner.    DETAILED DESCRIPTION - A biodiesel production method involves pre-processing the kitchen waste by sorting, crushing and dehydrating in vacuum to obtain hogwash oil. Methanol, hogwash oil and a catalyst are weighed, where the catalyst is solid acid catalyst or solid alkali catalyst. The catalyst is dissolved in methanol, and the hogwash oil and methanol are dissolved with catalyst into a reaction kettle, stirred and heated at 80-350 degrees C for 3-60 minutes. Decompressing and distilling is carried out after the reaction is finished. The methanol is recycled, and the product is kept for dividing into layers, where lower layer is glycerol and upper layer is biodiesel.
NOVELTY - A straw enzymolysis saccharification efficiency improving method involves crushing a straw with water content of 5-70% to 1.5-5.0 cm length. The water content is heated by a steam explosion reactor. The steam explosion reactor instantaneously releases the pressure to obtained solid-liquid mixture. Solid-liquid separation is processed on solid-liquid mixture. The solid-liquid mixture is cleaned with de-ionized water, followed by drying and crushing to 0.5-l.4cm, adding cellulose and water and separating to obtain liquid glucose and xylose.    USE - Method for improving straw enzymolysis saccharification efficiency.    ADVANTAGE - The method enables improving steam explosion pre-processing efficiency and reducing energy consumption of crushing process.
NOVELTY - This utility model claims a kind of new-type aeration artificial wetland sewage treatment system, comprising a wetland pool, the bottom of anti-seepage treatment, two sides of the marsh tank of the marsh tank are respectively provided with a water inlet pipe and a water outlet pipe, the marsh tank is arranged, in the sewage into a wetland pool, after being processed by a water outlet pipe, a marsh tank is filled with filler, the filler is planted with wetland plant, and further comprises an aeration pipe, the aeration pipe network comprises an aeration main pipe and a plurality of air branch pipe, an aeration main pipe along the edge of the marsh tank arranged on the two outer sides of the marsh tank, an aeration branch pipes are extended into the bottom of the wetland tank and an aeration main pipe opening part is provided with a main control valve, a branch aerating pipe connected with air main pipe is provided with an adjusting valve. Air way is flexible, but by the switch-controlled air pipe valve, the artificial wetland sections in aerobic, anaerobic, anoxic state or adjust any one kind of oxygen supply state so that the system is in the best working condition according to the need.
NOVELTY - Kojic acid derivative is new.    USE - Kojic acid derivative used as antioxidant for stabilizing biodiesel and related seed oils (all claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing Kojic acid derivative, which involves performing esterification of kojic acid or ricinoleic acid using an immobilized lipase catalyst and fungal species such as Mucor and Candida antarctica, where lipase is immobilized on anion exchange resins or porous acrylic resins at 60-80 degrees C in a continuous or discontinuous reactor.
NOVELTY - This utility model belongs to the energy field is a kind of high-concentration large-particle straw marsh gas fermentation device, comprising a fermentation tank (11) and liquid storage tank (1), the top of the tank body is provided with a feeding pipe (10) and a marsh gas nozzle (9), bottom of the tank body is provided with a slag (7), a feeding pipe (10) is equipped with a weight (6) and sealed feeding pipe (10), tank body is installed on the upper part cone slag-stopping ring plate (14), a slag-stopping ring plate (14) is connected with the feeding pipe (10) is connected with the slag-stopping ring plate (14) and the upper end of the inner wall of the tank body is connected with the lower tank body is equipped with liquid slag separating plate (16), the bottom of the liquid slag separating plate (16) is provided with a sieve pore, the periphery wall of the tank body and connected with the fermentation tank (11) is provided with a liquid discharging tube (3), fermentation tank (11) body is equipped with a connecting pipe (4). This utility model claims a high-concentration large particle straw marsh gas ferment device can be directly digestion large-particle straw, low energy consumption, smooth feeding and discharging, the input-output ratio is low.
NOVELTY - Synthesis of cephalosporin side chain intermediate involves reacting bromine and isobutyric acid; continuously reacting with chlorine to obtain alpha -bromo-isobutyric acid and hydrogen chloride; adding alpha -bromo-isobutyric acid into solvent; further reacting with catalyst and isobutylene; decompressing and distilling to obtain alpha -bromo-butyric acid tert-butyl ester; adding alpha -bromo-butyric acid tert-butyl ester and demethylation cefotaxime into solvent; reacting with alkali potassium carbonate; and adding phase transfer catalyst for alkylation reaction.    USE - Synthesis of cephalosporin side chain intermediate.    ADVANTAGE - The method has simple process, high conversion rate and yield, environment friendly, and low cost.    DETAILED DESCRIPTION - Synthesis of cephalosporin side chain intermediate comprises dropping bromine raw material into isobutyric acid to react; continuously reacting with chlorine to obtain alpha -bromo-isobutyric acid and hydrogen chloride; adding alpha -bromo-isobutyric acid into solvent; adding catalyst and isobutylene; completely reacting; decompressing and distilling to obtain alpha -bromo-butyric acid tert-butyl ester; adding alpha -bromo-butyric acid tert-butyl ester and demethylation cefotaxime into solvent; reacting with alkali potassium carbonate; adding phase transfer catalyst for alkylation reaction to obtain (Z)-2-2-amino-4-thiazolyl-t-butyloxycarbonyl (dimethoxyphenyl) ethyl imine; adding water and/or ethanol as solvent; performing ester hydrolysis under alkali; adding inorganic acid to adjust pH and to obtain (Z)-2-amino alpha -((2-(tert-butoxy)-1,1-dimethyl-2-oxo-ethoxy) imino)-4-thiazole acetic acid.
NOVELTY - An environmentally-friendly caking agent comprises 50-70% palm oil as grease, 10-15% industrial wax and 20-40% dodeca-primary amine or stearic acid as surfactant.    USE - Environmentally-friendly caking agent (claimed).    ADVANTAGE - The environmentally-friendly caking agent is economically prepared.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for processing of environmentally-friendly caking agent, which involves adding palm oil and industrial wax into mixing tank, heating, stirring, adding surfactant, continuously stirring at 100-200 degrees C for 20-40 minutes, and processing.
NOVELTY - Biological organic fertilizer, comprises 50-65 wt.% fermented and cured organic matter, 10-20 wt.% powdered carbon, 5-20 wt.% shell powder, 1-5 wt.% seaweed powder, 1-5 wt.% chitin and 0.1-0.2 wt.% mixed powder.    USE - The biological organic fertilizer is useful for fruit trees (claimed).    ADVANTAGE - The biological organic fertilizer supplies nutrients required by growth and development of the plant at each stage from the aspects including water retention and nutrition slow release, improves soil physical and chemical properties, promotes formation of soil aggregates, and doesn't causes perpetual harms to the soil. The method is environmentally-friendly since waste aquaculture by-product is changed into valuable product.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) mixing organic matter, adding appropriate amount of water to organic matter, stirring once for every 1-2 weeks, composting the organic matter for 2-4 weeks, retting the processed organic matter for 20-30 days and stirring for 1-2 times during composting, adding remaining raw materials to composted organic matter to obtain product, and drying the product until moisture content of the product reaches 4% or less.
NOVELTY - This utility model claims a motor function acid ion water strawberry disease system device, comprising a power function acid ionized water producing device, storing and conveying device and a spraying device, wherein the function of the acid ionized water producing device comprises a front water treatment device, electrolytic device, electrolytic agent supply device, a control device, an automatic cleaning device for acid ion water physical and chemical index detecting device, the storing and conveying device comprises an acid water storage device, an alkaline water storage device, an acidic water conveying device, an alkaline water conveying device. This utility model uses electric function acid ionized water for replacing the original farm chemical for preventing and treating the diseases of strawberry, and no residue, no pollution to the environment, the cost is low, and use of chemical pesticide traditional method has obvious advantages.
NOVELTY - This utility model claims a kind of high pressure air storage chamber of the biogas pool, comprising a fermentation chamber, with the first feeding part connected with a fermentation chamber and a pressure chamber, the fermentation chamber is provided with a gas storage chamber, a gas storage chamber is provided with a second feeding port and a water outlet, a feeding port is provided with a first one-way valve which can be opened to the air storage chamber of the water outlet is provided with a opening for air outside the second valve outlet is connected with the water pressure chamber is connected with the water outlet channel, and a pumping system, comprising a fermentation chamber top part with the gas storage chamber of the air inlet pipe, the air inlet pipe is set in the fermentation chamber for pumping air in the air chamber, the air chamber is set with marsh gas outlet pipe. A the marsh gas generated in the fermentation of a pumped storage gas storage chamber, keeping the ferment chamber is in a low voltage state, which is good for fermenting and producing the marsh gas chamber, at the same time continuously to the gas storage chamber supplying marsh gas to ensure the pressure in the gas storage chamber and guarantee the normal use of the marsh gas passes through.
NOVELTY - A high-energy industrial alcohol type fuel comprises 65-70 wt.% methanol, 10-15 wt.% sugar waste liquid, 5-8 wt.% pine fragrance with a concentration of 27.5 %mass, 1-3 wt.% hydrogen peroxide, 1.5-3 wt.% xylene, 1-3 wt.% phytate, 1.5-2 wt.% benzotriazole, 3-5 wt.% acetone, 0.01-0.05 wt.% ferrocene, 0.1-0.5 wt.% lavender oil, and 1.5-1 wt.% rubber swelling inhibitor.    USE - High-energy industrial alcohol type fuel (claimed).    ADVANTAGE - The high-energy industrial alcohol type fuel is environmentally-friendly, economical, safe, energy-saving, and renewable energy source, completely replaces industrial diesel, natural gas, liquefied gas, coal, and electricity, uses a wide raw material source, has stable performance characteristics, and efficiently solves energy-requirement problems.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high-energy alcohol type fuel, which involves injecting methanol into a mixing tank, adding pine fragrance, hydrogen peroxide, xylene, phytate, benzotriazole, acetone, ferrocene, and rubber swelling inhibitor, allowing to stand for 30-60 minutes, pouring sugar waste liquid and lavender oil, stirring for 10-20 minutes, and allowing the mixed solution to stand still for 2-4 hours at room temperature.
NOVELTY - Use of Enterobacter gergoviae for preparing microbial flocculant, is claimed.    USE - The flocculant is useful for improving sludge settlement in sewage treatment (claimed).    ADVANTAGE - The preparation method has simple processes and a low cost. The flocculant has high activity, strong heat resistance, good pH tolerance and no secondary pollution, and has a flocculation rate of 90%.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1) preparing the microbial flocculant, comprising culturing Enterobacter gergoviae strain suitable for culture in a fermentation culture medium, and isolating the cells or bacterial liquid microbial flocculant; (2) microbial flocculant, obtained as mentioned; and (3) use method of the microbial flocculant for improving sludge settlement in sewage treatment, comprising adding the microbial flocculant into the wastewater to be treated, where the volume ratio of the microbial flocculant and the water to be treated is 2-10%, and processing for less than 0.5 minutes.
NOVELTY - A kind of excrement processing system, wherein a spiral stirring rod processing tank in a channel shape with the cross beam, the cross beam is provided with a stirring device, the stirring device is provided with a position of the upper end of the spiral stirring rod is provided with a radial direction of the oil cylinder, a stirring device is provided with a blower and a transverse power mechanism, one side of the cross beam is equipped with a feces, the feces pipe is provided with a plurality of excrement; two ends of the cross beam are set with vertical sliding mechanism and the side wall of the excrement treatment tank and one side of the excrement treatment tank is provided with a liquid excrement groove, groove channel of the excrement is excrement pump, waste pump is connected with the cross beam pipe is connected to the bottom of the excrement treatment tank is provided with air supply pipe, it solves the problem that the anaerobic marsh gas or filling adding strain to oxygen supplying system for garbage fermentation process, the fermentation is not complete, the problem of environment pollution, and it is widely applied to farm the animal excrement and town refuse dump processing using the human excrement and organic matter.
NOVELTY - This utility model claims a mud film reactor, a gas biological bacteria to solve the problem that the reactor and sewage fully contact caused by the big energy consumption and a water outlet in a mesh or grid, is easy to operate in the grid or grid in stacking, which seriously influences the efficiency of the reactor and so on; This utility new type mud membrane bioreactor is provided with biological filler, the biological filler is attached with bacteria of activated sludge in the reactor is provided with a stirrer, the reactor further is provided with an annular separating sieve and the annular separating sieve and fixedly connected and synchronously rotating with the stirring shaft of the rotary brush. In the reactor is provided with biological filler and for making the effective separation of a barrier device, and is provided with self-cleaning function, it does not need to add extra power consumption. This utility model of the membrane bioreactor is provided with simple structure, convenient use, small energy consumption, green and environment-friendly, and has good economic benefit and so on.
NOVELTY - This utility model claims a kind of artificial wetland watertight, wherein comprising a main board (3) and a channel, wherein the main board (3) at one side is provided with a plurality of drainage frame (6), wherein the frame (6) and the water channel (5) are arranged on the main board (3), the draining frame (6) and the first channel (5) is further provided with a side channel (7), the drain frame (6) is provided with a water tank (2), the water tank (2) is provided with a plurality of water through holes (1), the outlet water tank (2), the upper part is further provided with multiple permeable holes (4), the main board (3) and the draining frame (6) is made of glass steel. A main board set in the reaction tank, and outlet is set on the water tank and can quickly discharge the sewage, effectively solves the problem that sewage treatment system for constructed wetland leakage, is provided with good treatment effect, high treatment effect, strong anti-impact composite, stable operation and convenient management and so on, suitable for popularization and use.
NOVELTY - A nitrogen phosphorus removing method involves using rest sludge alkaline anaerobic fermentation liquid comprising organic acids, followed by mixing nitrogen phosphorus in the organic acids, combining ammonia alkali plant residues and a molecular sieve to absorb nitrogen phosphorus in the fermentation liquid. The rest sludge is added into a reactor, followed by adjusting pH of the residual sludge, and maintaining temperature of the reactor. The residual sludge is subjected to anaerobic fermentation, followed by taking sample. The sample is centrifuged.    USE - Method for removing nitrogen phosphorus from sludge fermentation liquid.    ADVANTAGE - The method enables removing nitrogen phosphorus from sludge fermentation liquid with improved organic acid recycling effect, in an inexpensive manner.    DETAILED DESCRIPTION - A nitrogen phosphorus removing method involves using rest sludge alkaline anaerobic fermentation liquid comprising organic acids, followed by mixing nitrogen phosphorus in the organic acids, combining ammonia alkali plant residues and a molecular sieve to absorb nitrogen phosphorus in the fermentation liquid. The rest sludge is added into a reactor, followed by adjusting pH of the residual sludge to 9-10, and maintaining temperature of the reactor at 35-40. The residual sludge is subjected to anaerobic fermentation for 10-20 days, followed by taking sample. The sample is centrifuged to obtain supernatant comprising organic acid and nitrogen phosphorus. The supernatant is treated under alkaline condition by adding alkali residue, followed by removing precipitate, adding molecular sieve, and determining a molecular sieve adding quantity by the residual nitrogen content in the supernatant. The resultant supernatant is subjected to secondary centrifugation to obtain supernatant comprising organic acid and ammonia nitrogen and orthophosphate, followed by recycling clear liquid to the city sewage factory.
NOVELTY - A spray-type polymethacrylate biological diesel pour point depressant is prepared by mixing organic solvent and a polymethacrylate pour point depressant composition in a biodiesel ester vessel, followed by controlling temperature at 40-60 degrees C, and stirring at speed of 300-500 rpm for 0.5-2 hours, and cooling to room temperature, where the depressant comprises polymethacrylate biological diesel pour point depressant and propane at a mass ratio of 1:1-3, the mass ratio of organic solvent and a polymethacrylate pour point depressant composition is 1:2.    USE - Spray-type polymethacrylate biodiesel pour-point depressant.    ADVANTAGE - The depressant is convenient to carry, and has improved effect of low temperature fluidity of biodiesel.    DETAILED DESCRIPTION - A spray-type polymethacrylate biological diesel pour point depressant is prepared by mixing organic solvent and a polymethacrylate pour point depressant composition in a biodiesel ester vessel, followed by controlling temperature at 40-60 degrees C, and stirring at speed of 300-500 rpm for 0.5-2 hours, and cooling to room temperature, where the depressant comprises polymethacrylate biological diesel pour point depressant and propane at a mass ratio of 1:1-3, the mass ratio of organic solvent and a polymethacrylate pour point depressant composition is 1:2, the organic solvent is butyl acetate, amyl acetate or hexyl acetate. An INDEPENDENT CLAIM is also included for a method for preparing spray type polymethacrylate biological diesel pour point depressant.
NOVELTY - A straw enzymolysis saccharification efficiency improvement method involves crushing, drying and packing fresh straw in a sealed device, and carrying out anoxic storage. Steam heating is carried out on the dried straw in a steam explosion reactor and pressure is released instantaneously to obtain solid-liquid mixture. The solid-liquid mixture is washed with deionized water. The obtained solid is dried and mixed with cellulose and water. pH value of the mixture is adjusted to carry out enzymatic hydrolysis on the mixture. Solid-liquid separation is carried out on the mixture to obtain liquid.    USE - Method for improving enzymolysis saccharification efficiency of straw.    ADVANTAGE - The method enables improving the enzymolysis saccharification efficiency of the straw with high enzymatic saccharification rate.    DETAILED DESCRIPTION - A straw enzymolysis saccharification efficiency improvement method involves crushing, drying and packing fresh straw in a sealed device, and carrying out anoxic storage. Steam heating is carried out on the dried straw in a steam explosion reactor and pressure is released instantaneously to obtain a solid-liquid mixture. The solid-liquid mixture is washed with deionized water. The obtained solid is dried and mixed with cellulose and water. pH value of the mixture is adjusted to 4.5-5.5 to carry out enzymatic hydrolysis on the mixture. Solid-liquid separation is carried out on the mixture to obtain liquid with glucose and xylose content.
NOVELTY - A kind of city road rainwater runoff ecological co-processing device, the device is composed of a city road rainwater runoff ecological processing tank and the biological purifying unit residence, city road rainwater ecological water in a processing tank in order at intervals is provided with a weir plate, screen plate and a through hole baffle plate, overflow weir plate, a screen plate and a through hole clapboard divides the box body is divided into a sequence of the overflow chamber, water chamber, water distribution room and retention purifying a four chamber, the retention unit is set on the purifying biological retention purifying chamber, a gravel layer, a sand filtering layer, a planting layer and the plant, the device can float to remove particulate matter and soluble pollutant with different grain diameters in the rainwater runoff, the grading control of pollutants in the runoff water, but also can make a rainwater runoff storage and retention for plant growth unit need to save water, but also can realize the city road rainwater runoff water quality multi-target water-flow control.
NOVELTY - A biological slow release fertilizer comprises 100-250 pts. wt. urea formaldehyde coated urea, 100-250 pts. wt. microbial inoculums, 200-400 pts. wt. potassium sulfate, 150-240 pts. wt. calcium super phosphate, 50-250 pts. wt. calcium-magnesia phosphate, 20-100 pts. wt. monoammonium phosphate, 1-20 pts. wt. humic acid, 1-20 pts. wt. ferrous sulfate, 1-20 pts. wt. zinc sulfate, 0.1-1 pts. wt. ethylenediaminetetraacetic acid chelated manganese, 1-20 pts. wt. ammonium citrate and borax.    USE - Biological slow release fertilizer for peanut.    ADVANTAGE - The fertilizer improves peanut yield and quality, and has wide application range.    DETAILED DESCRIPTION - A biological slow release fertilizer comprises 100-250 pts. wt. urea formaldehyde coated urea, 100-250 pts. wt. microbial inoculums, 200-400 pts. wt. potassium sulfate, 150-240 pts. wt. calcium super phosphate, 50-250 pts. wt. calcium-magnesia phosphate, 20-100 pts. wt. monoammonium phosphate, 1-20 pts. wt. humic acid, 1-20 pts. wt. ferrous sulfate, 1-20 pts. wt. zinc sulfate, 0.1-1 pts. wt. ethylenediaminetetraacetic acid chelated manganese, 1-20 pts. wt. ammonium citrate and borax, where the urea formaldehyde coated urea is prepared by reacting urea with formaldehyde to generate the urea formaldehyde and coating urea formaldehyde particle on a surface of the urea, microbial inoculums composition is prepared by fermenting liquid, absorbing the liquid by using sterilized grass, adding ferrous sulfate and ammonium sulfate, mixing, granulating at low temperature and spraying the mixture on the particle surface to microbial inoculums, and the fertilizer is prepared by mixing mentioned components in a mixer, stirring the mixture for 6-8 minutes, measuring and packaging to obtain a finished product. An INDEPENDENT CLAIM is also included for preparing biological slow release fertilizer.
NOVELTY - A biomass fuel production method involves adding 0.5-2 pts. wt. acid into sludge, and stirring the mixed solution. The mixture is added with 8-12 pts. wt. coal, 3-5 pts. wt. water reducing agent and 0.1-0.5 pts. wt. biomass enzyme, and stirred. The mixture is aged for 24 hours and granulated to obtain finished product.    USE - Method for producing biomass fuel by utilizing paper-making sludge and domestic sludge.    ADVANTAGE - The method enables producing biomass fuel in simple, convenient and safe operation, and environmental-friendly manner.
NOVELTY - A papermaking pulp decomposition method involves utilizing crop straw as raw material, and crushing the material. The crushed particle is soaked to form raw material slurry. Engineering bacteria seed is amplified by secreting thermophilic glycosidase. Primary and secondary strain culturing process is performed. The thermophilic glycosidase is induced when OD value of the strain liquid reaches 0.4-0.8. The raw material slurry is added with the strain liquid, and treated at room temperature. The treated slurry is boiled, and crushed. The crushed particle is molded after baking process.    USE - Method for decomposing papermaking pulp by utilizing engineering bacteria enzyme.    ADVANTAGE - The method enables decomposing papermaking pulp in simple and cost-effective manner.    DETAILED DESCRIPTION - A papermaking pulp decomposition method involves utilizing crop straw as raw material, and crushing the material. The crushed particle is soaked for 20-30 hours to form raw material slurry. Engineering bacteria seed is amplified by secreting thermophilic glycosidase. Primary and secondary strain culturing process is performed. The thermophilic glycosidase is induced at 25-37 degrees C when OD value of the strain liquid reaches 0.4-0.8. The raw material slurry is added with the strain liquid, and treated at room temperature. The treated slurry is boiled, and washed and crushed. The crushed particle is molded after conducting papermaking and baking process, where IPTG of thermophilic glycosidase is 0.2-0.7 mM.
NOVELTY - Amino acid is reacted with anhydrous tetrahydrofuran as solvent in presence of triphosgene decomposition catalyst, to obtain amino acid N-carboxyanhydride. The triphosgene decomposition catalyst is chosen from activated carbon, pyridine, triethylamine, piperidine, piperazine, morpholine and N-methyl morpholine.    USE - Preparation of amino acid N-carboxyanhydride (claimed).    ADVANTAGE - The method provides amino acid N-carboxyanhydride with high yield.
NOVELTY - Extracting high purity 1-deoxynojirimycin, involves pre-treating raw materials, conducting enzymolysis of raw materials, filtering product, acidifying filtrate, filling filtrate into cationic resin column, eluting the column using ammonia to obtain ammonia eluate, conducting membrane separation of the ammonia eluate to remove impurities, concentrating separated product, conducting column chromatography of concentrated solution, eluting column by ammonia water, collecting and concentrating eluate, crystallizing concentrate, and drying crystallized product.    USE - The method is useful for extracting high purity 1-deoxynojirimycin (claimed).    ADVANTAGE - The method provides high extraction rate of 1-deoxynojirimycin with purity higher than 98%, is environmentally-friendly, and extracts 1-deoxynojirimycin with improved quality.    DETAILED DESCRIPTION - Method for extracting high purity 1-deoxynojirimycin, involves pre-treating raw materials; conducting enzymolysis of raw materials, filtering product, acidifying filtrate, filling the filtrate into cationic resin column, eluting the column loaded with the filtrate using ammonia to obtain ammonia eluate, conducting membrane separation of the ammonia eluate to remove impurities, concentrating separated product, conducting column chromatography of concentrated solution by cationic resin column, eluting the column by ammonia water, collecting the eluate, concentrating the eluate, crystallizing concentrate, and drying crystallized product to obtain 1-deoxynojirimycin.
NOVELTY - A carbon-based slow-release fertilizer is prepared by dissolving soluble salts containing trace elements in 100 pts. wt. water at 25-100 degrees C, adding 150-450 pts. wt. carbon adsorbent, uniformly mixing, drying, crushing and sieving.    USE - Method for preparing carbon-based slow-release fertilizer (claimed).    ADVANTAGE - The fertilizer is safe, economical and convenient to use. It has wide raw material source, low cost and simple manufacturing. It improves the yield and quality of crop.
NOVELTY - Cis-form p-menthyl-3,8-diol is directionally synthesized by adding homogeneous catalyst and acid catalyst to Citronella extract containing 75-85% citronellal in water solvent, and cyclizing.    USE - Directional synthesis of cis-form p-menthyl-3,8-diol for pesticides, medicine, food, cosmetics, and agricultural chemicals.    ADVANTAGE - Cis-form p-menthyl-3,8-diol has high purity, and directional synthesis is environment-friendly, improves yield, and has high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart for synthesis reaction of cis-form p-menthyl-3,8-diol. (Drawing includes non-English language text).
NOVELTY - Chlorinated disproportionated rosin copper salt (I), is new. (I) is a viscous dark blue color substance at room temperature, has specific gravity of 1.07, and soluble in organic solvents.    USE - (I) is useful in disinsectization and sterilization (claimed).    ADVANTAGE - The method: is simple and does not discharge pollutants.    DETAILED DESCRIPTION - Chlorinated disproportionated rosin copper salt of formula (I), is new. (I) is a viscous dark blue color substance at room temperature, has specific gravity of 1.07, and soluble in organic solvents. An INDEPENDENT CLAIM is also included for preparation of (I).
NOVELTY - Production of high phosphorus organic fertilizer comprises mixing 70-95 wt.% pig manure, and 5-30 wt.% mushroom compost, sawdust, and other high fiber waste; adding 0.02 wt.% organic material decomposing agent, mixing, and adjusting moisture at 55-70%; and carrying out fermentation by adding calcium superphosphate or phosphorus-containing waste acid, and adjusting pH to neutral.    USE - Method for the production of high phosphorus organic fertilizer (claimed).    ADVANTAGE - The pig manure is rich in humus, thus activating inorganic phosphorus for odor removal. The method overcomes defects of low utilization rate of phosphate fertilizer, and realizes environmental protection in production and soil improvement.
NOVELTY - An additive comprises raw materials e.g. Radix Paeoniae alba extract, Litsea cubeba oil, oleanolic acid, cinnamyl acetate, guar gum, isoliquiritigenin, Liriope spicata saponin B, paeonol, sodium glutamate, chlorogenic acid, vitamin B12, glycerin monostearate, D-galactose, alpha -humulene, vitamin E, methionine chromium, lauryl aldehyde, and zinc sulfate and carrier e.g. wheat bran, peanut shell powder, and montmorillonite.    USE - An additive for pig feed (claimed).    ADVANTAGE - Additive is safe, non-toxic, and environment-friendly, enhances immune system of pigs, improves feed intake, promotes rapid and healthy growth of pigs, has good detoxification effect, and reduces mycotoxin damage in pigs.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of additive which involves sieving and mixing Radix Paeoniae alba extract, oleanolic acid, paeonol, sodium glutamate, chlorogenic acid, vitamin B12, vitamin E, and peanut shell powder to form 1st mixture, sieving and mixing cinnamyl acetate, Litsea cubeba oil, alpha -humulene, lauryl aldehyde, and montmorillonite to form 2nd mixture, sieving and mixing guar gum, isoliquiritigenin, Liriope spicata saponin B, glycerol monostearate, D-galactose, zinc sulfate, and wheat bran to form 3rd mixture, and uniformly mixing mixtures.
NOVELTY - This utility model claims a kind of used for organic fertilizer production of the fermentation tank of the heating device, belonging to the field of organic fertilizer processing technology field. This utility model comprises (1), with an insulating layer (10) of the tank body (2), a tank bottom (3), the tank body (2) is installed on the supporting column (4), wherein the tank body (2) is provided with the outer wall of the snake-shaped heating pipe (5), the snake-shaped heating pipe (5) is connected with the heat conducting oil heater (6); This utility model can mix the raw material of organic fertilizer to heat, and the heating time is short, the heating is uniform.
NOVELTY - Treatment method of organic solid waste in large scale fruit and/or vegetable planting base, involves grinding fruit and/or vegetable waste, inoculating 0.1-0.5% compound microbial agent, uniformly mixing, composting and fermenting for 15-20 days, turning pile and stacking once in every day, and implementing batch-type ventilation and aeration, where the compound microbial agent comprises 60-80 %mass microbial agents verotoxin (VT), 10-30 %mass Trichoderma and 5-20% Aspergillus niger.    USE - The method is useful for treating organic solid waste, preferably agricultural and forestry wastes chosen from manure, straw and leaves (claimed) which is useful as fertilizer.    ADVANTAGE - The method is less labor intensive, and rapid, as fermentation duration is controlled within 20 days (fermentation cycle is remarkably shortened) and improves quality of compost products. In method, fermentation field area is saved by 30-50%, fruit/vegetable waste after being treated contains more than 5% organic matters.
NOVELTY - A Bacillus amyloliquefaciens NJZJSB3 (CGMCC NO: 6966) strain capable of promoting growth of canola, is new.    USE - The B.amyloliquefaciens is useful for promoting growth of canola (claimed).    ADVANTAGE - The strain is gram-positive, rod-shaped, capable of producing spores and facultative anaerobic microbe, provides positive results for catalase, nitrate reductase, starch hydrolysis and gelatin hydrolysis tests, and negative result for methyl red test, ferments glucose, fructose, cellobiose, sucrose, dextrin, galactose, mannitol and xylitol, does not ferment sorbitol, can utilize citrate, and produces organic fertilizer having more than 90% organic nitrogen, 6-10% nitrogen phosphorus and potassium nutrient, and 45% organic matters.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing organic fertilizer, which involves isolating the NJZJSB3 strain, inoculating the strain into a microbial decomposition mixture of thoroughly decomposed pig manure compost and rapeseed meal, and performing solid fermentation to obtain the microbial organic fertilizer.
NOVELTY - Constructing barrier containing biological fertilizer for stabilizing and protecting island sand, involves selecting island with sand dune windward middle and lower positions, configuring foundation sand bags and allocating space for the configured sand bags and placing the bags in a triangle shape, where the bag contains biodegradable fiber, powdered sheep manure, carbon, clay, water retention agent and biological bacterium fertilizer, filling the base additive into fiber bag, sealing and displaying the bags on designed configuration.    USE - The method is useful for constructing barrier containing biological fertilizer for stabilizing and protecting island sand (claimed), which is useful for managing moving dune.    ADVANTAGE - The method enables to arrange foundation sandbags in shapes of an island shape, a straight line shape, and a crescent moon shape on the surface of a moving dune, and the sand-protecting barrier to integrate the functions of wind erosion control, improves local soil environment and recovers vegetation.    DETAILED DESCRIPTION - Constructing barrier containing biological fertilizer for stabilizing and protecting island sand, involves selecting island with sand dune windward middle and lower positions, configuring 3-5 foundation sand bags and allocating space for the configured sand bags of 2-4 m x 2-4 m and placing the bags in a triangle shape, where the bag comprises biodegradable fiber as base and additive, 20-30 kg aeolian sand, 0.5-1 kg powdered sheep manure, 1-2 kg crushed and rotten plant straw, 0.5-1 kg carbon, 1-2 kg clay, 50-100 g water retention agent, 20-30 g biological bacterium fertilizer and plant seeds with germination capacity in desert chosen from Hedysarum mongolicum and Artemisia desertorum, filling the base additive into fiber bag, sealing and displaying the bags on designed configuration.
NOVELTY - Microbial agent comprises 47-51% Trichoderma viride, 16-20% Aspergillus niger, 11-15% Bacillus subtilis, 8-12% Roseateles sp. and 8-12% Aspergillus foetidus.    USE - The microbial agent is useful for preparing fermented organic fertilizer (claimed), improving growth condition and quality of crops.    ADVANTAGE - The agent improves manure effect and function of fertilizer, increases yearly output and saves more resources and reduces production cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of applying the microbial agent, which involves adding 3-5 wt.% microbial agent with respect to fermented organic fertilizer and adjusting water content to 50-70 %mass.
NOVELTY - Invention can be used in live farming and agriculture for processing of organic, phytogenous and biological wastes to high-efficiency organic fertilisers, biogas, heat and electric power. Proposed plant comprises intake tank 5, pumps 7, intake and discharge pipelines 8 and 14, digester 9, biogas discharge pipeline 10, compressor 11, has-holder 13 and gas boiler 18 located directly in stock building 2 that have common main line 20 to collection of biogas and intermediate effluents storage 16. Note here that biogas generator is divided into modular units that include extra device 12 to remove moisture from biogas and common control unit 21. Number of modular units is defined by that of stock buildings.    USE - Process engineering.    ADVANTAGE - Stable operation, lower costs, higher efficiency and reliability.1 dwg
NOVELTY - The electrode device comprises: a proton exchange membrane (208) having a first side (210) and a second side (212); a first electrode (214) that includes a carbon material and is positioned at the first side of the proton exchange membrane; and a second electrode (216) positioned at the second side of the proton exchange membrane opposite the first electrode. The proton exchange membrane spaces the first electrode and the second electrode at a distance of less than or equal to 50 microns. The first electrode and the second electrode directly contact the proton exchange membrane.    USE - The electrode device is useful in a liquid environment for ionizing a liquid such as water (all claimed), generating hydrogen from water, generating ozone from water, and purifying a liquid.    ADVANTAGE - The electrode device utilizes the DLC material that facilitates electrical conductivity required to perform the function of the electrode device thus improving effectiveness of the electrode device.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a system for ionizing a liquid; and    (2) a method for ionizing a liquid.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic cross sectional view of a liquid electrode device.    Proton exchange membrane (208)    First side (210)    Second side (212)    First electrode (214)    Second electrode. (216)
NOVELTY - Processing biomass, comprises (a) heat-treating biomass (1) so that the moisture content is decreased to less than 8 wt.%, (b) supplying the heated biomass to a mill (3) and hot milling, (c) supplying a coolant (6, 7) to the mill for cooling the biomass, and (d) discharging the ground biomass together with the heated coolant from the mill.    USE - The method is useful for processing biomass.    ADVANTAGE - The method carries out rapid cooling of the biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a plant for the processing of biomass by the above mentioned method, comprising (i) a heat treatment device (2) for heat treatment of biomass, (ii) the mill with an inlet (30) for supplying hot biomass from the heat treatment device, (iii) at least one coolant supply and (iv) an outlet for the joint discharge of ground biomass and heated coolant.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic block diagram of the plant for the processing of biomass.    Biomass (1)    Heat treatment device (2)    Mill (3)    Coolant (6, 7)    Inlet (30)
NOVELTY - The apparatus has a hydrogen gas supply unit (5) that supplies the hydrogen gas in which hydrogen is contained in source gas from desulfurization unit (1) in an upstream. A controller (7) responds to the factor in accumulation supply time which supplies source gas, accumulation feed-rate of source gas, and the accumulation operation time of hydrogen generating apparatus. The controller controls flow volume of the hydrogen gas supplied from hydrogen gas supply unit with respect to increase the flow volume of source gas.    USE - Hydrogen generating apparatus for use in fuel cell system (claimed), for making hydrocarbon fuel such as town gas and liquefied petroleum gas (LPG), source gas, etc.    ADVANTAGE - The hydrogen generating apparatus continues operation without reducing the amount of hydrogen generation can be realizable.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the hydrogen generating apparatus. (Drawing includes non-English language text)    Desulfurization unit (1)    Modification unit (2)    Recycle line (4)    Hydrogen gas supply unit (5)    Controller (7)
NOVELTY - A woody biomass fuel comprises mixture of base material containing wooden organic components, and secondary material discharged from biomass industry, in specified ratio.    USE - Woody biomass fuel is used for driving machine and motor vehicle.    ADVANTAGE - The woody biomass fuel having stable combustion efficiency is manufactured by simple method, and is economical and environmentally-friendly.
NOVELTY - The system has a pre-heater (3) which pre-heats filtered raw material oil. A reactor (5) has solid catalyst (51) converted into cracked distillate which makes pre-heated raw material oil, and hydrocarbon. A high temperature fractionating column (6) sends hydrocarbon oil to back stage. A low-temperature fractionating column (7) emits naphtha gas components other than cracked distillate of condensed quality of light oil to back stage. A recovery unit (9) recovers light oil obtained by cooling cracked distillate of condensed quality of light oil at cooling tower (8).    USE - System for manufacturing light oil such as diesel fuel using waste edible oil and plant-derived fats and oils. Uses include but are not limited to tempura oil, frying oil, rapeseed oil, soy bean oil, sesame oil, safflower oil, cottonseed oil, rice bran oil, peanut oil, sunflower oil, corn oil, olive oil, palm oil, coconut oil, Jatropha oil and peanut oil.    ADVANTAGE - The recovery unit recovers light oil obtained by cooling cracked distillate of condensed quality of light oil at cooling tower, so that the yield of light oil is improved. The heavy oil is separated by the high temperature fractionating column is re-circulated to reactor, so that the need of exhaust valve and recovery tank are reduced. Since the installation area of gas introduction line and reflux line is small, the structure of the system is simplified. The reflux line has the seal structure, so that the back flow of gas from reactor is prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for light oil manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of light oil manufacturing system. (Drawing includes non-English language text)    Pre-heater (3)    Reactor (5)    High temperature fractional distillation column (6)    Low-temperature fractional distillation column (7)    Cooling tower (8)    Light oil recovery unit (9)    Solid catalyst (51)
NOVELTY - Preparing isosorbide, comprises dehydrating sorbitol to remove water using water-compatible Lewis acid to obtain isosorbide and sorbitan.    USE - The method is useful for preparing isosorbide (claimed).    ADVANTAGE - The method produces isosorbide with high yield in simple, environmentally friendly and cost-efficient manner, does not produce wastewater, makes use of raw material derived from biomass, and recycles water-compatible Lewis acid.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for isosorbide prepared by the above method.
NOVELTY - The system has a methanization unit for supplying renewable raw materials and/or waste. A boiler ensures hygienization of the raw materials and/or waste or dries digestate output from the methanization unit. A storage station stores one or multiple portions of biogas produced by the methanizaion unit. A control device controls the methanization unit. A cogeneration group and the boiler optimize the production of energy within the system. The control device maintains an output of electricity of the cogeneration group between 70 and 100% of maximum capacity of the cogeneration group.    USE - System for combined production of energy e.g. electricity, heat energy and gas energy, from renewable raw materials and/or waste e.g. agricultural waste and waste of an agroalimentary industry.    ADVANTAGE - The system approximately ensures the production of the energy independence of a territory of multiple square kilometers. The system enables combined production of energy in a reliable environmental friendly, simple and cost-effective manner. The system is utilizable in profitable manner and/or produced in short-term.    DETAILED DESCRIPTION - The boiler is designed as a wood boiler or a household refuse boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a system for combined production of energy. '(Drawing includes non-English language text)'
NOVELTY - Preparation of 3-amino-N-cyclopropyl-2-hydroxyl-hexanamide involves epoxidating trans-2-hexenoic acid or its 1-4C alkyl ester and optionally esterifying to obtain 3-propylepoxyethane-2-carboxylic acid or its 1-4C alkyl ester; ring opening the 3-propylepoxyethane-2-carboxylic acid or its 1-4C alkyl ester by nitrile and optionally esterifying to form 3-amino-2-hydroxyl hexanoic acid or its 1-4C alkyl ester; and reacting 3-amino-2-hydroxyl hexanoic acid or 1-4C alkyl ester with cyclopropylamine to form 3-amino-N-cyclopropyl-2-hydroxyl-hexanamide.    USE - For preparation of 3-amino-N-cyclopropyl-2-hydroxyl-hexanamide (claimed) an intermediate for the preparation of pharmaceutical products, such as antiviral medicaments for e.g. used to synthesize Telaprevir, a medicine for the treatment of hepatitis C.    ADVANTAGE - The operations are uncomplicated, the reactive conditions are mild, and the reactions can be carried out with materials readily available at low price and having low toxicities. By using water as the solvent in the epoxidation reaction, the method is more economic and clean as compared with the prior art techniques, which employ solvents such as ethanol or dichloromethane. The method uses trans-2-hexenoic acid as staring material, renders a total yield of greater than 61% of the final product 3-amino-N-cyclopropyl-2-hydroxyl-hexanamide, the purity of which can be as high as above 99.4%. The method is suitable for industrial production because: the operations are simple and convenient; the materials are readily available; the yield is high; the purity of the product is good; and the requirement of equipments is low.
NOVELTY - Ethanol is obtained by reacting a raw material gas (10) containing carbon monoxide and hydrogen in the presence of a catalyst. The catalyst is dispersed in a medium oil whose boiling point at reaction pressure is higher than the reaction temperature. Reaction is carried out by introducing raw material gas into the medium oil.    USE - Manufacture of ethanol used for preparing ethanol-mixed gasoline or bioethanol used as automotive fuel.    ADVANTAGE - The method enables direct and efficient manufacture of ethanol. The medium can be handled easily at normal temperature. The hydrophilic medium oil prevents catalyst and water from contacting and poisoning of catalyst by water. Hence, reverse reaction or reduction in carbon monoxide concentration is suppressed. The synthesis gas can be obtained by effectively using waste materials, such as bagasse which is a strained residue of sugarcane discharged from refined-sugar factories, empty fruit bunch discharged from palm-oil extraction factories, chaff discharged from rice milling plants, corn stover discharged from maize factories, and municipal solid waste.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for ethanol manufacturing apparatus (1) consisting of a catalytic reaction portion (2). The medium oil is a mixed oil of hydrophobic medium oil and hydrophilic medium oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the manufacturing method of ethanol.    Ethanol manufacturing apparatus (1)    Catalytic reaction portion (2)    Gas-liquid separation portion (3)    Distillation portion (4)    Raw material gas (10)
NOVELTY - Biogas plant (1) comprises (a) at least one receiving container (2) for receiving biomass, (b) at least one fermenter (3), (c) at least one digestate storage device (4), and (d) at least one device for distributing the biomass from the receiving container to the fermenter and/or the digestate storage device, which is adjustable such that the biomass is distributed to the fermenter or the digestate storage device. The fermenter and/or the digestate storage device comprise at least one pressure door.    USE - Used as a biogas plant.    ADVANTAGE - The biogas plant ensures the cleaning of the fermenter without high construction costs and associated high costs.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic overview of the biogas plant.    Biogas plant (1)    Receiving container (2)    Fermenter (3)    Digestate storage device (4)    Distribution device (6)
NOVELTY - Method for collecting potassium from livestock dung carbonized material, involves preparing carbonized material by heating livestock dung at 300-600 degrees C in oxygen deficiency atmosphere, carbonizing by contacting with mineral acid aqueous solution, and eluting potassium in a carbonized material, where pH of mineral acid aqueous solution after potassium elution is 7-10, and temperature of the liquid at the time of potassium elution is 50-70 degrees C.    USE - The method is useful for collecting potassium from livestock dung carbonized material (claimed) which is utilized as phosphorus fertilizer raw material.    ADVANTAGE - The method suppresses elution of phosphorus and is suitable for middle scale process.
NOVELTY - A rice bran roasted meat is prepared by (A) mixing 89.87-95.25 wt.% salt, 2.78-5.56 wt.% sauce, 0.93-1.85 wt.% D-ascorbic acid, and 0.93-2.78 wt.% polyphenols to obtain bacon agent; (B) cutting meat into strips, threading, adding 3-4wt.% bacon agent/kg strips, and pickling for 18-30 hours to obtain marinated meat; (C) drying, charcoal baking for 1-3 hours, mixing rice bran, and roasting for 3-4 hours; and (D) taking out, cooling, slicing, packaging, and cold refrigerating at - 5 degrees C.    USE - Method for preparation of rice bran roasted meat (claimed).    ADVANTAGE - The method is simple and suitable for modern industrial production plant, and can be used to manufacture meat and internal organs of pork, beef, lamb, and donkey. The meat has beautiful appearance, bright color and luster, rich flavor, appropriate moisture content, and no fumes smell, does not contain benzopyrene and other polycyclic aromatic hydrocarbon, and meets national meat product standard.
NOVELTY - System comprises (a) an algae growth unit (150) for producing algae and a molten salt gasifier reactor (120) comprising a molten salt for receiving a mixture of water and at least a portion of the algae, or (b) carbon-containing material source, a water source, a molten salt gasifier reactor for receiving a carbon-containing material, water and a mixture of molten salts, where the molten salt gasifier reactor produces gaseous stream comprising hydrogen and carbon dioxide from the algae and water and the algae growth unit receives the carbon dioxide.    USE - The system and method are useful for production of hydrogen used in fuel cells for providing heat and electricity (all claimed) and upgrading of oils, and carbon sequestration or production of carbon dioxide used for growth of algae and further for production of hydrogen, and various other gases including methane, carbon monoxide, hydrogen sulfide and water vapor.    ADVANTAGE - The system and method enable production of hydrogen from both renewable and non-renewable sources, greatly impact production of petroleum resources and allow production of fertilizer in overlooked geographical areas. The system and method are environmentally-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing hydrogen which involves contacting a carbon-containing material with water and a molten salt in a molten salt reactor to produce a gaseous mixture of hydrogen and carbon dioxide, separating the gaseous mixture into purified hydrogen and purified carbon dioxide, and conveying the purified carbon dioxide to an algae growth unit for consumption by algae, where the molten salt comprises sodium hydroxide and sodium carbonate and the carbon-containing material comprises algae.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic representation of system for hydrogen production and carbon sequestration.    Molten salt gasifier reactor (120)    Algae growth unit (150)
NOVELTY - Processing lignocellulosic raw material by enzyme saccharification process, by subjecting lignocellulosic raw material to chemical treatment, dehydrating chemically treated lignocellulosic raw material and simultaneously washing the raw material using water, removing impurities, subjecting impurities removed raw material to solid-liquid separation by solid-liquid separator to separate solid contents and liquid portions from the raw material and subjecting the solid contents to enzyme saccharification process.    USE - The method is useful for processing lignocellulosic raw material used for production of alcohol preferably ethanol or methanol used as fuel, succinic acid and lactic acid.    ADVANTAGE - The method enables efficient washing of impurities including chemicals and lignin from the chemically treated lignocellulosic raw material and obtaining pretreated raw material comprising saccharides favorable for enzyme saccharification process.    DETAILED DESCRIPTION - Method for processing lignocellulosic raw material by enzyme saccharification process, involves subjecting lignocellulosic raw material to chemical treatment, dehydrating chemically treated lignocellulosic raw material and simultaneously washing the raw material using water, draining out water from the raw material, removing impurities adhered to the raw material, subjecting impurities removed raw material to solid-liquid separation by solid-liquid separator to separate solid contents and liquid portions from the raw material and subjecting the solid contents to enzyme saccharification process.
NOVELTY - The water treatment apparatus (S) has a sludge separation tank (2) which separates the activated sludge which biologically treats sewage (100) into a supernatant liquid (101) and thickened sludge (102). A nitrification tank (3) processes the supernatant liquid. The thickened sludge and effluent from nitrification tank flow into an anaerobic tank (5). A thickened sludge transfer unit transfers the thickened sludge to nitrification tank.    USE - Water treatment apparatus.    ADVANTAGE - The thickened sludge separated by the sludge separation tank is transferred to the nitrification tank for biologically treating the sewage, so that nitrogen and phosphorus in the sewage can be removed stably. Hence the quality of treated water is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for water-treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the water treatment apparatus.    Sludge separation tank (2)    Nitrification tank (3)    Anaerobic tank (5)    Sewage (100)    Supernatant liquid (101)    Thickened sludge (102)    Water treatment apparatus (S)
NOVELTY - Invention refers to a multielement matrix filter-press water electrolysis unit consisting of electrolysis cells containing porous cathode, anode and electrolyte-containing matrix, as well as wetting elements containing an electrolyte cavity and a porous membrane permeable for water vapours and non-permeable for liquid, with water supply to cathodes in the form of water vapour mixed with hydrogen; besides, wetting elements and electrolysis cells are spatially separated from each other and insulated as to metal and electrolyte and combined into two separate sections, in which vapour-hydrogen mixture circulates via a common closed circuit, thus maintaining the same temperature in sections; with that, in the wetting element liquid electrolyte is separated from gas of vapour-hydrogen mixture with a hydrophilic membrane with gas shutoff properties, and gas pressure is higher than electrolyte pressure.    USE - Metallurgy.    ADVANTAGE - Reliable and high-efficient operation during a long period of time.5 cl, 4 dwg
NOVELTY - The apparatus has multiple supporting units (10) that are installed within a reservoir. A connection stick (20) is provided to connect the supporting units. An assemblage rod is formed in both ends of the connection stick. An air supply pipe (35) is provided in upper portion of a horizontally installed discharge tube (34), to supply the outside air. Several stirrers (30) are installed at the supporting units.    USE - Apparatus for treating liquid waste such as livestock excretion, food sewage and foul water ejected from home. Can also be used in river.    ADVANTAGE - Since the structure of the liquid waste treating apparatus is simplified, the installation of the liquid waste treating apparatus can be facilitated easily. Since the large particle in the bottom of the reservoir is stirred effectively, the whole stirring performance of the liquid waste treating apparatus can be improved. The blockage of the coarse-grained foreign substance within the treated water in the upper portion of discharge tube can be prevented, by inhaling the outside air through the air supply pipe. Since the innumerable vortex is generated while the treated water is discharged through discharge tube, the stirring efficiency of the liquid waste treating apparatus can be improved and the agitation time of the treated water stored within the reservoir can be shortened. Hence, the quality of the treated water can be increased.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view liquid waste treating apparatus.    Supporting unit (10)    Connection stick (20)    Stirrer (30)    Discharge tube (34)    Air supply pipe (35)
NOVELTY - This utility model claims a kind of sewage biogas system. The system comprises a buffer tank, a multi-anaerobic tank, a water-sealed tank, vertical torch combustion furnace and a heating liner. Sewage residence and neutralizing buffer tank into the anaerobic degradation generate a large amount of marsh gas in the adjusting tank, and by collecting the two anaerobic tank to generate marsh gas through the pipeline through the tank filter to be sent into the vertical combustion furnace, a flame to burn. , Vertical combustion furnace is set with heat, continuously burning torch to heat water and heat. Heat, a cooling water temperature and water tank, the cold water in the water tank into the heating container is heated. The utility model using the device, it can change the waste into valuable stuff, but also by using marsh gas combustion to heat water tank can be used for bathing pool, hot water supply and dining hall, security room in winter. It not only saves the energy cost, but also reduces the marsh gas directly discharging the pollution to the nature, which effectively realizes the energy saving and emission reduction.
NOVELTY - A 7-amino-3-acetyl-8-oxo-5-thia-1-azabicyclo(4.2.0)oct-2-ene-2-carboxylate is dissolved in dichloromethane system in presence of tri-n-butylamine and (S-2-Benzothiazolyl)-(Z)-2-(2-aminothiazol-4-yl)-2-trityloxyimino-thioacetic acid amine, to obtain cefdinir ester fluid. The cefdinir ester fluid is distilled with dichloromethane to obtain brown viscous liquid and cefdinir ester solid. The cefdinir ester solid is purified, to obtain cefdinir.    USE - Preparation of cefdinir (claimed).    ADVANTAGE - The cefdinir having high purity is prepared by simple method, without environmental pollution.
NOVELTY - Wastewater comprising ammonia is subjected to stripping process, to obtain ammonia-containing mixed gas. The obtained mixed gas of ammonia is provided to absorption-crystalline tower. Concentrated sulfuric acid is provided to absorption-crystalline tower and reacted with ammonia at 50-55 degrees C and under atmospheric pressure of 0.03 MPa, to obtain ammonium sulfate crystals.    USE - Recycling of ammonia used as raw material for fertilizer.    ADVANTAGE - The method enables recycling of ammonia by a simple process without carrying out evaporation, concentrating and crystallizing processes, and is environmentally-friendly.
NOVELTY - Gasification of sludge comprises collecting biomass material, drying, controlling the water content of the biomass material, mixing the biomass material, semi-carbonized material or carbonized material to obtain mixed material, adding the mixing material into sludge to make the mixed mud, adjusting water content of sludge to 50-65%, forming the mud sludge into spherical or rod-shaped, gas drying the formed mud sludge until water content is lower than 20%, and performing gasification to the material form in a gasification furnace using a combustion burner.    USE - The method is useful for gasification of sludge (claimed).    ADVANTAGE - The method processes 80% of the sludge with reduced cost of more than 50% in eco-friendly manner.    DETAILED DESCRIPTION - Gasification of sludge comprises collecting the biomass material, drying, controlling the water content of the biomass material to less than 20%, mixing the biomass material, semi-carbonized material or carbonized material to obtain mixed material with water content of 80-85%, adding the mixing material into sludge in a volume ratio of (0.5-1.5):(3-4.5) to make the mixed mud, adjusting water content of sludge to 50-65%, forming the mud sludge into spherical or rod-shaped, gas drying the formed mud sludge until water content is lower than 20%, performing gasification to the material form in a gasification furnace using a combustion burner, where the diameter of the spherical form is 5-30 mm, the diameter of the rod form is 5-20 mm, and the length of 5-40 mm, the biomass material is agriculture and forestry waste or wood furniture waste, the sludge is town sewage or domestic sewage, and the sewage has a water content of 80-85%.
NOVELTY - Caffeic acid and tryptamine are subjected to condensation reaction at 25-35 degrees C for 8-12 hours in a solvent, a condensing agent and an organic alkali. The reaction solution is concentrated to remove the solvent, an aqueous solution of extraction solvent and an acid, is added to the product, organic phase is separated, washed, dried and filtered to obtain filtrate. The filtrate is concentrated to obtain N-caffeoyl tryptamine.    USE - Manufacture of N-caffeoyl tryptamine (claimed).    ADVANTAGE - The N-caffeoyl tryptamine is easily and economically at high yield and purity without affecting environment under mild reaction conditions.
NOVELTY - A high-temperature encapsulating material comprises 10-15 wt.% magnesium oxide, 5-10 wt.% boric oxide, 8-15 wt.% sodium borate, 30-50 wt.% ceramic fibers and remainder of calcium oxide.    USE - High-temperature encapsulating material for manufacturing oxide fuel cell.
NOVELTY - Greenhouse cucumber planting substrate comprises corn straw, pig manure and vinegar, where the volume ratio of the corn straw, pig manure and vinegar is 2.5-3.5:3:4-4.5.    USE - The planting substrate is useful for growth of greenhouse crops including cucumber, tomato, lettuce and rape, preferably cucumber (all claimed).    ADVANTAGE - The planting substrate reduces the continuous cropping disorder.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the substrate, which involves (a) crushing the decomposed corn straw, and passing the crushed component over 5 mm sieve, (b) crushing the pig manure and vinegar residue, and passing the crushed components over 5 mm sieve, and (c) mixing the crushed components obtained in the steps (a) and (b), adding and mixing the obtained mixture with water, removing the organic matter from the mixture when the water content of the mixture is 60-70%, pressing the mixture in one side of length 15 cm to obtain cube, cylindrically digging a small hole having diameter of 4 cm and height of 5 cm, then drying the mixture, placing the culture medium cubes in planting bed, burying the middle of the cube in soil, and performing traditional greenhouse management.
NOVELTY - Slow release fertilizer, contains 12-17 pts. wt. Rhizobium, 12-17 pts. wt. round brown Azotobacter, 12-17 pts. wt. Bacillus megaterium, 12-17 pts. wt. B.mucilaginosus, 12-15 pts. wt. urea, 1-2 pts. wt. zinc sulfate, 1-2 pts. wt. ammonia molybdate, 5-18 pts. wt. calcium superphosphate, 18-20 pts. wt. ammonium bicarbonate, and 2-5 pts. wt. borax.    USE - The slow release fertilizer is useful for Dahne odera (claimed).    ADVANTAGE - The slow release fertilizer contains several nutrients and hormones, increases plants universality and resistance, control diseases, and prevents D.odera from yellow leaves disease.
NOVELTY - Preparing vinyl acetylene, comprises carrying out dimerization reaction of acetylene in presence of non-aqueous phase catalyst, where acid gas is introduced into the reaction system in the reaction process.    USE - The method is useful for preparing vinyl acetylene (claimed).    ADVANTAGE - The method can prolong the service life of the non-aqueous phase catalyst to efficiently produce vinyl acetylene.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for vinyl acetylene product, prepared by the method.
NOVELTY - Preparing Bacillus vallismortis strain that is preserved under a preservation number of CGMCC No.7571, is claimed.    USE - The method is useful for preparing Bacillus vallismortis strain, which is useful as growth promoting agents and antiviral agents in tobacco (all claimed).    ADVANTAGE - The method is capable easily of preparing Bacillus vallismortis strain with improved storage and transportation property in an environmental friendly manner.
NOVELTY - A transformer insulating oil sample is evacuated and mixed gas in oil is separated to ensure total volume of mixed gas in chamber after separation. A certain volume of sample gas is extracted from the separated mixed gas, and the mixed gas is separated to obtain hydrogen, carbon monoxide, methane, ethylene, ethane and acetylene. The concentration of each gas is detected. The transformer aging degree is detected according to concentration of gas component in measured oil sample calculated using gas concentration, gas volume in chamber, and oil-sample volume.    USE - Detection of transformer aging degree (claimed).    DETAILED DESCRIPTION - A transformer insulating oil sample with a volume V(oil-sample) is evacuated and mixed gas dissolved in the insulating oil is separated to ensure total volume of the mixed gas in a gas chamber to be V(gas) after separation. A certain volume of sample gas is extracted from the separated mixed gas, and the mixed gas is separated from the sample gas to obtain hydrogen, carbon monoxide, methane, ethylene, ethane and acetylene. The concentration C(gas-i-detect) of each of hydrogen, carbon monoxide, methane, ethylene, ethane and acetylene is detected using a gas sensor. The concentration C(i-in-oil) of a gas component in the measured oil sample is calculated using a formula given by, C(i-in-oil)=(C(gas-i-detect)x V(gas))/((1- eta )x V(oil-sample)), where eta is degassing coefficient. The transformer aging degree and fault type is then analyzed and determined according to the concentration C(i-in-oil).
NOVELTY - A mixed refrigerant comprises 10-30 wt.% dichlorofluoroethane and pentafluoropropane, 10-30 wt.% propane or difluoroethane, 10-30 wt.% trifluoromethane, 15-40 wt.% carbon tetrafluoride, 1-10 wt.% krypton gas, methane and 1-15 wt.% argon gas or nitrogen gas.    USE - Mixed refrigerant.    ADVANTAGE - The refrigerant has low manufacturing cost and temperature ranges from -120 to -160 degrees C, and occupies less volume.
NOVELTY - The method involves blowing connecting a gas striping tower and an absorption device through an air pump, and connecting a valve and a pipeline to form a gas circulation loop to realize air stripping of dissolved gas and ammonia nitrogen in biogas slurry. Gases are filtered and absorbed by an absorbing device. An alkali absorbing tank is connected with a gas inlet valve and the pipeline. An acid absorbing tank air outlet is connected with the air pump through the valve and the pipeline.    USE - Cycle closed-type filler-free method for removing ammonia nitrogen and recovering nutrient in biogas slurry.    ADVANTAGE - The method enables providing stable and reliable performance for removing ammonia nitrogen and recovering nutrient.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a cycle closed-type filler-free method.
NOVELTY - A wastewater is pumped into a two-effect evaporator, to carry out evaporation. The evaporated mother liquor is passed through a rectification tower, to recover light components. A sulfuric acid is added to the mother liquor, and stirred, to obtain a mixture. The obtained mixture is allowed to stand, to separate out layers. A pressure reduction distillation is carried out on the lower water layer containing glycerol, to remove the water from the layer. An absorption decolorization is performed on the glycerol, and filtered, obtain the extracted glycerol.    USE - Extraction of glycerol from biodiesel wastewater (claimed).    ADVANTAGE - The glycerol is efficiently extracted from the biodiesel wastewater by environmentally-friendly and economical method.    DETAILED DESCRIPTION - A wastewater is pumped into a two-effect evaporator, to carry out secondary-effect evaporation. The secondary-effect evaporated mother liquor is passed through a rectification tower, to recover light components. A sulfuric acid is added to the mother liquor, to obtain a mixture. The pH of the obtained mixture is adjusted to 5-6. 40-60 wt.% Water is added with respect to the weight of the mother liquor, and stirred. The mixture is allowed to stand, to separate out layers. An upper oily layer is recovered, introduced into biodiesel plant, and recycled. A pressure reduction distillation is carried out on the lower water layer containing glycerol for 0.5-2 hours, to remove the water from the layer. 0.2-0.6 wt.% Active carbon is added to the obtained glycerol, with respect to the weight of the mother liquor, and absorption decolorization is performed. The glycerol, which is obtained after the absorption decolorization, is filtered, to remove impurities and obtain the extracted glycerol.
NOVELTY - The device has an oil cylinder whose front side is provided with an automatic straw collecting and pre-processing system and a movable chassis integrated system. The oil cylinder is connected with a screw gear. The screw gear is connected with a cutting blade wheel. The cutting blade wheel is connected with a conveying auger. The conveying auger is connected with a soil shaking part, a short distance quick conveying mechanism and a feed opening part. A crusher is connected with a cyclone separator. The cyclone separator is connected with a forming machine.    USE - Automatic farm waste collection device for a straw crushed compact molding combined machine.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of an automatic farm waste collection device.
NOVELTY - A biological diesel oil modification method involves utilizing sulfuric acid as catalyst. The bio-diesel is prepared by an ester exchange reaction. A cyclopentadienyl tri-carbonyl manganese is added to the ester exchange reaction process.    USE - Method for modifying biological diesel oil for diesel engine vehicle.    ADVANTAGE - The method enables achieving strong adaptability, and energy conservation and emission reduction.
NOVELTY - Organic fertilizer containing sugar residues and trace element comprises 10 pts. wt. sugar residues, 32 pts. wt. humic acid, 10 pts. wt. amino acid, 10 pts. wt. plant ash, 10 pts. wt. lignin, 15 pts. wt. traditional Chinese medicine dregs, 8 pts. wt. bentonite, 4 pts. wt. biological bacteria, and 1 pt. wt. trace element fertilizer.    USE - Organic fertilizer.    ADVANTAGE - The sugar residues are reused, thus, protecting the ecological environment. By adding humic acid, sugar residues are converted into forms, which can be absorbed by crops, thus, increasing the sugar content of crop. The organic fertilizer has simple and convenient preparation. The forming effect of the organic fertilizer during granulation is good.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising weighing the raw materials, crushing, mixing and stirring uniformly, fermenting at 71 degrees C for 9 days, turning every other day during the fermentation period, controlling the pH of the mixed material at 6-7.8, granulating, drying, and filtering to obtain the product.
NOVELTY - Organic fertilizer comprises 15 pts. wt. furfural residue, 13 pts. wt. chicken manure, 5 pts. wt. amino acid, 15 pts. wt. humic acid, 12 pts. wt. bone powder, 20 pts. wt. lignin, 15 pts. wt. bentonite, 4.5 pts. wt. biological bacterium, and 0.5 pt. wt. microelement fertilizer.    USE - Organic fertilizer used for promoting the growth of crops.    ADVANTAGE - The organic fertilizer reduces the content of carbonate ion (CO32-) and bicarbonate ion (HCO3-) in the soil, improves the soil physical and chemical properties, reduces the alkalinity of soil and chloride ion (Cl-) content, and increases organic matter, potassium, and nitrogen in saline soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising weighing the raw materials, crushing, uniformly mixing to obtain mixed material, fermenting at 74 degrees C for 11 days, turning every other day, controlling the pH of the mixed material at 6-8, granulating, drying, and filtering.
NOVELTY - Organic fertilizer comprises 15 pts. wt. furfural residue, 15 pts. wt. chicken manure, 5 pts. wt. amino acid, 15 pts. wt. humic acid, 15 pts. wt. bone powder, 20 pts. wt. lignin, and 15 pts. wt. bentonite.    USE - Organic fertilizer used for promoting the growth of crops.    ADVANTAGE - The organic fertilizer reduces the content of carbonate ion (CO32-) and bicarbonate ion (HCO3-) in the soil, improves the soil physical and chemical properties, reduces the alkalinity of soil and chloride ion (Cl-) content, and increases organic matter, potassium, and nitrogen in saline soil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising weighing the raw materials, crushing, mixing uniformly to obtain mixed material, fermenting at 74 degrees C for 11 days, turning every other day, controlling the pH of the mixed material at 6-8, granulating, drying, and filtering to obtain the product.
NOVELTY - Treatment of kitchen garbage into fertilizer comprises collecting the kitchen garbage, performing solid and liquid separation, adding strain to solid waste residue to ferment, converting, performing compression dehydration, heating and solidifying.    USE - Method of treating kitchen garbage into fertilizer (claimed).    ADVANTAGE - The method reduces kitchen waste volume to minimum, converts useful substance into biological diesel oil, and is harmless.    DESCRIPTION OF DRAWING(S) - The drawing is a process flow diagram illustrating the treatment of kitchen garbage into fertilizer (Drawing includes non-English language text).
NOVELTY - An oil-based bio-organic fertilizer comprises 85-90 pts. wt. oil-contaminated soil residue, 15-20 pts. wt. ammonium bicarbonate, 7-10 pts. wt. cotton straw powder, 2-3 pts. wt. cypress powder, 10-13 pts. wt. peel, 1-3 pts. wt. weathered coal, 3-4 pts. wt. ammonium chloride, 7-9 pts. wt. sesame cake, 2-4 pts. wt. borax, 1-2 pts. wt. paraffin, 1-2 pts. wt. potassium mineral powder, 4-5 pts. wt. sepiolite powder, 64-70 pts. wt. swill, 12-17 pts. wt. brown sugar, and 76-80 pts. wt. human or animal feces.    USE - Oil-based bio-organic fertilizer.    ADVANTAGE - The fertilizer has high organic matter content, large active material amount, and balanced major elements and trace metal content. The product improves soil quality and structure.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of oil-based bio-organic fertilizer comprising:    (A) taking sepiolite powder, adding 6-8 times amount of water, heating at 80-90 degrees C, stirring, adding oil-contaminated soil residue, ammonium bicarbonate, and cotton straw powder, stirring for 20-30 minutes, drying, and granulating to particle size of 1-2 mm;    (B) dissolving brown sugar in 1.8-2 times amount of water, adding 10-15 wt.% fermenting agent, 0.1-0.3 wt.% wintergreen oil, 1-2 wt.% alum, stirring at 30-40 degrees C for 15-20 days to ferment, adding 1-2 wt.% ammonium molybdate, and stirring;    (C) mixing cypress powder, peel, and weathered coal, inoculating with 0.5-0.8 wt.% of efficient microbes (EM) liquid culture, adding water to moisture content of 60-65%, and fermenting at room temperature for 3-5 hours; and    (D) mixing soil mixture, EM fermentation product and remaining raw materials, adding 2-4 wt.% humic acid mixture, and 0.1-0.2 wt.% Chinese herbal medicine, stirring, fermenting stack at room temperature for 10-12 hours, turning over, adding sugar fermentation product, mixing, fermenting stack for 2-4 hours, and drying.
NOVELTY - A cultivation material comprises 30-40 wt.% waste tea leaves, 24-30 wt.% sawdust, 20-30 wt.% cotton seed hull, 6-10 wt.% soybean powder, 2 wt.% calcined lime powder, 2 wt.% gypsum, 0.5 wt.% calcium superphosphate, and 0.5 wt.% potassium dihydrogen phosphate.    USE - A cultivation material used for slippery mushroom (claimed).    ADVANTAGE - The cultivation material is inexpensive, provides mushroom with good quality, and is environment friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the cultivation material, comprising:    (A) mixing waste tea leaves, sawdust, and cotton seed hull with 2% aqueous solution of lime for 2 hours, and maintaining moisture content of 50-55% to obtain a pre-wet mixture;    (B) adding soybean powder, gypsum, and calcium superphosphate, slowly adding potassium dihydrogen phosphate, stirring, and maintaining moisture content at 65%;    (C) folding high-pressure polyethylene bag cartridge having length of 60 cm, and a thickness of 0.05 mm, sterilizing at 100 degrees C, and discharge cooling gas; and    (D) keeping for 10-12 hours, and naturally cooling to lesser than 25 degrees C.
NOVELTY - Preparation of neratinib involves condensation of (E)-4-dimethylamino-but-2-enoic acid (4-amino-3-cyano-7-ethoxy-quinolin-6-yl)-amide and 3-chloro-4-(pyridin-2-ylmethoxy)-benzaldehyde, and then reduction to form neratinib.    USE - For preparation of neratinib (claimed) useful for treating cancer.    ADVANTAGE - The method is simple, is economical and environment-friendly, and is suitable for industrial production.
NOVELTY - Preparation of atorvastatin (Avanafil) involves performing substitution reaction of cytosine and 3-chloro-4-methoxy benzyl halogen (III) to form 6-(3-chloro-4-methoxy-benzylamino)-1H-pyrimidin-2-one (V); reacting N-pyrimidin-2-ylmethyl-formamide (IV) with (V) to form 6-(3-chloro-4-methoxy-benzylamino)-2-oxo-1,2-dihydro-pyrimidine-5-carboxylic acid (pyrazin-2-ylmethyl)-amide (VI); and condensation of (S)-1-pyrrolidin-2-yl-methanol with (VI) to form atorvastatin (Avanafil).    USE - For preparation of atorvastatin (Avanafil) (claimed) for the treatment of male erectile dysfunction.    ADVANTAGE - The preparation method is simple, economic and environment-friendly, and suitable for industrial production.    DETAILED DESCRIPTION - Preparation of atorvastatin (Avanafil) involves performing substitution reaction of cytosine and 3-chloro-4-methoxy benzyl halogen of formula (III) to form 6-(3-chloro-4-methoxy-benzylamino)-1H-pyrimidin-2-one (V); reacting N-pyrimidin-2-ylmethyl-formamide (IV) with (V) to form 6-(3-chloro-4-methoxy-benzylamino)-2-oxo-1,2-dihydro-pyrimidine-5-carboxylic acid (pyrazin-2-ylmethyl)-amide (VI); and condensation of (S)-1-pyrrolidin-2-yl-methanol with (VI) to form atorvastatin (Avanafil).    X=Br, Cl, or I.
NOVELTY - A ginseng continuous cropping soil biological activator comprises 2-8 wt.% Bacillus subtilis, 2-8 wt.% actinomycete, 5-20 wt.% xylanase, 5-20 wt.% cellulase, 10-20 wt.% urease, 1-4 wt.% potassium dihydrogen phosphate, 0.1-0.5 wt.% ferrous sulfate, 0.1-0.4 wt.% boric acid, 0.1-0.5 wt.% manganese sulfate, 0.05-0.2 wt.% copper sulfate, 0.1-0.4 wt.% zinc sulfate, 0.05-0.2 wt.% ammonium molybdate, and balance organic material.    USE - Ginseng continuous cropping soil biological activator.    ADVANTAGE - The biological activator can improve physicochemical and biological properties of soil to increase ginseng continuous cropping yield, prevent disease and improve ginseng quality.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the ginseng continuous cropping soil biological activator, comprising uniformly mixing raw materials, adjusting water content to 60% and adjusting pH value to 6.5, and composting.
NOVELTY - A selenium-rich bioorganic fertilizer comprises 75-85 wt.% organic material, 14-24 wt.% maifan stone, 0.003 wt.% selenium-rich fertilizer, and 0.005 wt.% fermentation bacteria.    USE - Selenium-rich bioorganic fertilizer.    ADVANTAGE - The fertilizer prevents soil compaction, hardening, alkalinization and desertification; increases organic material and beneficial bacterial contents of soil; and improves crop growth and nutrient deficiency caused by diseases and harmful bacteria, thus, reducing pesticide dosage.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of bioorganic fertilizer by mixing organic material, maifan stone and selenium-rich fertilizer, adding fermentation bacteria, adding water while uniformly stirring until water content is 50%, covering with straw mat for insulation, turning and ventilating when temperature reaches 45-65 degrees C, repeating turning and ventilating step 5-6 times when temperature reaches 45-65 degrees C, drying fermented product, sieving, weighing, and packaging.
NOVELTY - Extraction of capsaicin from pepper involves (a) taking fresh pepper, removing dust, drying the pepper at constant weight and preparing dry pepper, (b) removing stem and seed of the dry pepper, (c) crushing processed pepper into powder by using a crusher and collecting dry pepper powder, (d) carrying ultrasonic extraction in prepared pepper powder using organic solvent and filtering to obtain product, and (e) carrying out reduced pressure condensation on the product.    USE - The method is useful for extracting capsaicin from pepper (claimed).    ADVANTAGE - The method is simple, convenient, rapid, stable, low in energy consumption, cost-effective, energy-saving, environmentally-friendly, and reliable, and has high extraction efficiency.
NOVELTY - Straw returning type selenium-enriched garlic planting method comprises selecting proper planting time, transplanting to a clack; planting and fertilizer water management, preventing and treating insect pests. The planting and fertilizer water management step involves crushing garlic straw, adding 2 kg fermentation agent per 1000 kg straw and 2-8 kg urea, putting into fermenting tank, covering with soil layer and black film, fermenting for 5-7 days, applying 450 kg straw fertilizer, 10 kg diammonium phosphate, 10 kg base fertilizer, and 10 kg diammonium phosphate for the second time.    USE - A straw returning type selenium-enriched garlic planting method.    ADVANTAGE - The method not only improves the quality of the garlic, but also supplies the nutrient needs of garlic in the growth process, at the same time saves using amount of fertilizer, and greatly reduces planting cost.
NOVELTY - Preparation of tandutinib (I) involves: condensation of 6-methoxy-7-(3-piperidin-1-yl)-3,4-4-one (II) and N-(4-cyclopropyl oxygen phenyl)-1-piperazine (III) and organic base under action of condensing agent, promoter and solvent at 0-120 degrees C to obtain planar degree of nylon (I). The compound (II) and (III) is in a mol ratio is 1:1-2.    USE - For preparation of tandutinib (claimed); for treating diseases such as acute bone myeloid leukemia, multiple myeloma, and myelodysplastic syndrome.    ADVANTAGE - The method produces tandutinib easily, and in simple technique, mild reaction condition, environment and quality, suitable for industrialized production, promotes the development of the economy and technique of the raw material medicine.
NOVELTY - Preparation of lapatinib (I), involves: condensation reaction of 6-(5-((2-para ethyl amino) methyl)-2-3-yl)-4-dihydroquinazolin-4-one (II) and 3-chloro-4-(3) aniline (III) in presence of organic alkali and condensating agent.    USE - In preparation of lapatinib (claimed) for the treatment of advanced or metastatic breast cancer.    ADVANTAGE - The method is simple and is environment friendly, requires mild reaction condition, and is suitable for industrialized production, and economical.
NOVELTY - Separation and purification of tripterine by mixing Celastrus orbiculatus concentrate and silica gel, and drying to obtain granular materials; filling separation column with silica gel and dichloromethane-methanol solution, adding granular materials, eluting with dichloromethane-methanol and aqueous ammonia, and adding anhydrous sodium sulfate to remove water; and collecting eluting liquid, recovering eluent to obtain pure tripterine, and washing with methanol or ethanol.    USE - Method for separation and purification of tripterine (claimed).    ADVANTAGE - The method is simple, efficient, environment-friendly, and suitable for industrial production, and has high yield.    DETAILED DESCRIPTION - Separation and purification of tripterine comprises mixing Celastrus orbiculatus concentrate and 60-80 mesh silica gel at mass ratio of 1:1, and drying to obtain granular materials; filling 10-30 cm separation column with 200-300 meshes silica gel and dichloromethane-methanol solution at volume ratio of 25:1-15:1, adding granular materials, eluting with dichloromethane-methanol at volume ratio of 20:1-5:1 and aqueous ammonia, and adding anhydrous sodium sulfate to remove water; and collecting eluting liquid to obtain tripterine crude solution, recovering eluent at 40-60 degrees C under reduced pressure to obtain pure tripterine, and washing with methanol or ethanol. The volume ratio of dichloromethane and methanol is 25:1-15:1. The volume ratio of methanol and aqueous ammonia is 100:0.1-0.5.
NOVELTY - An organic fertilizer preparation method involves mixing farmland or orchard waste with clay, and fermenting to obtain a first fermentation product. The first fermentation product is mixed with kitchen waste and fermented at 60-80 degrees C to obtain a second fermentation product. The second fermentation product, farmland or orchard waste, livestock waste and clay are mixed together to obtain an organic fertilizer.    USE - Method for preparing organic fertilizer.    ADVANTAGE - The method enables preparing organic fertilizer with reduced discharge of waste, in an environment-friendly, inexpensive, safe and reliable manner.
NOVELTY - A carbonic acid method sugar refinery filter mud and manioc waste comprehensive treatment method involves preparing materials comprising mud powder, manioc waste, carbamide, monopotassium phosphate and corn powder. The mud powder is prepared into cassava dregs. The cassava dregs are dissolved by adding urea, monopotassium phosphate and water to obtain mixture. The mixture is mixed with corn powder to obtain mixed material. The mixed material is placed in fermentation tank for aerobic fermentation and rotting through inlet end of the fermentation tank. The mixed material is turned up.    USE - Method for comprehensive treatment of carbonic acid method sugar refinery filter mud and manioc waste.    ADVANTAGE - The method enables comprehensive treatment of carbonic acid method sugar refinery filter mud and manioc waste with reduced alkalinity of the carbonic acid method filter mud, and improved content of fertilizer effect components.    DETAILED DESCRIPTION - A carbonic acid method sugar refinery filter mud and manioc waste comprehensive treatment method involves preparing materials comprising mud powder, manioc waste, carbamide, monopotassium phosphate and corn powder at a weight ratio of 1-2:0.04-0.05:0.002 -0.003:0.03-0.05:0.00-0.005. The mud powder is prepared into cassava dregs. The cassava dregs are dissolved by adding urea, monopotassium phosphate and water to obtain mixture. The mixture is mixed with corn powder to obtain mixed material. The mixed material is placed in fermentation tank for aerobic fermentation and rotting through inlet end of the fermentation tank. The mixed material is progressively turned up and pilled up towards the outlet end to form a regular fermentation gradient, after heating fermented materials at more than 55 degrees C for 2 days. The temperature is maintained for 5-7 days, increasing turning for 2-3 days and maintaining temperature at 37-40 degrees C to obtain a decomposed filter mud organic fertilizer.
NOVELTY - A biological organic fertilizer comprises 90-95 pts. wt. base materials, 0.5-1 pts. wt. biological fermentation agent, 0.5-1 pts. wt. fast rotting agent, 0.5-1 pts. wt. humic acid, 0.05-1.5 pts. wt. preservatives, 0.1-0.2 pts. wt. soil conditioning agent and 0.1-0.3 pts. wt. pH regulator.    USE - Biological organic fertilizer.    ADVANTAGE - The fertilizer has strong ability to fight against soil-borne disease.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing a biological organic fertilizer, which involves mixing and stirring a base material, a biological fermentation agent, the humic acid, a fast rotting agent and the preservatives to obtain a mixed material, fermenting the mixed material in a fermentation tank at 25-65 degrees C for 4-6 days, drying the obtained fermented material under air atmosphere, crushing the dried material to obtain a crushed material, adding a soil conditioning agent and a pH regulator into the crushed material and packing to obtain a finished product.
NOVELTY - A Bacillus cereus ZZ12 strain having preservation date of March 15, 2013 in China microorganism bacterial strain preservation management committee common microorganism centre and preservation number of CGMCC NO:7322, is new.    USE - Bacillus cereus ZZ12 strain for producing heteroauxin, degrading polycyclic aromatic hydrocarbon anthracene, and preparing biological fertilizer (all claimed).    ADVANTAGE - The strain has better anthracene degradation capacity, and produces the heteroauxin with high yield and better salt and alkali resistance.
NOVELTY - A Arthrobacter pascens strain ZZ21 having preservation number of CGMCC No:7325 preserved at China General Microbiological Culture Collection Center on March 15th, 2013, is new.    USE - Arthrobacter pascens strain ZZ21 for producing heteroauxin, for degrading polycyclic aromatic hydrocarbon fluoranthene and preparing bio-fertilizer (all claimed).    ADVANTAGE - The strain has better degradation effect on polycyclic aromatic hydrocarbon fluoranthene, and produces heteroauxin with high yield and better salt and alkali resistance.
NOVELTY - Fertilizer comprises common nitrogen fertilizer, 60-day controlled release fertilizer, 90-day controlled release fertilizer and 120-day controlled release fertilizer.    USE - The fertilizer is useful for peanut (claimed).    ADVANTAGE - The fertilizer can perform sustained and stable supply against requirements for the nitrogen fertilizer of the peanuts during the growth and development processes, prevent affecting nitrogen fixation of rhizobia and normal growth and development of plants due to too high nitrogen concentration in soil in a certain period of time, and further prevent affecting the growth and development of the plants due to insufficient nitrogen concentration in the soil in a certain period of time to realize supply according to requirements.
NOVELTY - 3-acetyl-5-acetimido-2-(N-phenothiazinyl)-1,3,4-thiadiazole is new.    USE - 3-acetyl-5-acetimido-2-(N-phenothiazinyl)-1,3,4-thiadiazole for anti-gram bacteria medicine (claimed) and pesticide.    ADVANTAGE - Preparation of 3-acetyl-5-acetimido-2-(N-phenothiazinyl)-1,3,4-thiadiazole is simple, short, and environment-friendly and has high yield.    DETAILED DESCRIPTION - 3-acetyl-5-acetimido-2-(N-phenothiazinyl)-1,3,4-thiadiazole of formula (I) is new.. An INDEPENDENT CLAIM is included for preparation of 3-acetyl-5-acetimido-2-(N-phenothiazinyl)-1,3,4-thiadiazole.
NOVELTY - The system has a blade that is formed in the inner circumference of an inner container. A penetration hole is formed in the circular ring. A drive motor (200) is arranged at the main portion (100). A sprocket (170) is formed in the outer periphery of the main portion. A cooling supply unit (500) is connected to the rotary joint and nozzle (N), to supply the cooling water to the main portion through the supply tube to space between the inner container and the outer container (140), such that food waste or sludge is cooled in the rapidly.    USE - Sorting system for icing dried food trash or sludge in domestic and industrial application.    ADVANTAGE - As the inside and outer temperature difference of the storage tank is minimized, the cooling efficiency of the fodder decay can be improved by providing the dried food category waste in the sludge cooling line. The unnecessary raw material used in the sorting system can be prevented. The fire hazard at the storage tank can be prevented. The installation place and the demand of the sorting system can be utilized effectively. The productivity of the sorting system for icing dried food trash or sludge in domestic and industrial application can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the sorting system for icing dried food trash or sludge in domestic and industrial application.    Main portion (100)    Outer container (140)    Sprocket (170)    Drive motor (200)    Cooling supply unit (500)    Nozzle (N)
NOVELTY - A soil disease preventing and soil fertility improving method involves storing biogas slurry, and sowing soil anaerobic fermentation raw material. A soil anaerobic fermentation raw material is scattered in a greenhouse cultivation soil. Soil tillage is conducted on the raw materials. Flood irrigation is conducted on cultivated field through the slurry and water. A soil layer is submerged by a liquid. A diffuse irrigation planting soil is covered by plastic and pressing films for sealing. A soil is uncovered by plastic film to conduct soil tillage, followed by ventilating and drying.    USE - Method for preventing soil disease and improving soil fertility of greenhouse.    ADVANTAGE - The method enables preventing soil disease and improving soil fertility of greenhouse with sterilizing effect, inexpensive, high strength, biogas slurry consumption, improved soil physical and chemical properties and acid-base equilibrium, disease-insect resistance of the crop, absorption efficiency and fertilizer efficiency by killing harmful bacteria.    DETAILED DESCRIPTION - AA soil disease preventing and soil fertility improving method involves storing biogas slurry in a storage pool. A soil anaerobic fermentation raw material is sown at high temperature in summer. A soil anaerobic fermentation raw material is uniformly scattered in the greenhouse cultivation soil at carbon-nitrogen ratio of 15-40: 1. Soil tillage is conducted on the evenly-scattered anaerobic fermentation raw materials. Flood irrigation is conducted on cultivated field through the biogas slurry and water. A soil layer is submerged by a liquid at a muddy state. A diffuse irrigation planting soil is covered by plastic film and pressing film for sealing. A greenhouse is depressed at temperature more than 40 degrees C. A planting soil is uncovered by plastic film to conduct soil tillage, followed by ventilating and drying from aerobic to anaerobic condition.
NOVELTY - A biogas digester internal and external sealing treatment method involves carrying out sealing treatment on interior of a biogas digester body, and externally sealing an outer wall of the biogas digester below a vault and arch angles. The digester is sealed by adopting three-layer coating. Cement sand mortar is adopted for coating of two layers. Plain mortar is adopted for coating of the third layer. The outer wall is coated for three times i.e. horizontally, vertically and horizontally.    USE - Method for internal and external sealing treatment of biogas digester.    ADVANTAGE - The method enables sealing a biogas digester with long life span, in a simple and practical manner, and ensuring repairing of an old biogas digester.    DETAILED DESCRIPTION - A biogas digester internal and external sealing treatment method involves carrying out sealing treatment on interior of a biogas digester body, and externally sealing an outer wall of the biogas digester at width of 20 cm below a vault and arch angles. The digester is sealed by adopting three-layer coating. Cement sand mortar is adopted for coating of two layers, where thicknesses of the coatings are 1-1.5 cm and 0.4-0.6 cm. Plain mortar is adopted for coating of the third layer. The outer wall is coated for three times i.e. horizontally, vertically and horizontally, where coating thickness is 0.1 cm.
NOVELTY - A bagasse pre-treating method involves drying, crushing and sieving bagasse to obtain a raw material with grain size of 18-40 meshes, and adding the raw material with a mixed aqueous solution of 1-3% sodium hydroxide and 0.5-1.5% hydrogen peroxide. The obtained mixture is pre-treated at 25-42 degrees C for 12-36 hours under condition of stirring. The pre-treated mixture is filtered and washed with distilled water until pH of the mixture reaches 6.5-7.5. The mixture is dried at 60-80 degrees C to obtain pre-treated bagasse.    USE - Method for pre-treating bagasse that is utilized for fermenting and converting microorganism to alcohol.    ADVANTAGE - The method enables increasing cellulose hydrolysis rate, and improving enzymolysis resistance property of the bagasse.
NOVELTY - A propylene and propane is separated by weighing metal organic framework material, compressing metal organic framework material under pressure to form tablet, separating sieved particle as adsorbent into mixed gas of propylene and propane, filling fixed bed tube type reactor with obtained adsorbent, pre-treating adsorbent, using prepared propylene and propane as raw material gas, subjecting raw material gas into fixed bed tube type reactor filled with adsorbent by modulating partial pressure, temperature, and total pressure of raw material gas.    USE - Separation of propylene and propane (claimed).    ADVANTAGE - Separation process is simple and low in cost and has good effect.    DESCRIPTION OF DRAWING(S) - The drawing shows a graph of X-ray diffraction spectrum of metal organic framework particle. (Drawing includes non-English language text).
NOVELTY - A biological organic bacteria fertilizer comprises 40 wt.% human manure, waste crop straw residue, paper bagasse, and mushroom waste; 30 wt.% sugar mill residue; 30 wt.% crop straw; and 1 pt. wt. additive containing 40 wt.% complex microbial inoculant NSC-7, 30 wt.% lactic acid bacteria, 10 wt.% polyaspartic acid, 5 wt.% syrup, 5 wt.% Bacillus subtilis, 5 wt.% Trichoderma, and 5 wt.% bioenzyme activating agent.    USE - Bioorganic fertilizer used for improving soil and quality of crops, balancing nutrients of soil, and increases yield.    ADVANTAGE - The fertilizer is free of pollution and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of biological organic bacteria fertilizer by mixing human manure, waste crop straw residue, paper bagasse, mushroom waste, sugar mill residue, and crop straw to obtain mixture; adding water to complex microbial inoculant NSC-7, Bacillus subtilis, and Trichoderma while stirring, and sprinkling to mixture until moisture content is 50-60%; uniformly mixing, piling into 1 m deep and 2 m length, covering with plastic, and fermenting for 24 hours by controlling inner temperature to 75 degrees C and moisture content to 60-65%; adding lactic acid bacteria, polyaspartic acid, syrup, and bioenzyme activating agent while stirring when fermentation temperature has returned to normal, and continuously accumulating for 12 hours to obtain semi-finished materials with very strong unique aroma; putting into square tile sealed container with thickness not exceeding 100 mm, placing 60 W infrared bulbs 1 m above the material and 1.5 m apart, spraying little water, and controlling temperature to 55 degrees C and moisture to 60-65% inside the container for 6 hours; and granulating at 80 degrees C to obtain particles having humidity of 25-30%, and packaging.
NOVELTY - Automatic domestic wastewater recycling device with no motor comprises box body (1) set with wastewater interfaces (2). The box body is provided with wastewater inlet grid (3), wastewater deposition grid (4), biological bed grid (5), and sludge grid (7). The wastewater grid is provided with filter (9).    USE - Automatic domestic wastewater recycling device with no motor.    ADVANTAGE - The device does not need electric energy consumption.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of automatic domestic wastewater recycling device.    Box body (1)    Wastewater interfaces (2)    Wastewater inlet grid (3)    Wastewater deposition grid (4)    Biological bed grid (5)    Sludge grid (7)    Filter (9)
NOVELTY - A sludge microorganism is hydrolyzed by inoculating thermophilic bacillus to luria broth (LB) culture medium at 40-60 degrees C and at 100-120 revolutions/minute (rpm) for 24-36 hours obtain activated thermophilic bacillus, fermenting activated thermophilic bacillus for 12-24 hours at 40-80 degrees C to obtain thermophilic fermented solution, and taking 75-200 ml thermophilic fermented liquid supernatant, and adding water in residual sludge to obtain 300 ml mixed solution, and incubating mixed solution at 60-80 degrees C for 1-6 hours.    USE - Method for the hydrolysis of sludge microorganism (claimed).    ADVANTAGE - The method promotes cracking rate of microorganism and improves hydrolysis rate of sludge.    DETAILED DESCRIPTION - Hydrolysis of sludge microorganism comprises:    (A) inoculating thermophilic bacillus to LB culture medium at 40-60 degrees C at 100-120 rpm for 24-36 hours obtain activated thermophilic bacillus, fermenting activated thermophilic bacillus for 12-24 hours at 40-80 degrees C to obtain thermophilic fermented solution, and taking 75-200 ml thermophilic fermented liquid supernatant, and adding water in residual sludge to obtain 300 ml mixed solution, and incubating mixed solution at 60-80 degrees C for 1-6 hours; and    (B) sterilizing fermentation culture medium with 10 g skim milk, 3 g yeast extract powder, 6.7 g ammonium sulfate, 0.5 g sodium chloride, 1.2 g dipotassium phosphate, 0.7 g potassium phosphate, and 0.5 g magnesium sulfate heptahydrate, and 1000 ml water with pH of 7 at 105 degrees C for 15 minutes.
NOVELTY - Producing biogas by fermenting livestock manure involves mixing manure and sewage of livestock farms in preprocessing tank, diluting into suspension with solid content rate of 8-12%, feeding pretreated material to anaerobic reactor, and fermenting material in anaerobic reactor, where the material by intermittent feeding, fermentation is performed at 25-40 degrees C, the reaction is carried out until volumetric biogas production rate reaches 0.6 m3/m3x d and biogas content and carbon dioxide content are stabilized to respectively 55-70% and 30-45%.    USE - The method is useful for producing biogas by fermenting livestock manure chosen from sheep manure, pig manure and cow dung. The biogas is used directly after purification as fuel gas, remainder gas for turbine power generation by biogas power generator and slurry and residue as organic fertilizer (all claimed).    ADVANTAGE - The method is environmentally-friendly.    DETAILED DESCRIPTION - Method for production of biogas by fermenting livestock manure involves mixing manure and sewage of livestock farms in preprocessing tank, diluting into suspension with solid content rate of 8-12%, feeding the pretreated material into anaerobic reactor through feed pump and pipe, and fermenting the material in the anaerobic reactor, where the material is fed for 1-3 times per day at rate of 1 divide by 25-1 divide by 15 to capacity of reactor by intermittent feeding for 15-20 days, the amount of sludge inoculated is 15-30% of the reactor, raw materials in the reactor is equal to 80-90% volume of the reactor, fermentation is performed at 25-40 degrees C and pH of 6.8-7.2, the reaction is carried out until volumetric biogas production rate reaches 0.6 m3/m3x d and biogas content and carbon dioxide content are stabilized to respectively 55-70% and 30-45%.
NOVELTY - Method for extracting biological active substances in crayfish by-products, involves sequentially carrying out enzymolysis treatment on crushed crayfish shells and crayfish heads, removing crayfish meat, spraying and drying filtered solution, carrying out organic acid leaching treatment on filtered solid, spraying and drying filtered solution, adding the filtered solid into ethanol to be treated, carrying out rotary evaporation on the filtered solution, and carrying out hydrogen peroxide immersion de-coloring treatment on the filtered solid.    USE - The method is useful for extracting biological active substances in crayfish by-products (claimed), which is used for sequentially obtaining food-grade standard hydrolyzed protein powder, organic calcium, astaxanthin and chitin products.    ADVANTAGE - The method is simple process and environmentally-friendly, shortens production period, improves product additional value, and reduces wastewater emission.    DETAILED DESCRIPTION - Method for extracting biological active substances in crayfish by-products, involves boiling crayfish with water to obtain crayfish shells and crayfish heads as raw materials, sequentially carrying out enzymolysis treatment on crushed crayfish shells and crayfish heads, removing crayfish meat, spraying and drying filtered solution to obtain hydrolyzed protein powder, carrying out organic acid leaching treatment on filtered solid, spraying and drying filtered solution to obtain organic calcium, adding the filtered solid into ethanol to be treated, carrying out rotary evaporation on the filtered solution to obtain astaxanthin rough product, and carrying out hydrogen peroxide immersion de-coloring treatment on the filtered solid to obtain de-colored chitin.
NOVELTY - A Lactobacillus strain (CGMCC NO. 6495), is new.    USE - The Lactobacillus strain is useful in agents for deodorization of excrement preferably in-situ deodorization of the human excrement (all claimed) in public toilets and clinical laboratories.    ADVANTAGE - The Lactobacillus strain is utilized as single strain for in-situ deodorization of the human excrement, hence deodorization effect is stable and influence of temperature is less. The Lactobacillus strain provides better deodorization effect under normal temperature conditions both in laboratory and public toilets sites or environments.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for usage method of the above-mentioned Lactobacillus strain, which involves applying/contacting activated, cultured and expanded culture liquid of the above-mentioned Lactobacillus strain to the excrement.
NOVELTY - Use of Bacillus thuringiensis is claimed in agriculture for promoting decomposition in corn straw. The B.thuringiensis is deposited as CGMCC NO: 5437. The straw is dry or wet straw.    USE - The B.thuringiensis is useful for promoting decomposition in corn straw and for producing soil fertilizer (all claimed).    ADVANTAGE - The fertilizer has decomposition rate of 51.6-55.3% and 41.6-57.8% respectively in pot experiment and field using dry corn straw powder and fresh straw, and increases emergence rate of wheat by 8.2-16.8%, hence rapid decomposition of straw, effects of seedling protection and increased yield of the succeeding wheat are realized.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) fertilizer comprising B.thuringiensis and adjuvant; and (2) fermentation method involves inoculating B.thuringiensis in liquid Luria-Bertani medium, performing culture at 30-37 degrees C and 200-220 revolutions per minute (rpm) for 10-16 hours to obtain first culture, inoculating 5-10% first culture into liquid Luria-Bertani medium, performing culture at 30-37 degrees C and more than 200-220 rpm for 20-28 hours to obtain second culture, selecting second culture as solid fermentation medium, transferring 8-12% fermentation medium to separate flask and culturing in shaker at 30-37 degrees C for 120-168 hours, where the solid fermentation culture medium comprises 28-32 pts. wt. corn cob powder, 68-72 pts. wt. water, 0.05 pts. wt. calcium carbonate, 0.075 pts. wt. dipotassium phosphate and 0.035 pts. wt. magnesium sulfate.
NOVELTY - A Issatchenkia orientalis yeast strain deposited as CGMCC NO: 6496, is new.    USE - The I.orientalis yeast strain is useful for in-situ deodorization of animal and fowl excrement (all claimed).    ADVANTAGE - The strain has stable deodorization effect, cannot be easily affected by temperature and still has good effect at 1-5 degrees C.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of using the above-mentioned strain for deodorizing animal and fowl excrement.
NOVELTY - Method for culturing Myrciaria cauliflora, involves performing stem planting, watering planted stems, applying fertilizer to planted stems, and pruning and stunting product. The fertilizer is prepared by mixing and fermenting sheep feces, sika deer feces, leaven and distillers yeast at a weight ratio of 2:1:0.2:2.5 at 22-28 degrees C for 21 days. The stunting is performed using stunting agent comprising 27 wt.% cupric sulfate, 18 wt.% manganese, 7 wt.% iodized salt and 48 wt.% water.    USE - The method is useful for culturing M.cauliflora (claimed).    ADVANTAGE - The method is pollution free, and utilizes specially-prepared fertilizers and thus fruits can be obtained in 2 years after stem planting.
NOVELTY - A Bacillus subtilis strain JUWE1001 deposited as CGMCC NO. 7034, is new.    USE - The B.subtilis strain JUWE1001 is useful for preparing microbial organic fertilizer (claimed), promoting decomposition of soil organic matter and plant root growth, enhancing soil fertility, controlling soil enzyme activity, improving microbial community structure in soil and inhibiting harmful fungi, bacteria including Mycoplasma and virus.    ADVANTAGE - The strain has strong stress resistance and produces rich physiological active substances with high activity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of culturing the strain, which involves (a) inoculating the strain JUWE1001 in beef extract and peptone slant culture, and culturing at 35-39 degrees C for 45-50 hours, (b) inoculating culture from slant culture to corn powder medium and culturing at 35-39 degrees C and 180-220 revolutions per minute (rpm) for 22-26 hours, and (c) inoculating 1-5 weight/weight% inoculum obtained in step (b) in fermentation medium containing corn powder and fermenting at 35-38 degrees C, 0.05 MPa, and 0.8-1 volume per volume per minute (vvm) ventilation rate for 2-3 days.
NOVELTY - Method for preparing nano-fertilizer, involves (a) mixing nano-chitosan, potassium dihydrogen phosphate, choline chloride and humic acid, heating the obtained mixture, agitating and cooling the obtained mixture, adding trace element to the obtained mixture, and fermenting the obtained mixture at normal temperature to obtain a water fertilizer, (b) mixing biological nutrient soil and chitosan, stirring and maintaining temperature at 50 degrees C, and fermenting and turning for every three days, and (c) mixing the water fertilizer and soil product.    USE - The method is useful for preparing nano-fertilizer (claimed).    ADVANTAGE - The nano-fertilizer is environmentally-friendly and improves plant growth.    DETAILED DESCRIPTION - Method for preparing nano-fertilizer, involves (a) mixing 40-60 pts. nano-chitosan, 15-20 pts. potassium dihydrogen phosphate, 5-10 pts. choline chloride and 20-30 pts. humic acid, heating the obtained mixture at 80 degrees C in a water bath, agitating and cooling the obtained mixture, adding 2-8 pts. trace element to the obtained mixture, and fermenting the obtained mixture at normal temperature for 3 days to obtain a water fertilizer, (b) mixing biological nutrient soil and chitosan in a ratio of 1:1, stirring for 30 minutes, maintaining temperature at 50 degrees C, and fermenting and turning for every three days for 5-7 times, where the turning time is 30 minutes, and (c) mixing the water fertilizer and soil product in the weight ratio of 2:3. An INDEPENDENT CLAIM is included for nano-fertilizer, which is prepared by the above-mentioned method.
NOVELTY - Egg shell vacuum dryer comprises (a) a dryer (2) to ensure drying of the introduced egg shell at a high temperature vacuum, (b) a vacuum pump to maintain vacuum inside the dryer, (c) a high temperature boiler (3) to heat the dryer, (d) a cooling tower (4) to cool water vapors occurred when the egg shell is dried by suction, (e) a filter unit (5) to filter the water cooled in the cooling tower, and (f) a water tank (6) to store water filtered by the filter unit.    USE - The dried egg shell is used as fertilizer.    ADVANTAGE - The egg shell vacuum dryer: allows carrying out environment-friendly technology, which does not use chemical components, maintains nutritional ingredients of the eggshell, does not results in odor and avoids gas; and is economical. The dried egg shell increases crops production, improves seed quality and nature of the soil when used as the fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the egg shell vacuum dryer.    Dryer (2)    High temperature boiler (3)    Cooling tower (4)    Filter unit (5)    Water tank (6)
NOVELTY - A phosphoric liquid fertilizer producing method involves subjecting Acidithiobacillus ferrooxidans or Bacillus megaterium to digestion process for greater than or equal to 14 days, treating resultant product with 0.1-15 g phosphorus pentoxide, and increasing nitrogen, sulfur, potassium, magnesium and iron content.    USE - Method for producing phosphoric liquid fertilizer.
NOVELTY - Production of caprolactam comprises toluene is oxidised to benzoic acid by action of cobalt catalyst hydrogenating oxidized benzoic acid with palladium carbon catalyst to obtain cyclohexanecarboxylic acid; performing amidation of obtained product with nitrosylsulfuric acid to obtain cyclohexanone; performing oximation of obtained product to obtain cyclohexanone oxime; and rearranging of cyclohexanone oxime in amide solvent at 70-130 degrees C with pressure at 0-1 MPa, neutralizing, crystallizing, extracting, and refining.    USE - Method for producing caprolactam (claimed).    ADVANTAGE - The method is simple, increases yield of caprolactam, and has low cost.    DETAILED DESCRIPTION - Production of caprolactam comprises toluene is oxidised to benzoic acid by action of cobalt catalyst; hydrogenating oxidized benzoic acid with palladium carbon catalyst to obtain cyclohexanecarboxylic acid; performing amidation of obtained product with nitrosylsulfuric acid to obtain cyclohexanone; performing oximation of obtained product to obtain cyclohexanone oxime; and rearranging of cyclohexanone oxime in amide solvent at 70-130 degrees C with pressure at 0-1 MPa, neutralizing, crystallizing, extracting, and refining. The mole ratio of acid solvent and cyclohexanone oxime is 1-2:1. The heat is removed by rearrangement heat extraction solvent or heat external circulation method.
NOVELTY - Biomass-based organic polymer porous material comprises 2,5-dimethyl acyl furan and organic molecule containing amino group, which are alternately bonded to form organic polymer with linear or net-shaped structure.    USE - Biomass-based organic polymer porous material useful in the field of gas storage, separation, adsorption of water phase organic material and heavy metal ion, and catalytic material.    ADVANTAGE - The biomass-based organic polymer porous material has high specific surface area and pore volume.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for synthesis of biomass-based organic polymer porous material comprising adding 2,5-dimethyl acyl furan and amino group-containing organic molecule in an organic solvent, polymerization reacting, and filtering to obtain porous organic polymer material having high specific surface area and pore volume.
NOVELTY - Trichoderma virens ZY-01 strain capable of secreting cellulase enzyme (CCTCC No. M 2012205), is new. The 18S ribosomal DNA (18S rDNA) of the strain comprises fully defined 1714 nucleotides (SEQ ID NO: 1) as given in the specification.    USE - The cellulase is useful for efficient degradation of cellulose-rich biomass, preferably sugarcane bagasse, corn straw, rice or wheat straw (all claimed).    ADVANTAGE - The strain has high enzyme activity, and secretes cellulase with very high cellulose degrading activity. The method can adapt to wide range of reaction conditions and has easy preparation process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for: (1)separating and identifying the strain capable of secreting cellulase enzyme; (2)extracting and purifying the produced cellulase enzyme comprising (a) inoculating the strain into a fermentation culture medium for enzyme production, and fermenting at 30-40 degrees C for 3-5 days to obtain the fermented liquid, where the fermentation culture medium comprises sodium carboxymethyl cellulose, yeast extract, sodium chloride, magnesium sulfate heptahydrate, and dipotassium hydrogen phosphate, and (b) purifying and extracting cellulase by centrifuging the fermented liquid to obtain the supernatant, precipitating supernatant by ethanol precipitation method, and purifying supernatant by Sephadex G-75 (RTM: Cross-linked dextran gel) chromatography to obtain the purified cellulase; (3)cellulase, extracted and purified by the above mentioned method; and (4)use of cellulase for efficient degradation of cellulose-rich biomass.
NOVELTY - The method involves removing (S1) metal debris from a wooden chip. The wooden chip is dried (S2). The small elements equipped in wooden chip are grinded (S4). The dust generated in the small elements is absorbed (S5) using a bag filter. A binder is flowed (S6) into conditioner of barrel through transfer pipe. The pellet is cooled (S8). The cooled pellet is discharged (S9) through oscillating sorting apparatus. The fixed quantity of discharged pellet is packed (S10).    USE - Method for manufacturing pellet fuel from sawdust.    ADVANTAGE - The usage of the pellet is improved by supplying pellet necessary for the pellet fuel manufacturing process, and the economic resin feasibility is enhanced. The moisture included in the wooden chip is removed effectively, and the production cost of the pellet fuel is reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the manufacturing process of the pellet. (Drawing includes non-English language text)    Step for removing metal debris from pellet raw material (S1)    Step for drying pellet raw material (S2)    Step for grinding small elements equipped in pellet raw material (S4)    Step for absorbing dust generated in small elements (S5)    Step for flowing binder into conditioner of barrel through transfer pipe (S6)    Step for cooling pellet (S8)    Step for discharging pellet through oscillating sorting apparatus (S9)    Step for packing fixed quantity of discharged pellet (S10)
NOVELTY - The purifier has a fuming furnace fixed with a gas engine. Synthetic gas is generated in the fuming furnace, where moisture content is added in the synthetic gas. A cyclone box is fixed in a rear end of the fuming furnace for removing dust in the fuming furnace. The fuming furnace is fixed in a rear end of a condenser that is connected to a rear end of the cyclone box. The condenser collects pyroligneous liquor, the synthetic gas, the dust, and acidic gas. Another cyclone box removes tar droplets. An absorption tower removes moisture mist and the dust of an absorber.    USE - Biomass gasification synthetic gas purifier.    ADVANTAGE - The cyclone box is fixed in the rear end of the fuming furnace so as to remove dust in the fuming furnace, thus improving working stability of the gas engine, reducing pressure loss of the purifier and ensuring stable operation of the purifier.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification synthetic gas refinement method.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a biomass gasification synthetic gas purifier.
NOVELTY - Composite membrane comprise an at least one- layered polymeric support, a separation layer and a transition layer. The separation layer is continuous monomolecular layer of conjugated polymers, where a thickness of the separation layer of the conjugated polymer does not exceed 1 mu m. The transition layer is an interpenetrated layer of macromolecules of the support and the separation layer.    USE - The composite membrane is useful: for separating gas mixtures (claimed) such as removing acid gases from natural gas and biogas, separation of air oxygen and nitrogen, separation of helium from natural gas, removing carbon dioxide from combustion products and others; and as flat compact or asymmetric membranes or in the form of hollow fibers and other membrane configurations.    ADVANTAGE - The composite membrane: separates gas mixtures in an industrial manner; can be prepared in a simple and cost effective manner; and is chemically and mechanically stable for a long time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the composite membrane, comprising treating the surface of the polymer support with a solution of monomer or monomer mixture, where the monomers are adsorbed on the polymer support, and diffusing into surface layers of the support, due to the action of an oxidation agent on the adsorbed monomer, initiation and propagation of polymer chain to yield a dense molecular layer of conjugated polymer through subsequent in situ polymerization, where interpenetration of the support molecules and the conjugated polymer, occurs between the support and the separation layer, and removing the unreacted reaction components by washing.
NOVELTY - Producing biomethane involves: (i) providing an organic liquid biomethane substrate pre-conditioned by microbial fermentation such that at least 40 wt.% of the non-water content exists as dissolved volatile solids, which dissolved volatile solids comprise at least 25 wt.% of any combination of acetate, butyrate, ethanol, formate, lactate and/or propionate; (ii) transferring the liquid substrate into an anaerobic digestion system, followed by (iii) conducting anaerobic digestion of the liquid substrate to produce biomethane.    USE - The method is useful for producing biomethane (claimed).    ADVANTAGE - The bioliquid is, itself, a novel biomethane substrate composition, which permits very rapid conversion to biomethane. By using the method, safe enzymatic liquefaction of unsorted MSW can be achieved without high temperature pre-treatment. The method combines microbial fermentation with enzymatic hydrolysis of MSW as both a rapid biological pretreatment for eventual biomethane production as well as a method of sorting degradable organic components from otherwise unsorted MSW.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an organic liquid biomethane substrate produced by enzymatic hydrolysis and microbial fermentation of pretreated lignocellulosic biomass where at least 40 wt.% of the non-water content exists as dissolved volatile solids, which dissolved volatile solids comprise at least 25 wt.% of any combination of acetate, butyrate, ethanol, formate, lactate and/or propionate.
NOVELTY - Treating a biomass, comprises: inducing a composition comprising biomass and soil particles to be ensiled for a pre-determined period of time; drying the ensiled composition to obtain a pre-determined moisture content; mechanically separating the dried composition into a coarse fraction and a fine fraction; combining separated fractions with predetermined additives containing plant-derived lignocellulosic materials, pelletized feed material, agricultural processing residues, or by-products; and grinding the combined matter into pre-selected size particles.    USE - The method is useful for treating a biomass to produce livestock feed or fuel biomass (all claimed), where the treated biomass is used as cattle feed, feed additives, fuel pellets and for other purposes.    ADVANTAGE - The method is capable of efficiently treating a biomass in an industrial and cost-effective manner. The treated biomass produces highly digestible and palatable animal feed.    DETAILED DESCRIPTION - Treating a biomass, comprises: inducing a composition comprising biomass and soil particles to be ensiled for a pre-determined period of time; drying the ensiled composition to obtain a pre-determined moisture content; mechanically separating the dried composition into a coarse fraction and a fine fraction, while substantially removing soil particles from the composition; combining separated fractions with predetermined additives containing plant-derived lignocellulosic materials, pelletized feed material, agricultural processing residues, or by-products; and grinding the combined matter into pre-selected size particles.
NOVELTY - Distillate mixture comprises: (a) a first component comprising a petroleum distillate and/or distillate range hydrocarbons produced by a Fischer-Tropsch process, where the first component has a low temperature property value; and (b) a second component comprising an at least partially hydrotreated bio-distillate fraction produced from the conversion of biomass at an elevated temperature, where the distillate mixture has a low temperature property value which is lowered as compared to the low temperature property value of the first component.    USE - The distillate mixture is useful for reducing low temperature value of distillate component such as petroleum distillate or distillate range hydrocarbons produced by a Fischer-Tropsch process.    ADVANTAGE - The distillate mixture reduces low temperature value of distillate component in a cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a bio-distillate composition at a boiling of 320-700 degrees F and comprising either at least 40 wt.% of cycloparaffins and less than 5 wt.% of n-paraffins and iso-paraffins, or at least 15 wt.% of 2-ring compounds in which one of the rings is aromatic comprising substituted and non-substituted tetralins and/or substituted and non-substituted indans, where the bio-distillate composition is at least partially hydrotreated.
NOVELTY - Producing linear alkylbenzene product from bio-renewable feedstock comprising mixture of naturally-derived hydrocarbons involves separating the mixture of naturally-derived hydrocarbons into naphtha portion and distillate portion; reforming the naphtha portion to produce reformate product; separating the reformate product using high purity aromatics recovery separation process to produce benzene; separating normal paraffins portion from the distillate portion and dehydrogenating the normal paraffins portion to produce mono-olefins; and reacting the benzene and mono-olefins.    USE - For producing linear alkylbenzene product from bio-renewable feedstock such as coconut oil, babassu oil, castor oil, algae byproduct, beef tallow oil, borage oil, camelina oil, Canola (RTM: oil), choice white grease, coffee oil, corn oil, Cuphea Viscosissima oil, evening primrose oil, fish oil, hemp oil, hepar oil, jatropha oil, Lesquerella Fendleri oil, linseed oil, Moringa Oleifera oil, mustard oil, neem oil, palm oil, perilla seed oil, pongamia seed oil, pennycress seed oil, carinata seed oil, poultry fat, rice bran oil, soybean oil, stillingia oil, sunflower oil, tung oil, yellow grease, and cooking oil, having mixture of naturally-derived hydrocarbons e.g. natural oil (claimed).    ADVANTAGE - The method produces linear alkylbenzene from bio-renewable feedstock i.e. not extracted from earth.
NOVELTY - The device has an upstream device connected with a heat pipe. A heat pipe heat exchange section disk (2) is connected with a dust cleaning device (4). The dust cleaning device is utilized for removing a heat tube heat-exchanging section (1). A water temperature adjusting device (5) is connected with an end of a heat pipe. The heat pipe exchange section disk is connected with a dust removing section (3). Two ends of an ash part are located in a gas flow space. A pipe is inserted to a water heating chamber.    USE - Biomass gasification fuel gas waste heat recycling and purifying device.    ADVANTAGE - The device improves coke oil dirt removing effect and working efficiency. The device is simple in structure and reasonable in design, and has convenient operation, strong practicability and high heat exchange efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biomass gasification fuel gas waste heat recycling and purifying method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of a biomass gasification fuel gas waste heat recycling and purifying device.    Heat tube heat-exchanging section (1)    Heat pipe heat exchange section disk (2)    Dust removing section (3)    Dust cleaning device (4)    Water temperature adjusting device (5)
NOVELTY - This utility model claims a kind of alcohol waste water recycling processing system, comprising a paraffin separation tank inorganic sedimentation tank, the first water tank, a precise filter, a softener, a water tank, a steam pocket, a steam super-heater and coal gas producer, wherein the first water tank is aerated and a flocculating agent, and the second water tank is added into the catalytic oxygen scavenger and corrosion inhibiting agent, and a wax separating groove is connected with paraffin for a separated from the alcohol in the waste water. This utility model is the alcohol waste water recycling treatment system for waste water in the alcohol-containing a harmful substance is fully used, the treating waste water with dual purpose as a raw material source, which not only saves the water source, but also greatly reduces the processing cost of waste water zero discharge.
NOVELTY - The system has a driving control unit (400) that controls fuel cell (300) for producing power source to comply with the impedance power amount. The impedance power amount is made to cut off connection between the KEPCO system and the power source (100). The supply of the power to the impedance loading (200) is controlled independently with the fuel cell. The isolated operation is generated for independently transmitting power source in the impedance loading with the predetermined operator terminal (10).    USE - System for evaluating quality of voltage and power of fuel cell.    ADVANTAGE - The impedance value can be controlled, thus the electricity generated in the fuel cell can be coincided effectively with the electricity consumed in the load. The stable frequency and voltage are supplied to the single phase or three phase section. The power source can be blocked effectively. The generation of injury to the human body caused due to electric shock can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating the process of evaluating quality of voltage and power of fuel cell. (Drawing includes non-English language text)    Operator terminal (10)    Power source (100)    Impedance loading (200)    Fuel cell (300)    Driving control unit (400)
NOVELTY - Manufacture of high purity hydrogen involves supplying fuel gasification of synthetic gas in aqueous gasification catalyst and a carbon dioxide adsorbent into contact simultaneously with the adsorption of carbon dioxide in the synthesis gas, moving adsorbent generated to remove gaseous hydrogen and carbon dioxide in the aqueous catalyst, contacting catalytic gasification of carbon dioxide and water adsorbent regeneration gas with adsorbent to adsorb carbon dioxide and separates the carbon dioxide, and returning adsorbent to the gasification catalyst and carbon dioxide.    USE - Manufacture of high purity hydrogen (claimed).    ADVANTAGE - The high purity hydrogen is efficiently manufactured.    DETAILED DESCRIPTION - Manufacture of high purity hydrogen involves supplying fuel gasification of synthetic gas to the fluidized state in the aqueous gasification catalyst and a carbon dioxide adsorbent into contact simultaneously with the adsorption of carbon dioxide in the synthesis gas, absorbing carbon dioxide under partial pressure of hydrogen produced to facilitate a reduction, moving adsorbent generated to remove gaseous hydrogen and carbon dioxide in the aqueous catalyst, contacting catalytic gasification of carbon dioxide and water adsorbent regeneration gas with adsorbent to adsorb carbon dioxide and separates the carbon dioxide, and returning adsorbent to the gasification catalyst and carbon dioxide.
NOVELTY - The process tank (1) has an open frame (10) which extends around a bladder receiving space. Several vertically extending columns are formed in multiple mutually detachably connected standards, and are connected with each other by the horizontally extending girders at different girder height levels. A flexible wall of the bladder (50) in a circumferential direction tangential with respect to the central axis of bladder receiving space is enclosed by the inner side of a liner (30), and the outer side of the liner is abutted against the open frame.    USE - Industrial process tank used as storage tank for storing manure or chemical and fermentation vat for processing sludge in water treatment plant, for use in permanent and semi-permanent industrial process installations.    ADVANTAGE - The process tank can be manufactured at lower cost. The assembly and disassembly of process tank can be performed in simple manner. The process tank can be simply and rapidly erected, without utilization of external auxiliary scaffolding.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) an assembly of process tank; and    (2) a method for erecting process tank.    DESCRIPTION OF DRAWING(S) - The drawings show the perspective and schematic views of the process tank.    Process tank (1)    Open frame (10)    Coupling (22)    Liner (30)    Bladder (50)
NOVELTY - The apparatus has a discharge pipe (28) that is arranged in down stream end of a liner (10) which receives transfer screws (22,42) inside an inner container (11). A separator plate (14) is arranged between the inner container and an outer container (12) which are arranged on a concentric horizontal shaft. A modulation leg is placed in bottom surface of a cooling dome (40) and is provided with a shock absorber which relieves the vibration generated in the liner. The cooling dome is provided with an exhaust die (48) which exhausts the fuel generated in down stream end of the liner.    USE - Horizontal continuous carbonizing machine for processing bulk forest residue.    ADVANTAGE - The fuel of the desired form can be consecutively generated after performing thermal decomposition process, while horizontally smoothly transferring the bulk forest residue. The weight and cost of the horizontal continuous carbonizing machine can be reduced. The energy consumption of the horizontal continuous carbonizing machine can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the horizontal continuous carbonizing machine.    Liner (10)    Inner container (11)    Outer container (12)    Separator plate (14)    Transfer screws (22,42)    Discharge pipe (28)    Cooling dome (40)    Exhaust die (48)
NOVELTY - The device has a simple truck (1) which is provided with zinc-plated steel grid (2) and a zinc-plated steel grizzly screen that is connected with a disc (3) made of stainless steel. The stainless steel disc is connected with the stainless steel disc which is connected with a wheel (4) connected with a track (5). A motor (6) is connected with the wheel and an electric control cabinet which is electrically connected with an electric roller shutter door (7). The electric roller shutter door is electrically connected with the motor and is provided with a melting chamber (8).    USE - Device for melting bio-diesel oil from kitchen waste garbage, used in food waste treatment.    ADVANTAGE - The continuous melting process can be achieved. The simplified structure can be achieved. The pollution can be avoided. The device can be used efficiently. The melting efficiency of the bio-diesel oil can be improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for melting method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the bio-diesel oil melting device.    Simple truck (1)    Zinc-plated steel grid (2)    Stainless steel disc (3)    Wheel (4)    Track (5)    Motor (6)    Electric roller shutter door (7)    Melting chamber (8)
NOVELTY - A surface coal bed methane biological conversion process involves putting coal (6) into the container, adding methane microorganism aqueous solution and/or methane microorganism nutrient solution, converting the volatile component into methane gas, and collecting the methane gas. The container is a conversion kettle (1) is formed by the upper cover, the lower bottom and four sides of the wall. The kettle is provided with a gas collection pipe.    USE - As surface coal bed methane biological conversion process (claimed).    ADVANTAGE - The surface coal bed methane biological conversion process is convenient, controllable and fast; improves the utilization rate of the coal; greatly reduces the coal pollution to the environment; and has low cost.    DESCRIPTION OF DRAWING(S) - The figure shows a main view of the surface coal bed methane biological conversion process.    Conversion kettle (1)    Kettle wall (2)    Kettle cover (3)    Opening (4)    Bottom (5)    Coal (6)
NOVELTY - This utility model claims a kind of biological diesel oil methyl esterification producing enamel sleeve tube, comprising an upper joint (1) and the lower opening (4), the upper part is provided with a inlet and outlet branch pipe on the upper part of the sleeve (2), is provided with a lower inlet and outlet branch pipe in the sleeve (3) at the lower part. Wherein a is a biological diesel oil methyl esterification producing enamel sleeve, it can make the material in the sleeve is released so as to produce cyclic reaction, so as to improve product.
NOVELTY - The method involves adding inoculation sludge and alcohol waste water into an anaerobic acid-denitrifying composite unit (1), so as to degrade organic matter in anaerobic fermentation system waste water. The waste water obtained from the anaerobic acid-denitrifying composite unit is added into an anaerobic methane production unit, so as to generate methane gas as energy source. The waste water from anaerobic methane production unit is transformed into an aerobic reaction unit for performing nitrification process according to specific dissolved chemical oxygen demand ratio.    USE - Method for performing biological denitrification of alcohol waste water in carbon source.    ADVANTAGE - The efficiency of the alcohol waste water biological denitrification process can be improved at low energy consumption and at low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the alcohol waste water biological denitrification process.    Anaerobic acid-denitrifying composite unit (1)    Methane production unit (2)    Gas treatment system (3)    Gas collecting device (4)    Aerobic reaction unit (5)
NOVELTY - The device has a primary-level aerobic tank (3) and secondary anaerobic pool (2) that are alternately connected in series. The anaerobic pool and aerobic tank are provided with an aeration device (4). The bottom portion of the anaerobic tank is connected with a gas circulating pump (6) through the gas pipeline (8). One end of the water inlet (1) is connected with a water pump (7), and the other end is connected with the primary level anaerobic tank. The water outlet (5) is provided on the aerobic tank.    USE - Multi-level rural sewage anaerobic-aerobic combined nitrogen and phosphorus removal device.    ADVANTAGE - The nitrogen phosphorus substance can be removed. The rural existing condition can be fully utilized to avoid secondary pollution of methane. The device is environment-friendly. The popularization and use of the device is improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for multi-level rural sewage anaerobic-aerobic combined nitrogen and phosphorus removal method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-level rural sewage anaerobic-aerobic combined nitrogen and phosphorus removal device.    Water inlet (1)    Secondary anaerobic pool (2)    Primary-level aerobic tank (3)    Aeration device (4)    Water outlet (5)    Gas circulating pump (6)    Water pump (7)    Gas pipeline (8)
NOVELTY - The device has a main portion that is provided with conveying device (2), sludge low temperature hot tempering device (5), sludge anaerobic digestion device (10), sludge storage heat exchange device (8), heat exchanging device (7), draught fan (15), waste gas processing device (18), mechanical dewatering device and steam boiler. A pyrolysis vertical reaction kettle is provided with a stirrer. The anaerobic digestion reaction device is provided with sequencing batch continuous stirring anaerobic digestion reactor.    USE - Hot tempering biogas treatment device.    ADVANTAGE - The device obtains effective energy-recycling sludge treatment and saves energy.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hot tempering biogas treatment method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the hot tempering biogas treatment device.    Conveying device (2)    Sludge low temperature hot tempering device (5)    Heat exchanging device (7)    Sludge storage heat exchange device (8)    Sludge anaerobic digestion device (10)    Draught fan (15)    Waste gas processing device (18)
NOVELTY - The furnace has carbonizing furnace (1) which is connected with a combustion chamber (2) whose end portion is extended into carbonization furnace, while other end portion is connected with filling channel (4). The combustion chamber is connected with a chimney (11). The combustion chamber is provided at the lower portion of a flue gas recycling pipe (7) that is connected with a flue gas pipe through a valve (3). A secondary air inlet pipe (6) is connected with an air inlet pipe (14) that is connected with a carbonizing furnace through a valve.    USE - Flue gas heat recycling type biomass carbonizing furnace used for processing agriculture and forestry waste.    ADVANTAGE - The biomass carbonizing furnace can be operated efficiently, as the adaptability of the biomass carbonizing furnace is strong. The raw material used in biomass carbonizing furnace is cheap. The transportation and processing cost of the biomass carbonizing furnace is low. The pollution to the environment can be reduced effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the flue gas heat recycling type biomass carbonizing furnace.    Carbonizing furnace (1)    Combustion chamber (2)    Valve (3)    Filling channel (4)    Secondary air inlet pipe (6)    Flue gas recycling pipe (7)    Chimney (11)    Air inlet pipe (14)
NOVELTY - The pyrolysis reactor has a hollow cylinder (2) that is fixedly connected with a vibrating box (1). One end of a spring (14) is fixed on a bottom of a vibrating case. A vibrating motor (15) is installed in a space area of the vibrating case. A rotating shaft of the vibrating motor is connected with the vibrating box. An induction heating device is wound with an induction coil to heat the hollow cylinder in a circumferential direction.    USE - Biomass spiral vibrating electromagnetic induction pyrolysis reactor.    ADVANTAGE - The strong universality and high efficiency of the pyrolysis reactor can be realized, the pyrolysis process can be performed stably, and the reliability of the pyrolysis reactor can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass spiral vibrating electromagnetic induction pyrolysis reactor.    Vibrating box (1)    Hollow cylinder (2)    Power supply cabinet (11)    Spring (14)    Vibrating motor (15)
NOVELTY - Cotton straw is dried, crushed, and sodium hydroxide solution is added and processed for 15-75 minutes under pressure of 30-130 kPa. Thus, cotton straw is treated under high pressure.    USE - Method of treating cotton straw at high pressure (claimed).    ADVANTAGE - The method efficiently treats cotton straw at high pressure with excellent recyclability, by simple method.
NOVELTY - The method involves disinfecting and deodorizing the garbage conveyed by garbage conveying mechanism (1). The plastic in garbage is blown into cage by a fan (20) of bag breaking machine for recycling. The garbage bag is conveyed to rolling sieve (3) through connecting passage, and is crushed to grain size by knife-type crusher (4). The crushed garbage mixed with clay, lime and raw coal with a stirrer (9) is conveyed to extrusion molding machine (10). The molded coal is conveyed to coal burning boiler (12) and the coal is combusted to drive a generator (13) to generate electricity.    USE - Method for generating power using coal added with domestic garbage.    ADVANTAGE - The pollution produced during the generation of power can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram illustrating the process for generating power using coal added with domestic garbage.    Garbage conveying mechanism (1)    Rolling sieve (3)    Knife-type crusher (4)    Stirrer (9)    Extrusion molding machine (10)    Coal burning boiler (12)    Generator (13)    Fan (20)
NOVELTY - The furnace has a furnace body provided with a movable fire grate and a feed inlet. An upper part of the furnace body is provided with a furnace opening and extending through a pit smoke gasification combustion chamber. A furnace mouth is fixed with a biomass fuel storage box. A lower end of the biomass fuel storage box is fixed with the movable fire grate. The biomass fuel storage box is provided with a jacket. The jacket is fixed with a water replenishing port and an adjustable air inlet. An inner layer is sleeved with the biomass fuel storage box that is provided with multiple air holes.    USE - Multi-purpose firewood and coal saving furnace for use by a farmer for cooking and heating water.    ADVANTAGE - The furnace produces less black smoke during cooking and greatly reduces fuel consumption. The furnace has high heat efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a multi-purpose firewood and coal saving furnace.'(Drawing includes non-English language text)'
NOVELTY - The detector has a controller, an air sensor, an alarm and a 3G module that are respectively connected with a gas sensor. The alarm, 3G module and controller are connected with an exhaust device. The gas sensor is provided with a carbon monoxide sensor, a carbon dioxide sensor, a methane sensor, a sulfureted hydrogen sensor, a formaldehyde sensor and a hydrogen sensor.    USE - Household gas detector.    ADVANTAGE - The alarm automatically alarms, when the gas sensor detects the harmful gas. Hence the remote notification is provided through 3G module, if the host is not present at home.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram f the household gas detector. (Drawing includes non-English language text)
NOVELTY - A biomass conversion process involves hydrothermally liquefying (HTL) a biomass-containing feedstock in aqueous medium at temperature and pressure to form biomass conversion product comprising bio-oil fraction and aqueous fraction containing residual organics remaining after conversion of biomass-containing feedstock, each fraction separable from other fraction; and catalytically hydrothermally gasifying (CHG) the residual organics in aqueous fraction over a selected catalyst at temperature and pressure to form product gas containing medium- British thermal unit (BTU) gas.    USE - For conversion of biomass into product gas containing medium-British thermal unit gas (claimed) which is directly useful for process heating or to provide energy.    ADVANTAGE - The process of generation of bio-based fuels and residual organics suitable for generation of energy-producing hydrocarbon-containing product gases that together maximizes efficiency of biomass conversion in hydrothermal and gasification facilities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a system for conversion of a biomass comprising HTL stage that hydrothermally liquefies a selected biomass in an aqueous medium at temperature and pressure to form conversion product comprising separable bio-oil and an aqueous fraction containing residual organics; and CHG stage operatively coupled to the HTL stage configured to receive the aqueous fraction containing residual organics from the HTL stage that at temperature and pressure forms a product gas containing at least one medium BTU product gas.
NOVELTY - Producing biofuels and food co-products from fermentable plant biomass, which, as a result of adding extracts of microalgae cultures, comprises: (a) preparing an aqueous medium containing the biomass; (b) hydrolyzing and fermenting, simultaneously or sequentially, the biomass comprised in the aqueous medium of step (a); and (c) distilling the products obtained in step (b) for food and biofuel co-products.    USE - The method is useful for producing biofuels and food co-products from fermentable plant biomass, which, as a result of adding extracts of microalgae cultures. The food co-product is useful for preparing food product, food, and feed (all claimed).    ADVANTAGE - The method can optimize the production of the biofuel in terms of time and output, and can improve the protein composition of its co-products that are useful in the food industry, compared to similar methods for producing biofuels and co-products that do not use extracts of microalgae cultures.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are:    (1) food co-product obtainable by the method; and    (2) food product comprising the food co-product.
NOVELTY - The system (1) has anaerobic tank (23) which is provided for removing nitrogen from liquid mixture of object water and activated sludge. A nitrate-nitrogen sensor (92) is configured to measure the nitrate nitrogen concentration in liquid mixture. A control apparatus (7) is configured to determine whether supply amount of organic substance by feed pump (63) is changed based on the measured value of nitrate-nitrogen sensor for fixed time interval. The feed pump is operated, so that the amount of organic substance supplied is changed by predetermined amount.    USE - Water treatment system e.g. reclaimed-water manufacturing apparatus for processing object water containing pollutant material such as domestic waste water and sewage.    ADVANTAGE - The amount of organic substance supplied is changed by predetermined amount, so that the variation of the density of the ammonia nitrogen in aerobic tank can be suppressed. The measured value is low by low-pass filter, so that the control precision of the water treatment system can be improved. The adhesion of the sludge to nitrate-nitrogen sensor can be suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water treatment system.    Water treatment system (1)    Control apparatus (7)    Anaerobic tank (23)    Feed pump (63)    Nitrate-nitrogen sensor (92)
NOVELTY - An alcohol is mixed with a catalyst to prepare a catalyst-containing raw material fluid. The obtained catalyst-containing raw material fluid is mixed with oil or a fat to prepare a mixed solution. The mixed solution is subjected to microwave irradiation to synthesize a fatty acid ester. The fatty acid ester is an ester of the alcohol with a fatty acid containing the oil or fat. The fuel synthesizing process is enabled.    USE - Synthesis of fuel e.g. biodiesel fuel used for diesel engine.    ADVANTAGE - The method enables efficient synthesis of fuel with increased contact area between raw material(s) and concentrating a catalyst in the neighborhood of the interface.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel synthesizing apparatus, which has mixing portion to mix the catalyst-containing raw material fluid with fats and oils including alcohol and a catalyst, and produces the mixed solution, and the microwave exposure portion (100) which irradiates a microwave to the mixed solution. The microwave exposure portion has a function which synthesizes the fatty acid ester.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of synthesis of fuel.    Microwave exposure portion (100)    Mixer (101)    Reaction tube (102)    Stub tuner (103)    Movable short circuit board (104)
NOVELTY - Insect pest controlling agent comprises 1-chloro-3,3,3-trifluoropropene as active ingredient.    USE - The agent in form of aerosol is useful for controlling insect pest (all claimed), e.g. vermin and Blatta.    ADVANTAGE - The agent enables to stop the movement and kill the insect pest rapidly, is highly safe as it is free of risk of explosion or ignition, and has low global warming coefficient.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method for controlling insect pest involves preparing the above-mentioned agent and applying the prepared agent to the insect pest for stopping the movement or killing the pest; and    (2) device for stopping movement and killing pest comprises (a) container comprising above-mentioned agent containing 1-chloro-3,3,3-trifluoropropene as active ingredient and at least one pesticide, and (b) insect pest attached to the container for applying the insect pest controlling agent to insect pest which is made incompetent.
NOVELTY - Processing of biomass involves pretreating biomass under predetermined conditions to obtain chemical reaction product, and separating obtained product during or after biomass pretreatment into gaseous specific product, and liquid or solid-state other product.    USE - Processing of biomass used for manufacture of xylose, furfural, acetic acid, formic acid, levulinic acid and 5-hydroxy methyl furfural (all claimed).    ADVANTAGE - The high-purity xylose, furfural, acetic acid, formic acid, levulinic acid and 5-hydroxy methyl furfural are manufactured by processing the biomass.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of xylose;    (2) manufacture of specific byproduct;    (3) separation apparatus; and    (4) specific byproduct, which comprises furfural, acetic acid, formic acid, levulinic acid and 5-hydroxy methyl furfural.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the manufacture of xylose by processing biomass.
NOVELTY - Method for treating non-human animal infested with biting lice involves administering neonicotinoid internally to the animal such that the neonicotinoid is present systemically within the animal.    USE - The method is useful for treating non-human animal infested with biting lice. The non-human animal is sheep (all claimed).    ADVANTAGE - The method enables to treat non-human animal infested with biting lice cost-effectively and environmentally-friendly with less labor intensive.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) applicator designed for internal administration containing a composition to an animal comprising 2-80 weight/volume% neonicotinoid; and    (2) dosage regime to treat biting lice on a non-human animal involves administering a neonicotinoid internally with a dosage of 40 mg/kg or less.
NOVELTY - Biogas is generated from fermented liquor by methane fermentation. Ammonia contained in biogas is removed by supplying the emitted biogas to an impurity-absorption liquid. Ammonia-removed biogas is supplied to fermented liquor from impurity-absorption liquid, and air-dispersed ammonia concentration (mg ammonia/L biogas) is estimated when circulating biogas between fermented liquor and impurity-absorption liquid, by using the pH of fermented liquor.    USE - Estimation of air-dispersed ammonia concentration in biogas for adjusting ammonia concentration in fermented liquor (claimed).    ADVANTAGE - The method enables efficient manufacture of biogas.    DETAILED DESCRIPTION - Biogas is generated from fermented liquor by methane fermentation. Ammonia contained in biogas is removed by supplying the emitted biogas to an impurity-absorption liquid. Ammonia-removed biogas is supplied to fermented liquor from impurity-absorption liquid, and air-dispersed ammonia concentration (mg ammonia/L biogas) is estimated when circulating biogas between fermented liquor and impurity-absorption liquid by using a relationship given by, Ax exp(Bx pH or fermented liquor), where A and B are constants. INDEPENDENT CLAIMS are included for the following:    (1) method to adjust concentration of ammonia in fermented liquor; and    (2) biogas production system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas production system.    Methane fermentation tank (1)    Impurity-absorption tank (2)    Inlet tube (3)    Discharge pipe (4)    Discharge line (5)
NOVELTY - The hydrogen and oxygen generation apparatus (100) has a water-electrolysis apparatus (1) which electrolyzes water and generates hydrogen gas and oxygen gas. The dehumidifier (31,32) is accommodated with which the adsorption agent adsorbs moisture content. The measurement mechanism (6) is provided for calculating the quantity and temperature of the to-be-processed gas which are generated by the water-electrolysis apparatus. The dehumidifier is provided for supplying to-be-processed gas, and is implemented based on the result calculated by the measurement mechanism.    USE - Apparatus for generating hydrogen and oxygen.    ADVANTAGE - The fully dried hydrogen gas and oxygen gas can be obtained. The moisture content eliminated with dehumidifier can be grasped comparatively precisely. The productive efficiency of dry hydrogen and dry oxygen can be improved. The falling into the situation where heating of adsorption agent formed succeedingly is suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen and oxygen production method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen and oxygen generation apparatus. (Drawing includes non-English language text)    Water-electrolysis apparatus (1)    Pure water storage tank (2)    Measurement mechanism (6)    Dehumidifiers (31,32)    Hydrogen and oxygen generation apparatus (100)
NOVELTY - The hydrogen oxygen generator (1) has the hydrogen gas distribution channel that is formed, such that the hydrogen gas and water generated are distributed within the water electrolysis cell. The water-electrolysis module (10) generates hydrogen gas in the cathode side of the water electrolysis cell and generates oxygen gas by electrolyzing water in an anode side. The hydrogen gas distribution channel is comprised, such that a gas purge is carried out with hydrogen gas for a purge at the time of the stop of electrolysis of the hydrogen gas distribution channel.    USE - Hydrogen oxygen generator.    ADVANTAGE - The generated hydrogen and oxygen gas can be obtained with comparatively high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an method for operating hydrogen oxygen generator.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen oxygen generator.    Hydrogen oxygen generator (1)    Water-electrolysis module (10)    Hydrogen gas transfer pipe (20)    Dehumidifier (22)    Oxygen gas transfer pipe (30)
NOVELTY - The hydrogen oxygen manufacturing method involves transferring the hydrogen gas or oxygen gas generated by the water electrolysis cell to a to-be-supplied location using a transfer path (41). The pressure of the gas within the transfer path is measured using the pressure measuring apparatus. The pressure measuring apparatus is implemented to make the transfer path into a pressurized state, and to measure the pressure sequentially.    USE - Method for manufacturing hydrogen and oxygen gas.    ADVANTAGE - The state of the transfer path can be grasped to which hydrogen gas or oxygen gas leak from the transfer path which transfers hydrogen gas or oxygen gas generated by the water electrolysis cell.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a hydrogen oxygen manufacturing apparatus.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the hydrogen oxygen manufacturing apparatus.    Hydrogen oxygen manufacturing apparatus (1)    Water-electrolysis module (10)    Hydrogen gas transfer pipe (20)    Oxygen gas transfer pipe (30)    Transfer path (41)
NOVELTY - Medical device comprises a set of particles of titanium oxide, where at least a substantial amount of the particles are of micrometer-millimeter size, and at least 10 wt.% of the titanium oxide is in the amorphous form.    USE - The medical device is useful for the treatment of a wound, preferably a chronic wound (all claimed) and controlling infectious diseases, preferably bacterial diseases, where the medical device is a wound dressing. No biological data given.    ADVANTAGE - The medical device achieves increased antibacterial effect, and is eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for use of the set of particles of titanium oxide for the treatment of a chronic wound by achieving an absorbing effect in the wound.
NOVELTY - The apparatus (100) has a gas detection element (10), at which resistance value changes according to gas concentration. A resistor (20) is connected in series with gas detection element. A switch element (30) is connected in series with resistor. A control-signal output unit (40) outputs pulse signal which controls switching state of switch element. A capacitor (50) is arranged between near terminal and grounding potential at which electric current in resistor is flowed in. An output terminal (60) outputs terminal voltage of capacitor as a detection result according to gas concentration.    USE - Apparatus for controlling electricity supply of gas detection element used for detecting concentration of to-be-detected gas such as methane gas, liquefied petroleum gas, hydrogen, carbon monoxide, hydrogen sulfide, chlorofluocarbon, ammonia, poisonous gas and other combustible gas.    ADVANTAGE - Since the electric current flowing into resistor according to pulse signal can be limited, the apparent resistance value of resistor can be made larger than original resistance value. Since the resistance ratio can be made regular, the misdetection can be prevented. The appropriate electricity can be supplied to gas detection element without changing resistor, even when the resistance value of gas detection element is varied.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the apparatus for controlling electricity supply of gas detection element. (Drawing includes non-English language text)    Gas detection element (10)    Resistor (20)    Switch element (30)    Control-signal output unit (40)    Capacitor (50)    Output terminal (60)    Electricity supply control apparatus (100)
NOVELTY - The apparatus i.e. fuel cell system (1), has an accommodating part (20) accommodating a working fluid. A detection part i.e. surface acoustic wave solution sensor (35), converts a change in physical properties of the working fluid into an electric signal. A calculation part i.e. dielectric constant calculation part (55), calculates a physical-property value of the fluid from the electric signal. An adjustment part (65) adjusts the physical-property value of a reference fluid when the reference fluid is supplied to the detection part.    USE - Processing apparatus i.e. fuel cell system.    ADVANTAGE - The detection part can be calibrated in an effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a calibration method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a fuel cell system. '(Drawing includes non-English language text)'    Fuel cell system (1)    Accommodating part (20)    Surface acoustic wave solution sensor (35)    Dielectric constant calculation part (55)    Adjustment part (65)
NOVELTY - Manufacture of support material involves producing the sheet (A) containing an organic binder and composite fine particles (22) obtained by arranging an ion-conductive oxide (21) (a) on circumference of a metal oxide (20) having electroconductivity, producing sheet (B) containing ion-conductive oxide (b) and an organic binder, producing a sheet laminated material by installing the sheet (B) on sheet (A) and baking the sheet laminated material at 1000-1500 degrees C.    USE - Manufacture of support material used for solid oxide fuel cell.    ADVANTAGE - The method enables manufacture of support material with reduced curvature, generation of crack and contraction-shrinkage percentage difference. The solid oxide fuel cell containing support material has high output.    DESCRIPTION OF DRAWING(S) - The drawing shows schematic view of manufacture of solid oxide fuel cell support material by spray pyrolysis synthesis method.    Substrate (17)    Mixture (19)    Metal oxide (20)    Ion-conductive oxide (21)    Composite fine particles (22)
NOVELTY - Manufacture of porous electrode substrate involves manufacturing carbon short fiber, carbon-precursor fiber and precursor sheet obtained by dispersing carbon powder, and carrying carbonization process where weight decreasing rate of the precursor sheet is 65% or less.    USE - Manufacture of porous electrode substrate is used for fuel cell.    ADVANTAGE - The method enables economical manufacture of porous electrode having excellent thickness precision, gas air permeability, handability, and electroconductivity.
NOVELTY - The arrangement (10) has two pipes (14,16) connected at lower circumferential edge with two base plates (22,24) on which two interfacial layers (26,28) over pipes. Two copper layers (34,36) are formed on circumferential surfaces of pipes. Two electrolysis spaces (I,II) are formed between seal plates and interfacial layers. The gas separators (46,48) in electrolyzer (20) between pipes are used to lead out gases e.g. hydrogen and oxygen. An aperture (58) is formed between electrolysis spaces to completely receive isolating fluid (60) from electrolyzer in a pressure tank (12).    USE - Electrolyzer arrangement for creating hydrogen and oxygen from electrochemical decomposition electrolytes of water.    ADVANTAGE - The electrolyzer arrangement is simple and inexpensive in construction. The hydrogen and oxygen creation efficiency of the electrolyzer arrangement can be improved effectively by effectively increasing the pressure in the pressure tank.    DESCRIPTION OF DRAWING(S) - The drawings show the partial sectional and cross-sectional views of the electrolyzer arrangement.    Electrolyzer arrangement (10)    Pressure tank (12)    Pipes (14,16)    Electrolyzer (20)    Base plates (22,24)    Interfacial layers (26,28)    Copper layers (34,36)    Gas separators (46,48)    Aperture (58)    Fluid (60)    Electrolysis spaces (I,II)
NOVELTY - Preparing a transportation fuel comprises (a) producing a naturally occurring aqueous fluid containing greater than 1 wt.% of soluble carboxylic acids, (b) isolating at least a portion of the organic acids from the naturally occurring aqueous fluid, and (c) upgrading the isolated carboxylic acids.    USE - The process is useful for preparing a transportation fuel or a biofuel including middle distillate, a diesel fuel, a heating oil, a jet fuel, a kerosene, an aviation gasoline, a gasoline fuel or a lubricant base oil (all claimed).    ADVANTAGE - The process provides transportation fuel with high quality and improved solubility, chemical and physical properties and chemical stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing a biofuel comprising the steps (a) and (b) as above per se, blending the organic acids with biofuel to provide a blend, upgrading the blend, and providing a biofuel product.
NOVELTY - Producing a pelletized fuel product, comprises pelletizing at least partially carbonized biomass in an inert atmosphere.    USE - The methods are useful for producing a pelletized fuel product and pelletized carbonized fuel product (claimed).    ADVANTAGE - The methods provide uniform pelletized fuel products with increased energy value and improved combustion properties. The pelletized fuel products are ease to handle and store.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method for producing a pelletized carbonized fuel product, comprising at least partially carbonizing a biomass feed to produce at least partially carbonized biomass, and pelletizing the at least partially carbonized biomass in an inert atmosphere to produce a pelletized carbonized fuel product;    (2) an apparatus (10) for producing the pelletized fuel product, comprising a feeder (12) of at least partially carbonized biomass, a pelletizer (14) configured to receive and pelletize the carbonized biomass, and an inert gas source (16) configured to provide inert gas to the pelletizer; and    (3) an apparatus for producing a pelletized carbonized fuel product, comprising a feeder of raw biomass, a reactor configured to receive and at least partially carbonize the raw biomass, a pelletizer configured to receive and pelletize the at least partially carbonized biomass, and an inert gas source configured to provide inert gas to the pelletizer.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of an apparatus for producing a pelletized fuel product.    Apparatus (10)    Feeder (12)    Pelletizer (14)    Inert gas source (16)    Pelletizing chamber. (22)
NOVELTY - Chemically-modified mixed fuel comprises methane gas from at least two methane-production sources.    USE - The chemically-modified mixed fuel is useful in Kellogg primary reformer.    ADVANTAGE - The chemically-modified mixed fuel is: cost-efficient; renewable and/or a consistent resource; easy to use; easy to transport; and relatively clean with respect to the amount of time/resources it requires to convert the fuel to a usable form.
NOVELTY - Converting biomass comprises (a) providing a thermal reactor comprising at least one auger, and a first mixture comprising a heat carrier and at least one catalyst, (b) introducing a feedstock comprising biomass to the thermal reactor and contacting with the first mixture to produce a second mixture, where at least a portion of the feedstock is converted to condensable vapor intermediates via pyrolysis, and (c) conveying the second mixture through the reactor for a defined residence time prior to removal from the reactor.    USE - The biomass is useful as a feedstock for production of biofuels such as gasoline, diesel, oils and other products that can substitute for fuel products produced from non-renewable fossil fuels.    ADVANTAGE - The biomass is capable of economically converting biomass to biofuels with increased throughput without requiring maintenance of process equipment.    DETAILED DESCRIPTION - Converting biomass comprises (a) providing a thermal reactor comprising at least one auger, and a first mixture comprising a heat carrier and at least one catalyst, (b) introducing a feedstock comprising biomass to the thermal reactor and contacting with the first mixture to produce a second mixture, where at least a portion of the feedstock is converted to condensable vapor intermediates via pyrolysis, the catalyst facilitates the rate at which the feedstock is converted, and rotation of the auger increases heat transfer from the heat carrier to the feedstock and increases contact between the feedstock and the first mixture, and (c) conveying the second mixture through the reactor for a defined residence time prior to removal from the reactor.
NOVELTY - Method for preparing a mono-unsaturated alkene, involves contacting an aliphatic mono-unsaturated carboxylic acid with a ferulic acid decarboxylase 1 (Fdc1) polypeptide comprising an amino acid sequence exhibiting at least 21% sequence identity to a 503 amino acid sequence (SEQ ID NO: 1) fully defined in the specification, and a phenylacrylic acid decarboxylase 1 (Pad1) polypeptide comprising an amino acid sequence exhibiting at least at least 17% sequence identity to a 242 amino acid sequence (SEQ ID NO: 2) fully defined in the specification.    USE - The method is useful for preparing mono-unsaturated alkene preferably 4-30C alkene including terminal alkene and straight or branched chain alkene used for producing alkane which is used for generating biofuels and/or biochemicals (all claimed).    ADVANTAGE - The method enables improved production of alkenes.
NOVELTY - Refining natural oil comprises: providing feedstock comprising natural oil; reacting feedstock in presence of metathesis catalyst to form metathesized product comprising olefins and esters; providing dehydrogenation suppression agent in mixture with feedstock and/or the product; passivating metal-containing material with the agent; separating olefins in the metathesized product from esters in the metathesized product; and transesterifying esters in presence of an alcohol to form transesterified product and/or hydrogenating olefins to form fully or partially saturated hydrogenated product.    USE - The method is useful for refining natural oil and for producing fuel composition.    ADVANTAGE - The butenes are employed as low-molecular-weight olefin, offering a low cost, commercially available feedstock.    DETAILED DESCRIPTION - Refining a natural oil comprises: providing a feedstock comprising a natural oil; reacting the feedstock in the presence of a metathesis catalyst to form a metathesized product comprising olefins and esters; providing a dehydrogenation suppression agent in mixture with the feedstock and/or the metathesized product; passivating a metal-containing material with the dehydrogenation suppression agent; separating the olefins in the metathesized product from the esters in the metathesized product; and transesterifying the esters in the presence of an alcohol to form a transesterified product and/or hydrogenating the olefins to form a fully or partially saturated hydrogenated product. The metal-containing material comprises residual metathesis catalyst and/or hydrogen transfer agent and non-passivated metal-containing material is configured to participate catalyze, promote, and/or facilitate dehydrogenation of the natural oil and/or the metathesized product.
NOVELTY - The method involves producing a fuel cell, which laminates an electric power generation body material containing a membrane electrode assembly. The cell laminated body, which laminates the cell in a set of numbers, is fastened in a direction of lamination by fastening pressure. A specified pressure more than fastening pressure is applied to direction of the laminated body at an end surface of the direction of laminated body in a metallic foam body. A deviation thing (dst), which deviates from the metallic foam body, is removed by the application with specific pressure.    USE - Method for manufacturing a fuel cell.    ADVANTAGE - The deviation thing, which deviates from the metallic foam body is removed by the application of the specified pressure, so that scattering of a deviation thing is suppressed and the deviation thing is removed safely, thus preventing damage to the electric power generation body material by the deviation thing.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating phenomenon which has arisen in a metallic foam body layer at the time of a pressure application process. '(Drawing includes non-English language text)'    Deviation thing (dst)    Pressure force (Pa)    Metallic foam body layers (51, 52)    Gas diffusion side contact surfaces (51f, 52f)    Highly rigid element (65)
NOVELTY - The device has electrolyte, fuel electrode and air electrode layers (1,2). The electrochemical reaction cell is provided with a structure where the electrolyte layer are pinched between fuel electrode layer and air electrode layer which is electrically connected to a surface of a porous portion with tubular structure. The air electrode layer and conductive layer of an electrochemical reaction cell are connected in series in which fuel electrode layer is formed, such that a gas-seal layer is laminated on a conductive layer.    USE - Multistage electrochemical reaction device such as solid oxide fuel cell, water vapor electrolysis cell, and electrochemical nitrogen oxides decomposition cell.    ADVANTAGE - Since airtight layer can be formed in a corresponding section by sealing material, the fall of open-circuit voltage is suppressed, and a stable driving is performed. Since the compactness in electrical conduction material is not required, an electrically conductive electrical conduction material can be selected, so that the performance decrement by resistance loss is restrained. The electrochemical reaction cells are electrically connected for the conductive material layer, so that a contact with air is prevented and an oxidative degradation of the conductive material layer is suppressed. The choice of electrical conduction material spreads and application of a low-cost material is attained. An active auxiliary material is directly mixed in fuel electrode material, so that electrode reaction activity of the air electrode and fuel electrode is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of the connection structure. (Drawing includes non-English language text)    Fuel electrode layers, electrolyte layers, and air electrode layers (1,2)
NOVELTY - The invention relates to a process for preparing glycerin acetals and cetals. According to the invention, the process consists of the reaction of glycerin condensation with aldehydes and cetones, wherein glycerin is treated with a heterogenous catalyst consisting of previously calcined mixed sulphated oxides, in a ratio of 1.05...1.5% by weight, in relation to glycerin, afterwards, the aldehyde or cetone is dosed for 5...60 minutes, there is introduced an organic solvent which forms a heterogenous azeotropic mixture with the water, the reaction mass is heated until the azeotropic mixture distillation starts, after 45...240 minutes the reaction is finished, the catalyst is separated by filtration, from the filtrate the solvent and the aldehyde or cetone excess are removed by distillation at atmospheric pressure and under vacuum, there resulting glycerin acetal or cetal which may be used as such or may be purified by vacuum distillation, for being used as additive/component for bio-fuels or petro-chemical classic fuels or as ecological solvent.
NOVELTY - A hydroquinone dialkali metal salt reacts with carbon dioxide in the presence of alkali metal salt of phenol or naphthol in reaction medium to obtain 2,5-dihydroxy terephthalic acid.    USE - Manufacture of 2,5-dihydroxy terephthalic acid. Uses include but are not limited to raw materials for synthetic resins, such as polyester, polyamide, aramid, fluorescence agent, and pharmaceutical intermediate.    ADVANTAGE - The method efficiently and economically provides 2,5-dihydroxy terephthalic acid, with high yield and improved safety at low temperature and pressure. The method is environmentally-friendly. The reaction apparatus damage is suppressed. The reuse of alkali metal salt of phenol or naphthol is enhanced.
NOVELTY - A raw material fat-and-oil containing fatty acid(s) and fatty acid ester(s), and sulfur components is contacted with bromine-type oxidizing agent in liquid phase. The obtained product is washed with polar solvent or adsorption treated with adsorption agent. The washing or adsorption treatment is carried out simultaneously or after the contacting process to obtain de-sulfurized fatty acid or fatty acid ester.    USE - Manufacture of de-sulfurized fatty acid or fatty acid ester used as raw material for manufacture of alcohol (claimed), raw material of function raw materials e.g. surfactant, and biodiesel fuel.    ADVANTAGE - The method efficiently provides fatty acid or fatty acid ester with low content of sulfur component, without carrying out distillation of methyl ester.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of alcohol, which involves performing hydrogenation reaction using catalyst containing metal(s) chosen from group 8, group 9 and group 10 with respect to de-sulfurized fatty acid or fatty acid ester.
NOVELTY - The utility model claims a gasification furnace, especially a kind of a bio-fuel gasifying furnace. It comprises a furnace body, a slag tank, a first adjusting oxygen supply port, a first observation window, a chimney, a tar collecting device, a tar return pipe, air blower and is set the top of the furnace body, the furnace body is mainly composed of a material containing chamber, a combustion chamber and a heat exchange chamber, a slag box is set in the combustion chamber, the first adjustable oxygen supply and the combustion chamber, a first observation window is embedded in the furnace body, the chimney is set on the top of the furnace body, the tar collecting device is set on the chimney inner wall at the bottom of the tar reflux pipe is connected with the containing cavity of the tar collecting device, and the other one end near the combustion chamber is the highest burning point, air blower is connected with the blower and the combustion chamber. It can make the condensed tar collecting and re-burning, so as to reduce the tar to the environment and human health and a grade can control oxygen, observing a design is convenient for the user to completely control the whole combustion intensity.
NOVELTY - Gas separation and storage using carbon nano sheet involves injecting mixed gas having hydrophilicity into carbon nano sheet, saturating and cooling using water generated within water-saturated carbon nano sheet inter-layer.    USE - Gas separation and storage using carbon nano sheet (claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) gas preservation method using carbon nano sheet;    (2) carbon nano sheet gas storage material; and    (3) recovering method of gas.
NOVELTY - Biomass straw solid compact shaping particle fuel compressor relates to the biomass straw fuel producing device. A machine body, the machine body is a square cavity, top part is provided with a main hydraulic compressing cylinder, a main hydraulic compression piston rod of the hydraulic cylinder extends to the machine body, there is a horizontal compression push plate at the top of the machine body, a compression push plate is connected with the main hydraulic compression piston rod of the hydraulic cylinder, a left middle part of the upper side is connected with a set of feeding cylinder, feeding cylinder and the horizontal plane is 32-44 degrees, the lower machine body right side part is provided with a discharging port is provided with a discharging push plate of the left side wall of the machine body inner cavity, a discharging push plate opposite to the discharge hole is provided with a discharging hydraulic cylinder, a discharging hydraulic cylinder piston rod extends to the inner cavity of the machine body of the machine body left side, discharging push plate is connected with a discharging material of the hydraulic cylinder piston rod. This utility model solves the problem that the biomass straw fuel production, the current of the compressor has low production efficiency.
NOVELTY - Domestic garbage microwave non-oxygen continuous carbonization device, relating to the technical field of garbage processing, wherein the device comprises a feeding device, a discharging device, a microwave reactor and a steel belt conveying mechanism, a feeding device and a discharging device are respectively connected with the top of inner cavity and the inner cavity bottom of the microwave reactor, a steel belt conveying mechanism is fixed on the microwave reactor to the lower part, the microwave reactor is provided with a gas outlet, the shell of the microwave reactor is composed of a metal cylinder and a heat insulating material layer, an inner metal cylinder microwave carbonization reactor is multiple. The utility model uses microwave oxygen-free carbonization garbage principle, converting the electric energy into the microwave, a material carbonization reaction in the microwave reactor can be accurately controlled at a temperature at 500 to 900 degrees centigrade of high temperature, the domestic garbage is decomposed, but also will not generate environment harmful dioxin, and fuel carbon product also can be side product generation, changes waste into valuable by the magnetron.
NOVELTY - The utility model claims a household garbage fuel gas generator, in particular to a household garbage resource utilization of household garbage fuel gas generator. Domestic garbage resource utilization of the method is divided into two types, the first type is comprehensive processing is sorting, compost, embedding, and the other one is household garbage burning generating, our country in the city is made of burning power generation in small cities is not the compost so as to directly. Because our country domestic garbage thermal value is low, burning to generate electricity depending raw coal or oil, a device inlet, high cost and development. This utility new type household garbage fuel gas generator is a kind of not adding auxiliary fuel, domestic garbage combustion heat energy generated by the gasification of the environmental protection and resource comprehensive utilization technology, is the development of a totally-enclosed according to our country solid waste component and the thermal value, simple structure, stable operation, low cost and obvious effect.
NOVELTY - In existing technology, this utility new purpose of the utility model is to provide a kind of straw generator material monitoring device, the device comprises a material lifting motor (1), a motor (2), a distributor triangular bracket (3), upper and lower slide member (4), a distributor lifting rail 5, scattering material 6, scraping and pressing material plate, a camera 7, a device console 8. The operating switch 9. The device replacing the manual shifting by the operation of a distributor of the old technique flow method, it overcomes the existing technology in the flue gas, harmful gas and has high temperature, explosion and large labour intensity.
NOVELTY - The utility model claims a granulating machine technology field, especially relates to a kind of hydraulic biomass fuel granulator. The hydraulic biomass fuel granulator, comprising a machine body, a pressing wheel, a bearing seat, a protective plate, a protective plate, a template support frame, a hydraulic station and a main motor, wherein the plate a lower side of the first plate, the first plate are symmetrically provided with two sides of the lower end side of the base plate, two sides of the side of the base is set with blocking plate, a middle plate at two sides are symmetrically provided with bearing press cover, the outer side of a bearing cover are respectively set with a bearing seat and a bearing are respectively equipped with a bearing pressure cover, a bearing seat is provided with a bearing bottom plate. The beneficial effects are as follows: simple structure, reliable use, energy-saving, small floor area, light weight, high efficiency operation error rate is low, stable device stability and reduces the device cost on operation and maintenance, which effectively solves the problem that the traditional biomass fuel granulating machine in the electricity consumption and high stability is bad, the service life of the bearing.
NOVELTY - A core-shell magnetic composite comprises: a magnetic core; a shell containing a protective layer and a porous layer, where the protective layer is coated on a surface of the magnetic core and the porous layer is the outmost layer of the shell; and a hydrophobic functional group grafted to the shell.    USE - As core-shell magnetic composite useful for producing biodiesel (claimed).    ADVANTAGE - The composite combines various kinds of lipases, with improved tolerance to water and methanol contents and is recovered rapidly and reused repeatedly, to advantageously improve the yield and efficiency of related processes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing biodiesel, involving: performing a transesterification at an oil/alcohol molar ratio of 1/14.5 to 1/3 and a water content of 10-47 wt.% using a catalyst, where the catalyst is the core-shell magnetic composite.
NOVELTY - Portable campfire comprises: either sides made of n number of pieces of wood, where n is not defined, each piece has front and back sides, two sides, first and second ends and at least part of both sides of each piece of wood are each adjacent to at least part of one side of another piece of wood, or sides made of many pieces of wood, where each piece has first and second ends and three sides and at least part of two sides of each piece of wood are adjacent to sides of adjacent pieces of wood; and base made of flammable material. The first ends of pieces of wood are attached to base.    USE - Used as a portable campfire.    ADVANTAGE - The portable campfire: provides fire maintaining for up to one and a half hours; is easy to light, and self-contained; is available in a variety of sizes to provide easy transport; avoids the restrictions of areas where there are quarantines on bringing wood out of the area; and reduces the volcano effect.
NOVELTY - Preparation of dronedarone or its salts involves: reacting N-(2-butyl-benzofuran-5-yl)-methane sulfonamide compound with N-(2-butyl-benzofuran-5-yl)-methane sulfonamide compound or its salt, in a Grignard reaction and the obtained product is isolated and optionally converted into its salt.    USE - For preparation of dronedarone (claimed) for the treatment of arrhythmia.    ADVANTAGE - The process prepares dronedarone (I), starting from known and commercially available materials, and by applying simple, environmentally compatible reagents and solvents, to afford high overall yields and good purity of the product.    DETAILED DESCRIPTION - Preparation of dronedarone (I) or its salts involves: reacting N-(2-butyl-benzofuran-5-yl)-methane sulfonamide compound of formula (IV) with N-(2-butyl-benzofuran-5-yl)-methane sulfonamide compound of formula (VI) or its salt, in a Grignard reaction and the obtained product is isolated and optionally converted into its salt.    X=Cl or Br;    R=-NR1R2;    R1 and R2=H, alkyl, alkyloxy or aryl.    INDEPENDENT CLAIMS are included for the following:    (1) new N-(2-butyl-benzofuran-5-yl)-methane sulfonamide compounds (IV) and (VI) and N-(2-butyl-benzofuran-5-yl)-methane sulfonamide compound of formula (III);    (2) preparation of the compounds (VI), (IV) and (III); and    (3) preparation of the compound (I), involving: (a) halogenating the N-(2-butyl-benzofuran-5-yl)-methane sulfonamide (II) to obtain the compound (III); (b) converting the compound (III) obtained in step (a) into the compound (IV); (c) reacting the compound (V) with amine NH-R to obtain the compound (VI); and (d) reacting the compound (IV) with the compound (VI) in a Grignard reaction to obtain dronedarone (I), and the obtained product is isolated and optionally converting into its salt.
NOVELTY - Densification of a material, comprises compressing the material to form a log, while maintaining the log in a compressed state, heating the log to activate a binder, and then cooling the log to set the binder.    USE - The method is useful for densification of a material, which is baled, lignocellulosic biomass material (all claimed).    ADVANTAGE - The densification process reduces energy, storage and transportation costs associated with the utilization of material.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) an apparatus for compacting biomass material, comprising a barrel including a heating section and cooling section (28), a heat source coupled to the heating section, and a piston ram configured for being actuated to compress the material into a first log and push the first log into a second log disposed in one of the heating and cooling sections; and    (2) a system for densifying material comprising a press for compressing the material into logs, and a structure coupled to the press and holding under compression such logs that are received from the press, where the structure includes a heating section and a cooling section for simultaneously activating and setting binder in the logs.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic view of a compactor for densification of a biomass material.    Conveyor (5)    Bale (10)    Compactor barrel (20)    Receiving section (22)    Cooling section. (28)
NOVELTY - Hydrocarbon fuel (2000) is treated with steam, mixture of steam and hydrogen and/or syngas in pre-reformer to convert fuel to syngas, and a portion of sulfur content is removed from the fuel. The obtained syngas is fed into anode inlet of fuel cell system.    USE - Processing of hydrocarbon fuel e.g. saturated hydrocarbons, natural gas, biogas, gasoline, gasified coal, diesel, synthetic fuel, marine fuel and jet fuel used for solid oxide fuel cell assembly (claimed).    ADVANTAGE - The hydrocarbon fuel is economically processed by simple process. The processed fuel provides solid oxide fuel cell assembly with high electrical efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for solid oxide fuel cell assembly.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of solid oxide fuel cell assembly.    Hydrocarbon fuel (2000)    Anode off-gas (2006)    Recycle loop (2008)
NOVELTY - The device has a material transfer column (6) i.e. decarbonator-dehydrator, comprising pressurized water that is slackened at a pressure close to atmosphere in another material transfer column, where the device washes gas at a pressure close to atmospheric pressure in an vertical cooling exchanger e.g. vertical cooler (1) such as desulfurizer, by spraying water from top to bottom against current of ascending gas and at another pressure of 5 atmospheres in the former transfer column by counter current water washing of ascending gas with a cold water at 5 degree Celsius approximately.    USE - Device for washing gas i.e. biogas, from fermentation of agricultural wastes and agro food wastes and from water or household waste treatment station with cold water so as to be injected into a natural gas distribution network.    ADVANTAGE - The device enables washing the bio gas with cold water in an inexpensive manner so as to eliminate major portion of hydrogen sulfide, carbon dioxide and steam.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating circulation of fluids.'(Drawing includes non-English language text)'    Vertical cooler (1)    Level control valve (3)    Compressor (4)    Material transfer column (6)    Downstream pressure control valve (9)
NOVELTY - The device has a vertical cooling exchanger (1) i.e. desulfator, where a first washing process is carried out at pressure slightly higher than an atmospheric pressure in the vertical cooling exchanger by a flow of water distributed uniformly and migrating from top to bottom against flow of ascending gas. A second washing process is carried out at pressure of 5 atmospheres after passage of gas in a compressor in a material transfer column (6) i.e. decarbonator dehydrator, by washing the water against the flow of the ascending gas with cold water of 5 degrees Celsius.    USE - Cold water gas washing device for treatment of biogases output from anaerobic fermentation of livestock or vegetable wastes in agricultural or agroalimentary waste processing industry, and in a water or household refuse processing facility to be injected in a natural gas distribution network. Uses include but are not limited to biogases to be injected as organic-methane, carbon dioxide, steam and hydrogen sulfide in the natural gas distribution network.    ADVANTAGE - The device allows treatment of biogases output from anaerobic fermentation of livestock or vegetable wastes in simple and inexpensive manner by enabling two washing processes while reducing energy consumption during washing processes, and avoiding formation of residues.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating flow of fluid by a cold water gas washing device.'(Drawing includes non-English language text)'    Vertical cooling exchanger (1)    Material transfer column (6)
NOVELTY - The device has a separation unit comprising a flash column (19) and/or a phase separator (7). Pipes discharge gas (21) enriched with hydrogen and liquid (23). A column i.e. carbon monoxide column (27) is linked to one of the pipes, and another pipe is linked to a tank of the column to withdraw liquid enriched with methane (33). A third pipe is linked to a head of the column to withdraw carbon monoxide enriched gas (43). The pipes are placed under the column. The columns have same main axis such that the liquid is produced at pressure higher than that of the tank pressure.    USE - Device for cryogenically separating a mixture of methane, carbon monoxide and hydrogen to produce hydrogen enriched gas and a liquid mixture containing carbon monoxide and methane.    ADVANTAGE - The device cryogenically separates the mixture of methane, carbon monoxide and hydrogen when the methane is produced under pressure. The device is designed in such a way that maximum height of the apparatus is decreased, so as to reduce cost of the apparatus and transport cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for cryogenically separating a mixture of methane, carbon monoxide and hydrogen.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating a washing process with methane.    Phase separator (7)    Flash column (19)    Gas (21)    Liquid (23)    Carbon monoxide column (27)    Methane enriched liquid (33)    Carbon monoxide enriched gas (43)
NOVELTY - Electrolysis cell assembly (10) comprises: a first cell chamber (14) containing a first electrolyte salt solution and an anode (20); a second cell chamber containing a second electrolyte caustic soda solution and a cathode; a barrier physically separating the first solution from the second solution; and a eutectic electrode contacting the first and second electrolyte solutions (18). The eutectic electrode excludes mercury-free and comprises an alloy of bismuth, indium and tin, and is electrically interconnecting the first and second cells.    USE - The electrolysis cell assembly is useful for the commercial production of hydrogen and chlorine gases.    ADVANTAGE - The electrolysis cell assembly does not require the use of toxic liquid mercury-sodium amalgam electrodes.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an electrolysis system comprising: a first cell containing a first electrolysis salt solution of an alkali-metal and a halogen; a first cell anode for receiving electrical current from the first electrolysis salt solution; a second cell adapted to contain a second electrolysis caustic soda solution; a second cell cathode for delivering electrical current to the second electrolysis caustic soda solution; and a eutectic electrode electrically interconnecting the first electrolysis salt solution and the second electrolysis caustic soda solution, where the eutectic electrode is formed from a bismuth-indium-tin ternary alloy.    DESCRIPTION OF DRAWING(S) - The figure shows a cross-sectional view of an electrolysis apparatus.    Electrolysis cell (10)    Wall (12)    First cell (14)    Electrolyte solution (18)    Anode (20)
NOVELTY - The system has an absorption tower (56) which provides the absorption liquid (11) to absorb the hydrogen sulfide in the generated gas. A gas turbine (62) electric-power-generates the fuel in which the hydrogen sulfide is removed. A humidifying tower (64) sprays and humidifies the water content, cools waste gas, collects the water contents, and provides the combustion air to the gas turbine. The cooling water is supplied from the water recovery apparatus (65) through the cooling water supply system to a gasifier (50), the heat recovery unit (51) and a cooling tower (52).    USE - Gasification-power-generation system for gasifying carbon-type fuels such as coal, biomass, and heavy oil.    ADVANTAGE - The exhaust heat of the gasifier is guided to the gas turbine and the high generating efficiency can be achieved, even when the desulfurizing apparatus using the absorption liquid which operates at low temperature is installed between the gasifier and the gas turbine.    DESCRIPTION OF DRAWING(S) - The drawing shows a systematic view of the gasification-power-generation system. (Drawing includes non-English language text)    Absorption liquid (11)    Gasifier (50)    Heat recover unit (51)    Cooling tower (52)    Dust-removal apparatus (53)    Water washing tower (54)    Shift reaction device (55)    Absorption tower (56)    Gas turbine combustion device (60)
NOVELTY - Process for production of ethanol involves fermenting carbohydrate containing substrate in presence of one or more high alcohol tolerant yeasts having an alcohol tolerance of at least 100 g/1 and one or more maltotriose positive yeasts.    USE - The process, high alcohol tolerant yeasts and maltotriose positive yeasts and composition are useful for production of beer and ethanol (all claimed) used in food and beverage industry, or as an alternative energy source for fossil fuels.    ADVANTAGE - The process enables production of the ethanol with increased yield and rate without increase in production costs, as yeast strains having high alcohol tolerance and high ethanol production ability are used in the production process.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) use of one or more high alcohol tolerant yeasts and maltotriose positive yeasts in process for production of ethanol; and    (2) composition comprising one or more high alcohol tolerant yeast and/or their extracts, and one or more maltotriose positive yeast and/or their extracts, where the composition is a by-product of the above-mentioned fermentation process.
NOVELTY - A crystalline form I or amorphous form II of telaprevir is new. The crystalline form I is confirmed by X-ray powder diffraction pattern as given in the specification; and amorphous form II is confirmed by X-ray powder diffraction pattern given in Figure 2 of the specification.    USE - For preparation of a medicine for treating hepatitis C such as cirrhosis.    ADVANTAGE - The crystalline form I or amorphous form II of telaprevir have a good performance in terms of stability; is conducive to storage so as to comply with the requirements of the stability for a drug, and is conducive to the commercial production; is prepared with a low cost and industrial friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the crystalline form I or amorphous form II of telaprevir.
NOVELTY - The utility model claims a heat accumulating type connection heat carrier biomass carbon gas cogeneration a pyrolysis system, wherein the system comprises a biomass raw material preparation device and biomass pyrolysis device, collecting device and treatment device for the waste gas of the hot biomass pyrolysis device comprises a dry ash furnace, a moving bed pyrolyzing furnace and the heat-carrying medium heating device and biomass pyrolysis pre-drying the biomass volatile pyrolysis process sequence in the dry dust cleaning furnace and a bed pyrolyzing furnace zone, a process using a heat transfer medium, the drying step uses a low temperature flue gas from a coal gas heat accumulating type heat exchanging method as the heat transfer medium, and the high temperature flue gas with heat-carrying gas is used as heat transfer medium,. In addition, biomass pre-drying process and biomass volatile pyrolysis process generate a gas product processing is not carried out. The utility model is provided with a comprehensive effect the pyrolysis product quality is greatly improved, a heat efficiency is greatly improved, the gas treatment device is simplified, gas processing power consumption is greatly reduced, liquid product deep processing cost is reduced.
NOVELTY - This utility model claims a kind of marsh gas separating and purifying device belongs to marsh gas separating and purifying technology field. The purifying device comprises a gas storage tank, a packed bed reactor, a raw liquid storage tank, a regeneration tank, a liquid storage tank, a marsh gas tank and a marsh gas steel bottle are connected in turn, a packed bed reactor is further connected with a liquid storage tank, a gas storage tank and a reactor; This utility model is a device using a packed bed reactor, carrying out absorbing and separating the CO2 in marsh gas. This utility model selection for reaction device is simple, the reaction condition is mild, the operation is convenient, CO2 a high speed, separating marsh gas has high purity.
NOVELTY - This utility model claims a kind of the methyl alcohol flash evaporation de-separating device, comprising a rough tank, a pump, a heater, a tower, a condenser, a receiving tank with vacuum. A rough pump heater into the flash, the flash evaporation tower above the filler, the filler is methyl inlet, the upper part filler is connected with the condenser, flash evaporation of the methanol steam is condensed with vacuum and the receiver, flash discharge hole lower part and removing the alcohol methyl ester is printed by a pump, further processing. This utility model can make the reaction of methyl flash removing methanol and methanol in methyl removing completely, which is good for a methanol and improve the economic benefit of the bio-diesel.
NOVELTY - The plate (16) has a base body (34) made of plastic material. A support structure (32) is connected to or embedded in the base body. Multiple ribs (40) are extended between and perpendicular to two main surfaces (28, 30) of the plate. Mold elements (42) i.e. channel laths, pass forces applied by tensile elements into the support structure, where a fuel cell stack of a fuel cell is pressed together by the tensile elements. The mold elements are arranged on secondary surfaces (50) of the plate and on end sections of the ribs. The mold elements are connected with the ribs.    USE - End plate for a fuel cell stack of a fuel cell (claimed) for producing electric power.    ADVANTAGE - The design of the plate enables achieving rigidity of the plate at low weight of the plate. The support structure is connected to or embedded in the base body, so that a stable connection is achieved between the base body and the support structure, thus enabling manufacture of large quantities of the plate in an inexpensive manner. The fuel cell stack is compact and can be supplied with operating mediums in a space-saving manner.    DETAILED DESCRIPTION - The plastic material of the base body is embedded in fibers i.e. glass fibers.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of an end plate.    End plate (16)    Main surfaces of end plate (28, 30)    Support structure (32)    Base body (34)    Ribs (40)    Mold elements (42)    Secondary surfaces of end plate (50)
NOVELTY - The gasification reactor (1) has a reaction casing (2) whose one end is provided with a feed device (17) for supplying gasification material. The other end of reaction casing is provided with discharge device (12) for discharging residual substance. A supporting burner (6) is provided for maintaining minimum temperature in reaction zone (7) of reaction casing. A discharge port (9) is provided for discharging fuel gas. A coil is provided over entire longitudinal extent of reaction casing.    USE - Fixed bed gasification reactor for producing fuel gas from gasification material such as biomass, used in farm, brewery and biogas plant.    ADVANTAGE - Flexible and/or soft gasification materials such as biomass can be exploited efficiently. The wear resistance of the reaction casing can be improved. Efficient mixing and loosening of materials can be ensured. The hazard of stagnation of materials can be avoided. The simple structure of gasification reactor can be ensured. The fixed bed gasification reactor can be assembled easily. The need for building high ceilings can be prevented. The blockage of gasification material can be prevented. The reaction casing can be designed easily. The thermal expansion of reaction casing can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fixed bed gasification reactor.    Fixed bed gasification reactor (1)    Reaction casing (2)    Supporting burner (6)    Reaction zone (7)    Discharge port (9)    Discharge device (12)    Feed device (17)
NOVELTY - The reactor (1) has a horizontally arranged and rotatably mounted reaction cylinder (3) whose one end is supplied with a gasification material by a feeder (17). Non-gasified residue substance is removed at another end of the reaction cylinder by a discharge device (12). A supporting burner (6) is provided for starting and maintaining a minimum temperature in a reaction zone (20). A discharge port (9) discharges a combustible gas. The reaction cylinder is externally mounted with the ends such that the cylinder ends are sealed against each other by fixed housing parts (10, 19).    USE - Fixed bed gasification reactor for producing combustible gases from flexible and/or soft gasification material e.g. biomasses such as agricultural holdings, breweries and biogas plants.    ADVANTAGE - The reaction cylinder is externally mounted with the ends such that the cylinder ends are sealed against each other by the fixed housing parts, thus allowing the reactor to utilize a wide range of the biomass. The design of reaction cylinder allows a better access to inside of the reaction cylinder. The reactor is equipped with a drive, which is designed in simple and reliable manner and insensitive to small displacements in a longitudinal direction of the reaction cylinder due to thermal expansion.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic longitudinal sectional view of a fixed bed gasification reactor.    Fixed bed gasification reactor (1)    Horizontally arranged and rotatably mounted reaction cylinder (3)    Supporting burner (6)    Discharge port (9)    Fixed housing parts (10, 19)    Discharge device (12)    Feeder (17)    Reaction zone (20)
NOVELTY - Electrolytically synthesizing methanol and/or methane, comprises reducing carbon dioxide present in an electrolyte which is present in a liquid phase by introducing protons into the electrolyte through a proton-conducting membrane (2), at a critical point or in supercritical phase of the electrolyte.    USE - The method is useful for synthesizing methanol and/or methane.    ADVANTAGE - The method avoids costly methanol separation process and purification of the methanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out the above method, comprising a pressure-resistant reactor vessel (1) for accommodating the carbon dioxide-containing electrolyte present in the liquid phase, at the critical point or in the supercritical phase of the electrolyte, where the reactor vessel is divided by the proton-conducting membrane, into an anode chamber (3) having an anode for accommodating an aqueous electrolyte, and a cathode chamber (4) having a cathode for accommodating the carbon dioxide-containing electrolyte.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of a device for electrolytically synthesizing the methanol.    Reactor vessel (1)    Proton-conducting membrane (2)    Anode chamber (3)    Cathode chamber (4)    Pressure compensation pipe (5)
NOVELTY - Generating hydrogen involves: (a) exposing an aqueous liquid to carbon dioxide; and (b) passing a current through the aqueous liquid so as to generate hydrogen.    USE - The processes or methods are useful for generating hydrogen; producing methane and water; and for increasing rate of hydrogen production in electrolysis of aqueous solution (all claimed).    ADVANTAGE - By using the process, more hydrogen may be produced, or hydrogen may be produced at a greater rate, by hydrolysis of water in the presence of carbon dioxide than in its absence. More particularly, an increase in hydrogen production from electrolysis of water is observed on increasing the concentration of carbon dioxide and/or carbon dioxide derived species in the water. In particular, more hydrogen may be produced with lower power in the presence of carbon dioxide under pressure than is achievable at present. Hydrogen is produced in greater amount, or at a greater rate, than would be produced using the same conditions of electrolysis but without the step of exposing the aqueous liquid to carbon dioxide.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a method of producing methane and water involving: (a) exposing an aqueous liquid to carbon dioxide; (b) passing a current through the aqueous liquid so as to generate hydrogen; and (c) reacting the hydrogen with carbon dioxide so as to produce methane and water; and    (2) a method for increasing the rate of hydrogen production in electrolysis of an aqueous solution, involving exposing the aqueous solution to carbon dioxide prior to and/or during the electrolysis.
NOVELTY - Manufacturing an epoxy resin, where a brine containing sodium chloride is generated in the process, comprises electrolyzing the brine in order to produce hydrogen, chlorine and sodium hydroxide, and recycling at least one part of the hydrogen, chlorine and sodium hydroxide in the process.    USE - The process is useful for manufacturing an epoxy resin (claimed).    ADVANTAGE - The process is capable of easily, safely and eco-friendly preparing the epoxy resin with reduced amount of chloride waste and minimal amount of raw materials containing sodium and chloride. The process avoids handling, transportation and storage of dangerous chemicals, including chlorine, hydrogen and concentrated sodium hydroxide.
NOVELTY - The utility model claims a gas-solid combination biomass partition control a pyrolysis system, comprising a biomass raw material preparation device and biomass pyrolysis device, collecting device and treatment device for the waste gas of the hot biomass pyrolysis device comprises a dry ash furnace, the temperature in the pyrolysis furnace and a pyrolyzing furnace, a biomass pyrolysis sequence respectively enter into the third device zone. This utility model is the biomass raw material preparation device comprises a biomass crushing equipment and biomass forming machine, crushing device is a crusher or grinder, the sequence of a pyrolysis furnace using inert solid ball is used as heat transfer medium, wherein the biomass pyrolysis device further comprises a hot air furnace, a heating furnace, a inert ball corresponding to the hot flue gas fan and a conveying gas. The utility model is provided with a comprehensive effect the pyrolysis product quality is greatly improved, a heat efficiency is greatly improved, the gas treatment device is simplified, gas processing power consumption is greatly reduced.
NOVELTY - This utility model claims a kind of photo-decomposed and water-produced hydrogen integrated device, a LED chip on the package substrate, the transparent colloid is transparent substrate on the chip, then depositing with photolysis water material on the transparent substrate. Finally uniformly coating waterproof insulated paint in the electrode, so that the device is provided with waterproof property, and the device is immersed in water, the light emitted by the LED chip directly photolysis water material on a transparent substrate to make the material absorb photon generated electron hole pair to make the water into hydrogen.
NOVELTY - This utility model claims a kind of hydrogen fuel generating device, mainly comprising a reaction furnace, a hydrogen storage material and hydrogen storage tank material supplying source and the reaction furnace, a reaction furnace is set on the bottom of the heating control device and a gas storage tank, a recycling hydrogen storage or other combustion gas, using internal air and high temperature reaction furnace is carbon hydrogen gas or methanol and water produced by decomposing hydrogen, to be outputted to the application terminal, or a combustion as a heat source of the reaction furnace, providing a kind of energy-saving, hydrogen fuel generating device and environment-friendly.
NOVELTY - This utility model claims a kind of poison head and a head lamp device, comprising a front end cover and a back end cover, a front end cover and a rear end cover, and a containing space, the containing space is provided with an integrated circuit board and illumination light source, the integrated circuit board is provided with a processor and a processor connected to the CO gas sensor, CH4 gas sensor and a data transmission interface, the illumination light source is electrically connected with the processor, the front end cover is provided with the light from the light source passes through the window. This utility model is a toxic gas detection, illumination and data transmission connection with the overcomes the problem that the current technology has single function and small use range, realizing real time detection, and a harmful gas in real time, is convenient to carry and use.
NOVELTY - The device has air pump that is connected with gas distribution module by pipeline. The gas distributing module is respectively connected with alkane component gas detection functional module, carbon dioxide gas detection functional module, carbon monoxide gas detection functional module and hydrogen sulphide gas detection functional module which are connected with computer control system. The computer control system is connected with air pump, and gas distribution module, while connecting to comprehensive logging instrument through data transmission line.    USE - Continuous spectrum gas measuring logging device.    ADVANTAGE - The gas measuring logging can be performed continuously and the drilling construction accident oil exploration can be prevented.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a continuous spectrum gas measuring logging method.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the continuous spectrum gas measuring logging process. (Drawing includes non-English language text)
NOVELTY - This utility model claims a kind of domestic biomass semi-gasification furnace, comprising a base, the base is fixed with a coaxial line of the shell and a hearth, wherein the base is provided with the hearth outer wall vertical to the secondary oxygen supplying pipe, a secondary oxygen supply tube and the upper part of the hearth is provided with corresponding to the secondary oxygen supply hole, a hearth and a hearth refractory cement. Gasification and combustion hearth space share one and the lower part is gasification section, the upper part of the combustion section. A secondary oxygen supply tube along the outer wall of the hearth is provided with the secondary tube corresponding to the combustion chamber is provided with a secondary oxygen supply hole, and the lower end thereof is connected with the atmosphere, so that the secondary oxygen supplying pipe, the air is quickly heated, then enter into combustion chamber and the high temperature combustion gas for the second time. The hearth is refractory cement cast-in-situ structure and reduces the manufacturing and transportation cost on the premise of ensuring heat preservation effect, and is firm and durable. On the premise of ensuring the using effect of the lower, which simplifies the structure, saves the material and manufacturing cost.
NOVELTY - This utility model claims a kind of vertical pyrolysis reactor. The bottom of the discharge hole, a feeding device of biomass fuel gas outlet of top part comprises a reactor shell, a feeding device, a reactor, a reactor bottom fire grate is an ash outlet device, reactor, a feeding device located in the bottom of the reactor. The centre of the bottom of a feeding method, solves the problem of pyrogenation reactor of solid heat carrier biomass in a neck of the uniform distributing; is set with crushing device in the pyrolysis reactor to form organic combined with the rotation of the fire grate, a grate speed can accurately adjust the discharge amount by controlling the feeding speed and discharging speed, the thickness of the material layer, the air inlet amount, the air inlet a, the reaction temperature and so on to realize the precise air pyrolysis reaction. Pyrolysis reactor ash is more stable and more continuous production, reliability is greatly improved, a method of design and a crushing device is a device to a continuous process as long as the size of the biomass 10 cm.
NOVELTY - The utility model claims a biomass fuel gas purifying device, wherein a bottom end opening of the tank body, a water tank, a water pump, a water supply pipe, a water supply branch pipe and sprayer, the lower side of the tank body are respectively provided with an air outlet and an air inlet, the tank body vertical to the pool water, the spray thrower is set on the filter tank body upper part, the one end of the water supply branch pipe passes through the upper cover and the spray thrower is connected with the tank body and the other end is connected with the water supply pipe, the water outlet end of the water pump is connected with a water supply pipe, the water inlet end of which is connected with the water tank. Sprayer is capable of rotating said sprayer. This utility model claims a kind of simple structure, good purifying effect, low cost and easy solution; And the utility model is fit for biomass fuel gas, internal combustion engine or other gas device before using the purifying device.
NOVELTY - This utility model aims at providing a fluidized bed type biomass scale manufacture fuel oil reactor. The purpose of this utility model is realized as follows: it is composed of a feeding part, a carrier gas, a liner, an outer sleeve part of the feeding part is connected with tank body, the carrier gas is connected with a tank body, tank body is embedded in the outer sleeve part. This utility model is a fluidized bed type biomass scale manufacture fuel reactor, simple structure, low energy consumption and low cost, the utilization rate of the energy is high, it can realize mass production, extremely short energy, low energy consumption increased day by day nowadays, this utility model is provided with economic and social value.
NOVELTY - This utility model claims a biomass press block gasification combustion machine, comprising a fixed bed gasification furnace, a fixed bed gasification furnace comprises a gas outlet which is set on the top of the furnace body of the feeding hopper is set on the bottom of the furnace body of the gasification agent inlet, a fire grate, a , connected with the gasification agent inlet of the air blower, is provided with a gas outlet on the furnace body of the middle part in the vertical direction and a gas outlet is inclined upwards in the vertical direction is provided with a inertia dust catcher of sediment chamber, settling chamber is connected with a fuel gas outlet is connected with the combustion device for heating device connected with the combustion device of the settling chamber is connected with the air outlet. A biomass press block gasification this utility model provided by the combustion machine, which can improve strength and vaporizing burner of biomass fuel gasification rate, reduces the energy loss in the gasification process of biomass fuel makes full use of heat energy.
NOVELTY - This utility model claims a biomass semi-gasification furnace from bottom to top in turn comprises a base, a hearth and a combustion chamber. The hearth is made of refractory cement, the wall of the atmosphere with multiple secondary oxygen supply hole. The hearth uses fire-resistant cement casting, it will not be deformed because of high temperature in the gasification chamber and the service life is long. A secondary oxygen supply hole preset on the inner wall of the hearth, on one hand it saves the secondary hearth and the manufacturing cost of the oxygen pipe, on the other hand it solves the secondary oxygen supplying pipe caused by over-high temperature and deformation problem is even, the secondary oxygen supply; The hearth is made of refractory cement, a thicker, but also solves the problem that the feeding port as too close to the inner gasification a fuel so as to easy to be oxidized and deformed and prolong the service life thereof. As said above, this utility model and present, it has low cost and long service life.
NOVELTY - A biomass hot water furnace, comprising a hearth, a furnace body and a furnace body, the ash hopper, the furnace body centre lower part hearth is provided with a hearth, the upper end of the hearth is provided with a combustion-supporting device, wherein the hearth is provided with a water tank. In the furnace body is set in the outer lower part of the air outlet of the blower is divided into two paths, one path into the dust hopper on the upper part, and the other path passes through the first combustion-supporting air passage into the secondary combustion-supporting device for a secondary combustion-supporting wind channel. The furnace body is pot, and the bottom of the kettle is curved surface. This utility model make a or directly burning biomass solid fuel producing combustible gas and granular black carbon-by-level of a fully complete combustion, which can eliminate black smoke, improve the heat energy conversion efficiency of the fuel, it can save fuel cost and protects environment, and warming stove in straw cooking by combustion-supporting frame to provide hot water at the same time, improve the utilization ratio of the energy.
NOVELTY - A kind of minitype blast biomass furnace, comprising a hearth, a furnace body and a furnace body, the ash bucket, the upper end of the hearth lower part hearth is provided with a combustion-supporting device, the periphery is combustion-supporting passage of the secondary combustion-supporting device, the air outlet of the air blower is set in the lower part of the furnace body is divided into two paths, one path into the dust hopper by the air channel, and the other path is connected with the secondary combustion-supporting wind passage and the combustion-supporting channel. This utility model make a or directly burning biomass solid fuel producing combustible gas and granular black carbon-by-level of a fully complete combustion, which can eliminate black smoke, improve the heat energy conversion efficiency of the fuel, it can save fuel cost and protect environment by a combustion-supporting device.
NOVELTY - A kind of firewood and coal biomass furnace, comprising a furnace body and a hearth, the upper end of the hearth is provided with a combustion-supporting device, the secondary combustion-supporting device is set fire. The secondary combustion-supporting device is a ventilation channel, the air channel is provided with the wall thickness of the furnace body of the combustion-supporting air inlet channel. This utility model make a or directly burning biomass solid fuel producing combustible gas and granular carbon black gradually to a fully complete combustion, which can eliminate black smoke, improve the heat energy conversion efficiency of the fuel, it can save fuel cost and protect environment by a combustion-supporting device and fire. And the heat efficiency is high, saves more than 30% of energy, the temperature can reach 300 degrees centigrade, as a kind of cooking, ideal heating furnace.
NOVELTY - Method for preparing ethanol from lignocellulosic raw material, involves filtering lignocellulosic biomass using filter having mesh size of 60-600, and performing enzyme saccharification of the fiber separated by sieve treatment process.    USE - The method is useful for preparing ethanol from lignocellulosic biomass (claimed).
NOVELTY - The apparatus has workpiece alignment unit onto which a workpiece is passed. A fluid distribution support (113) has an apertured upper support surface (114) that provides a supporting fluid cushion for supporting and aligning workpiece when workpiece is passed onto alignment unit. The support surface has rectangular compartment (116a) and L-shaped compartment (116b) from which fluids of different pressure and flow rate are delivered. A differential pressure is generated across regions of support surface to cause the workpiece to be moved and aligned at alignment unit.    USE - Apparatus for aligning workpiece such as planar substrate e.g. wafer (all claimed) used in solar and fuel cells.    ADVANTAGE - The alignment locus towards the alignment stop can be provided, as differential pressure is generated across regions of the support surface to cause workpiece to be moved and aligned at workpiece alignment unit, and hence allows workpiece to be lifted higher above one region compared to another. The differential pressure can be created by altering the pressure supplied to regions or by altering the thickness or porosity of the porous air-permeable support.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of aligning workpieces.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of workpiece alignment apparatus.    Housing (111)    Fluid distribution support (113)    Support surface (114)    Rectangular compartment (116a)    L-shaped compartment (116b)
NOVELTY - Synthesizing aziridine compounds (I), comprises contacting imine derivatives (IA) with diazo compounds (IB) in the presence of a catalyst, where the catalyst is phosphorus derivatives (IV) or (V).    USE - The method is useful for synthesizing (I) (claimed) such as isotopically labeled aziridines, which are useful as intermediates for synthesizing unnatural alpha - and beta -amino acids, chiral auxiliaries, polymers, azasugars and heterocyclic entities such as oxazolidinones, imidazolidines, beta -lactams, and pyrrolidines. (I) has antitumor, antiviral and/or antibacterial properties. No biological data given.    ADVANTAGE - The method provides (I) with high yield in an environmental friendly manner.    DETAILED DESCRIPTION - Synthesizing aziridine compounds of formula (I) and their salts, comprises contacting imine derivatives of formula (R1-C(=NR3)-R2) (IA) and their salts or precursors with diazo compounds of formula (R4-C(=N2)-R5) (IB) and their salts in the presence of a catalyst, where the catalyst is phosphorus derivatives of formula (R8-P(=X)(R7)-NH-R6) (IV) or (R8-P(=X)(R7)-NF-R6) (V).    R1-R9 = any atom or group, preferably H, halo or a hydrocarbyl, where the hydrocarbyl is optionally substituted with cyclic alkyl, alkenyl, alkynyl, acyl, aryl, arylalkyl, arylalkenyl, arylalkynyl, alkylaryl, alkenylaryl or alkynylaryl group which optionally includes one or more heteroatoms in its carbon skeleton, and the two or more of R1-R9 together with the atom or atoms to which are attached may form a cyclic hydrocarbyl group which is optionally substituted and which is optionally include one or more heteroatoms N, O or S in its carbon skeleton; and    X = O, S or NR9, where R1 and R4 in the aziridine (I) are cis- or trans-.    INDEPENDENT CLAIMS    Indepedent claims included for compounds of formula (IV) and (V) or there salts.
NOVELTY - Preparation of alcohol-carbon liquid fuel involves grinding 65-70 wt.% charcoal, 29-34 wt.% (methyl)ethanol and 1 wt.% additive under stirring.    USE - Preparation of alcohol-carbon liquid fuel (claimed).    ADVANTAGE - The method enables preparation of alcohol-carbon liquid fuel with reduced energy consumption by environmentally-friendly process.
NOVELTY - Performing fermentation-drying of mushroom waste cultivation bed, involves mixing fermentation starting adjuvant with mushroom waste cultivation bed, placing mixture in a heat insulation container, circulating air in the container, performing fermentation for first time to obtain first fermentation product, mixing first fermentation product with new mushroom waste cultivation bed, placing the mixture in a heat insulation container, and circulating air in the container to perform fermentation for second time.    USE - The method is useful for performing fermentation-drying of mushroom waste cultivation bed, where the mushroom is enokitake mushroom (claimed).    ADVANTAGE - The method produces mushroom capable of producing antimicrobial substance, consumes less energy, and is cost-effective and simple.    DETAILED DESCRIPTION - Method for performing fermentation-drying of mushroom waste cultivation bed, involves mixing 15 pts. mass or more fermentation starting adjuvant with 100 pts. mass mushroom waste cultivation bed, placing mixture in a heat insulation container, circulating air in the container, performing fermentation for first time to obtain first fermentation product, mixing 30 pts. mass or more first fermentation product with 100 pts. mass new mushroom waste cultivation bed, placing the mixture in a heat insulation container, and circulating air in the container to perform fermentation for second time, where hypha of the mushroom has property of producing antimicrobial substance.
NOVELTY - A solid absorbing agent comprises hydrocarbon gas containing 0.2-10 mass% oxalic acid, and 90-99.8 mass% nitrogen containing compound.    USE - As a solid absorbing agent, useful for measuring NR3 content e.g. ammonia, methylamine, methyl amine, and trimethylamine content in the hydrocarbon gas (claimed).    ADVANTAGE - The solid absorbing agent avoids the disadvantages of the liquid absorbent, which is more helpful for field test of the hydrocarbon gas containing NR3 compound. The method accurately detects the hydrocarbon gas containing micro compound; and is simple and easy method.    DETAILED DESCRIPTION - A solid absorbing agent comprises hydrocarbon gas containing 0.2-10 mass% oxalic acid, and 90-99.8 mass% a compound of formula NR3.    R=H or 1-2C alkyl.    INDEPENDENT CLAIMS are included for the following:    (1) a hydrocarbon gas absorption tube comprising absorbing pipe having inner diameter of 2-7 mm; and absorbing agent, where the absorption tube is U-shaped or straight tube of the glass tube; and    (2) measuring NR3 content in the hydrocarbon gas involving absorbing NR3 by absorbent in a form of cation in absorption tube, and then desorbing the cation contained in the absorbent to obtain the desorption solution by water, measuring the corresponding cation concentration in the desorption liquid by ionic chromatography, and calculating the content NR3 of a hydrocarbon gas corresponding to the cation concentration.
NOVELTY - A bio-diesel fuel, comprises 60-80 wt.% 11-18C 6-furfuryl levulinic acid ester, furoic acid methyl ester, 10-20 wt.% levulic acid methyl ester and 10-20 wt.% ethyl levulinate.    USE - As bio-diesel fuel used in a bio memory disc (claimed).    ADVANTAGE - The diesel oil has high ketene value and oxidation stability, and has improved thermal efficiency of 30-40% compared with the traditional bio-diesel. The diesel oil can be 100% directly, but also can be used with petroleum diesel oil mix.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing bio-diesel oil, involving: condensing furfural and levulinic acid as raw material, under alkaline condition, to obtain 6-ethane propionic acid; (2) reacting 6-furfurylidene ethane propionic acid and esterifying straight-chain, branched, cyclic or monohydric 1-8C alcohol to obtain the 11-18C 6-furfurylidene acid ethane ester; (3) oxidizing furfural for preparing furoic; (4) carrying out esterification reaction of furoic and methanol to obtain the acid methyl ester; (5) performing further esterification of levulinic acid and methanol or ethanol to obtain a levulinic acid methyl ester or ethyl ester; and (6) reacting 6-furfurylidene acid ethane ester, acid methyl ester and acetyl acetone acid methyl (ethyl) ester compound to obtain bio-diesel.
NOVELTY - Method for improving effect of anaerobic digestion treatment of breeding manure involves crushing calcined magnesite industrial products, adding low-grade iron ore, and iron oxide mineral, adding mixture into anaerobic digester of breeding manure, mixing, improving activity of anaerophyte in anaerobic digester, increasing anaerobic digestion methane production efficiency of breeding manure, reducing concentration of residual chemical oxygen demand, ammonia nitrogen and phosphate in biogas slurry, improving quality of anaerobic digestion effluent, and treating biogas slurry.    USE - Method for improving effect of anaerobic digestion treatment of breeding manure (claimed).    ADVANTAGE - The method efficiently improves effect of anaerobic digestion treatment of breeding manure, by simple method.    DETAILED DESCRIPTION - Method for improving effect of anaerobic digestion treatment of breeding manure involves crushing calcined magnesite industrial products containing magnesium oxide content of more than 80%, and less than 5% carbonate minerals, forming crushed powder with 320 meshes, adding low-grade iron ore, and limonite, oolitic or hematite, and iron oxide mineral, adding mixture into anaerobic digester of breeding manure, mixing, improving activity of anaerophyte in anaerobic digester, forming magnesium-ammonium phosphate and iron sulfide precipitate, increasing anaerobic digestion methane production efficiency of breeding manure and methane concentration in generated gas, improving anaerobic energy source conversion efficiency and energy source quality, reducing concentration of residual chemical oxygen demand, ammonia nitrogen and phosphate in the biogas slurry, improving quality of anaerobic digestion effluent, and reducing post-treatment pollutant load, and treating biogas slurry.
NOVELTY - Bispyribac sodium, organic solvent, catalyst, dehydrating agent, and benzophenone oxime added to a reactor and reacted for 6-36 hours. The reaction product is filtered and distilled under reduced pressure, to recover the organic solvent. The obtained product is recrystallized using toluene, to obtain pyrimidine salicylic acid.    USE - Manufacture of pyrimidine salicylic acid used for herbicide.    ADVANTAGE - The method enables manufacture of pyrimidine salicyclic acid with high productivity, and is environmentally-friendly.
NOVELTY - Manufacture of iloperidone involves reacting (Z)-N-((2,4-difluorophenyl)(phenyl)methylidene)hydroxylamine or its salt, 1-(4-(3-bromopropoxy)-3-methoxyphenyl)ethan-1-one, lithium hydroxide, and methyl isopropyl ketone solvent in presence of catalyst for 1.5-4 hours.    USE - Manufacture of iloperidone (claimed).    ADVANTAGE - The method enables manufacture of iloperidone by a simple and environmentally-friendly process with excellent quality, and high yield.
NOVELTY - An alcohol gasoline additive comprises 50% lipid solubilizer, 10-20% hydrocarbon solubilizer, 8-15% alcohol reinforcing agent, 8-10% combustion-supporting catalyst, 0.5-1% metal corrosion inhibitor, and 0.5-1% antioxidant anti-adhesive agent.    USE - Alcohol gasoline additive (claimed).    ADVANTAGE - The alcohol gasoline additive effectively improves alcohol gasoline combustion parameter, reduces oil consumption, and can be directly used for modulating finished product of ethanol gasoline.
NOVELTY - A bio-based methanol and gasoline-power reinforcing agent contains calorific value-improving component containing 15-26 volume% yeast extract of fatty acid soap and naphthenic hydrocarbon, 61.5-62.5 volume% fatty amine, and catalyst component containing 11.5-13.5 volume% cycloalkane.    USE - Bio-based methanol and gasoline-power reinforcing agent (claimed).    ADVANTAGE - The bio-based methanol and gasoline-power reinforcing agent is environmentally-friendly, economical and non-toxic, and has improved acceleration performance.
NOVELTY - A bio-based anti-swelling methanol gasoline degumming agent contains 40-50 volume% alkyl diphenylamine, 25-30 volume% petroleum sulfonate containing barium petroleum sulfonate and sodium petroleum sulfonate, 25-30 volume% anti-adhesive component, 14-17 %mass yeast fatty acid soap containing 16-18C fatty acid oil yeast extract and triethanolamine petroleum yeast, and 8-16 volume% fatty acid amines. The fatty acid amine is ethanolamine and/or diethanolamine.    USE - Bio-based anti-swelling methanol gasoline degumming agent (claimed).    ADVANTAGE - The bio-based anti-swelling methanol gasoline degumming agent is economical, non-toxic and environmentally-friendly, and has excellent anti-swelling degumming effect.    DETAILED DESCRIPTION - A bio-based anti-swelling methanol gasoline degumming agent contains 40-50 volume% alkyl diphenylamine, 25-30 volume% petroleum sulfonate containing barium petroleum sulfonate and sodium petroleum sulfonate in volume ratio of 1:2, 25-30 volume% anti-adhesive component, 14-17 %mass yeast fatty acid soap containing 16-18C fatty acid oil yeast extract and triethanolamine petroleum yeast, and 8-16 volume% fatty acid amines. The fatty acid amine is ethanolamine and/or diethanolamine. The 16-18C fatty acid oil yeast extract is obtained by fermentation of oil and petroleum yeast EAM-AC16 with deposition number of CGMCC NO.7429. An INDEPENDENT CLAIM is included for preparation of bio-based anti-swelling methanol gasoline degumming agent.
NOVELTY - Preparation of metal welding gas involves mixing ethyl acetate, toluene, xylene, petroleum ether, methanol, acetone and ferrocene to obtain primary additive, mixing sodium tripolyphosphate, trisodium phosphate, anhydrous sodium pyrophosphate and hydrogen peroxide to obtain secondary additive, injecting additive into electric machine in predetermined ratio, and filling liquefied petroleum gas or propane.    USE - Preparation of metal welding gas (claimed).    ADVANTAGE - The metal welding gas is environmentally-friendly and economical, and is efficiently prepared.
NOVELTY - Preparation of straw fuel composite involves mixing chopped wheat straw and rice straw, and pressing into blocks, mixing block of straw, coal and sludge formed in the pretreated feedstock and forming straw, coal and paper sludge raw material, mixing straw material and raw sludge, pulverizing, adding coal agent, clay, lime and water, such that the weight ratio of straw material, raw sludge, coal material, coal agents clay, lime and water is 50:20:5:5:5:2:12, mixing, press-molding at 200 degrees C for 20-60 minutes, carbonizing, cutting, and then cooling.    USE - Preparation of straw fuel composite (claimed).    ADVANTAGE - The method efficiently and economically provides straw fuel composite.    DETAILED DESCRIPTION - Preparation of straw fuel composite involves mixing chopped wheat straw and rice straw, and pressing into blocks, mixing block of straw, coal and sludge formed in the pretreated feedstock and forming straw, coal and paper sludge raw material, mixing straw material and raw sludge, pulverizing, adding coal agent, clay, lime and water, such that the weight ratio of straw material, raw sludge, coal material, coal agents clay, lime and water is 50:20:5:5:5:2:12, mixing, press-molding at 200 degrees C for 20-60 minutes, carbonizing at 300-350 degrees C for 60-120 minutes and then cutting, processing obtained product at 850-950 degrees C and then cooling at -10 degrees C.
NOVELTY - Torrefaction of biomass comprises: receiving biomass having a given moisture content; heating the biomass in a generally inert environment by indirect contact; subsequently torrefying the biomass by exposing the biomass to a flow of combustion gases in the generally inert environment; and outletting the biomass with a reduced moisture content.    USE - The method is useful for torrefaction of biomass (claimed), where the torrefied biomass is useful as a fuel in combustion, co-firing in large coal power plants, heavy fuel oil substitution, partial substitute for coke in carbon anodes, blast furnaces, iron ore pellets, activated carbon for gas purification, gold purification, metal extraction, and soil amendment and soil remediation (mining site rehabilitation).    ADVANTAGE - The method transforms biomass into products having increased energy density (e.g. combustion products) and increased carbon content.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic diagram of a thermo-transformation system.    Pneumatic circuit (14)    Rotary valve (21)    Feed screw unit (22)    Heated sleeve (24)    Cyclonic bed reactors (30)
NOVELTY - A fuel cell generating system includes a reforming material supply, a first heat adjustment device, a reforming device, a fuel cell stack and a second heat adjustment device. The reforming material supply outputs a reforming material. The first heat adjustment device is coupled to the reforming material supply and receives the reforming material. The reforming device has a reformer and a heater. The reformer is coupled to the first heat adjustment device. The reformer receives the reforming material and outputs an air current to the first heat adjustment device. The fuel cell stack is coupled to the first heat adjustment device and the heater. The fuel cell stack receives the air current. The second heat adjustment device is coupled to the fuel cell stack and the first heat adjustment device.
NOVELTY - Production of alicyclic diepoxy compound (I) involves reacting powdered alicyclic olefin compound (II) and hydrogen peroxide solution in presence of powdered solid carrier and powdered solid catalyst.    USE - Production of alicyclic diepoxy compound. Uses include but are not limited to pharmaceutical, medical supply of coating agent, adhesive agent, ink and sealant.    ADVANTAGE - The alicyclic diepoxy compound is produced by environmentally-friendly and simple method with high yield, selectivity and reaction rate. The catalyst used during production of alicyclic diepoxy compound can be reused.    DETAILED DESCRIPTION - Production of alicyclic diepoxy compound of formula (I) involves reacting powdered alicyclic olefin compound of formula (II) and hydrogen peroxide solution in presence of powdered solid carrier and powdered solid catalyst.    R1-R12=H, halo, alkyl optionally containing halo, or optionally substituted alkoxy.
NOVELTY - A super-paramagnetic mesoporous solid alkali solid alkali catalyst contains potassium fluoride-magnesium oxide-magnesium-iron oxide (I).    USE - Super-paramagnetic mesoporous solid alkali solid alkali catalyst is used for preparing biodiesel oil (claimed).    ADVANTAGE - The biodiesel oil is prepared with yield of 75-94%, using the super-paramagnetic mesoporous solid alkali solid alkali catalyst.    DETAILED DESCRIPTION - A super-paramagnetic mesoporous solid alkali solid alkali catalyst contains potassium fluoride-magnesium oxide-magnesium-iron oxide of formula: KF/xMgO.MgFe2O4 (I).    x=more than 0 and less than 4.    An INDEPENDENT CLAIM is included for preparation of super-paramagnetic mesoporous solid alkali solid alkali catalyst, which involves mixing magnesium oxide material, magnesium-iron oxide material and potassium fluoride solution.
NOVELTY - Production of organic microbial fertilizer comprises 1.5-2.0% biochemical fulvic acid, 20-25% nitrogen phosphorus potassium, 8-10% organic matter, 0.30-0.50% sodium humate and potassium humate, and 0.30% carbendazim.    USE - Production of organic microbial fertilizer.    ADVANTAGE - The method uses high effective biocontrol Trichoderma strain, straw, wheat bran and other cheap materials in sterile conditions according to Good Manufacturing Practices. It produces soil microbial inoculum for preventing and treating soil borne disease of plants, promoting plant growth, increasing utilization ratio of fertilizer, and inducing strength and resistance to diseases of plants.
NOVELTY - An Artemisia annua leaves are crushed. Water and certain amount of enzyme are added to crushed leaves and thermostated. The solution is cooled and filtered. The filtrate is repeatedly extracted with an organic solvent, and dried. Organic solvent is added to the filter cake. The obtained solution is thermostated, cooled and filtered. The filter cake is washed with organic solvent and discarded. The obtained liquid and the filtrate are washed with sodium hydroxide, neutralized by washing with distilled water, concentrated, to obtain crude artemisinin.    USE - Extraction of artemisinin (claimed).    ADVANTAGE - The method enables efficient extraction of artemisinin with reduced impurities, and improved devices requiring low extraction rate by simple and environmentally-friendly process.    DETAILED DESCRIPTION - An Artemisia annua leaves are crushed. 2-20 Times the weight of water and a certain amount of enzyme are added to the crushed leaves and reacted at 30-60 degrees C for 30-120 minutes. The solution is cooled and filtered. The filtrate is repeatedly extracted with an organic solvent, dried and the cold cake is left to stand. 50-100 Times the weight of an organic solvent is added to the filter cake and reacted at 30-60 degrees C. The obtained solution is thermostated for 30-120 minutes, cooled and filtered. The filter cake is washed with organic solvent and discarded, to obtain combined filtrate and washing liquid. The liquid and the filtrate are washed with 2% sodium hydroxide, neutralized by washing with distilled water, concentrated under reduced pressure at 50 degrees C, to obtain crude artemisinin.
NOVELTY - An alcohol fuel comprises 10-15 wt.% fatty alcohol polyoxyethylene ether, 3-5 wt.% methyl tertiary butyl ether, 3-5 wt.% tertiary butyl alcohol, 2-5 wt.% isopropyl alcohol, 2-5 wt.% ethyl ether, 2-5 wt.% alkyl phenol polyoxyethylene ether, 2-5 wt.% 2,6-di-tert-butyl-p-cresol, 0.5-2 wt.% petroleum ether, 3-8 wt.% alkylamine, 0.5 wt.% dispersant, 0.5 wt.% alkali metal active agent, 0.5 wt.% isopropyl ether, 1-5 wt.% aliphatic ketone, 0.5-3 wt.% aliphatic ether, 0.5-3 wt.% metal salt, 0.3-2 wt.% ferrocene, 0.2-1.5 wt.% methanol.    USE - Alcohol fuel is used as gasoline.    ADVANTAGE - The alcohol fuel has favorable oil consumption and does not cause damages.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of alcohol fuel, which involves placing fatty alcohol polyoxyethylene ether, methyl tertiary butyl ether, tertiary butyl alcohol, isopropyl alcohol, ethyl ether, alkyl phenol polyoxyethylene ether, 2,6-di-tert-butyl-p-cresol, petroleum ether, alkylamine, dispersant, alkali metal active agent, isopropyl ether, aliphatic ketone, aliphatic ether, metal salt, and ferrocene in an autoclave, heating at 20-40 degrees C for 3-5 hours, adding methanol, circulating for 2-3 hours, leaving for 12 hours, and canning.
NOVELTY - Biogas production comprises (a) hydrolyzing the biomass in a hydrolyzer (2), (b) passing into a separator (3), in which the hydrolysed biomass is separated into a liquid fraction and a solid fraction, (c) supplying the liquid fraction again into the hydrolyzer, and (d) fermenting the solid fraction in a fermentor (4), and transferring into a final storage (6).    USE - The method is useful for biogas production.    ADVANTAGE - The method can be carried out in a cost efficient manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a biogas production device retrofit kit comprising at least one hydrolyzer and the upstream connected fermenter, where (a) the biogas device is retrofitted between the hydrolyzer and the fermenter by the separator, (b) the hydrolysis product from the hydrolyzer separates into the liquid and solid fraction, (c) the separator for the liquid fraction comprises a return line to the hydrolyzer, and (d) the separator for the solid fraction comprises a connecter to the fermenter.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic representation of the biogas plant.    Hydrolyzer (2)    Separator (3)    Fermentor (4)    Final storage (6)    Conditioning device (8)
NOVELTY - Synthesizing polymerized biomass gas for combustion comprises (i) collecting the poultry excrement and placing in a dehydration-alcoholization integrated tower to carry out non-pressure natural polymerization, (ii) conveying dehydrated-alcoholized excrement into a mixing tank through guide pipe, adding wood powder, rice straw powder, and wheat straw powder, and stirring to obtain biomass slurry, and (iii) adding chemical combustion improver in synthesized biomass slurry, and completing polymerization, collecting gas and slurry for combustion use.    USE - The method is useful for synthesizing polymerized biomass gas for combustion (claimed).    ADVANTAGE - The method has simple operation process and uses simple device, discharges less amount of sulfur dioxide without any harmful odor, thus it is environmentally friendly; and reduces the manufacturing cost. The biomass gas is convenient to transport and is safe.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of synthesizing process of polymerized biomass gas (Drawing includes non-English language text).
NOVELTY - The apparatus injects diluted solution with specific SCOD concentration in food wastage while controlling concentration at an acid fermenter (100). A degassing warmed water tank (300) is used for adding degassing water to the fermented output. The fermented output added with degassing water is provided to an anaerobic tank (200).    USE - Anaerobic absorption apparatus of organic waste such as food wastage and livestock excretion.    ADVANTAGE - The organic waste can be efficiently processed at reduced time. The productivity of the biogas can be maximized and the bad small generation of the processing water can be minimized. The water quality of the processing water flowed out can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for an anaerobic absorption method of organic waste.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic absorption apparatus of organic waste. (Drawing includes non-English language text)    Acid fermenter (100)    Anaerobic tank (200)    Degassing warmed water tank (300)    Warmed water control valve (320)    Settling tank (400)
NOVELTY - Device for fire safety of diesel fuel synthesis system comprises: (i) a technical co-solvent vehicle and its facilities to ensure that the moisture content is 50% methanol, a combustible alcohol and diesel oil to dissolve a solvent, (ii) micro-shear stirring vessel and equipment for refinement of water molecules, (iii) that is at high risk of low flash point fuel technology and its location directly on the designated co-solvent, synthesis and processing technology generations 0 # diesel, eliminating the high risk that low flash point fuel transport to and from the trouble and risk in the road.    USE - The device is useful in biological diesel oil manufacturing technology and social public security management (claimed).
NOVELTY - A non-targeted component-containing gas is contacted with liquid solvent stream. The contacted non-targeted component-containing gas is subjected to phase separation process, to obtain non-targeted component-containing solvent and partially purified gas stream. The partially purified gas stream is subjected to mass transfer process, to obtain wet gas product. The wet gas product is further subjected to phase separation process and non-targeted components are removed (10), to obtain purified gas.    USE - Removal of non-targeted components used for production of methane (claimed).    ADVANTAGE - The method enables removal of non-targeted components economically by a safe process without inspecting pressure vessels frequently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of methane.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram explaining removal of non-targeted components.    Removal of non-targeted components (10)    Gas or multi-phase fluid streams (12,14,16)    Phase separation apparatus (18)
NOVELTY - The device has a crushing mechanism connected with a material inlet of a slicing mechanism, belt conveyors and a rotary sieve. A drying mechanism is provided with a rotary feeding cylinder and a rotating hot-blast stove, where a discharging end of the rotary feeding cylinder is connected with the belt conveyors of the crushing mechanism. A granulating mechanism is connected with a discharge end of a packaging machine screening mechanism. The belt conveyors are connected with a cooling mechanism.    USE - Biomass particle production line device.    ADVANTAGE - The device has low energy consumption, high production efficiency and small occupation volume, and is convenient to transport and store.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a biomass particle production line device.
NOVELTY - Fidaxomicin is dissolved in solvent at room temperature, heated at 40-50 degrees C and stirred. The obtained solution is cooled at 0-20 degrees C, filtered, and crystallized for 2-48 hours to obtain cake. The obtained cake is dried at 40-50 degrees C under vacuum for 1-4 hours, to obtain crystalline fidaxomicin.    USE - Manufacture of crystalline fidaxomicin (claimed).    ADVANTAGE - The method enables manufacture of crystalline fidaxomicin by a simple and rapid process with uniform size, and excellent stability and storability, recycling of solvent, and is environmentally-friendly.
NOVELTY - Organic fertilizer comprises 15 pts. wt. pepper meal, 15 pts. wt. humic acid, 10 pts. wt. amino acid, 5 pts. wt. tobacco, 30 pts. wt. bacterial sludge, 10 pts. wt. starch residue, and 15 pts. wt. bentonite.    USE - Organic fertilizer used for crops e.g. potatoes and corns.    ADVANTAGE - The organic fertilizer improves the physicochemical properties of soil, is converted by microorganisms in soil into components, which can be readily absorbed by crops, increases the production efficiency of crops, and has reduced environmental pollution. It increases the yield of potatoes by more than 11% and increases the yield of corns by more than 27%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of organic fertilizer comprising weighing the raw materials, uniformly mixing to obtain mixed material, fermenting at 72 degrees C for 11 days, turning every other day, controlling the pH of the mixed material at 6-8, granulating, drying, and filtering to obtain the product.
NOVELTY - Extracting imperatorin involves selecting and crushing Angelica dahurica, extracting in presence of non-polar organic solvent, at 3-90 degrees C and the pressure of 0.5-1 MPa for 40-80 minutes in subcritical extraction kettle, decompressing and analyzing extract, dissolving with alkaline water, alkali water solution and chloroform for 3 times, collecting the chlorine layer, recycling chloroform, refluxing and dissolving the crystal by ethanol solution, crystallizing, drying to obtain the imperatorin.    USE - For extracting imperatorin (claimed).    ADVANTAGE - The method is simple and convenient to operate and, environment-friendly, and easy to realize industrial production.
NOVELTY - Purifying tannin involves activating ion exchange resin column by using ethanol, sodium hydroxide solution, and hydrochloric acid solution; heating tannin at 48-52 degrees C, stirring and dissolving, and adding ethyl acetate; then dropping tannin solution in the resin exchange column, extracting the liquid in container at normal pressure, then dissolving in sodium bicarbonate and ethyl acetate, distilling and recycling ethyl acetate; and drying residue in oven to obtain tannic acid having high purity.    USE - For purifying tannin (claimed).    ADVANTAGE - The method purifies tannin that has five time higher purity; is simple, economical, efficient, energy-saving, environment-friendly, and high yield.    DETAILED DESCRIPTION - Purifying tannin involves dropping ethanol 1-2 drops/second in an ion exchange resin column, then eluting salt water at speed of 1 drop/second for 2.5-3 hours; dropping a resin with sodium hydroxide solution having volume ratio of 1:4 at flow rate of 2 drops/second through the ion exchange resin layer for 2.5-3 hours, washing until pH of the outlet is 7.5-8; then adding resin and hydrochloric acid solution having volume ratio of 1:4 at speed of 2 drops/second in the column, and washing until the pH of the outlet solution is 5.5-6.5; heating tannin at 48-52 degrees C, stirring and dissolving, and adding ethyl acetate; then dropping tannin solution in the resin exchange column, extracting the liquid in container at normal pressure, then dissolving in sodium bicarbonate and ethyl acetate, distilling and recycling ethyl acetate; and drying residue in oven to obtain tannin having high purity.
NOVELTY - Extracting subcritical fluid osthole from buchtorm libanotis common cnidium fruit, involves: crushing common cnidium fruit as raw material, adding non-polar organic solvent, at 20-80 degrees C and at pressure of 0.3 to 1MPa and extracting for 30-60 minutes, to obtain extract; dissolving the extract in alkaline water, followed by decompressing and filtering the neutral precipitate, dissolving the precipitate in 95% of ethanol solution, followed by refluxing, crystallizing and drying to obtain osthole.    USE - For extracting subcritical fluid osthole (claimed) for relieving spasm, reduce blood pressure, and treating arrhythmia and enhancing immunologic function and antibacterial pesticidal effect.    ADVANTAGE - The method is simple and convenient, environment friendly, and is suitable for industrial production.
NOVELTY - A low-concentration oxygen-containing coal bed methane is extracted by (A) gas storage step, (B) compressing gas step, (C) gas purification process of the coal bed gas, (D) gas cooling step, (E) rectifying and separating gas, and (F) storage of obtained liquid in liquefied methane storage tank. The step (A) includes storing concentration of oxygen-containing coal bed gas in gas cabinet at 0.001-0.005 MPaG. The step (C) comprises removing mercury, desulfurizing, removing carbon dioxide and dehydrating.    USE - Method for extracting low-concentration oxygen-containing coal bed methane (claimed).    DETAILED DESCRIPTION - Low-concentration oxygen-containing coal bed methane is extracted by (A) gas storage step, (B) compressing gas step, (C) gas purification process of the coal bed gas, (D) gas cooling step, (E) rectifying and separating gas, and (F) storage of obtained liquid in liquefied methane storage tank. The step (A) includes storing concentration of oxygen-containing coal bed gas in gas cabinet at 0.001-0.005 MPaG. The step (B) comprises pressurizing the gas at 0.35-0.4 MPaG and lowering temperature of coal bed gas to 80 degrees C. The step (C) comprises removing mercury, desulfurizing, removing carbon dioxide and dehydrating. The step (D) comprises cooling purified gas to 140-160 degrees C, where coal bed gas and cool liquid mol fraction is not more than 15%. The step (E) comprises introducing cooled coal bed gas to rectification tower, liquefying and separating methane in coal, introducing liquefied methane into rectifying tower and reboiler, and performing evaporation and distillation.    DESCRIPTION OF DRAWING(S) - The drawing is a schematic block diagram illustrating a method for extracting low-concentration oxygen-containing coal bed methane. (Drawing includes non-English language text).
NOVELTY - This utility model claims a kind of new-type marsh gas treatment system is used for solving the problem that lacks an effective to produce a biogas kitchen garbage processing process and marsh gas treatment system is effectively used, by carrying out a series of processing to marsh gas and achieve good treatment and effective utilization of the marsh gas.
NOVELTY - Preparing conjugated linoleic acid involves: using stannate as catalytic agent, linoleic acid as raw material to prepare the conjugated linoleic acid.    USE - For preparing conjugated linoleic acid (claimed).    ADVANTAGE - The method prepares conjugated linoleic acid using catalyst which has high catalytic efficiency, is cheap and has stable performance, in simple post treatment, with low production cost, high production process which does not produce pollution.    DETAILED DESCRIPTION - Preparing conjugated linoleic acid involves: preparation of stannate under the protection of nitrogen at 300-40 degrees C for 2 hours; adding 0.011 mol/l linoleic acid to silane solution into reactor, then adding the solution total mass stannate, nitrogen for 10 minutes to remove oxygen in the reactor; isomerization reaction of reactant by heating and reacting for 6-24 hours at 180 degrees C; centrifuging and separating 1-20% catalyst of first step, and then molecular distillation to obtain conjugated linoleic acid.
NOVELTY - Preparation of (2S)-2-(4-(1-(2,4-diaminopteridin-6-yl)pent-4-yn-2-yl)benzamido)pentanedioic acid (Pralatrexate) (I) involves: hydrolyzing N-(4-(1-(2)-3,4-di-oxo-n-butyl)benzoyl)-L-glutamic acid alkyl ester (II) to obtain (2S)-2-(4-(6,7-dioxohept-1-yn-4-yl)benzamido)pentanedioic acid (IV); and cyclizing the (2S)-2-(4-(6,7-dioxohept-1-yn-4-yl)benzamido)pentanedioic acid (IV) using oxime such as 2,4,5,6-tetra amino-group (III) under suitable condition to obtain (I).    USE - For preparation of pralatrexate (claimed) used in the treatment of refractory peripheral T cell lymphoma.    ADVANTAGE - The method is simple, economical and environment-friendly, and is suitable for industrial production.    DETAILED DESCRIPTION - Preparation of (2S)-2-(4-(1-(2,4-diaminopteridin-6-yl)pent-4-yn-2-yl)benzamido)pentanedioic acid (Pralatrexate) (I) involves: hydrolyzing N-(4-(1-(2)-3,4-di-oxo-n-butyl)benzoyl)-L-glutamic acid alkyl ester of formula (II) to obtain (2S)-2-(4-(6,7-dioxohept-1-yn-4-yl)benzamido)pentanedioic acid (IV); and cyclizing the (2S)-2-(4-(6,7-dioxohept-1-yn-4-yl)benzamido)pentanedioic acid (IV) using oxime under suitable condition to obtain (I).    R=methyl, ethyl, propyl, isopropyl, butyl, isobutyl, tertiary butyl, or optionally substituted phenyl.
NOVELTY - The utility model claims a biomass fuel equipment technology field, especially relates to a kind of forming machine of the biomass fuel. A feeding hopper, a pelleting chamber and a power mechanism, a feeding hopper outlet is provided with a feeding chamber, wherein the feeding chamber is provided with a feeding auger, a feeding outlet is connected with pelleting room, the lower part is provided with a discharging port, a granulating chamber in the granulation chamber is equipped with granulating mechanism and cutting mechanism, mechanism, a feeding packing auger are respectively connected with a power mechanism, a granulating mechanism comprises an inner gear ring, an annular mould, a pressing roller, a pressing roller bracket and pressing roller main shaft, a mould is provided with an annular inner gear ring and the annular die cavity is provided with a pressure roller support frame, a press roller, a press roller is set at one end of press roller wheel, roller wheel is engaged with the inner gear ring, a pressing roller main shaft is fixed connected with is connected with the power mechanism in the centre of the pressing roller support frame, a pressing roller main shaft. This utility model can use the service life of the die extend annular pressing roller and more than 50%, and the forming efficiency is improved, the energy consumption can be reduced by more than 50%.
NOVELTY - Production of bio-char from crop straw using large scale field comprises building soil pyrolysis tank; drying straw in pyrolysis pool in soil; igniting straw for less than 5 minutes, carrying out complete combustion with oxygen, completely covering combustion zone with soil, extinguishing for less than 3 minutes; and covering soil for 2 hours.    USE - Method for producing bio-char from crop straw using large scale field (claimed).    ADVANTAGE - The bio-char has high uniform carbonization and carbonization degree, and low smoke amount.
NOVELTY - Production of biomass energy comprises crushing wood block, corn core, straw and agricultural livestock manure, and machine pressing into square block to prepare biomass; adding biomass into reciprocating pushing grate furnace for thermalization reaction, producing mixed gas, tar and wood vinegar; sending mixed gas into gas-liquid separator, separating tar and pyroligneous combustible gas, discharging combustible gas into air outlet; sending tar and wood vinegar into standing separation tank, cooling, standing and layering, separating, and collecting tar and wood vinegar.    USE - Method for producing biomass energy (claimed).    ADVANTAGE - The method has low cost.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of biomass energy production (Drawing includes non-English language text).
NOVELTY - Blast furnace slag particle and biomass particle direct contact reaction device comprises feeding device (10), reaction device (20), separating device (30) and gas purifying and collecting device (40). The feeding device is provided with discharge pipe. The reaction device bottom is provided with discharge opening, and at the top is provided with air outlet. The separating device is provided with blast furnace slag particle outlet (343) and biomass particle slag outlet (345).    USE - Blast furnace slag particle and biomass particle direct contact reaction device.    DETAILED DESCRIPTION - Blast furnace slag particle and biomass particle direct contact reaction device comprises feeding device (10), reaction device (20), separating device (30) and gas purifying and collecting device (40). The feeding device is provided with discharging pipe, and used for feeding blast furnace slag particles and biomass particles into reaction device. The reaction device bottom is provided with discharge opening, and at the top is provided with air outlet. The reaction device is used for mixing and performing contact reaction of blast furnace slag particles and biomass particles. The separating device is provided with blast furnace slag particle outlet (343) and biomass particle slag outlet (345).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of blast furnace slag particle and biomass particle direct contact reaction device.    Feeding device (10)    Reaction device (20)    Separating device (30)    Gas purifying and collecting device (40)    Blast furnace slag particle outlet (343)    Biomass particle slag outlet (345)
NOVELTY - Preparation of pharmaceutical dextran and levulose by dual enzyme immobilization coupled multistage membrane separation, comprises: co-immobilizing dextran sucrase and dextranase in sodium alginate microspheres to obtain dual enzyme-immobilized spheres; adding the dual enzyme-immobilized spheres into a sucrose solution used as a substrate to form an immobilized dual enzyme/sucrose reaction system; and directly obtaining the pharmaceutical dextran in the hyperfiltration membrane separation stage.    USE - The method is useful for preparing pharmaceutical dextran and levulose (claimed).    ADVANTAGE - The method has the advantages of lower cost, environment friendliness, high safety and high efficiency, is simple to operate, implements oriented adjustable production of high-quality pharmaceutical dextran with target molecular weight, and obtains the high-purity high-added-value levulose byproduct.    DETAILED DESCRIPTION - Preparing pharmaceutical dextran and levulose by dual enzyme immobilization coupled multistage membrane separation, comprises: co-immobilizing dextran sucrase and dextranase in sodium alginate microspheres to obtain dual enzyme-immobilized spheres; adding the dual enzyme-immobilized spheres into a sucrose solution used as a substrate to form an immobilized dual enzyme/sucrose reaction system; and after the reaction product is separated by a multistage membrane system composed of hyperfiltration membranes and a nanofiltration membranes, directly obtaining the pharmaceutical dextran in the hyperfiltration membrane separation stage, and obtaining the high-purity levulose solution in the last nanofiltration membrane separation stage, where the enzymes and macromolecular dextran contained in the trapped solution of the first-stage hyperfiltration membrane return to the immobilized dual enzyme/sucrose reaction system to participate in the reaction again, thus implementing cyclic utilization of the enzymes.
NOVELTY - Preparation of pharmaceutical dextran and levulose by dual enzyme coupled multistage membrane separation, involves: simultaneously adding dextran sucrase and dextranase into a sucrose solution used as a substrate to form a dual enzyme/sucrose reaction system; and after the reaction product is separated by a multistage membrane system composed of ultrafiltration membranes and a nanofiltration membranes, directly obtaining the pharmaceutical dextran in the ultrafiltration membrane separation stage, and obtaining the high-purity levulose solution in the last nanofiltration stage.    USE - The method is useful for preparing pharmaceutical dextran and levulose (claimed).    ADVANTAGE - The method has the advantages of lower cost, environment friendliness, high safety and high efficiency, is simple to operate, implements oriented adjustable production of high-quality pharmaceutical dextran with target molecular weight, and obtains the high-purity high-added-value levulose byproduct.    DETAILED DESCRIPTION - Preparation of pharmaceutical dextran and levulose by dual enzyme coupled multistage membrane separation, involves: simultaneously adding dextran sucrase and dextranase into a sucrose solution used as a substrate to form a dual enzyme/sucrose reaction system; and after the reaction product is separated by a multistage membrane system composed of ultrafiltration membranes and a nanofiltration membranes, directly obtaining the pharmaceutical dextran in the ultrafiltration membrane separation stage, and obtaining the high-purity levulose solution in the last nanofiltration membrane separation stage, where the enzymes and macromolecular dextran contained in the trapped solution of the first-stage ultrafiltration membrane return to the dual enzyme/sucrose reaction system to participate in the reaction again, thus implementing cyclic utilization of the enzymes.
NOVELTY - A kind of kitchen garbage carbonization device, especially is carried out by use of heating device and the kitchen garbage cracking device to reuse the device. It is opening on the upper part of the shell, the upper part of the shell is a cover body, the lower part is a heating device, the heating device is installed on the upper part cracking device, heating device for heating cracking device, cracking device is a stirring device, the rotating shaft of the stirring device is connected with the cover body, the lower end of the rotating shaft is provided with a stirring paddle, the lower part of the shell is a discharging port, a discharging port connected with carbonization device makes full use of the kitchen garbage, the kitchen garbage is a renewable resource.
NOVELTY - The equipment has a sterilizer (100) which is used for sterilizing the livestock excretions, to remove the harmful material and bad smell of excretions. A separator (200) is used to separate a solid from liquid. A dehydration unit (300) is used to dehydrate the excretions, to lower the water content in excretions. The contaminated gas ejected from tub portion (710) is passed inside dryer. The dryer (700) is used for applying heat in livestock excretions molded product, to dry the product for manufacturing solid fuel. A crusher is used to crush the fuel stored in storage unit (800).    USE - Equipment for making solid fuel using livestock excretions such as pig ordure and cow dung.    ADVANTAGE - The livestock excretions can be efficiently dried and the solid fuel of the high efficiency can be manufactured. The livestock excretions drying efficiency and energy efficiency of the equipment can be improved by recycling the manufactured solid fuel in-line. The exhaust gas generated in-line is recycled. The solid economy effect can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the equipment for making solid fuel using livestock excretions. (Drawing includes non-English language text)    Sterilizer (100)    Separator (200)    Dehydration unit (300)    Dryer (700)    Tub portion (710)    Storage unit (800)
NOVELTY - A production device for oxygen-rich micro-emulsified blended biodiesel is disclosed. The device comprises a housing (1) inside which a vertical stirrer (2) is provided. The vertical stirrer (2) is rotated by a power source. The shaft of the vertical stirrer (2) is disposed with a flat and straight stirring paddle (5) or a paddle-like rotor blade. At the lower part of the shaft of the vertical stirrer (2), a turbine or a circular curved rotor (6) is disposed. The top part of the housing (1) is disposed with more than one material inlets (8) and each material inlet (8) is connected to a quantitative feeding device (9) through a pipe (17). At the lower part of the housing (1), a finished product outlet (12) is disposed. At the top part of the housing (1), there is an opening offering oxygen-rich water supply. This method includes the following steps: (1) Input the crude biodiesel into the emulsified biodiesel plant, then switch on stirring system. After that, add National III Standard Diesel and stir for 5 min. (2) Add the hydrophilic agent and stir for 1 min to 15 min. (3) Add butanol and isopentane, then continue to stir the mixture indirectly for 15min. (4) Add the oxygen-rich water, then stir for 15 min. wait and observe the emulsified oil for a certain period of time until it becomes clean, transparent and with no stratification. The finished product is produced.
NOVELTY - A carbon source and a silicon source are placed in a crucible along with a growth substrate. The crucible is placed in a furnace, heated, sintered, and cooled to obtain graphite paper, graphite sheet, glass plate, or carbon fiber based silicon carbide nanowire film. The film is used as working electrode, platinum sheet metal is used as counter electrode, silver/silver ion electrode is used as reference electrode, and dilute sulfuric acid is used as electrolyte, and catalytic decomposition of water is carried out to obtain silicon carbide nanowire thin film.    USE - Preparation of silicon carbide nanowire thin film based on hydrogen production by photoelectric catalytic decomposition of water (claimed).    ADVANTAGE - The method enables efficient, simple, economical, environmentally-friendly and uniform growth of silicon carbide nanowire thin films, without peeling off of substrate, with energy conservation effect, by using easily available raw materials.    DETAILED DESCRIPTION - A carbon source and a silicon source are placed in a high-purity graphite crucible, and graphite paper, graphite sheet, glass plate, or carbon fiber are placed in the crucible as silicon carbide nanowire growth substrate. The crucible is placed in a high-temperature furnace, heated to 1400-1700 degrees C, thermally sintered for 1-10 hours, and cooled along with the furnace to room temperature to obtain graphite paper, graphite sheet, glass plate, or carbon fiber based silicon carbide nanowire film. The thin film is used as working electrode, platinum sheet metal is used as counter electrode, silver/silver ion electrode is used as reference electrode, 0.1M dilute sulfuric acid is used as electrolyte, and a voltage of 0-3 V is applied, and catalytic decomposition of water is carried out to obtain silicon carbide nanowire thin film by hydrogen production.
NOVELTY - A hydrogen thermal cracking method involves utilizing 5-15% biomass raw material, performing pyrolysis of the biomass raw material, and carrying out thermal cracking at 350-400 degrees C.    USE - Method for performing hydrogen thermal cracking process.    ADVANTAGE - The method enables performing hydrogen thermal cracking process with high quality.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for performing hydrogen thermal cracking process.'(Drawing includes non-English language text)'
NOVELTY - A diesel oil composition comprises base diesel oil, and additive comprising Mannich base obtained by reacting alkylphenol, aldehyde and piperazine polyamine. The base diesel oil contains biodiesel.    USE - Diesel oil composition (claimed).    ADVANTAGE - The diesel oil composition has improved oxidation stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for improving the oxidation stability of biodiesel oil, which involves adding additive to base oil.
NOVELTY - A gas phase alcoholysis method involves (1) performing pretreatment on raw materials, (2) performing hydrolysis, (3) performing gas phase alcoholysis in which acid-base catalyst is not used and gasified methanol steam is uniformly contacted with fatty acid to perform gas phase alcoholysis on fatty acid, and (4) distilling.    USE - A gas phase alcoholysis method for manufacturing biodiesel (claimed).    ADVANTAGE - Preparation process is low-cost, not strict in raw material requirements, suitable for acid oil, swill-cooked dirty oil, and catering waste oil, suitable for national conditions, high in yield, and simple in process operation, realizes automatic control and totally closed operation of system, achieves zero waste gas and wastewater discharge, has stable and reliable product quality, and reaches various index standard.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for esterification column comprising barrel, head, and skirts in which head mounted on bottom of cylinder is fixed, skirts set is at bottom of cylinder, head around position of lower cylinder is installed in methanol vapor feed intake, first discharge opening is installed at bottom of cylinder, and upper portion of cylinder is attached to 2nd discharge port.    DESCRIPTION OF DRAWING(S) - The drawing shows an invention craft flow graph of gas phase alcoholysis method. (Drawing includes non-English language text).
NOVELTY - The reformer has a fuel reforming portion that includes an indirect heating portion (250) for heating the inner portion of a hydrogen component extractor. The hydrogen component extractor is arranged for removing the rest gas component from the gas. A gas generation portion is arranged for generating the gas. A direct heating portion (240) is provided for directly heating up the gas generation portion. The inner portion of one side of the hydrogen component extractor is vacant.    USE - Fuel reformer of fuel cell system (claimed).    ADVANTAGE - The fuel reformer is directly heated up using the direct heater so as to reduce the time reaching the starting temperature. The starting temperature can be stably controlled. The deterioration of the catalyst is prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fuel reformer. (Drawing includes non-English language text)    Fuel reformer (210)    Water gas shift reactor (220)    High temperature shift reactor (221)    Direct heating portion (240)    Indirect heating portion (250)
NOVELTY - The system has oxygen-hydrogen mixture gas purifier (7) that is provided for purifying electrolyte from oxygen-hydrogen mixture gas generated in oxyhydrogen gas generator (1). The generator is supplied with electrolyte and generates oxygen-hydrogen mixture gas. The filter is used for filtering out impurity included in electrolyte supplied from supply of water circle. The purified water in internal space is connected with mixing gas inlet port and mixing gas outlet port of refining units (71-77). The feeding line (78) is provided for supplying oxygen-hydrogen mixture gas to refining unit.    USE - System for generating mixed gas of hydrogen and oxygen used in mechanism of car.    ADVANTAGE - The oxyhydrogen gas generator can minimize the degradation of the oxygen-hydrogen mixture gas. The system can minimize the damage of the equipment by removing the electrolyte included in the oxygen-hydrogen mixture gas. The oxygen-hydrogen mixture gas purifier collects the electrolyte included in the oxygen-hydrogen mixture gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view illustrating the process of refining oxygen-hydrogen mixture gas in oxygen-hydrogen mixture gas purifier. (Drawing includes non-English language text)    Oxyhydrogen gas generator (1)    Oxygen-hydrogen mixture gas purifier (7)    Refining units (71-77)    Feeding line (78)    Backflow prevention valve (781)
NOVELTY - This utility model claims a kind of marsh gas circulating anaerobic reactor, belonging to the technical field of sewage treatment, wherein the main structure is composed of a shell, a water inlet, a water outlet, a marsh gas, marsh gas circulating stirring device, a marsh gas compressor, a marsh gas pipe, separating module, wherein the shell is a closed cylindrical tank body, the bottom side wall of the tank body is provided with a water inlet, the top of the side wall is provided with a water outlet, the top of the upper side is provided with a marsh gas outlet, the inner tank body is provided with a biogas circulation stirring device is connected with the marsh gas compressor, a marsh gas compressor in the tank body, and the inlet is connected with a marsh gas pipe is connected with the marsh gas inlet, the upper part of the tank body is provided with a separation module, which is connected with the water outlet, the utility model is compared with the traditional anaerobic fermentation tank, greatly optimizing the mass transfer effect and improves the volume load and shortens the residence time, reduces the energy consumption, reduces the floor, especially suitable for high SS and anaerobic treatment of high oil organic sewage.
NOVELTY - Producing androstenedione comprises inoculating yeast strain to a double liquid phase in a culture medium, keeping a certain temperature, adding plant phytosterin and then stirring and fermenting by membrane separation technology to obtain the androstenedione (AD) solution and then concentrating and decoloring by active carbon, filtering the mixture and then concentrating, re-crystallizing and drying in vacuum, where the purity of the crystal AD is more than 99%.    USE - The method is useful for producing androstenedione (claimed).    ADVANTAGE - The method simply produces the androstenedione with high conversion rate and low production cost in an eco-friendly manner.
NOVELTY - A condensation reaction is carried out on 4-((4,4-dimethoxy-3-hydroxy)butyl)benzoic acid and L-glutamic acid diester, to obtain 4-((4,4-dimethoxy-3-hydroxy)butyl)benzoyl-L-glutamic acid diester. Halogenation and acidolysis are carried out on obtained compound, to obtain 4-((4-oxo-3-halogenated) butyl) benzoyl-L-glutamic acid diester (V). Cyclization and basic hydrolysis are carried out on the intermediate (V) and 2,4-diamino-6- hydroxypyrmidine (VI), to obtain 2-((4-(2-(2-amino-4-oxo-3H,4H,4aH,7H,7aH-pyrrolo(2,3-d)pyrimidin-5-yl)ethyl)phenyl)formamido)pentanedioic acid.    USE - Preparation of pemetrexed (claimed).    ADVANTAGE - The pemetrexed diacid is economically prepared without polluting the environment, by a simple method.
NOVELTY - The device has a stainless steel filtering screen whose periphery is fixed with a purifying cylinder wall. An atomized sprayer is connected with a water inlet branch pipe through a water inlet main pipe and a water spraying pump. The pump is connected with a suction pipe that extends into a water storage tank. A connecting pipe passes through a purifying cylinder for purifying gas that is passed through a gas outlet. A fuel gas heating device burns the gas through an inlet passage. A gas-water bath purifying device is connected with a pipeline.    USE - Tail gas purifying device.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of a tail gas purifying device.
NOVELTY - A natural gas synthesizing method involves desulfuring and decarburizing synthetic gas, and increasing methane concentration to greater than or equal to 95%. Raw materials are filled in a methanation reactor to perform multistage methanation reaction. The gas released from the methanation reaction is entered into a heat exchanger to perform multistage heat recovery process. Saturated steam is obtained. The reactor inlet is filled with feed gas. Product gas is dehydrated, and methanation catalyst reaction is carried out. Passivation process is performed on the catalyst, where the product gas is methane.    USE - Method for synthesizing natural gas from synthetic gas.    ADVANTAGE - The method enables synthesizing natural gas with strong operability and wide application prospect.
NOVELTY - High thermal anti-corrosion alcohol-based fuel comprises 80-95 wt.% alcohol, 2-8 wt.% combustion-supporting agent, 0.01-0.2 wt.% corrosion inhibitor and 0.1-1 wt.% safety stabilizer.    USE - High thermal anti-corrosion alcohol-based fuel.    ADVANTAGE - The fuel is safe, saves energy and environment-friendly.
NOVELTY - Preparing rivaroxaban intermediate 5-chlorothiophene-2-carboxylic acid comprises reacting 5-chlorothiophene-2-formaldehyde in alkaline aqueous solution of sodium hypochlorite.    USE - The method is useful for preparing rivaroxaban intermediate 5-chlorothiophene-2-carboxylic acid (claimed).    ADVANTAGE - The method: is environmentally-friendly; has mild reaction conditions; is inexpensive and simple; produce product with high yield and purity; overcomes defects of current technology; has simple post-processing operation; and is suitable for modern industrial mass production.
NOVELTY - Human waste in rural schools is converted to clean energy and organic fertilizer by drawing waste from rural toilet waste tank (1) to tower digester (4) using sewage pump (2) to generate biogas, carrying out self-gravity organic ferment in above ground level tower digester, and discharging organic environment-friendly fertilizer from tower digester.    USE - Conversion of human waste in rural schools to clean energy and organic fertilizer (claimed).    ADVANTAGE - The method is environment-friendly and eliminates human waste sludge.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for device for converting human waste in rural schools to clean energy and organic fertilizer comprising which comprises water conveying pipeline (3) connecting toilet waste tank (1) and bottom of sewage pump (2), tower digester (4) connected to sewage pump outlet by water conveying pipeline, gas tube (5) connecting switch (6) and tower digester, gas-water separator (7), air bag (8), air pressure gauge (9), controller (10), booster pump (11), and branched gas tube to rural school cafeteria gas (12) and working gas (13).    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic diagram of the device for converting human waste in rural schools to clean energy and organic fertilizer. (Drawing includes non-English language text).    Toilet waste tank (1)    Sewage pump (2)    Water conveying pipeline (3)    Tower digester (4)    Gas tube (5)    Switch (6)    Gas-water separator (7)    Air bag (8)    Air pressure gauge (9)    Controller (10)    Booster pump (11)    Rural school cafeteria gas (12)    Working gas (13)
NOVELTY - Biological oxidation and high temperature pyrolysis reaction kettle comprises a kettle body including an insulating layer, a kettle wall, and an insulating layer at the outer wall of the kettle. The inner cavity of the kettle extends to form multiple stirring edges. The height of the stirring edge is 1/4 to 1/2 of the kettle body radius. The stirring edge and the inner side of the kettle wall are provided with a heat conducting pipe. The stirring edge and the inner side of the kettle wall are provided with an integrated air outlet cavity for flowing superheated vapor flow.    USE - Used as a biological oxidation and high temperature pyrolysis reaction kettle.    ADVANTAGE - The kettle enhances heat energy utilization efficiency; uniformly heats the biomass in the kettle body; adopts feeding-discharging control method of the reaction kettle; and reduces the use of kettle body sealing equipment, and lowers technical cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for feed and discharge controlling method of the biological oxidation and high temperature pyrolysis reaction kettle, comprising rotating the kettle during feeding using the power device in a clockwise direction and feeding the biomass through the material exchange interface when the kettle body rotates clockwise by the stirring edge, and rotating the kettle during discharging using the power device in an anticlockwise direction and discharging the processed material through the material exchange interface when the kettle body rotates anticlockwise by the stirring edge.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic representation of the biological oxidation and high temperature pyrolysis reaction kettle.
NOVELTY - Biodiesel is prepared by performing catalytic reduction on fatty acid triglyceride oils.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - Preparation of biodiesel is environment-friendly and has no waste discharge, high reduction rate, and low cost, and metal catalyst can be recycled and reused.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for mixed alcohol biodiesel containing diesel oil pour point depressant.
NOVELTY - The system has heat supply unit (30) that supplies heat to the hydrolysis and sterilization unit included in the organic waste after supplying organic waste to the hydrolysis and sterilization unit (10). An anaerobic digestion unit (20) is digested with anaerobic and sterilization unit by passing rough organic waste by the anaerobic digestion unit or the hydrolysis and sterilization unit.    USE - System for sterilizing and collecting high-temperature hydrolysis for biogas production.    ADVANTAGE - The energy efficiency using the heat transmission through in-line thermal cycling process can be improved effectively while processing the biogas production at the high temperature so as to heighten the effectiveness of the production. The manufacturing cost of the sterilizing and collecting system can be improved effectively. The thermal transfer efficiency through the heat transfer process can be improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for sterilizing and collecting high-temperature hydrolysis for the biogas production.    DESCRIPTION OF DRAWING(S) - The drawing shows the block diagram of the system for sterilizing and collecting high-temperature hydrolysis for biogas production.(Drawing includes non-English language text)    Hydrolysis and sterilization unit (10)    Anaerobic digestion unit (20)    Heat supply unit (30)    Heat transfer element (40)    Heat transfer elements (410,420)
NOVELTY - The drier has a carbonization furnace (10) formed in the grain drier portion (1a). A turbo cleaner (70) is set to collect dust in a drying tank (60), when the hot air is supplied to drying tank. A hot air pipe (40) is connected to the drying tank, for ejecting the hot air of the high temperature flowing from a lead portion (30) formed in the rear end of the hot air pipe. A temperature controller (50) is formed in the leading end of the hot air pipe, to control the temperature of the hot air in the hot air pipe, when synthetic gas in furnace is ejected to outside portion.    USE - Drier for drying rice husks using synthesis gas of carbonization system, installed in agricultural industry.    ADVANTAGE - The energy utilization rate of the drier can be improved. As the need for using oil burner in the grain drier is eliminated, the cost of the grain drier can be reduced. The environment-friendly grain drier can be comprehensively implemented. As the discharge temperature of hot air is ejected from the drying tank, the amount of the outside air can be controlled by the hot air pipe. Hence the inner portion of the drying tank is easily maintained with the optimal temperature. The damage of the grains by the hot air of high temperature can be prevented. The grains can be dried to the uniform temperature by eliminating the temperature deviation of the waste heat.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the drier.    Drier portion (1a)    Carbonization furnace (10)    Lead portion (30)    Hot air pipe (40)    Temperature controller (50)    Drying tank (60)    Turbo cleaner (70)
NOVELTY - Method for preparing gamma -aminobutyric acid by biotransformation, involves using glutamate dicarboxylase variants with glycerol as substrate.    USE - The method is useful for preparing gamma -aminobutyric acid by biotransformation which is used for producing biodiesel.    ADVANTAGE - The method is cost-effective and environmentally-friendly.
NOVELTY - Preparing plant medicine comprises taking garlic bulbs, fruit of Litsea cubeba and onion bulbs, as raw material, crushing the raw material into small blocks, adding water for 10 times, stirring and soaking at normal temperature for 10 hours, carrying out volatile oil measurement, extracting the raw material, adding 30% of volatile oil and an anhydrous sodium sulfate, filtering the raw materials, mixing the raw material extracts in the ratio of 1:1:1, mixing 5 pts. wt. of the volatile oil, adding 10-80 wt.% of an alcohol, and stirring and mixing to obtain the mixed solution.    USE - The method is useful for preparing plant medicine, which is useful for preventing tobacco aphid (claimed).    ADVANTAGE - The method safely and simply prepares the plant medicine with less toxicity and without pollution, thus improving production quality of tobacco leaves.    DETAILED DESCRIPTION - Preparing plant medicine comprises taking part of raw material comprising garlic bulbs, fruit of Litsea cubeba and onion bulbs, crushing the raw material into small blocks, adding water for 10 times, uniformly stirring, soaking at normal temperature for 10 hours, carrying out volatile oil measurement, extracting the raw material by adding 30% of volatile oil and anhydrous sodium sulfate according to the ratio of 1:1:1, standing for overnight, filtering the raw material, uniformly mixing the raw material to obtain a volatile oil solution, mixing 5 pts. wt. of the volatile oil, adding 10-80 wt.% of an alcohol, and stirring and mixing to obtain the mixed solution.
NOVELTY - A blue algae fertilizer preparing method mixing blue algae with biomass charcoal to obtain a blue alga-biomass charcoal mixture, and carrying out aerobic composting of the blue alga-biomass charcoal mixture in a constant-temperature and constant-humidity incubator to obtain the blue alga compost, where the blue algae-biomass carbon mixture is present at concentration of 50-80%, with the pH value of 8.0-9.5, the culturing box is heated at 30-60 degrees C.    USE - Method for preparing blue algae fertilizer.    ADVANTAGE - The method enables reducing the loss of ammonium nitrogen and total nitrogen in the blue alga compost composting process, and improving the seed germination index of mixed compost, in a simple, safe, and environmentally friendly manner.
NOVELTY - A raw fertilizer preparing method involves taking dried crop straw, monosodium glutamate, bran, cotton vegetable phellodendron, mildew feed, canal mud, organic fertilizer hametz, biological enzyme, compound additive and compound amino acid. The raw materials are formulated and crushed. Bioenzyme and proper amount of water is mixed. Compound additive is added and mixed uniformly. Water is added and blended to obtain organic fertilizer particle. Amino acid formulation is added to the drum. The organic fertilizer particle is dried to obtain the raw fertilizer particles.    USE - Method for preparing raw fertilizer.    ADVANTAGE - The method enables preparing raw fertilizer with absorption property, better buffer performance, high fertilizer efficiency and high yield.    DETAILED DESCRIPTION - A raw fertilizer preparing method involves taking 25-30 wt.% dried crop straw, 5 wt.% monosodium glutamate, 5 wt.% bran, 5 wt.% cotton vegetable phellodendron, 5 wt.% mildew feed, 5 wt.% canal mud 12 wt.% organic fertilizer hametz, 1 wt.% biological enzyme, 1 wt.% compound additive and 1 wt.% compound amino acid. The raw materials are formulated and crushed. The raw materials are placed in fermenting tank. Bioenzyme and proper amount of water is mixed. The tank is sealed to fermented at 50-60 degrees C for 16-18 days. Compound additive is added and mixed uniformly. Water is added and blended to obtain organic fertilizer particle. The organic fertilizer particle is placed in coating drum. Amino acid formulation is added to the drum. The organic fertilizer particle is sent to a drier to dry at 25-30 V for 2-2.5 hours to obtain the raw fertilizer particles.
NOVELTY - A biological organic fertilizer comprises 30-65 wt.% livestock and poultry manure, 10-30 wt.% oil crop seed cake dreg of edible oil, 0.05-0.3 wt.% biological active strains and the balance of danty.    USE - Biological organic fertilizer for various crops and fruit trees through reasonable-formula fertilizer application.    ADVANTAGE - The fertilizer has increased organic matter content, humic acid content, amino acid content and biological flora content through microbial fermentation, so that the absorption and utilization ratio of nutrients such as ammonia, phosphorus, potassium and various trace elements of the fertilizer is increased and the utilization ratio of the fertilizer is increased, and can be prepared in convenient, and cost effective manner.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing biological organic fertilizer.
NOVELTY - A microbial organic fertilizer is obtained by performing fermentation on raw materials using inoculated bacteria liquid, where the inoculated bacterial liquid comprises brewer yeast, Bacillus subtilis, Lactobacillus fermenti and EM bacteria, the raw materials comprise human and animal excreta, crop straw, banana skin and Chinese medicine compound, and the Chinese medicine compound comprises Rhizoma polygonati, Chinese yam, Codonopsis pilosula, Antifebrile dichroa, Celastrus angulatus, Areca catechu and Andrographis paniculata.    USE - Microbial organic fertilizer for improving a soil structure.    ADVANTAGE - The organic fertilizer has better fertilizer efficiency and simple and eco-friendly preparation effect.    DETAILED DESCRIPTION - A microbial organic fertilizer is obtained by performing fermentation on raw materials using inoculated bacteria liquid, where the inoculated bacteria liquid comprises 45 wt.% brewer yeast, 35 wt.% Bacillus subtilis, 13 wt.% Lactobacillus fermenti and 7 wt.% EM bacteria, the raw materials comprise 48 wt.% human and animal excreta, 38 wt.% crop straw, 12 wt.% banana skin and 2 wt.% Chinese medicine compound, the inoculation amount of the inoculated bacteria liquid is 1 wt.%, and the Chinese medicine compound comprises 3 pts. wt. Rhizoma polygonati, 6 pts. wt. Chinese yam, 3 pts. wt. Codonopsis pilosula, 3 pts. wt. Antifebrile dichroa, 8 pts. wt. Celastrus angulatus, 3 pts. wt. Areca catechu and 3 pts. wt. Andrographis paniculata, and the microbial organic fertilizer is a fermentation product with moisture content of 15-20%. INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing microbial organic fertilizer    (2) a method for applying microbial organic fertilizer.
NOVELTY - A Chrysanthemum trace element content improving method involves preparing a trace element-rich organic fertilizer by mixing chromium(III) chloride, sodium selenite, magnesium sulfate heptahydrate, zinc sulfate and an organic liquid fertilizer, and fermenting the obtained mixture, and preparing a trace element-rich organic solvent. Chrysanthemum fertilization process is performed by applying the organic fertilizer, and uniformly spraying the organic solvent on leaves of Chrysanthemum in an early bud period to obtain a trace element-rich Chrysanthemum.    USE - Method for improving a trace element content of a Chrysanthemum.    DETAILED DESCRIPTION - A Chrysanthemum trace element content improving method involves preparing a trace element-rich organic fertilizer by mixing chromium(III) chloride, sodium selenite, magnesium sulfate heptahydrate, zinc sulfate and an organic liquid fertilizer, and fermenting the obtained mixture at 26-35 degrees C for 3-5 weeks to obtain the trace element-rich organic fertilizer. Trace element-rich organic solvent is prepared by mixing the chromium(III) chloride, the sodium selenite, the magnesium sulfate heptahydrate, the zinc sulfate and the organic liquid fertilizer, stirring the obtained mixture, and fermenting the mixture at 26-35 degrees C for 2-4 weeks to obtain the trace element-rich organic solvent. Chrysanthemum fertilization process is performed by applying 35-50 kg trace element-rich organic fertilizer per hectare, diluting the trace element-rich organic solvent by water, and uniformly spraying the diluted trace element-rich organic solvent on leaves of Chrysanthemum in an early bud period to obtain a trace element-rich Chrysanthemum with chromium content of 18-52 mu g chromium/g, selenium content of 14-50 mu g selenium/g, magnesium content of 82-126 mg magnesium/g and zinc content of 5-16 mg zinc/g.
NOVELTY - Black fungus cultivation method involves providing raw material that comprises 40 - 50% bamboo scrap, 30 - 40% slag, 12 - 20% lime, 2% gypsum, 1% salt and 1% dry matter.    USE - Black fungus cultivation method (claimed).    ADVANTAGE - The method enables providing high fungi permeability, better water permeability, quick growth speed, shortened full bag time, rational carbon and nitrogen content, high nutrient effect, nutrient balance enough nutrient supply, and improving yield and quality of a product. The bamboo replaces bran with slag that widens planting raw material, and has reduced production cost. The fungus has high social benefit, and changes waste into valuable resource, thus saving energy and reducing emission.
NOVELTY - A natural warming-type organic waste treatment equipment has a fermentation tank provided with a stirring device that is provided with a front bracket, a back bracket, a stirring shaft and a spiral belt. Ends of the tank are provided with a feeding port and a discharging port. The stirring shaft is arranged with a stirring rod. The stirring device is operated at a frequency and provided with the twice-advancing twice-retreating stirring turning process for 6 minutes plus minus 0.5 hours until the fermentation tank is charged the next time.    USE - Natural warming-type organic waste treatment equipment.    ADVANTAGE - The equipment prevents need of natural gas and electricity, and treats organic waste in a convenient and effective manner.    DETAILED DESCRIPTION - A natural warming-type organic waste treatment equipment has a fermentation tank provided with a stirring device that is provided with a front bracket, a back bracket, a stirring shaft and a spiral belt. Ends of the tank are provided with a feeding port and a discharging port. The stirring shaft is arranged with a stirring rod. The stirring device is operated at a frequency that the stirring device carries out twice-advancing twice-retreating stirring turning when the fermentation tank is charged and is provided with the twice-advancing twice-retreating stirring turning process for 6 minutes plus minus 0.5 hours until the fermentation tank is charged the next time. An INDEPENDENT CLAIM is also included for a method for treating organic waste, which involves crushing and dehydrating organic waste into the fermentation tank, obtaining organic mixture, carrying out feeding back turning stirring device for 4-8 days, placing the mixture in the discharging port, and adding primary organic fertilizer.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of a natural warming-type organic waste treatment equipment.
NOVELTY - An organic fertilizer production method involves mixing organic waste with separated livestock and poultry excrement. High-efficient microbial fermentation bacteria are added with the mixture. The mixture is placed into a solar energy bio fermentation tank to carry out primary fermentation. The gas generated during the fermentation process is introduced into a gas purifying device through a gas collecting pipe. Secondary fermentation is carried out on the semi-fermented mixture followed by crushing and sieving the fermented material to obtain finished product.    USE - Method for producing organic fertilizer.    ADVANTAGE - The method enables producing the organic fertilizer with high fermentation efficiency.    DETAILED DESCRIPTION - An organic fertilizer production method involves carrying out solid-liquid separation on livestock and poultry excrement, and mixing organic waste with the separated livestock and poultry excrement. High-efficient microbial fermentation bacteria are added with the mixture. The mixture is placed into a solar energy bio fermentation tank to carry out primary fermentation for 5-12 days. The gas generated during the fermentation process is introduced into a gas purifying device through a gas collecting pipe. Secondary fermentation is carried out on the semi-fermented mixture for 12-30 days. Ferrous sulfate solution is placed in a crystallization vessel as spraying absorption liquid and crystallized followed by crushing and sieving the fermented material to obtain finished product.
NOVELTY - The system has an import field (10) in which the food waste and sludge are taken-in from a vehicle. An object processing unit processes the processing object in the import field from the upward direction to the downward direction. A bad smell exhausting unit discharges the bad smell to a predetermined place. A bad smell leak cut-out unit (40) blocks and collects the bad smell of the processing object. A waste-water treatment unit (50) processes the waste water generated during the processing of the processing object.    USE - System for treating food waste and sludge such as animal manure and plants waste.    ADVANTAGE - As the need for transfer device for the movement of the processing object is not required, the installation space of the system is reduced and the cost of the system is reduced. The leakage of stench or bad odor is prevented reliably.    DESCRIPTION OF DRAWING(S) - The drawing shows a perspective view of the food waste and sludge processing system.    Import field (10)    Fermenter (25)    Storage tank (26)    Bad smell leak cut-out unit (40)    Waste-water treatment unit (50)
NOVELTY - A high nitrogen-containing composite microbial fertilizer comprises 10-33 wt.% urea, 5-20 wt.% microbial strain agent, 10-40 wt.% organic materials, and 30-70 wt.% water.    USE - High nitrogen-containing composite microbial fertilizer.    ADVANTAGE - The method transforms and fixes active small molecular amide nitrogen to slow-release macromolecular organic nitrogen through biochemical reaction of microorganisms, improves content of nitrogen nutrient and utilization rate of urea, guarantees activity and amount of microorganisms, and reduces pollution on natural environment caused by easy loss of nitrogen. The fertilizer is a novel, long-acting, and environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of high nitrogen-containing composite microbial fertilizer by mixing raw materials, adding to fermentation container while stirring, fermenting for 15-25 days to obtain a lot of gas, detecting ammonium nitrogen concentration to less than 2 wt.%, adding potassium dihydrogen phosphate, and mixing to obtain liquid or solid dosage forms of fertilizer.
NOVELTY - O-veratraldehyde is synthesized by combining Lewis acid catalyst and veratrole, adding glyoxylic acid and hydrochloric acid, performing substitution reaction to form 2,3-dimethoxybenzyl chloride, cooling, adding water and organic solvent, letting mixture stand to stratify, extracting organic phase, adding methenamine and organic acids, performing oxidation reaction, washing with water, letting mixture stand to stratify, extracting organic phase, concentrating under reduced pressure, and cooling.    USE - Synthesis of o-veratraldehyde (claimed).    ADVANTAGE - Synthesis of o-veratraldehyde is environment-friendly and easy to operate, and has mild conditions, low energy consumption, high yield, and raw materials that are easy to obtain, and o-veratraldehyde has good quality.    DESCRIPTION OF DRAWING(S) - The drawing shows an image of the reaction route of the synthesis of o-veratraldehyde. (Drawing includes non-English language text).
NOVELTY - Preparation of antimalarial artemisinin drug comprises artemisinic acid as starting raw material, generating dihydro acid, reducing to obtain dihydro peroxide, oxidizing, rearranging under acid catalysis, adding in organic solvent under oxygen atmosphere by catalytic rearrangement and purifying to obtain artemisinin. The organic solvent is common organic solvent, and acid is Bronsted acid or Lewis acid, at mol ratio of acid and dihydro peroxide acid derivative of 1:1-100.    USE - Method of preparation of antimalarial artemisinin drug (claimed).    ADVANTAGE - The method is easy to obtain, environment-friendly, simple, and has low cost, short synthetic route, high reaction selectivity, high total yield, and is suitable for industrial production.
NOVELTY - 2-Hydroxy-4-amino-5-methylpyridine heterocyclic compound is new.    USE - 2-Hydroxy-4-amino-5-methylpyridine heterocyclic compound used for synthesizing omeprazole compound (claimed).    ADVANTAGE - The simple and environment-friendly method uses raw materials with low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of 2-hydroxy-4-amino-5-methylpyridine heterocyclic compound.
NOVELTY - This utility model claims a stirring device, comprising a feeding port and a discharging port of the storage bin shell, a rotating shaft is set on the storage bin shell and an internal rotation driving device is connected with the rotating shaft, and the rotating shaft are arranged in parallel along the axial direction with a stirring blade, wherein the stirring blade is provided with an air cavity, the stirring blade is further provided with a cavity and the air storage bin shell cavity of the gas hole, the rotating shaft is provided with a communicated with the air cavity of the gas pipe. This utility new type stirring device, the floor area is small, the sludge on the storage bin shell is isolated from the outside environment, it can avoid the loss of the secondary pollution and sludge nutrient, and by stirring the stirring blade and air to the sludge, capable of promoting rapid propagation of oxygen consumption in sludge, sludge faster fermentation process, fully fermenting the sludge, the sludge processing period.
NOVELTY - The utility model claims an anaerobic reactor delivery of the mixing device, comprising a sewage pump, a feeding pump, a feeding pump is equipped with the first end extends into the anaerobic reactor through a feeding pipe inner cavity side wall of the anaerobic reactor, the other end of the feed pump through the valve and the upper-layer material liquid feeding pipe extends into the inner cavity of the anaerobic reactor of the anaerobic reactor outer side peripheral wall are respectively set with three drain pump and is connected with the inner cavity of the anaerobic reactor. This utility model has compact structure, reasonable design, easy processing, low cost, low energy consumption and pollution, simple to install, convenient to use, small operation intensity.
NOVELTY - The utility model claims a dry-type anaerobic fermentation device, comprising a feeding straw machine, a bucket elevator shell on the bottom base in the collecting tank, the air outlet bucket elevator shell side wall is set with a bucket elevator feed inlet and the straw machine set with the straw machine discharge hole corresponding to close is connected with a bucket elevator shell top part is set with a bucket elevator and elevator bucket with the bucket elevator shell on the upper part is set with pushing conveyor provided with a pushing conveyor feeding port corresponding to the interface, the material pushing conveyor tail end is provided with a discharging opening insert into anaerobic fermentation tank. This utility model has compact structure, reasonable design, easy processing, simple operation and maintenance, low comprehensive cost, advanced dry feeding mode, which avoids the blocking phenomenon feeding, feeding, the material greatly by crushing and kneading, water seal and air seal increases the fermentation area and improves the yield by the following formula inclined feeding way, solves the problem that the anaerobic fermentation tank is sealed.
NOVELTY - A veratrole is prepared by performing methylation reaction using pyrocatechol as raw material with phase transfer catalyst and methylating agent in inorganic aqueous base solution.    USE - Preparation of veratrole (claimed).    ADVANTAGE - Preparation process is mild, convenient to operate and safe, and has high yield, good quality, low energy consumption, and environmental protection.
NOVELTY - Stable ivabradine hydrochloride crystal form II i.e. ivabradine hydrochloride hemihydrate (I) is new. The differential thermal spectrogram of (I) shows endothermic peak at about 154 degrees C, exothermic peak at about 160 degrees C and peak for thermal decomposition temperature at 194 degrees C; and X-ray powder diffraction pattern with peaks and infrared spectrum with characteristic absorption wavelengths as given in the specification. (I) belongs to monoclinic crystal system with space group of P21(4) and cell parameters of a equal to 5.4874 (10) Angstrom , b equal to 43.4767 (7) Angstrom and c equal to 11.4892 (2) Angstrom .    USE - Used as stable ivabradine hydrochloride crystal form II.    ADVANTAGE - (I) does not absorb moisture easily, has good stability and is convenient to store. The preparation is simple and easy, without using high boiling point and high toxicity solvent, thus it is environmentally friendly and suitable for industrial production.    DETAILED DESCRIPTION - Stable ivabradine hydrochloride crystal form II i.e. ivabradine hydrochloride hemihydrate (I) is new. The differential thermal spectrogram of (I) shows endothermic peak at about 154 degrees C, exothermic peak at about 160 degrees C and peak for thermal decomposition temperature at 194 degrees C; and X-ray powder diffraction pattern with peaks and infrared spectrum with characteristic absorption wavelengths as given in the specification. (I) belongs to monoclinic crystal system with space group of P21(4) and cell parameters (measured single-crystal X-ray crystallography analysis at 296 K) of a equal to 5.4874 (10) Angstrom , b equal to 43.4767 (7) Angstrom , c equal to 11.4892 (2) Angstrom , beta equal to 98.144 (2) degrees , volume of 2713.38 (8) Angstrom 3, Z equal to 2 and density of 1.258 g/cm3. An INDEPENDENT CLAIM is also included for preparing (I).
NOVELTY - An electrolyte comprises water, inorganic strong acid, optional inert supporting electrolyte, organic compound which is used as organic sacrificial agent, has more than two functional groups which interacts to strengthen reducibility of the organic compound and does not directly chemically reacts with a photo-anode material of the photo-electrocatalytic hydrogen production system.    USE - Electrolyte is used for photo-electrocatalytic hydrogen production system (claimed).    ADVANTAGE - The photo-electrocatalytic hydrogen production system comprising the electrolyte has phototransformation efficiency of 1.9-12%.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for photo-electrocatalytic hydrogen production system, which has direct current voltage output unit, optical anode, cathode and electrolyte.
NOVELTY - This utility model claims an improved injection molding large granule urea combined barrate pelleting equipment, comprising a combined pelleting barrate, a cooler and a moving bed, moving bed cooler comprises a variable passage area bottom plate, the urea-comprising particles and a feeding port, an air inlet, an air outlet, a discharging port and a discharge drum from the combined pelleting of urea-comprising particles from the feeding port of the mobile bed cooler enter into the upper part of moving bed cooler, and a dynamic bed layer in the moving bed cooler, the cooling air from the variable passage area on the bottom plate of the air inlet enter into moving bed cooler through the urea particles discharged from the air outlet of the moving bed from the condenser part, cooling and discharging to sieve to obtain the finished product sieving machine from the discharge hole on the variable passage area. The device uses mobile bed cooler, combined cooling drum component, simplifies the large grained urea combined barrate pelleting technique, saves energy and reduces the cost.
NOVELTY - This utility model belongs to cold-resistant air lifting type soft membrane biogas tank, wherein the tank body is made of concrete, to support a ceramic standard component, an upper support face mask soft film; the pool bottom is provided with a heating pipe, the upper part of the pool body is covered with a toughened glass heat preservation cover. The said cold-resistant air lifting type soft membrane biogas tank, wherein it is as follows: the soft film is a red mud, wherein the bracket is composed of ceramic standard component. It can be widely used in high-cold frozen soil area, the tank body is not easy to be damaged, the safety is high, the construction is simple, the cost is low and so on.
NOVELTY - This utility model claims a belongs to the technical field of sewage treatment is a treatment lead-containing waste water of the artificial wetland system. The system is composed of a high position water tank, a tank body and a water collecting tank, the tank body is filled with substrate, high position water tank is provided with a water inlet pipe, a water inlet pipe is opened at the base, a water inlet pipe is installed a rotor flow meter adjusting feeding quantity, distance bottom 8-12 cm is set with drain pipe, water collecting bearing water outlet, water outlet pipe of the front end has micro-pore filter screen; the substrate to planting emergent aquatic plant rich in heavy metal enrichment. Lead-containing waste water flows to the artificial wetland unit from the high position water tank, after adsorption of a substrate of the plant, precipitation, adsorption, etc. the function of filtering, degrading, microorganism, the pollutant intercepting. The artificial wetland is lead-containing waste water treatment effect is good and stable, the removal rate is about 99%, and it does not need other power, simple structure, convenient operation and management, small floor area, high processing efficiency, low cost and beautify the environment.
NOVELTY - This utility model claims a kind of biomass modifying agent preparation device, a complete set of device comprises a movable inserting board case, concrete surface, a circulating water pipe, a temperature and humidity sensor, the upper ceiling, a movable inserting board case building ceiling, lower part building concrete table-board, a movable inserting board case is divided into three of a rectangle, U-shaped bottom slot, and the fixing column is composed of the rectangular vertical plate is inserted in the U-shaped slot on the bottom, a rectangular plate are connected and fixed by fixing column, rectangular plate is inserted in the slot of the fixing column; The circulating water pipe is composed of connecting a drain pipe, a water spraying pipe and a tap water pipe is connected with the water barrel, the water barrel of the water pump. Movable plug board box is provided with a collector and a humidity sensor. This device convenient for assembly and disassembly, efficiency is high, and it can be uninterrupted production. Producer can real internal environment humidity and temperature to control, and realizes the automatic water circulation, it will not loss.
NOVELTY - The utility model claims a marsh gas planting integrally, comprising a planting greenhouse marsh gas pool, further comprising a biogas liquid tank and a solid-liquid separating device, a marsh gas tank and the solid-liquid separating device is connected with the feeding port, liquid tank and the liquid outlet of the solid-liquid separating device is connected with the biogas pool is respectively connected with the liquid outlet of a planting greenhouse irrigation system is connected with the air outlet of the planting greenhouse of the marsh gas tank to marsh gas lighting device, marsh gas heating device. This utility model utilize biogas slurry through the irrigation water planting shed, capable of effectively preventing and controlling plant in the greenhouse soil transfer the occurrence of diseases and insect pests, so as to reduce the planting of farm chemical and chemical fertilizer in the greenhouse to reduce the crop pesticide residue, improving crop quality.
NOVELTY - Improving whiteness of metakaolin using natural biomass comprises: (i) uniformly mixing kaolin powder with 5-7 wt.% natural biomass raw material powder; and (ii) calcining the mixture at greater than or equal to 900 degrees C for greater than or equal to 2 hours and cooling.    USE - The method is useful for improving whiteness of metakaolin using natural biomass (claimed).    ADVANTAGE - The method generates carbon dioxide and water which are easy to treat and hardly corrode equipment; does not generate corrosive gases e.g. hydrochloric acid, chloride and ammonia; and is safe to operate and environmental-friendly.
NOVELTY - Special controlled-release fertilizer for biological control of soil-borne disease of watermelon, comprises 80-150 pts. wt. bio-fertilizer, 80-150 pts. wt. sulfurated high molecular polymer coated urea, 150-250 pts. wt. humic-acid coated urea, 150-250 pts. wt. humic-acid coated potassium sulfate and 150-250 pts. wt. diammonium phosphate.    USE - The special controlled-release fertilizer is useful for biologically controlling soil-borne disease of watermelon (claimed).    ADVANTAGE - The special controlled-release fertilizer enables to meet nutrient need of watermelon, and can not only provides a disease preventing function to the watermelons, but also enables nutrient release to meet a watermelon absorbing requirement.    DETAILED DESCRIPTION - Special controlled-release fertilizer for biological control of soil-borne disease of watermelon, comprises 80-150 pts. wt. bio-fertilizer, 80-150 pts. wt. sulfurated high molecular polymer coated urea, 150-250 pts. wt. humic-acid coated urea, 150-250 pts. wt. humic-acid coated potassium sulfate and 150-250 pts. wt. diammonium phosphate, where the bio-fertilizer is formed by compounding and granulating solid culture, 5-20 pts. wt. urea and 20-40 pts. wt. diatomite, and the solid culture is prepared from 40-60 pts. wt. Actinomycetes and 40-60 pts. wt. Pochonia chlamydosporia through solid cultivation according to the existing method. INDEPENDENT CLAIMS are included for the following:    (1) method for preparing the fertilizer which involves preparing the above-mentioned raw materials and mixing the prepared raw materials; and    (2) application method of the above-mentioned fertilizer.
NOVELTY - Preparing non-soluble potassium fertilizer involves (a) grinding potassium mineral to not greater than 5 cm, (b) pulverizing crushed potassium to 200 mesh size or more, and (c) carrying micro-crystallization process while adding activating agent to potassium, and grinding mixture to 400 mesh size.    USE - The method is useful for preparing non-soluble potassium fertilizer (claimed).    ADVANTAGE - The non-soluble potassium fertilizer is not easily lost with rainwater, such that used for reducing soil viscosity, enhances the soil looseness, reduces unique characteristics of soil hardening, and utilizes 100% potassium-bearing minerals. The method is simple, easy in operation, cost-effective, environmentally-friendly, and suitable for industrial production, and has excellent effect.
NOVELTY - Microbial fertilizer comprises probiotic bacterium endospore culturing solution, an aqueous polyol solution, biodegradable filler, biodegradable polymer and nutrient substance.    USE - As microbial fertilizer.    ADVANTAGE - The microbial fertilizer has increased shell life and maintains the survival rate of probiotic bacteria.
NOVELTY - Fertilizer comprises greater than or equal to 5% plant nutrient absorption enhancers, and greater than or equal to 1% multiple trace elements.    USE - The fertilizer is useful for promoting growth of crops (claimed) useful in agriculture and forestry production.    ADVANTAGE - The fertilizer is utilized in minimal rate and prepared simply and easy for storage and transportation, maintains pH of the acidic soil between 7-9, protects ecological environment, and improves particle strength to 8 or more and grain size to 2.0-4.6 mm.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves taking potassium sulfate, magnesium sulfate and zeolite powder as auxiliary raw material, adding the trace elements and plant nutrient absorption enhancers with the above-mentioned mixture, and uniformly stirring and blending the mixture.
NOVELTY - A Bacillus subtilis strain ZN0871vll deposited as CCTCC NO: M2011208 and capable of scavenging organic carbon, is new.    USE - The B.subtilis strain is useful for recycling organic wastewater (claimed) from printing industry, dyeing industry, petrochemical industry and paper making industry.    ADVANTAGE - The strain enables quick and efficient recycling of organic wastewater by trapping the organic carbon with low energy consumption.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the method of recycling organic wastewater which involves adding 20-146.4 mg mutant strain ZN0871v11 with 50-15700 mu l eluent for adsorbing organic wastewater and reacting for 3-5 minutes; centrifuging the mixture for 2-5 minutes at a speed of 8000-12000 rotations per minute (rpm); recovering supernatant fluid as recycled organic matter and the precipitate as regenerated strain ZN0871vll.
NOVELTY - Biological fermentation of liquid dung and biogas slurry, involves (a) preparing raw materials and tools for biological fermentation of liquid dung and biogas slurry, (b) performing aerobic deodorized fermentation, and (c) performing anaerobic fermentation optimized treatment, and performing secondary fermentation to obtain finished product.    USE - Biological fermentation of liquid dung and biogas slurry (claimed).    ADVANTAGE - The method completely eradicates harmful pathogenic bacteria, changes liquid dung and biogas slurry into a beneficial biological liquid fertilizer, and solves the problem on pollution caused by the liquid dung and biogas slurry. The biogas slurry has 0.005 wt.% molybdenum, 10-14 wt.% boron, 12-16 wt.% iron, 15-18 wt.% manganese, 8-12 wt.% zinc, 20-24 wt.% phosphorus, 15-18 wt.% copper, and 12-16 wt.% molybdenum.    DETAILED DESCRIPTION - Biological fermentation of liquid dung and biogas slurry, involves (a) preparing raw materials and tools for biological fermentation of liquid dung and biogas slurry, (b) performing aerobic deodorized fermentation, and (c) performing anaerobic fermentation optimized treatment, and performing secondary fermentation to obtain finished product. The deodorized fermentation is performed using 1-1.2 kg deodorizing agent, 0.1-0.12 kg complex essential microbial agent comprising photosynthetic bacteria, lactic acid bacteria, yeast, Gram-bacteria and more than 80 kinds of soils and crops beneficial microflora, and 0.1-0.12 kg brown sugar.
NOVELTY - Use of paper-making wastewater is claimed for producing biological microbial inoculum. The microbial inoculum is produced by extracting paper-making black liquid by pulping using potassium base, adding black liquid, sugar or molasses and humic acid or fluorophosphate into fermenter, adjusting pH to less than or equal to 8, introducing ozone into the fermenter, sterilizing for 2 hours, adding anaerobic and facultative microbial composition, allowing to propagate and adding black liquid aerobic bacteria into fermenter.    USE - The paper-making wastewater is useful for producing biological microbial inoculum (claimed).    ADVANTAGE - The microbial inoculum is produced by simple and cost-effective method, and rich in nutrients e.g. phosphorus and potassium humate, has high number of living microorganism and high quality. The paper-making liquid is utilized properly, hence environment pollution problem is solved and cost for environmental protection is saved.    DETAILED DESCRIPTION - Use of paper-making wastewater is claimed for producing biological microbial inoculum. The microbial inoculum is produced by extracting paper-making black liquid by pulping using potassium base, adding 100 pts. wt. black liquid, 1-5 pts. wt. sugar or 2-10 pts. wt. molasses and 0-20 pts. wt. humic acid or 0-5 pts. wt. fluorophosphate into fermenter, adjusting pH to less than or equal to 8, introducing ozone into the fermenter, sterilizing for 2 hours, adding 1-3 pts. wt. anaerobic and facultative microbial composition into the fermenter after 1 hour, allowing to propagate for 72 hours, and adding 0.1-10% black liquid aerobic bacteria into the fermenter with respect to the composition until bacterial count reaches greater than or equal to 20 billion/l. An INDEPENDENT CLAIM is included for method of producing the biological microbial inoculum, which involves using paper-making wastewater.
NOVELTY - Method for preparing an edible fungus culture medium using disposable chopsticks, involves (a) cleaning, deoiling and rinsing, (b) airing, (c) crushing, (d) proportioning, namely adjusting the proportion with respect to the different varieties of mushrooms and fungi, (e) bagging, (f) sterilizing, namely sterilizing at normal temperature, (g) inoculating under a sterile condition, (h) spawn running by culturing at constant temperature of 22-25 degrees C and (i) fruiting management by using different management methods with respect to different fungi.    USE - The method is useful for preparing an edible fungus culture medium using disposable chopsticks (claimed).    ADVANTAGE - The method reduces the production cost, widens the material source, is environmentally-friendly and convenient to perform, and improve the requirement of urban residents on the fungi.    DETAILED DESCRIPTION - Method for preparing an edible fungus culture medium using disposable chopsticks, involves (a) cleaning, deoiling and rinsing by placing in clean water, removing dirt, rubbing with washing oil, and flushing the residue with water, (b) drying the clean chopsticks by placing under sun and preventing mildew, (c) crushing, (d) proportioning, namely adjusting the proportion of the cotton seed shell, wooden meal, bran, and gypsum with respect to the different varieties of mushrooms and fungi, (e) bagging, (f) sterilizing at 100 degrees C for 18 hours, (g) inoculating under a sterile condition, (h) spawn running by culturing at constant temperature of 22-25 degrees C and (i) fruiting management by using different management methods with respect to different fungi.
NOVELTY - Boratricyclo(8.4.0.02,7)tetradeca-pentaen-4-yl acetate or propionate is reacted with propan-2-yl (4aS,7aS)-octahydro-1H-pyrrolo(3,4-b)pyridine-1-carboxylate to obtain a condensed intermediate. The condensed intermediate is hydrolyzed in the presence of an acid and deprotected to obtain in a reaction solvent to obtain moxifloxacin. The moxifloxacin is converted into its salt to obtain moxifloxacin hydrochloride.    USE - Manufacture of moxifloxacin hydrochloride (claimed).    ADVANTAGE - The moxifloxacin hydrochloride with excellent quality is manufactured by a one-pot synthesis. The used solvent can be directly recycled and reused.    DETAILED DESCRIPTION - 4-(Acetyloxy)-9-cyclopropyl-12,13-difluoro-11-methoxy-6-oxo-3,5-dioxa-9-aza-boratricyclo(8.4.0.02,7)tetradeca-1(14),2,7,10,12-pentaen-4-yl acetate or 9-cyclopropyl-12,13-difluoro-11-methoxy-6-oxo-4-(propanoyloxy)-3-dioxa-9-aza-boratricyclo(8.4.0.02,7)tetradeca-1(14),2,7,10,12-pentaen-4-yl propanoate is reacted with propan-2-yl (4aS,7aS)-octahydro-1H-pyrrolo(3,4-b)pyridine-1-carboxylate to obtain tert-butyl (4aS,7aS)-6-(4,4-bis(acetyloxy)-9-cyclopropyl-13-fluoro-11-methoxy-6-oxo-3,5-dioxa-9-aza-boratricyclo(8.4.0.02,7)tetradeca-1(14),2,7,10,12-pentaen-12-yl)-octahydro-1H-pyrrolo(3,4-b)pyridine-1-carboxylate or tert-butyl (4aS,7aS)-6-(9-cyclopropyl-13-fluoro-11-methoxy-6-oxo-4,4-bis(propanoyloxy)-3,5-dioxa-9-aza-boratricyclo(8.4.0.02,7)tetradeca-1(14),2,7,10,12-pentaen-12-yl)-octahydro-1H-pyrrolo(3,4-b)pyridine-1-carboxylate as condensed intermediate. The condensed intermediate is hydrolyzed in the presence of an acid and deprotected to obtain in a reaction solvent to obtain moxifloxacin. The moxifloxacin is converted into its salt to obtain moxifloxacin hydrochloride.
NOVELTY - Method for cultivating mushroom using biogas digester liquid, involves using corncob and biogas digester liquid as main raw materials, adding certain amount peanut bran as auxiliary material, and adding into culture medium, where the culture medium comprises 500 kg corncob, 50 kg peanut cake, 500 kg liquid methane, 7.5 kg gypsum powder, 10 kg superphosphate, 25 kg lime powder, 2 kg of urea, and 400 kg water.    USE - The method is useful for cultivating mushroom using biogas digester liquid (claimed).    ADVANTAGE - The method is sufficient in sources of raw materials, convenient, low in cost, and quick.    DETAILED DESCRIPTION - Method for cultivating mushroom using biogas digester liquid, involves using corncob and biogas digester liquid as main raw materials, adding certain amount peanut bran as auxiliary material, and adding into culture medium, where the culture medium comprises 500 kg corncob, 50 kg peanut cake, 500 kg liquid methane, 7.5 kg gypsum powder, 10 kg superphosphate, 25 kg lime powder, 2 kg of urea, and 400 kg water, where the method particularly involves mixing the raw materials to prepare biogas, fermenting and inoculating the mushroom, and maintaining the mushroom at temperature of 15-20 degrees C and air humidity of 85-95%.
NOVELTY - Method for partial nitrification of granular sludge involves processing urban sewage treatment plant sludge in simulated wastewater reactor such that chemical oxygen demand (COD) concentration is 350-450 mg/L, ammonium ion concentration is 80-100 mg/L, performing aerobic aeration, settling for 12-16 minutes, drying, supplying the sludge into reactor, maintaining the COD and ammonium ion concentrations, performing aerobic aeration, settling for 3-8 minutes, drying, maintaining the COD and ammonium ion concentrations, settling for 1.5-3 minutes, draining, and nitrifying.    USE - Method for partial nitrification of granular sludge (claimed).    ADVANTAGE - The granular sludge is processed efficiently with nitrite accumulation rate of 80% within 80 days, mean grain size of greater than 800 mu m, ammonium ion removal rate of 100% and chemical oxygen demand removal rate is 94%.    DETAILED DESCRIPTION - Method for partial nitrification of granular sludge involves processing urban sewage treatment plant sludge in simulated wastewater reactor such that chemical oxygen demand (COD) concentration is 350-450 mg/L, ammonium ion concentration is 80-100 mg/L, performing aerobic aeration for 7.2-7.5 hours, settling for 12-16 minutes, drying for 3-6 minutes, supplying the sludge into reactor, controlling COD concentration to 350-450 mg/L and ammonium concentration of 80-100 mg/L, performing aerobic aeration for 7.2-7.5 hours, settling for 3-8 minutes, drying for 3-6 minutes, maintaining the COD concentration and ammonium ion concentration, settling for 1.5-3 minutes, draining for 3-6 minutes, and nitrifying.
NOVELTY - A thick bamboo fiber sewage treatment filler contains thick bamboo fiber as base material.    USE - Thick bamboo fiber sewage treatment filler (claimed).    ADVANTAGE - The sewage treatment filler enables shortening of starting time of bioreactor and improvement of chemical oxygen demand and the average ammonia-nitrogen removal effect. The thick bamboo fibers are uniformly distributed and fully unfolded in the bioreactor after film hanging, and agglomeration is avoided. The probability for microbes to contact with sewage is enhanced, and the mass transfer function is enhanced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of thick bamboo fiber sewage treatment filler.
NOVELTY - Fertilizer and its preparation method, are claimed. The fertilizer comprises biogas slurry, carbon source, nitrogen source, trace elements, Trichoderma viride culture, and selenium ore powder. The method involves mixing biogas slurry, carbon source, nitrogen source and mineral powder containing trace element selenium, carrying out anaerobic fermentation, performing biochemical reaction, adding T.viride liquid to product, mixing materials, performing fermentation, filtering product, and sub-packaging obtained product.    USE - The fertilizer is useful for providing selenium to tea tree root (claimed).    ADVANTAGE - The fertilizer can be easily absorbed by plant, and provides organic selenium to tea tree.    DETAILED DESCRIPTION - Fertilizer and its preparation method, are claimed. The fertilizer comprises 50-75 pts. wt. biogas slurry, 20-45 pts. wt. carbon source, 1-2 pts. wt. nitrogen source, 5-10 pts. wt. trace elements, 5-10 Trichoderma viride culture of concentration 106-108 cells/ml, and 270 mu g/kg selenium ore powder. The method involves mixing biogas slurry, carbon source, nitrogen source and mineral powder containing trace element selenium at 25-32 degrees C, carrying out anaerobic fermentation under stirring condition, performing biochemical reaction for 8-10 days, adding the T.viride liquid to product, mixing materials, performing anaerobic fermentation at 20-28 degrees C for 5-7 days in tank, filtering fermented product, and sub-packaging the obtained product.
NOVELTY - Microbial inoculum comprises white-rot fungus, Lactobacillus acidophilus, Trichoderma viride, Bacillus subtilis and Candida utilis.    USE - The microbial inoculum is useful for fermenting straw feed (claimed).    ADVANTAGE - The microbial inoculum is environmentally-friendly, ferments straw feed efficiently and thus straw feed contains large amount of living biological cells, decomposition enzymes and other active components, highly improves utilization rate of straw feed and increases protein content and nutritional value in feed, and creates good precondition for utilization of straw as a resource.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of above-cited microbial inoculums, which involves (a) inoculating white-rot fungus in potato dextrose agar medium, L.acidophilus in de Man, Rogosa and Sharpe (MRS) agar medium, T.viride in Sabouraud agar culture medium, B.subtilis in nutrient agar culture medium and C.utilis in corn agar culture medium with Tween 80 (RTM: Polysorbate 80) for activating and culturing the inoculated strains at 26-37 degrees C for 3 days to obtain 5 first generation strains, (b) inoculating the obtained 5 first generation strains individually into the nutrient agar culture medium respectively, culturing at 30 degrees C for 3 days to obtain expansion culture, and (c) mixing the obtained microbial culture liquid in a suitable volume ratio.
NOVELTY - Biological compound fertilizer comprises first formula and second formula. The first formula comprises nitrogen phosphor and potassium, and raw materials comprising fresh semi-dried chicken manure, calcium magnesium phosphate fertilizer, potassium fulvic acid, borax, copper sulfate pentahydrate, zinc sulfate heptahydrate, ferrous sulfate heptahydrate, amino acids, microbial agents, synergist and conditioner.    USE - The biological compound fertilizer is useful for grape.    DETAILED DESCRIPTION - Biological compound fertilizer comprises first formula and second formula. The first formula comprises 30% nitrogen phosphor and potassium in a ratio of 1:0.8:1.2, and raw materials comprising 62.8 pts. fresh semi-dried chicken manure, 0.2 pts. calcium magnesium phosphate fertilizer, 23.8 pts. potassium fulvic acid, 2 pts. borax, 1 pts. copper sulfate pentahydrate, 1 pts. zinc sulfate heptahydrate, 1 pts. ferrous sulfate heptahydrate, 3.2 pts. amino acids, 2 pts. microbial agents, 1 pts. synergist and 2 pts. conditioner. The second formula comprises 25% nitrogen phosphor and potassium in a ratio of 1:0.8:1.38, and raw materials comprising 76 pts. fresh semi-dried chicken manure, 4 pts. potassium sulfate, 2 pts. amino acid chelated (complexed) zinc, boron, copper and ferrum, 8.5 pts. nitrohumate, 3.5 pts. amino acids, 3 pts. microbial preparation, 1 pts. synergist and 2 pts. conditioner. The fertilizer is obtained by stirring the above materials uniformly, spray granulating and drying at a low temperature or air drying.
NOVELTY - Ring opening and alkylation condensation is performed for epichlorohydrin and 2-methyl-5-nitroimidazole using ethyl acetate as solvent and macroporous acidic high-molecular resin as catalyst, to obtain ornidazole crude product. The obtained crude product is centrifuged and supernatant liquid is separated, to obtain mother liquor containing catalyst. The mother liquor is activated, catalyst is recycled, remainder product is distilled, residue is decolored, filtered, crystallized and centrifuged, to obtain ornidazole.    USE - Manufacture of ornidazole (claimed).    ADVANTAGE - The method efficiently provides ornidazole with high yield and catalytic activity by economical and environmentally-friendly process.
NOVELTY - The bamboo charcoal has raw material that is composed of bamboo processing residuum and alkali lignin. The discharged raw materials after molding the bamboo charcoal raw material are cut into required specifications through saws. The discharged materials are placed into a carbonization furnace and carbonized in pile mode. The hot compression plasticizing molding bamboo charcoal main portion is obtained by cooling after carbonization of discharged materials.    USE - Heat pressing plastic formed bamboo charcoal used in paper manufacturing industry and wood manufacturing industry.    ADVANTAGE - Since the bamboo charcoal is obtained with high carbon content, the production efficiency of the bamboo charcoal can be improved. The production time of the bamboo charcoal can be reduced. The generation of the large amount of lignin in the process of pulping and papermaking, and the stress of environmental management can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for manufacturing heat pressing plastic formed bamboo charcoal.
NOVELTY - A Bacillus subtilis strain, preferably MMR-1 (CGMCC 6871), is new.    USE - The B.subtilis strain or biologically pure culture of the microorganism is useful in microbial fuel cell for generating electricity (all claimed).    ADVANTAGE - The B.subtilis strains are facultative anaerobe and enlarge the power generating microorganism.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) biologically pure culture of bacterial straincm the above-mentioned B.subtilis; and (2) microbial fuel cell comprising the above-mentioned B.subtilis strain or biologically pure culture.
NOVELTY - Purifying arsenic and nitrate containing sewage includes oxidation denitrifying bacteria with a solid culture medium including anhydrous sodium citrate, dipotassium phosphate, potassium dihydrogen phosphate, magnesium sulfate heptahydrate, potassium nitrate, and iron chloride tetrahydrate in anaerobic activated sludge sewage treatment plant, adding iron (II) chloride enriched in anaerobic condition, selecting red bacteria solid culture medium for separating to obtain iron oxide, denitrifying bacteria strain, culturing, and further anaerobic culturing.    USE - Method for purifying arsenic and nitrate containing sewage (claimed).    ADVANTAGE - The method is simple, and has convenient operation, low processing cost and no secondary pollution.    DETAILED DESCRIPTION - Purifying arsenic and nitrate containing sewage comprises:    (A) oxidation denitrifying bacteria with a solid culture medium including 5 g/l anhydrous sodium citrate, 1 g/l dipotassium phosphate, 0.5 g/l potassium dihydrogen phosphate, 0.2 g/l magnesium sulfate heptahydrate, 2 g/l potassium nitrate, and 0.998 g/l iron chloride tetrahydrate in anaerobic activated sludge sewage treatment plant, adding 2-20 mM iron (II) chloride (FeCl2) enriched in anaerobic condition for 3-10 days, selecting red bacteria solid culture medium for separating to obtain iron oxide, and denitrifying bacteria strain;    (B) culturing the obtained bacterial suspension containing 2-10 vol.% of the liquid medium at 10-30 degrees C, and culturing the oscillation rate under conditions at 60-150 revolutions/minute for 3-10 days for enrichment culture; and    (C) transferring enrichment broth which is 2-10 vol.% of inoculum to a solution containing nitrate and arsenic wastewater, controlling the pH value at 4-10, at 10-26 degrees C, and anaerobic culturing under aerobic conditions for 3-30 days.
NOVELTY - Purifying cefditoren sodium salt by depleting the E-isomer content in a mixture of Z- and E-isomers of 7-(2-methoxyimino-2-(2amino-thiazol-4-yl) acetamido)-3-(2-(4-methylthiazol -5-yl) vinyl)-3-cephem-4-carboxylic acid sodium salt(II), comprises: either (i) preparing Z- and E- isomer of (II) in a solvent, and (ii) adding a inorganic salt to the solution of step (i); or the steps (i) and (ii) as above persteps, (iii) isolating Z-isomer enriched mixture of Z- and E- isomers of (II), and (vi) optionally converting Z-isomer enriched mixture of Z- and E- isomer of (II) of step (iii) to cefditoren pivoxil.    USE - The method is useful for purifying cefditoren sodium salt (claimed).    ADVANTAGE - The method simply and highly purifies cefditoren sodium salt with high yield, while reducing the multiple steps, in an economical and an environmental friendly manner.
NOVELTY - A biological soil conditioner comprises waste sugar alcohol, peat, and sugarcane filter mud at weight ratio of 2000-5000:100-300:500-800.    USE - Biological soil conditioner.    ADVANTAGE - The soil conditioner keeps soil nutrition, improves crop yield and reduces heavy metal content in crops.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the biological preparation of the soil conditioner which comprisess:    (a) preparing 2000-5000 pts. sugar mill alcohol waste liquid subjected to acid and alkali treatment;    (b) preparing 500-800 pts. sugar mill filter residue obtained from microorganism fermentation;    (c) mixing the products of steps (a) and (b) and adding 100-300 pts. peat.    Preparation of the sugar mill alcohol waste liquid subjected to acid and alkali treatment comprises storing the sugar mill alcohol waste liquid in a tank, adding 37.5 wt.% dilute sulfuric acid until the pH of the waste liquid is below 1, storing the sugar mill alcohol waste liquid at a normal temperature for 5-10 days, then adding ammonium hydroxide to regulate the pH to 6-7.    Preparation of the sugar mill filter residue obtained from microorganism fermentation comprises fermenting the sugar mill filter residue and a microorganism fermentation agent for 5-15 days.
NOVELTY - A 2-((6-ethyl-1-oxoindane-4-carbonyl)amino)-acetic acid methyl ester (I) is new.    USE - A 2-((6-ethyl-1-oxoindane-4-carbonyl)amino)-acetic acid methyl ester (I) used as plant defense inducer (claimed) useful for preventing and controlling diseases and insect pests of crops or cash crop.    ADVANTAGE - The compound (I) carries out green environment-friendly plant protection.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the compound (I).
NOVELTY - Preparation of levofloxacin comprises taking levofloxacin acid, adding antioxidant, solvent and N-methyl piperazine, reacting, concentrating and recycling N-methyl piperazine to obtain residue, adding water and trichloromethane to residue, adjusting pH to 7 using hydrochloric acid, stratifying, concentrating extracted layer, adding methanol and pulping.    USE - Method for preparing levofloxacin (claimed).    ADVANTAGE - The method improves quality and appearance of product, ensures high recovery rate, reduces operation cost, and realizes environment-friendly operation.
NOVELTY - Preparation of briquette binder comprises uniformly mixing 35-60 pts. wt. coal powder, 5-20 pts. wt. bentonite, 30-50 pts. wt. solvent water and 0.5-3 pts. wt. catalytic agent, placing in high-pressure reactor, introducing reducing gas, and adjusting initial pressure to 1-5 MPa; heating to 320-380 degrees C for 20-60 minutes, and controlling reaction at 20-40 MPa; and cooling to room temperature, extruding or centrifuging, and separating. The reducing gas comprises carbon monoxide (CO), hydrogen (H2), methane (CH4), and mixture of nitrogen (N2) and oxygen (O2) gases with 5-100 wt.% CO content.    USE - Method for preparing briquette binder (claimed).    ADVANTAGE - The method is simple and convenient to operate; has wide raw material source and low cost; and improves adhesive property.
NOVELTY - An aviation kerosene/diesel preparation method involves preparing oxygen-containing organic compounds with carbon chain length of 8-16 by selecting lignocelluloses-based carbonyl-containing platform compounds and furan platform compounds as raw materials on a solid catalyst, effectively removing carbon-carbon double bonds and carbon-oxygen double bonds to prepare saturated oxygen-containing organic compounds by hydrogenation of the alkylated product and conducting hydrodeoxygenation for the hydrogenated alkylation product to obtain biomass aviation kerosene and high grade diesel fuel.    USE - Method for preparing aviation kerosene/diesel.    ADVANTAGE - The method enables preparing the aviation kerosene/diesel with high energy density and stability.    DETAILED DESCRIPTION - An aviation kerosene/diesel preparation method involves preparing oxygen-containing organic compounds with carbon chain length of 8-16 through acid-catalyzed alkylation reaction by selecting lignocelluloses-based carbonyl-containing platform compounds and furan platform compounds as raw materials on a solid catalyst, effectively removing carbon-carbon double bonds and carbon-oxygen double bonds to prepare saturated oxygen-containing organic compounds by hydrogenation of the alkylated product and conducting hydrodeoxygenation for the hydrogenated alkylation product by using a metal-solid acid bifunctional catalyst to obtain biomass aviation kerosene and high grade diesel fuel.
NOVELTY - An industrial cracking furnace cracking product value maximization model construction method involves establishing a cracking furnace cracking product yield prediction model, based on steam cracking experiment data. Industrial cracking furnace target cracking product mole content data is acquired. A cracking furnace cracking product value maximization model is established based on the corrected and checked model, and is adopted to optimize operation of the cracking furnace such that total value of petrochemical products produced by the industrial cracking furnace is maximized.    USE - Method for constructing an industrial cracking furnace cracking product value maximization model.    ADVANTAGE - The method enables maximizing the total value of petrochemical products produced by the industrial cracking furnace, thus effectively improving income of the petrochemical production enterprises.    DETAILED DESCRIPTION - An industrial cracking furnace cracking product value maximization model construction method involves establishing a cracking furnace cracking product yield prediction model, based on steam cracking experiment data. Industrial cracking furnace target cracking product mole content data is acquired and is adopted to correct and check the established prediction model, such that a calculation result of the prediction model and an actual operation result of the industrial cracking furnace are same. A cracking furnace cracking product value maximization model is established based on the corrected and checked model, and is adopted to optimize operation of the cracking furnace such that the total value of petrochemical products produced by the industrial cracking furnace is maximized.
NOVELTY - An industrial cracking furnace cracking product value maximization model construction method involves establishing an industrial cracking furnace cracking product prediction model in an olefin production device, based on steam cracking experiment data. Operating cracking depth data of the industrial cracking furnace is adopted to correct and check the established prediction model. A cracking furnace cracking product value maximization model is established based on the corrected and checked model, and is adopted to optimize operation of the cracking furnace.    USE - Method for constructing an industrial cracking furnace cracking product value maximization model.    DETAILED DESCRIPTION - An industrial cracking furnace cracking product value maximization model construction method involves establishing an industrial cracking furnace cracking product prediction model in an olefin production device, based on steam cracking experiment data. Operating cracking depth data of the industrial cracking furnace is adopted to correct and check the established prediction model. A cracking furnace cracking product value maximization model is established based on the corrected and checked model, and is adopted to optimize operation of the cracking furnace such that the total market price of cracking products produced by the cracking furnace is maximized.
NOVELTY - Preparation of biological tar product involves collecting and treating biomass, carrying out self-pyrolysis on the biomass, generating biologic high-temperature mixed gas, purifying, separating, standing, separating by using tar acetic acid mixed liquid, generating biologic gas by using pneumatic equipment, generating biologic tar, and preparing the biologic tar product.    USE - Preparation of biological tar product (claimed).
NOVELTY - An environmentally-friendly solid fuel is obtained by mixing powder obtained by crushing dried rice straw, corn stand and/or barley straw to size of 80-200 meshes, fluffed waste paper, and additive containing cottonseed oil, oleic acid, stearic acid and/or hydroxyethyl cellulose.    USE - Environmentally-friendly solid fuel (claimed).    ADVANTAGE - The environmentally-friendly solid fuel is economical, and has high calorific value.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of environmentally-friendly solid fuel.
NOVELTY - Water is removed from oil by dehydration reaction, methyl ester is prepared by esterification of methanol and free fatty acid present in oil. Then, methyl ester and glycerol are produced by transesterification of oil and methanol, and carboxy-containing compound (I) is prepared from glycerol. The carboxy-containing compound (I) is mixed with 7-12C alkyl benzene, and product is mixed with methyl ester, to drop pour point of biodiesel.    USE - Method for dropping pour point of biodiesel (claimed).    ADVANTAGE - The pour point of biodiesel is reduced without mixing with diesel oil.    DETAILED DESCRIPTION - Water is removed from oil by dehydration reaction, methyl ester is prepared by esterification of methanol and free fatty acid present in oil. Then, methyl ester and glycerol are produced by transesterification of oil and methanol, and carboxy-containing compound of formula: CH2=C(CH3)-COOR (I) is prepared from glycerol. The carboxy-containing compound (I) is mixed with 7-12C alkyl benzene, and product is mixed with methyl ester, to drop pour point of biodiesel.    R=5-12C alkyl.
NOVELTY - Method (M1) for preparing potato biomass, involves (a) subjecting potato powder to extrusion molding, and (b) adding enzyme to the extrusion molded material.    USE - The method (M1) is useful for preparing potato biomass which is useful for preparing bioethanol (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) method (M2) for preparing bioethanol, involves subjecting the above-mentioned prepared potato biomass to saccharification, fermentation and distillation; and    (2) bioethanol, prepared by the above-mentioned method (M2).
NOVELTY - A 1-(pyridin-4-yl)piperazine preparing process involves protonizing or quaternizing 4-chloropyridine or 4-cyanopyridine onto a pyridine nitrogen atom and reacting with piperazine in water or in lower alcohol containing 1-3 carbon atoms, under catalysis by a d-metal or cerium, in a positively charged complex or in the form of a compound.    USE - Process for preparing 1-(pyridin-4-yl)piperazine and its 1,1-dialkyl-1-ium derivative.    ADVANTAGE - The process enables preparing the 1-(pyridin-4-yl)piperazine and its 1,1-dialkyl-1-ium derivative in an economical and eco-friendly manner.
NOVELTY - Preparation of biodiesel by membrane comprises mixing raw material oil and 10-20% methanol or ethanol, heating at 70-90 degrees C, passing through functional polymer membrane at 1-2 kg/cm2, obtaining biodiesel oil and glycerol emulsion, adding precipitating agent, precipitating glycerol from the emulsion to obtain crude biodiesel oil, refining the crude biodiesel oil by passing through adsorption column, micro-filtering, and adding antioxidant to obtain refined biodiesel.    USE - Preparation of biodiesel by membrane (claimed).    ADVANTAGE - The method uses greatly increased selection range of raw material oil, achieves complete reaction of raw material oil and fatty acid, ensures the quality of biodiesel, provides no wastewater and no pollution, does not require the removal of impurities by distillation, and greatly saves energy consumption.
NOVELTY - An additive is prepared by mixing 45-55 wt.% 3-5C monohydric mixed alcohol, 20-30 wt.% isobutenylamide isoheptyl ester and 25-30 wt.% surfactant.    USE - Additive is used for improving water resistance of methanol gasoline.    ADVANTAGE - The additive having improved water-phase separating property of methanol gasoline, and high water resistance is economically prepared.
NOVELTY - The method involves establishing proton exchange membrane fuel cell prototype model. The operating parameters of the fuel cell are determined according to predetermined formula. The input current, output current and output voltage of the fuel cell are measured and optimized using the mean square error of operating parameters. The fuel cell parameters obtained using the standard adaptive differential evolution technique, are initialized so as to easily perform the optimizing processing of fuel cell.    USE - Proton exchange membrane fuel cell optimizing processing method.    ADVANTAGE - The optimizing processing precision and stability of the proton exchange membrane fuel cell can be improved. The convergence speed of the fuel cell can be improved. Better convergence time of the fuel cell can be guaranteed. The calculation complexity of the fuel cell parameters can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the proton exchange membrane fuel cell optimizing processing method. (Drawing includes non-English language text)
NOVELTY - The device has a main portion which defines a reaction space and a diaphragm (200). The diaphragm is provided with in the reaction space. A cathode (410) is provided in the cathode chamber. A power supply (500) is respectively connected with the anode (310) and the cathode so as to form a loop. The anode chamber is provided for containing organic compound and microorganism. The cathode chamber is provided to contain carbon dioxide and microorganism.    USE - Device for synthesizing bio-diesel fuel.    ADVANTAGE - The device can be capable of effectively synthesizing the bio-fuel in efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the device for synthesizing bio-diesel fuel.    Outlet (7)    Diaphragm (200)    Anode (310)    Cathode (410)    Power supply (500)
NOVELTY - This utility model claims a kind of environment-protecting and energy-saving renewable energy thermal cracking furnace, comprising a combustion , cracking gas cooling device in said combustion is provided with a reaction kettle, a pyrolysis gas cooling device comprises a cooling tank, a cooling device for cooling the reaction liquid tank, a gas collecting tank is connected with the cooling device, wherein the reaction kettle is provided with a material inlet and a cracking gas outlet, a material inlet and a cracking gas outlet rapid joint, air guide pipe and the liquid cooling tank is connected with the gas collecting tank by cracking gas with the combustion of fuel gas pipeline connected to the biological wastes and urban garbage thermal cracking process, which not only reasonably useful resource, but also has a good environmental protection effect by the device.
NOVELTY - Converting, in an aqueous medium, a feedstock including polyol into hydrocarbons and mono-oxygenated compounds containing greater than or equal to 5C, comprises contacting the feedstock with a catalyst at a temperature of 180-350 degrees C and a pressure of 0.5-20 MPa. The catalyst includes metal consisting of groups 7-11 of the periodic table of the elements deposited on a substrate. The substrate includes titanium oxide on which 1-50 wt.% of tungsten is deposited.    USE - The method is useful for converting, in an aqueous medium, a feedstock including polyol into hydrocarbons, mono-oxygenated compounds containing greater than or equal to 5C (claimed), mono-ketones and carboxylic acids, where: the hydrocarbons and mono-oxygenated compounds are useful as biofuel in fuel pool or as chemical intermediates in the field of chemistry and petrochemistry; the hydrocarbons include methane, ethane, propane, butane, pentane, hexane, cyclopentane and methylcyclopentane; the mono-oxygenated compounds include hexanol, pentanol, butanol, propanol, ethanol and methanol; and the mono-ketones and carboxylic acids include hexanone, pentanone, butanone, propanone and acetone.    ADVANTAGE - The method enables the conversion of feedstock including polyol into hydrocarbons, mono-oxygenated compounds, mono-ketones and carboxylic acids with improved selectivity and high yield in an environmentally friendly manner.    DETAILED DESCRIPTION - Converting, in an aqueous medium, a feedstock including polyol of formula (CnH2n+2On) (I) into hydrocarbons and mono-oxygenated compounds containing greater than or equal to 5C, comprises contacting the feedstock with a catalyst at a temperature of 180-350 degrees C and a pressure of 0.5-20 MPa. The catalyst includes metal consisting of groups 7-11 of the periodic table of the elements deposited on a substrate. The substrate includes titanium oxide on which 1-50 wt.% of tungsten is deposited.    n = 3-6.
NOVELTY - The apparatus (1) has a reaction tank (11) which stores water (W) for decomposition. A hydrogen gas collection unit (12) is provided for separating and collecting the hydrogen gas from a mixed gas (Vp) of oxygen gas and hydrogen gas generated in the reaction tank. A bubble generator (13) is provided for generating micro-bubbles (MB) in the water stored in the reaction tank. The water molecules are decomposed by a physicochemical reaction generated during collapse of micro-bubbles in the water in the reaction tank.    USE - Hydrogen gas manufacturing apparatus of electrolysis system, used in combustion-type engine.    ADVANTAGE - The combustion efficiency of the internal combustion-type engine can be improved. The size of the hydrogen gas manufacturing apparatus is reduced. The cost of the hydrogen gas manufacturing apparatus is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for hydrogen gas manufacturing method.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross sectional view of the hydrogen gas manufacturing apparatus. (Drawing includes non-English language text)    Hydrogen gas manufacturing apparatus (1)    Reaction tank (11)    Hydrogen gas collection unit (12)    Bubble generator (13)    Micro-bubble (MB)    Mixed gas (Vp)    Water (W)
NOVELTY - An electrochemical reaction device has a cathode (1) containing nickel, copper or ruthenium and generates carbon monoxide and oxide ion from carbon dioxide, a porous electrolyte (3) which permeates oxide ion generated with methane supplied towards cathode, and an anode (2) which generates hydrogen and carbon monoxide from methane and permeates the electrolyte, and oxide ion, and containing copper.    USE - Electrochemical reaction device is used for manufacturing fuel gas (claimed) for solid oxide fuel cell.    ADVANTAGE - The electrochemical reaction device is economical. The fuel gas is economically manufactured, using the electrochemical reaction device.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of fuel gas.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the electrochemical reaction device.    Cathode (1)    Anode (2)    Porous electrolyte (3)    Cell (10)
NOVELTY - The system has carbonizing machine (1) which is provided to decompose biomass fuel and to generate carbonized material. A 2-stage gasifier (2) is provided with reductor (2b) as gas reforming unit to reform the combustible pyrolysis gas containing tar which is volatilized at the time of the generation of combustor (2a). The combustor is a hot gasifier unit to gasify the carbonized material. Tar suction unit (3) is provided for supplying carbonized material to combustor from carbonizing machine and the generated gas is emitted from the reductor are made to contact.    USE - System for decomposing biomass fuels such as waste material type biomass, such as wood type biomass, and municipal solid waste.    ADVANTAGE - The carbonized material supplied to gasifier from carbonizing machine is used for the tar removal in generated gas, in order to suppress the addition of installation by utilizing the intermediate product within the process of biomass carbonization gasification, and to obtain cheap and rational tar reduction effect. The removed tar is decomposed in the high temperature atmosphere of combustor, so that the tar in generated gas is removed, and used for high quality product as fuels such as gas engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the biomass carbonization and gasification system. (Drawing includes non-English language text)    Carbonizing machine (1)    Gasifier (2)    Combustor (2a)    Reductor (2b)    Tar suction unit (3)
NOVELTY - An electrochemical cell (10) has electrolytic membrane (11) which exhibits oxygen-ion electroconductivity, oxygen electrode (12) formed in one main surface (11A) side of the electrolytic membrane, and hydrogen electrode (13) containing metal oxide containing metallic nickel and cerium, formed in other main surface (11B) side of the electrolytic membrane.    USE - Electrochemical cell is used for hydrogen production apparatus (claimed).    ADVANTAGE - The electrochemical cell has high electrolysis reaction efficiency for long period of time. The hydrogen production apparatus containing the electrochemical cell has suppressed deterioration of the catalytic function of the hydrogen electrode resulting from electrolysis reaction.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic sectional view of structure of the electrochemical cell.    Electrochemical cell (10)    Electrolytic membrane (11)    One main surface of electrolytic membrane (11A)    Other main surface of electrolytic membrane (11B)    Oxygen electrode (12)    Hydrogen electrode (13)
NOVELTY - A system comprises: biomass composition comprising cellulose, hemicellulose or lignocellulose; acid treatment vessel for combining the biomass composition with acid; first press operatively coupled to the acid treatment vessel for removing water from acid treated biomass composition; heat treatment vessel operatively coupled to first press for combining the dewatered, acid treated biomass composition with hot water; second press operatively coupled to heat treatment vessel to separate a liquid precursor hydrozate from a solid precursor hydrozate; and process control system.    USE - For producing a liquid precursor hydrozate and a solid precursor hydrozate (claimed); for the hydrolyzation of ensiled biomass; for producing biofuels e.g. alcohols; as coproducts for absorbent media, animal or human food and food additives, building products such as composite boards and sheets, animal bedding, combustible fuels such as burning pellets, adhesive and plastic additives, bio-plastics or soil additives.    ADVANTAGE - The obtained liquid precursor has significant economic value, and is suitable for uses such as lower cost and improved efficiency ethanol production. The liquid precursor hydrozate is used for producing alcohol with lower cost, and improved efficiency. The liquid precursor is used for producing biofuels that reduces transportation costs from the feedstock source to the biorefinery; that reduces process energy use; that reduces feedstock storage requirements at the biorefinery; that reduces the size, cost and operating energy usage of a biorefinery.
NOVELTY - Obtaining a Methylobacterium preparation involves growing a mono-culture or co-culture of Methylobacterium in media that comprises a liquid phase and a solid phase, where the solid phase provides for increased yield of the Methylobacterium relative to yield obtained by growing the Methylobacterium in liquid media alone.    USE - For obtaining Methylobacterium preparation; for preparation of fermentation product; for treating a plant or a plant part (claimed) such as cereal plants for promoting nodal root formation; used as an inoculum in bioremediation; and for production of recombinant proteins.    ADVANTAGE - The method is efficient production method of large quantities of Methylobacterium; prepares high titer Methylobacterium cultures where production time per batch is significantly reduced; uses culture medium comprised of inexpensive and readily available components.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: 1) a Methylobacterium preparation comprising the solid substance obtained by the method, where a mono-culture or co-culture of Methylobacterium is adhered to it; 2) treating a plant or a plant part with Methylobacterium involving applying a composition comprising the Methylobacterium preparation to the plant or plant part; and 3) a fermentation product comprising a solid substance where a mono-culture or co-culture of Methylobacterium is adhered to it, where the solid substance is not a photosynthetic microorganism, and where the fermentation product is essentially free of contaminating microorganisms.
NOVELTY - Plant-derived raw material comprises decomposing microorganisms, to which an aerobic fermentation is accelerated, and other vegetable raw material which has deodorizing effect, where deodorizing material comprises waste material which has deodorizing effect, occurrence of malodorous gas is reduced, livestock farming installations, preferably mold livestock barn, and ventilation with external air is blocked.    USE - As plant-derived raw material.
NOVELTY - Matrix-container biogas plant comprises synchronous fermenters with electronically controlled central distribution and with uniform filling, lined up according to the principle of communicating tubes. The fermenters are supplied with immobilized, methanogenesis bacterium strains at 32-38 degrees C continuously from a pre-storage container and fresh bio-substrate from locally available materials are collected when required, crushed, mixed and homogenized with liquid. The required amount of substrate is accurately determined and the used substrate is transported out externally.    USE - Used as a matrix-container biogas plant.    ADVANTAGE - The matrix-container biogas plant: is compact and robust; can be operated with local raw materials of different composition and in an environmentally friendly manner; and ensures low investment- and operating costs.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic side view of the fermenter.    Fermenter (1)    Control unit (2)    Circulation system (6)    Chamber (7)    Valve (9)
NOVELTY - The biogas reactor (1) has housing (7) which is provided with an inlet (2) for organic material and a biogas outlet (3). A material displacement device (6) is provided with a shaft (5). Two outlets (12,13) are provided in a gas producing section (10) from which organic material is returned to the inlet of housing. The shaft is arranged such that it provides heat to the biogas reactor. The material displacement device is provided with a baffle (17).    USE - Biogas reactor.    ADVANTAGE - The biogas reactor can be controlled more precisely by more advanced grafting. By giving the possibility of mixing organic material from different outlets, it becomes possible to graft the incoming material either with an optimal mixture of organic material and/or micro organisms that will optimize the biogas production. Sanitation of the organic material that is used in the biogas reactor is ensured. The biogas reactor demands less energy, the production of biogas is faster, and all production processes can be performed in the same chamber.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing biogas using biogas reactor.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biogas reactor.    Biogas reactor (1)    Inlet of housing (2)    Biogas outlet (3)    Shaft (5)    Material displacement device (6)    Housing (7)    Gas producing section (10)    Outlets of gas producing section (12,13)    Baffle (17)
NOVELTY - A kind of marsh gas purifying system, comprising: the first stage inlet separator, a granular solid material and water to form a purifying marsh gas in the marsh gas removing marsh gas generated by the light source, the first stage compressor is connected with the first stage inlet separator for compressing the first purifying marsh gas to form a compressed gas, the compressor is connected with the first stage compressor, for compressing said first compressed gas to form a compressed gas, the inlet separator is connected with the secondary compressor, which is used for removing the second compression in the marsh gas for particulate solid material and water to form a purifying marsh gas, and purifying device is connected with the secondary inlet separator for removing the second purifying of marsh gas is carbon dioxide and water to obtain the purified marsh gas. The marsh gas purifying system capable of improving the content of methane in marsh gas.
NOVELTY - This utility model claims a biomass dry distillation and drying device, comprising a drying tower, a vertical drainage device, of a combustion system, the dry distillation reactor dry distillation reactor feeding device, a dry distillation reactor, reactor gas collection and utilization system, a gas carbon discharge water tank,... This utility model can transform the biomass to a fuel gas, and a carbon to realize energy circulation and recycling, this utility model adopts said structure greatly improves the reaction speed of the dry distillation, the cooling and drying the biomass gas at the same time to greatly save the energy of the first plate. It can be widely used in treatment of domestic garbage of kitchen waste, medical waste, sludge and so on from the harmless and resource, said angle.
NOVELTY - A biomass fuel gas energy-saving furnace, the utility model is provided with an ash outlet (18 at the bottom of the furnace body (1), furnace body (1) is annular and is provided with a water tank (12), a furnace cover (13) and the water tank (12) furnace body cylinder (14), air outlet pipe (3) is connected with one end of the side connected with the upper end of the furnace body (1), and the other end is connected with the purifier (4), one end of the air inlet pipe (2) is connected with the lower end of the furnace body (1), and the other end is connected with the fan (5). The utility model is provided with a is capable of burning the domestic garbage as fuel in the combustible, combustion efficiency is high, there is no smoke and dust, environment-friendly, energy-saving high-efficiency energy-saving;
NOVELTY - The utility model claims a biomass carbonizing, calorific value gas centralized gas supply system, comprising a carbonizing device, distillation device, cooling device and staticizing transmission and distribution device, wherein the kiln device is connected with the dry distillation device is connected with a kiln device produced gas supply dry distillation kettle for heating in the carbon production process, the dry distillation device is connected with the cooling purifying device, wherein the cooling purifying device and the distribution device is connected with air storage tank, air storage tank is connected with the air cylinder. Using carbonizing and carbonization to achieve biomass carbon, gas, oil, liquid co-producing, gas concentration. A carbonizing device with large volume, high yield and at the same time capable of producing gas, wood tar and pyroligneous, gas is directly supplied to a dry distillation kettle for heating, which saves a destructive distilling and heating fuel, reduce the operation cost.
NOVELTY - A carbon-based solid acid catalyst structure is obtained by growing carbon nanotubes on surface of stainless steel material as support material, and vulcanizing and oxidizing polysulfide on carbon nanotubes.    USE - Carbon-based solid acid catalyst structure is used for biodiesel product.    ADVANTAGE - The carbon-based solid acid catalyst structure is efficiently prepared with high purity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of carbon-based solid acid catalyst structure.
NOVELTY - A bio-based corrosion inhibitor of methanol and gasoline contains 30-40 volume% metal corrosion component comprising 2,6- di-t-butyl-p-cresol as aliphatic phenol and N,N'-disalicylidene propylene diamine as fatty amine, 30-35 volume% chelating component containing benzotriazole fatty amine salt, and 25-40 volume% oxidation inhibition component containing yeast fatty acid soap containing 16-18C fatty acid oil yeast extract and petroleum yeast, and fatty acid amine.    USE - Bio-based corrosion inhibitor of methanol and gasoline (claimed).    ADVANTAGE - The bio-based corrosion inhibitor is environmentally-friendly, non-toxic and economical, and exhibits excellent anti-corrosion effect with respect to brass, steel, zinc, aluminum and copper.    DETAILED DESCRIPTION - A bio-based corrosion inhibitor of methanol and gasoline contains 30-40 volume% metal corrosion component comprising 2,6- di-t-butyl-p-cresol as aliphatic phenol and N,N'-disalicylidene propylene diamine as fatty amine in volume ratio of 1:2, 30-35 volume% chelating component containing benzotriazole fatty amine salt, and 25-40 volume% oxidation inhibition component containing yeast fatty acid soap containing 16-18C fatty acid oil yeast extract and petroleum yeast, and fatty acid amine. The 16-18C fatty acid oil yeast extract is obtained by fermentation of oil and petroleum yeast EAM-AC16 with deposition number of CGMCC NO.7429. An INDEPENDENT CLAIM is included for preparation of bio-based corrosion inhibitor of methanol and gasoline.
NOVELTY - Preparation of anhydrous crystal form I of sitagliptin phosphate involves crystallizing by stirring a suspension of sitagliptin phosphate solid at a crystallization temperature, separating crystallized crystals, washing, and drying to obtain anhydrous crystal form I of sitagliptin phosphate. The suspension contains solvent chosen from acetone, acetonitrile, mixture of 1-4C alkanol and water, mixture of ethylene glycol and water, mixture of acetone and water, and mixture of acetonitrile and water.    USE - Preparation of anhydrous crystal form of sitagliptin phosphate used for pharmaceutical composition (claimed).    ADVANTAGE - The anhydrous crystal form of sitagliptin phosphate having favorable quality is prepared under mild reaction conditions by simple and energy-saving method, with high product yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for pharmaceutical composition, which comprises predetermined amount of the anhydrous crystal form I of sitagliptin phosphate, and auxiliary material(s).
NOVELTY - Preparation of erlotinib hydrochloride crystal involves dissolving erlotinib free alkali monomer in mixed solvent of alcohol and solvent chosen from ketone, halogenated hydrocarbon, ester and ether.    USE - Preparation of erlotinib hydrochloride crystal (claimed).    ADVANTAGE - The erlotinib hydrochloride crystal is stably produced without affecting the environment.
NOVELTY - The apparatus has a processing tank having an inlet port. A water tank is connected with portion of processing tank. A heater is installed at the water tank so as to heat the fluid in water tank. A driver is installed inside the processing tank, for rotating a rotation shaft on which an outside transfer screw and inner side transfer screw are integrally mounted. A controller is arranged to control the heater or the driver.    USE - Apparatus for treating organic waste e.g. food waste or livestock excretion, during production of fertilizer.    ADVANTAGE - The organic waste and sawdust in the processing tank can be effectively mixed by rotation of outside transfer screw and inner side transfer screw, so that microorganism in organic waste can be optimized. Thus high quality fertilizer of organic matter can be produced.
NOVELTY - Preparing clean biomass fuel comprises mixing wet cow dung and 15-25 wt.% straw fibers in a stirrer, transferring the mixture into stockyard for aerobic fermentation, dehydrating the fermented mixture to 40-60%, transferring into pressure ball machine and naturally drying the obtained fuel pellets.    USE - The method is useful for preparing clean biomass fuel using wet cow dung (claimed).    ADVANTAGE - The method is simple, economical and converts waste into useful product.
NOVELTY - A sugarcane leaf pelleting machine comprises: on base (11) electric motor (1) connected with coupling (2) and speed reduction box (3), and connected with rolling wheel (5) through vertical rotating shaft (6) and bearing (8), and particle forming chamber (7) that is provided with pressure plate (9), forming annular die of biomass grain and forming particle collecting plate (10), where particle formation pressure plate is provided with particle forming hole bushing (4) and rolling wheels working surface have rolling groove (12).    USE - As sugarcane leaf pelleting machine (claimed).    ADVANTAGE - The sugarcane leaf pelleting machine comprises longitudinal groove modification that according to size and diameter of hole pitch changes particle forming hole on roller working surface, which improves pressure of material as compared to that in traditional roller surface, formation of biomass grain by annular die is easier, granulating disc and rotary bearing with heat load are in best working state, extends system working time and service life, and solves problems of granulator apparatus such as small roller pressure, difficulty in particle formation using annular die, maintaining biomass grain quality, inability to work continuously for long time and high maintenance cost. The imprived sugarcane leaf pelleting machine has simple structure, can work continuously for long time, and has low maintenance cost.    DESCRIPTION OF DRAWING(S) - The figure shows the sugarcane leaf pelleting machine.    Electric motor (1)    Coupling (2)    Reduction box (3)    Particle forming hole bushing (4)    Rolling wheel (5)    Vertical rotating shaft (6)    Particle forming chamber (7)    Bearing (8)    Pressure plate (9)    Particle collecting plate (10)    Base (11)    Rolling groove (12)
NOVELTY - A biomass boiler fuel comprises: 60-80 wt.% hard material, 20-35 wt.% soft material, and 0-10 wt.% mixing material.    USE - As biomass boiler fuel, and combustion process using biomass boiler fuel (all claimed).    ADVANTAGE - The biomass boiler fuel comprises specific ratio of fuel materials that optimizes adjustment and distribution parameter of fire grate of boiler to make fuel burn completely, such that boiler has high working efficiency and improves running economical efficiency. By fuel ratio parameter boiler is convenient to adjust, has strong operability, and improves technical level of fuel ratio parameter of boiler.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for combustion process using biomass boiler fuel involving: performing combustion process at process parameters of vibration frequency of biomass boiler grate of 38-42 Hz, intervals for activating grate to vibrate of 150-350 seconds, and grate vibration time for each time of 5-7 seconds.
NOVELTY - Preparing biomass gasified tar cracking catalyst involves firstly synthesizing graphitized mesoporous carbon carrier according to equal volume dipping method, the graphitized mesoporous carbon carrier into aqueous solution containing nickel salt, ultrasonic processing and standing, then drying the material under hydrogen and nitrogen atmosphere, to obtain the nickel carrying mesoporous carbon composite catalyst.    USE - For preparing biomass gasified tar cracking catalyst (claimed).    ADVANTAGE - The method is simple; has high catalytic activity, and long service life; and has catalytic conversion rate of more than 95%.
NOVELTY - Multi-stage pyrolysis of corn stalk to form 5-hydroxymethyl furfural, 4-vinyl phenol and bio-oil, involves i) processing corn stalk to pyrolysis at 220-280 degrees C under oxygen-free condition, and then gas-solid separation to form 5-hydroxymethyl furfural; ii) passing residual solid particle obtained in step (i) under oxygen-free condition to pyrolysis at 300-380 degrees C, and then gas-solid separation to give 4-vinyl phenol; and iii) passing residual solid particles of the obtained product (ii) under oxygen-free condition to pyrolysis at 450-550 degrees C, and then to gas-solid separating to give bio-oil.    USE - In multi-stage pyrolysis of corn stalk to produce 5-hydroxymethyl furfural, 4-vinyl phenol and bio-oil (claimed).    ADVANTAGE - The method is simple; provides large scale production of 5-hydroxymethyl and 4-vinyl phenol; and produces bio-oil with high quality.
NOVELTY - Improving efficiency of biodiesel synthesis reaction involves 1) putting low carbon alcohol and raw material oil in a mol ratio of 5:1-30:1 into reaction kettle, adding acidic catalyst (0.5-5 wt.%), stirring; 2) mixing, and raising temperature of mixed liquid to 50-62 degrees C; 3) starting circulating pump, opening circulation pump of reaction kettle at bottom of mixed solution, where mixed liquid with the bottom of kettle goes to reaction kettle top, spraying then to reaction kettle through liquid jet device, circulating for 2 hours, until sampling assay, and 4) separating.    USE - For improving efficiency of biodiesel synthesis reaction (claimed).    ADVANTAGE - The method realizes liquid phase reaction and vapor-liquid phase reaction, has mild reaction condition, short reaction time and high reaction efficiency, and is easy for large-scale industrial production.    DETAILED DESCRIPTION - Improving efficiency of biodiesel synthesis reaction involves 1) putting low carbon alcohol and raw material oil in a mol ratio of 5:1-30:1 into reaction kettle, adding acidic catalyst (0.5-5 wt.%) into the reaction kettle, stirring; 2) mixing, and raising temperature of mixed liquid to 50-62 degrees C; 3) starting circulating pump, opening circulation pump of reaction kettle at bottom of mixed solution, where the mixed liquid with the bottom of the reaction kettle goes to the reaction kettle top, spraying then to the reaction kettle through a liquid jet device, circulating for 2 hours, until sampling assay, 4) separating: after the reaction is finished, dividing into layers, where the upper layer is biodiesel.
NOVELTY - The utility model claims a kind of a metal magnesium or aluminum continuous hydrogen-making combined supplying system of heat and power device, comprising a reactor, a liquid box, a metal magnesium or aluminium, hydrogen fuel battery, the tail material box, hot water system, a peristaltic pump, a water supply pump, a hydrogen circulating pump, the first electromagnetic valve, an electric ball valve, a third electromagnetic valve, a fourth electromagnetic valve, a fifth electromagnetic valve, a water-gas separating drain valve, a first pressure sensor, a second pressure sensor, a liquid level sensor, a liquid level sensor, a third liquid level sensor, the liquid level sensor, the fifth liquid level sensor, an intelligent control unit, wherein the reactor is a sealed container, in the reactor is provided with a liquid level sensor and a liquid level of the second liquid level sensor and low liquid level, the top of the reactor through the pipeline. This utility model is suitable for generating heating, has scientific design, reasonable structure, convenient making, safe and environment-friendly energy-saving.
NOVELTY - The utility model claims a kind of a metal magnesium continuous producing hydrogen and magnesium hydroxide, comprising a reactor, a water tank, a metal magnesium, hydrogen fuel battery, the tail material box, a hydrogen collecting tank, a radiator, a pump, a water pump, a hydrogen circulating pump, the first electromagnetic valve, an electric ball valve, a third electromagnetic valve, a fourth electromagnetic valve, a water-gas separating drain valve, a first pressure sensor, a second pressure sensor, a liquid level sensor, a liquid level sensor, a third liquid level sensor, the liquid level sensor, the fifth liquid level sensor, an intelligent control unit, wherein the reactor is a sealed container, in the reactor is provided with a liquid level sensor and a liquid level of the second liquid level sensor and low liquid level, the top of the reactor through the pipeline. This utility model is suitable for power generation, heating and is provided with scientific design, reasonable structure, convenient making, safe and environment-friendly energy-saving.
NOVELTY - A kind of efficient anaerobic reactor, relating to the technical field of environment-friendly device, comprising an anaerobic reaction tank, an anaerobic reaction tank is connected a water inlet pipe passes through the lower end of the backflow pipe connected with the gas-liquid separator, an anaerobic reaction tank, an anaerobic reaction tank on the right side is connected with the water outlet pipe, an anaerobic reaction tank comprises a first reaction chamber and a second reaction chamber, a reaction chamber is provided with a first reaction chamber gas skirt, a first reaction chamber gas skirt is set at the upper end of the second reaction chamber gas skirt through biogas lift pipe connected with the gas-liquid separator, a second reaction chamber, the second reaction chamber gas skirt upper end of the gas collecting pipe connected with the gas-liquid separator, a first reaction chamber gas skirt and the second reaction chamber gas skirt lower part are provided with an air seal. This utility model has simple and reasonable structure design, it has high volume load rate, in the inner cycle because of the anaerobic reaction tank, the mass transfer effect, large amount of sludge age is long, the reaction efficiency is high, it saves investment and floor area and low running cost.
NOVELTY - The layer has a removable separation layered body (3) separating a refractory lining (1) of a bottom of a metallic combustion boiler. Stuck pieces (2) are produced by melting biomass ash from biomass. The layered body is penetrated in the stuck pieces that are arranged in an upper part (4). The layered body is chemically inert relative to the refractory lining at temperature value of 1700 degree Celsius. The layered body is formed by loose inert material with particle size in range of 0.3 to 0.6 mm. The layered body is made of arenaceous quartz and zirconic sand based on zirconium silicate.    USE - Protective layer for preventing sticking of biomass ash to an internal refractory lining of a combustion boiler.    DESCRIPTION OF DRAWING(S) - The drawing shows a sectional view of a protective layer.    Refractory lining (1)    Stuck pieces (2)    Removable separation layered body (3)    Upper part (4)
NOVELTY - The utility model claims a kind of the biological carrier and ecological restoration technology for breeding sewage of the system, the system comprises in turn through a pipeline connected with a sedimentation tank, a diluting air tank, a filter tank, open plant cell, plant and fish pond. Compared with the existing technology, this utility model claims a biological treatment, purifying technology and device of high efficiency and low energy consumption in livestock and poultry breeding sewage, making the heavy eutrophic culture field biogas liquid livestock and poultry breeding sewage discharge standard by biological carrier and multilevel ecological water treatment cleaning system, the utility model is simple operation and a construction cost and operation cost and management cost is low, good sewage treatment effect, providing important guarantee for the production of ecological agriculture and non-polluted agricultural products.
NOVELTY - A biological oil is prepared by completely mixing bio-oil and additive in which additive consists of octanol and micro-molecular alcohol and micro-molecular alcohol consists of methanol, ethanol, propanol, isopropanol, or butanol.    USE - Preparation of biological oil (claimed).    ADVANTAGE - Preparation process is simple and low in cost, improves stability, and has convenient operation, and biological oil has low moisture and viscosity growth rates and long shelf-life.
NOVELTY - A biomass combustion gas preparing method involves grinding biomass reaction material, followed by carrying out gasification reaction to produce synthesis gas. The obtained gas is purified to remove particulates, acid gases and tar. The gas is deeply purified to remove sulfide, followed by carrying out methanation, and removing saturated water vapor, carbon dioxide and unreacted hydrogen and nitrogen.    USE - Method for preparing biomass combustion gas by utilizing solid organic waste.    ADVANTAGE - The method enables preparing fuel gas with reduced burning of coke oil content, and improving production rate.
NOVELTY - The device has a coal economizer (3) and an air pre-heater (4) fixed on a tail gas channel that is arranged in a tail smoke channel (2) and a desulfurization device (5). A bag-type duster (6), a draught fan (7) and a chimney are connected with a high temperature dust remover (9). A high temperature fan (10) is connected with a low temperature pyrolytic carbonization furnace (11) that is provided with a drying chamber (1101) and a carbonization chamber. A biomass carbon discharge hole is formed on a cooling device (15).    USE - Boiler flue gas low temperature pyrolysis biomass device.    ADVANTAGE - The device fully utilizes a waste heat boiler flue gas and provides high carbon producing rate and high energy comprehensive utilization rate. The device is convenient to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a boiler flue gas low temperature pyrolysis biomass method.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a boiler flue gas low temperature pyrolysis biomass device.'(Drawing includes non-English language text)'    Tail smoke channel (2)    Coal economizer (3)    Air pre-heater (4)    Desulfurization device (5)    Bag-type duster (6)    Draught fan (7)    High temperature dust remover (9)    High temperature fan (10)    Low temperature pyrolytic carbonization furnace (11)    Cooling device (15)    Drying chamber (1101)
NOVELTY - The method involves utilizing fuel to generate gas by a pyrolysis process. Carbon monoxide is obtained from reaction of carbon dioxide with charcoal. A biomass is arranged with an oven grill for the pyrolysis process. Temperature of the gas is reduced through a heat exchanger. Nitrogen oxide (NOx) and sodium oxide (Sox) are removed from the gas by filtering process. A gas engine is coupled with an electric generator to drive a gas combustion engine for production of carbon monoxide (CO) by pyrolysis process. Combustion gases are mixed with hydrogen, carbon monoxide and carbon dioxide.    USE - Method for obtaining electrical energy from renewable biomass.    ADVANTAGE - The method enables using biomass source, so as to generate electrical energy in independent manner, improving energy efficiency of the biomass source, producing electrical energy from hydrogen, and utilizing a renewable energy source so that cost of electric energy generation is low.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram illustrating a method for obtaining electrical energy from renewable biomass.
NOVELTY - The system has an igniting device arranged at an air inlet of a combustion chamber, where an outlet of bottom of the combustion chamber is connected with a discharging pipe. An upper part of a raw material storage tank is provided with a raw material inlet, where a lower part of the raw material storage tank is provided with a raw material outlet. An air pipeline is connected with a fan inlet in a carbide furnace that is provided with a biomass material inlet. A flue gas dedusting ash hopper is arranged on a flue gas outlet pipe.    USE - Biomass dry carbonization system.    ADVANTAGE - The system has high thermal efficiency during entire biomass carbonization process, and achieves final solid coke yield upto 50-60 percentage.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a biomass dry carbonization system.
NOVELTY - An acrylonitrile waste gas removing method involves preparing a catalyst. Different contents of transition metals are uniformly loaded on a carrier. A copper is loaded to the catalyst carrier followed drying and baking to obtain an acrylonitrile tail gas catalytic combustion catalyst. The catalyst is prepared by placing in a fixed bed quartz tube reactor followed by adding the acrylonitrile and mixed gas of oxygen and nitrogen into a reaction furnace, combusting, catalyzing and removing the waste gas.    USE - Method for removing acrylonitrile waste gas.    ADVANTAGE - The method enables removing acrylonitrile waste gas with better effect.    DETAILED DESCRIPTION - An acrylonitrile waste gas removing method involves preparing a catalyst by taking a microporous molecular sieve ZSM-5 as a carrier. Different contents of transition metals are uniformly loaded on a carrier using a rotary evaporation impregnation. A 2 % copper is loaded to the 10 % catalyst carrier, where the carrier is silicon-aluminum of silicon dioxide/aluminum oxide with weight ratio of 26-347 followed drying and baking to obtain an acrylonitrile tail gas catalytic combustion catalyst. The catalyst is prepared by placing in a fixed bed quartz tube reactor at 150-500 degrees C followed by adding the acrylonitrile and mixed gas of oxygen and nitrogen with space velocity of 10000-37000 h-1 into a reaction furnace, combusting, catalyzing and removing the waste gas, where the volume ratio of the acrylonitrile and oxygen is 0.3:1-10.
NOVELTY - Alcohol-based fuel oil comprises 70-75 pts. wt. methanol, 4-6 pts. wt. dimethylbenzene, 200 pts. wt. solvent oil, 4-6 pts. wt. paraffin oil, 4-6 pts. wt. glycerol and 5-10 pts. wt. water.    USE - Alcohol-based fuel oil.    ADVANTAGE - The fuel oil is clean, efficient, stable, economical and safe.
NOVELTY - Inoculum accelerator comprises methanobacterium of class Euryarchaeota, domain Archaea and order Methanobacteriales. The methanobacterium is provided for producing insoluble gas i.e. methane for allowing the removal of organic carbon from anaerobic environment by using hydrogen and fermented organic compound for the production of acetic acid.    USE - Inoculum accelerator used in biogas digesters for accelerating the processing of litter.    ADVANTAGE - The inoculum accelerator enables to accelerate the processing of litter efficiently.
NOVELTY - Fertilizer is prepared using 20-22 pts. wt. nitrogen fertilizer, 12-14 pts. wt. phosphate fertilizer, 13-15 pts. wt. potash fertilizer, 2-3 pts. wt. microelement fertilizer, 3-5 pts. wt. fermented waste tea leaves and 1-2 pts. wt. additive. The microelement fertilizer comprises calcium oxide, sodium borate and zinc in a ratio of 2:1:1. The additive is rock phosphate powder, diatomaceous earth or phoxim (pesticide).    USE - The fertilizer is useful for strengthening corn (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) mixing waste tea leaves and anaerobic strains chosen from Erwinia carotovora, Lactobacillus acidophilus and Bacillus in a ratio of 1:1000-1:200 to obtain mixture, (b) adding water to the mixture obtained in step (a) in a ratio of 10:5-10:7, and fermenting the mixture at 35-66 degrees C for 4-6 days, and (c) drying the fermented residue, granulating and mixing the granules with nitrogenous fertilizer, phosphate fertilizer, potash fertilizer and micronutrient fertilizer using special apparatus, stirring uniformly and then regranulating to obtain the product.
NOVELTY - Production of charcoal involves controlling moisture of timber having length of 15-20 cm and diameter of 3-6 cm to 5-12%, by keeping timber in open space for 1-2 days, coating carbon on timber, heat-treating at 160-180 degrees C for 4-6 hours, pre-carbonizing at 200-300 degrees C for 2-3 hours, carbonizing at 400-600 degrees C for 5-7 hours, cooling to room temperature, pulverizing charcoal particles to size of 1-2 mm, adding asphalt binder and fine coal powder, stirring for 0.5-1 hour, compression-molding, drying for 1-2 hours, and heating to 500-700 degrees C for 4-6 hours.    USE - Production of charcoal (claimed).    ADVANTAGE - The method efficiently and economically provides high-calorific-value charcoal.    DETAILED DESCRIPTION - Production of charcoal involves controlling moisture of timber having length of 15-20 cm and diameter of 3-6 cm to 5-12%, by keeping timber in open space for 1-2 days, coating carbon on timber, heat-treating at 160-180 degrees C for 4-6 hours, pre-carbonizing at 200-300 degrees C for 2-3 hours, carbonizing at 400-600 degrees C for 5-7 hours, cooling to room temperature, pulverizing charcoal particles to size of 1-2 mm, adding asphalt binder and fine coal powder, stirring for 0.5-1 hour, compression-molding, drying for 1-2 hours, and heating to 500-700 degrees C for 4-6 hours.
NOVELTY - Fertilizer comprises 500-1000 g bovine blood, 2000-3000 g livestock and poultry excrement mixture, 100-200 g cane sugar and 2500-3000 g organic soil.    USE - The fertilizer is useful for improving yield of peach trees (claimed).    ADVANTAGE - The fertilizer is prepared by simple method using widely available and low cost raw materials source, and increases yield of peaches by 28%. The peach fruit has good mouthfeel, size of 1 cm longer than common fruit and more sufficient water content.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method of preparing the fertilizer, which involves mixing bovine blood, livestock and poultry excrement mixture, cane sugar and organic soil, adding mixture into fermentation tank, and fermenting the mixture for 9-11 days.
NOVELTY - Method for preparing biofertilizer, involves culturing Rhizobium, Azotobacter chroococcum, Bacillus megaterium and B.mucilaginosus, respectively, to obtain microbial fertilizer composition, where the seed culture includes 2-3 ml Rhizobium, 2-4 ml A.chroococcum, 1-2 ml B.megaterium and 1-2 ml B.mucilaginosus.    USE - The method is useful for preparing biofertilizer which is used for flue-cured tobacco (claimed).    ADVANTAGE - The biofertilizer improves yield and quality of tobacco, disease resistance and stress resistance of tobacco, soil structure, ecological environment, and utilization ratio of soil nutrition of the tobacco, inhibits spreading of harmful bacteria in soil through mass propagation of beneficial microorganism, decomposes insoluble phosphorus and potassium in the soil into soluble phosphorus and potassium to be absorbed by crops, increases organic nutrition and inorganic nutrition to the plants to prevent loss of nutrition, reduces application amount of the fertilizer, and overcomes soil caking caused by mass application of fertilizer in successive years.
NOVELTY - An apparatus consists of liquid fertilizer manufacturing unit, blower, deodorization tower, water injection area, high-temperature high-speed fermentation unit, and control unit for controlling additive input of high-temperature high-speed fermentation unit.    USE - Apparatus is used for manufacturing liquid fertilizer from livestock excretion.
NOVELTY - A fuel biomass comprises agricultural biomass such as origin potato pulp, wheat straw, waste cereal grains, grasses, stems, sunflower husk and sugar sorghum    USE - Fuel biomass for use in co-firing boilers in houses, flats and public buildings, and power stations installed in municipalities and industries.    ADVANTAGE - The fuel biomass improves softening temperature of boilers , reduces corrosion of structural steel high-temperature boiler and furnace parts.
NOVELTY - Manufacturing granular organic fertilizer composition, comprises preparing a raw material powder comprising siliceous compound, calcium compound, and organic matter, mixing the material powder and an acidic solution, and granulating in an assembler to form particles, and drying the particles.    USE - The method is useful for manufacturing granular organic fertilizer composition (claimed).    ADVANTAGE - The fertilizer composition has simple manufacturing process, increases the crop growth and yield, and ensures convenient fertilization and thus saves labor.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the granular organic fertilizer composition, comprising siliceous compound, calcium compound, organic matter and trace elements in a granular powder form.    DESCRIPTION OF DRAWING(S) - The figure shows a schematic process flow for manufacturing granular organic fertilizer composition (Drawing includes non-English language text).
NOVELTY - The apparatus has a heat exchanger (80) that heat-exchanges the outside air supplied to a gas circulation unit (72). The gas circulation unit circulates the outside air to a combustion device (30) through a dryer (60). A waste product supplying unit (10) is provided to supply the combustible waste. An absorbent manufacture unit (100) is provided to manufacture an absorbent, and to synthesize the discard incinerate material to the zeolite material. The mixture of silicone, sodium hydroxide, potassium hydroxide and aluminum component are provided in gasification unit.    USE - Combustible waste gasification apparatus.    ADVANTAGE - Since the generation rate of the discard incinerate material is reduced, the environmental contamination is reduced. The manufacturing cost of the combustible waste gasification apparatus is reduced. The adsorption performance and ion exchange performance of the combustible waste gasification apparatus are improved effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for manufacturing adsorbent.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the combustible waste gasification apparatus. (Drawing includes non-English language text)    Waste product supplying unit (10)    Combustion device (30)    Dryer (60)    Gas circulation unit (72)    Heat exchanger (80)    Absorbent manufacture unit (100)
NOVELTY - This utility model claims a kind of a raw material gas methane device, the gas is condensed into liquid to be recycled, the raw material gas pipeline to form liquid seal, the cost is saved and the economic benefit is obvious. A kind of a raw material gas methane, comprising a raw material gas pipeline, the raw material gas through the U-shaped pipe is connected with the nitrogen washing tower, a U-shaped pipeline comprises a cooling medium loop, the device comprises a bracket connected with the U-shaped pipeline of the reverse spraying pipe, spraying pipe is connected with the separating tank, separating tank is respectively connected with the nitrogen washing tower and storage tank. Increasing a reverse spraying pipe on the upper part of the U-shaped pipeline before raw material gas enters the nitrogen washing tower is connected to the separation tank, a gas-liquid separation, the separated liquid in the tank storage to a sale or for use with other device through guide pipe.
NOVELTY - The radio frequency scrubber has a screw-type tuner that is mounted on a treatment of waste gas reactor (80) for varying the length of the treatment of waste gas reactor. Multiple treatment of waste gas reactors process the waste gas with the plasma discharge phenomenon with super high frequency. A power supply unit (10) provides electricity to a high frequency oscillator (20). A temperature sensor (110) measures the inner temperature of the treatment of waste gas reactor. An oxygen generator (70) supplies oxygen to treatment of waste gas reactors.    USE - Radio frequency scrubber for waste gas.    ADVANTAGE - The treatment of waste gas reactors process the waste gas with the plasma discharge phenomenon with super high frequency, and thus reduces time and cost to process waste gas, ensures mass production, maintenance, simple structure and repair of the radio frequency scrubber, and also easily controls frequency of the radio frequency scrubber.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a radio frequency scrubber. (Drawing includes non-English language text).    Power supply unit (10)    High frequency oscillator (20)    Oxygen generator (70)    Treatment of waste gas reactor (80)    Temperature sensor (110)
NOVELTY - Production method of glucan-chitosan complex from yeast biomass of brewing waste involves mechanical and ultrasonic treatment of yeast biomass, destruction of proteins by treatment of the obtained suspension using alkali reagents with further extraction of a target product. As biomass, Saccharomyces living yeast is used. First, yeast is frozen to -15 degrees C during 24 hours. After mechanical destruction, biomass is treated for 15 minutes at 20 degrees C in an ultrasonic bath with frequency of an emitter of 35 kHz and voltage of 285 W. Biomass is acidified with chlorhydric acid till pH=5.5 and treated with ferment preparation in the amount of one pellet containing lipase - 3500 units of Ph.Eur., amylase - 4200 units of Ph.Eur. and protease - 250 units of Ph.Eur. per kilogramme of biomass in terms of dry substance; then, lipid components of yeast are removed. Fermentation is performed at t=20-29 degrees C during 30-60 minutes. Destruction of proteins is performed at 55 degrees C by means of a water bath during 60 minutes by treatment using 4% water solution of caustic soda at the ratio of yeast biomass and alkali, which is equal to 1:4. The medium is neutralised and hydrosol of glucan-chitosan complex is deposited by centrifugation during 10 minutes. The deposit is dried at t=55 degrees C during 48 hours.    USE - Biotechnologies.    ADVANTAGE - Invention allows improving the quality of the obtained complex and its biological activity.3 ex
NOVELTY - Rhodium doped strontium-titanate particles have primary particle diameter of 70 nm or less. The rhodium doped strontium-titanate particles have light absorption rate of 0.6 or more at wavelength of 570 nm and 0.7 or more at wavelength of 1800 nm.    USE - Rhodium doped strontium-titanate particles are used as hydrolyzing photocatalyst (claimed) for manufacturing hydrogen.    ADVANTAGE - The rhodium doped strontium-titanate particles has excellent photocatalytic activity and crystallinity, and high specific surface area.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) hydrolyzing photocatalyst, which contains rhodium doped strontium-titanate particles;    (2) manufacture of rhodium doped strontium-titanate particles, which involves preparing aqueous solution by dissolving titanium compound, rhodium compound, strontium compound and hydrophobic complex agent in water, drying, and baking; and    (3) hydrolyzing method, which involves contacting water and rhodium doped strontium-titanate particles, and irradiating visible light.
NOVELTY - The system (10) has high pressure gas-liquid separation apparatus (22) which carries out gas-liquid separation of high-pressure hydrogen led-out from water-electrolysis apparatus (12). A waste-water line (26) emits high pressure liquid water separated with high pressure gas-liquid separation apparatus. A permeate flow rate variable mechanism (98) changes water quantity transmitted from anode side of electrolysis apparatus to cathode side, so that permeate flow rate emitted from electrolysis apparatus is adjusted to become setting water quantity of orifice in line.    USE - Water-electrolysis system.    ADVANTAGE - Since the permeate flow rate emitted from the water-electrolysis apparatus is adjusted to become setting water quantity of the orifice, the valve is maintained to drain regularly on waste-water line from gas-liquid separation apparatus. Hence the count of control of valve on which high-pressure water acts as much as possible can be reduced, and durability of the valve can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the operating method of water-electrolysis system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the water-electrolysis system. (Drawing includes non-English language text)    Water-electrolysis system (10)    Water electrolysis apparatus (12)    High pressure gas liquid separation apparatus (22)    High pressure waste-water line (26)    Permeate flow rate variable mechanism (98)
NOVELTY - Producing butane gas, comprises: (a) anaerobic digestion of an organic raw material to produce biogas, where the digestion is performed at 30-40 degrees C; (b) treating the biogas produced from step (a) with reagent comprising lime water, potassium hydroxide at 35-45 degrees C and maintaining water pressure to 4 kg/cm2 to produce purified methane gas; and (c) treating the methane gas produced from step (b) with an acetylene radical at 160-170 degrees C.    USE - The process is useful for producing butane gas (claimed), which is useful as an alternative of liquefied petroleum gas.    ADVANTAGE - The simple process provides combustible butane gas with high yield in an economical and environmental friendly manner, and allows conversion of methane to butane at 81.8% conversion rate.
NOVELTY - This utility model claims a kind of low-concentration coal-bed secondary absorption condensation device, wherein the device is composed of a nitrogen adsorption and methane adsorption system. A methane and nitrogen at a separation coefficient of the different adsorbent, a first low-concentration coal bed gas by nitrogen in a nitrogen adsorption, nitrogen adsorbent bed, finishing the first absorbing and concentrating the above the coal bed gas and concentrated by the first time and the methane desorption separating the adsorbent, to finish the second time absorbing and concentrating of methane, a vacuum pump in methane absorption system, absorb gas in the coal bed methane concentration to 30%. The device investment cost is low, the system is simple, the separation effect is good, and it can effectively promote the recovery of low-concentration coal bed gas.
NOVELTY - This utility model claims a method for improving natural gas a gas burning efficiency of the device, belonging to the natural gas purification field, mainly composed of a furnace body, and is provided with a combustion chamber and an exhaust port of the two sides of the furnace body, a combustion chamber is provided with an air inlet and an air inlet, the end face of the combustion chamber is provided with an oxygen inlet, an igniter and a steam inlet, the steam inlet of the end point and the end point, and is connected with the end of the guide tube. This utility model stable combustion, high reaction efficiency, and it also can reduce by-product is generated, which effectively prevents blockage of the pipeline device.
NOVELTY - This utility model claims a kind of low-concentration coal-bed enrichment system pressure swing adsorption, comprising in turn connected in series connected with the air blower, a cooling device and a pressure swing adsorption device, the pressure swing adsorption device comprises at least four adsorption towers is provided with air outlet, which is used for the air inlet pipe of the absorption tower air inlet, which is used for the vacuum tube of the absorption tower vacuum extraction, a blow-down pipe of the absorption tower and a pressure boost pipe of the absorption tower, the upper part of said vacuum pipe is provided with a vacuum-pumping of the vacuum pump, the air outlet of the boosting tube is provided with sealed valve, the absorption tower and the bottom of the interface is connected with the air inlet pipe and a vacuum tube through valve, the absorption tower and the top of the interface is connected with the blow-down pipe and a boosting pipe through valve. This utility model is low-concentration coal bed gas pressure swing adsorption enrichment system can effectively improve the methane content in the coal, so as to meet the use requirement of the coal bed gas for purifying natural gas.
NOVELTY - The method involves removing trace organic pollutants in gas from an air inlet (2). Hydrogen peroxide is added into a hydrogen peroxide tank (8). Hydrogen peroxide is volatilized and uniformly mixed through a perforated gas distribution plate (4). Organic pollutants in hydrogen peroxide solution are entered into a middle homogeneous catalytic oxidation chamber. UV light gas is passed through an iron oxide particle filter material layer (6). Volatile organic pollutant catalyzing and oxidizing process is performed to remove water vapor and hydrogen peroxide gas.    USE - Organic pollutant gas purifying method.    ADVANTAGE - The method enables completely removing volatile organic matter and hydrogen peroxide through the iron oxide particle filter material layer by performing Fenton oxidation reaction treatment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for an organic pollutant gas purifying device.    DESCRIPTION OF DRAWING(S) - The drawing shows a front view of a radiator shell.    Air inlet (2)    Perforated gas distribution plate (4)    Iron oxide particle filter material layer (6)    Hydrogen peroxide tank (8)
NOVELTY - The method involves obtaining castor oil by hydrogenation deoxidization reaction. The castor oil is mixed with raw materials under deoxygenation catalyst reaction of 200-450 degrees centigrade. Feeding speed of the hydrogenation deoxidization reaction is 0.1-5 per hours, and reaction pressure is in range of 2-10 MPa. Hydrogen isomerization products are obtained by stage fractionation process at 200-500 degrees centigrade.    USE - Bio based aviation fuel castor-oil preparation method.    ADVANTAGE - The method enables reducing carbon deposit and sulfur compounds in an engine, so as to reduce environmental pollution.
NOVELTY - The system has propane gas-liquid separating tanks (V1-1-V1-4) that are connected with propane heat exchanger (CB-1). A compressing unit is provided with ethane compressor (C2-1). The ethane gas-liquid separating tanks (V2-1-V2-3) are connected to ethane heat exchanger (CB-2). The methane compressors (C3-1,C3-2) and methane compressor cooler (E3-1,E3-2) are connected with methane heat exchanger (CB-3). The methane compressor (C3-2) is connected with nitrogen deep circulation mechanism. A nitrogen economizer (E4-2) and nitrogen expansion compressor (C4-2) are connected with each other.    USE - Natural gas liquefaction tandem type liquefying system used in manufacture of plate-fin heat exchanger device.    ADVANTAGE - The natural gas pre-cooling heat load on the liquefying system is reduced. The productivity of the plate-fin heat exchanger device is improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the natural gas liquefaction tandem type liquefying system.    Ethane compressor (C2-1)    Methane compressors (C3-1,C3-2)    Nitrogen expansion compressor (C4-2)    Propane heat exchanger (CB-1)    Ethane heat exchanger (CB-2)    Methane heat exchanger (CB-3)    Methane compressor coolers (E3-1,E3-2)    Nitrogen economizer (E4-2)    Propane gas-liquid separating tanks (V1-1-V1-4)    Ethane gas-liquid separating tanks (V2-1-V2-3)
NOVELTY - Production (M1) of an alkylbenzene product from natural oil involves deoxygenating natural oil to form paraffins; hydrocracking first portion of paraffins to form first stream of normal or lightly branched paraffins in 9-14C and second stream of isoparaffins; dehydrogenating first stream to provide mono-olefins; optionally recycling the hydrogen to support deoxygenation of natural oil; alkylating benzene with mono-olefins under alkylation conditions to provide alkylation effluent comprising alkylbenzenes and benzene; and isolating alkylbenzenes to provide alkylbenzene product.    USE - For production of alkylbenzene from natural oil (claimed) and for producing biofuel.    ADVANTAGE - The methods provide production of alkylbenzene and biofuel from natural oils i.e. oils that are not extracted from the earth; and produce renewable alkylbenzenes and biofuels from easily processed triglycerides and fatty acids from vegetable, nut, and/or seed oils.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method (M2) for production of alkylbenzene product from natural oil source triglycerides involving deoxygenating triglycerides to form deoxygenated product comprising water, carbon dioxide, propane, first portion of paraffins and second portion of paraffins; fractionating deoxygenated product to separate first and second stream of paraffins; hydrocracking first stream of paraffins to form normal paraffin stream and isoparaffin stream; dehydrogenating normal paraffin stream to provide mono-olefins; alkylating benzene with mono-olefins under alkylation conditions to provide alkylation effluent comprising alkylbenzenes and benzene; and isolating alkylbenzenes to provide alkylbenzene product.
NOVELTY - Method for preparing nutritional additive, involves culturing microalgae in culture medium, producing biomass derived from the microalgae in the medium, and adding acid to the biomass in order to hydrolyze the biomass and preparing hydrolyzate of biomass as nutritional additive. The acid is acid chosen from sulfuric acid, hydrochloric acid, nitric acid and phosphoric acid.    USE - The method is useful for preparing nutritional additive (claimed) which is used in biofuel, foodstuff, feed additive, pharmaceutical and bioactive substance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing target substance, which involves culturing microalgae or microorganisms in culture medium comprising the nutritional additive.
NOVELTY - Method for saccharifying biomass, involves saccharifying biomass with the protein (A), protein (B), or enzyme composition.    USE - The method is useful for saccharifying biomass chosen from processed material of timber or ground material, pulps, papers, bagasse, rice straw, maize stalk or leaf, palm empty fruit bunch (EFB), plant husk, and algae for producing sugar (all claimed).    ADVANTAGE - The method is cost-effective.    DETAILED DESCRIPTION - Method for saccharifying biomass, involves saccharifying biomass with the protein (A), protein (B), or enzyme composition, where the protein (A) comprises an amino acid sequence of SEQ ID NO: 2, having 85% or more of sequence identity with the amino acid of SEQ ID NO: 2, or in which one or several amino acids are deleted, substituted or added in amino acid sequence of SEQ ID NO: 2, and has xylanase activity, the protein (B) comprises an amino acid sequence of SEQ ID NO: 12, having 90% or more of sequence identity with the amino acid sequence of SEQ ID NO: 12 or in which one or several amino acids are deleted, substituted or added in the amino acid sequence of SEQ ID NO: 12, and has xylanase activity. Sequences not defined here may be found at ftp://ftp.wipo.int/pub/published_pct_sequences/publication. An INDEPENDENT CLAIM is included for method for producing sugar, involves performing above-cited steps.
NOVELTY - Providing (M1) a recombinant microorganism involves: a) providing a hybrid microorganism containing DNA from a host microorganism and a donor microorganism; and b) fusing DNA extracted from a second microorganism into the hybrid microorganism to form the recombinant microorganism.    USE - For producing a recombinant microorganism selected from bacteria, fungi, and yeast, preferably host or donor yeast cell capable of fermenting xylose, which is useful for fermenting sugar selected from hexoses, pentoses, and/or disaccharides to produce ethanol, where the hexoses are selected from glucose, fructose, galactose, mannose, and/or rhamnose, the pentoses are selected from xylose, L-arabinose, D-arabinose, and/or ribose, and the disaccharides are selected from sucrose, lactose, cellobiose, and/or maltose. The donor yeast cell is of a genus e.g. Brettanomyces, Candida, Citeromyces, Cyniclomyces, Debaryomyces, Tetrapisispora, Vanderwaltozyma, Torulaspora, Williopsis, Zygosaccharomyces, and Zygotorulaspora (claimed). The microorganisms are also useful for producing biofuels (such as bioethanol, biobutanol, and carbohydrates), bio-based chemicals (such as organic acids, polymers, and materials) and fine chemicals (such as fragrants, nutraceutical and pharmaceutical products).    ADVANTAGE - The method of producing recombinant yeast strains is rapid and reliable; provides recombinant yeast strains with enhanced xylose-fermentation capability and enhanced ethanol tolerance; is time-saving, and easier to operate; has higher gene recombination efficiency; and allows for efficient production of biofuel, such as bioethanol, from lignocellulosic biomass. The microorganism ferments a sugar mixture containing xylose having high sugar content i.e. greater than 50 g/l, preferably 100-300 g/l with the recombinant yeast strain to produce ethanol.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for new recombinant yeast strain produced by the method (M1).
NOVELTY - Depolymerizing and solubilizing coal and coal-derived constituents, involves: treating the coal with an aqueous solution comprising at least one oxidizing agent, forming thus treated coal and coal-derived constituents; and exposing the treated coal and coal-derived constituents to an aqueous solution comprising at least one enzyme effective for reacting with coal and coal-derived constituents.    USE - The method is useful for depolymerizing and solubilizing coal and coal-derived constituents (claimed).    ADVANTAGE - The method provides improved ways for enzymatic depolymerization and solubilization of highly complex structural biopolymers found in coal.
NOVELTY - Preparing methanol from carbon dioxide comprises: combining a photoactive multi-electron collector and an electron donor in the presence of light to form a two electron reduction product; and combining the two electron reduction product and carbon dioxide in the presence of at least one catalyst thus converting carbon dioxide to methanol.    USE - The process is useful for preparing methanol from carbon dioxide that is used to produce dimethyl ether (all claimed), where the methanol and dimethyl ether are used as synthetic internal combustion engine fuels, diesel fuels, gasoline-methanol mixed fuels, convenient energy storage and transportation materials in use and transportation of liquefied natural gas (LNG) or liquefied petroleum gas (LPG) and raw materials for producing olefins (e.g. ethylene) synthetic hydrocarbons, and their products and materials even for preparing single cell proteins for human or animal consumption.    ADVANTAGE - Carbon dioxide is recycled instead of being sequestered, which provides a way of disposal to the carbon dioxide produced by coal and other fossil fuel burning power plants and industries producing large amounts of carbon dioxide. The methanol and dimethyl ether minimize or eliminate disadvantages or dangers in use and transportation of LNG or LPG.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for the methanol produced from carbon dioxide by the process.
NOVELTY - Generating fuel gas from solid waste containing an organic fraction comprising biological cells enclosed by cellular membranes, comprises: squeezing the solid waste against a grid of small-bore holes, under a pressure higher than the bursting pressure of the cells, where the organic fraction is extruded through the holes to form a gel of a doughy consistency in which most of the cellular membranes are disrupted; and subjecting the extruded gel to anaerobic fermentation in a biodigester to produce fuel gas.    USE - The process is useful for generating fuel gas from solid waste containing organic fraction.    ADVANTAGE - The process: improves efficiency in the production of fuel gas by recycling the organic fraction of municipal solid waste; reduces the formation of solid sediments at the bottom of the biodigester, thus reducing the frequency of shutdowns necessary for breaking up the bottom layer; achieves a larger production of biogas while decreasing the amount of neutralized solids and consequently the expense required for their disposal; and is advantageous in the protection of the environment, since a greater consumption of biogas entails a lower consumption of fossil fuel. The gas that is generated has a very good quality and the conversion process is completed in a shorter time span than could be achieved.
NOVELTY - Catechol is added to 2,3-diamino toluene in reaction vessel, in nitrogen atmosphere. The reaction mixture is heated, filtered and washed with hot water to obtain 1-methyl-5,10-dihydro-phenazine. Dry air is passed to the reactor and the reaction mixture is reacted for 5-7 hours at 220-250 degrees C to form 1-methyl-phenazine, which is chlorinated in the presence of azobisisobutyronitrile as catalyst at 50-100 degrees C to form 1-trichloromethyl-phenazine. 1-Trichloromethyl phenazine is reacted with water under reflux for 1-5 hours to obtain phenazine 1-carboxylic acid.    USE - Synthesis of phenazine 1-carboxylic acid (claimed).    ADVANTAGE - The method is efficient, economical and environmentally-friendly.    DETAILED DESCRIPTION - Catechol is added to predetermined amount of 2,3-diamino toluene in reaction vessel, in nitrogen atmosphere. The reaction mixture is stirred, heated to predetermined temperature, reacted, filtered and washed with 60-80 degrees C hot water to obtain intermediate of 1-methyl-5,10-dihydro-phenazine. Dry air is passed to the reactor and the reaction mixture is reacted for 5-7 hours at 220-250 degrees C to obtain 1-methyl-phenazine. 1-Methylphenazine is chlorinated in the presence of azobisisobutyronitrile as catalyst at 50-100 degrees C to form 1-trichloromethyl-phenazine. 1-Trichloromethyl phenazine is reacted with water under reflux for 1-5 hours to obtain phenazine 1-carboxylic acid.
NOVELTY - Methanol is added to a reactor and n-butanol, isooctane, methyl tert-butyl ether, and ferrocene, are added, stirred and reacted, to obtain biofuel oil.    USE - Manufacture of biofuel oil (claimed).    ADVANTAGE - The biofuel oil is manufactured with high octane value, low heat value, excellent antiknock property, improved combustion rate, charging efficiency and high combustion temperature. The biofuel reduces the nitrogen oxide emission and carbon smoke discharge of the engine.
NOVELTY - The transducer has a circuit board fixed in a shell that is provided with multiple RS-232 digital signal output terminals. The circuit board is provided with a methane and carbon monoxide sensor that is connected with an AD input end of a single chip. An output pin of the single chip is connected with a wire connecting terminal. A sensor excitation circuit is connected with the methane and carbon monoxide sensor. The output pin of the single chip is connected with a wiring terminal by a universal asynchronous receiver transmitter (UART) output port.    USE - Methane and carbon monoxide measuring transducer.    ADVANTAGE - The methane carbon monoxide sensor measures the methane and carbon monoxide that are controlled by a microcontroller through the UART and electrically EPROM (EEPROM) single chip to program parameter output threshold calibration of the sensor alarm and methane and carbon monoxide sensor AD value through the UART module for directly outputting the UART digital signals to the computer in an efficient manner.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methane and carbon monoxide detecting transducer.
NOVELTY - The tower has a rectifying tower main body filled with fractionating coal bed methane and provided with a filler. The rectifying tower main body is adhered with a fire and explosion suppression material layer. The fire and explosion suppression material layer is paved with fire retardant wire mesh and the filler. A bottom part of the rectifying tower main body is provided with an evaporator. A liquid phase outlet of a gas-liquid separating tank is connected with the rectifying tower main body.    USE - Low-concentration coal layer gas liquefaction explosion-proof rectifying tower.    ADVANTAGE - The tower has better explosion suppression performance due to arrangement of the fire retardant and explosion suppression material in the rectifying tower main body. The explosion suppression material is divided into multiple small volume elements so as to cut off explosive chain reaction and avoid explosion when extracting methane during a gas rectifying and separating process. The tower can separate oxygen from the coal bed gas to achieve high recovery rate and high purity.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a low-concentration coal layer gas liquefaction explosion-proof rectifying tower.'(Drawing includes non-English language text)'
NOVELTY - The device has several adsorption towers (7) each of which is provided with pipe joints (8,9) and gas absorption device (10). The methane gas inlet pipe (1) is connected to pipe joint (8) via ventilation air inlet valve (11). The hot flue gas pipe (2) is connected to pipe joint (9). The desorption air outlet pipe (5) is connected to pipe joint (8) via desorption outlet valve (14). The purge gas air inlet pipe (3) is connected to pipe joint (9) via a cold air inlet valve (15).    USE - Multi-tower type temperature swing adsorption type methane gas concentration device used in coal mine.    ADVANTAGE - The methane gas can be adsorbed reliably using the gas adsorption device, so that the methane gas can be concentrated efficiently. The energy consumption of the device can be reduced and the heat energy utilization of the device can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multi-tower type temperature swing adsorption type methane gas concentration device.    Methane gas inlet pipe (1)    Hot flue gas pipe (2)    Purge gas air inlet pipe (3)    Desorption air outlet pipe (5)    Adsorption tower (7)    Pipe joints (8,9)    Gas absorption device (10)    Ventilation air inlet valve (11)    Desorption outlet valve (14)    Cold air inlet valve (15)
NOVELTY - Coal is crushed in a crusher and introduced into a coal pressurization gasification apparatus to obtain crude gas. The crude gas is washed in a water-washing device to obtain gas (a) and gas water. The gas water is sent to gas water treatment unit to obtain wastewater. The wastewater and pulverized coal are fed into a coal gasification device to obtain gas (b). The gas (a) and gas (b) are methanated in a methanation unit to obtain methane product.    USE - Coal gasification of natural gas to produce methane product (claimed).    ADVANTAGE - The coal gasification of natural gas is economical and effectively utilizes the wastewater.
NOVELTY - An aminobenze aldehyde derivative (I) is reacted with acrylonitrile derivative (II) in presence of acid, to obtain 3-cyano-quinoline derivative (III).    USE - Manufacture of 3-cyano-quinoline derivative used as intermediate for pharmaceuticals-and-agrochemicals.    ADVANTAGE - The method enables efficient manufacture of 3-cyano-quinoline derivative by environmentally-friendly and simple process.    DETAILED DESCRIPTION - An aminobenze aldehyde derivative of formula (I) is reacted with acrylonitrile derivative of formula: Y'-CH=CH-CN (II) in presence of acid, to obtain 3-cyano-quinoline derivative of formula (III).    X=halo, 1-6C alkyl or 1-6C alkoxy;    n=0-4;    Y'=-OR1 or NR2R3;    R1=H, 1-4C alkyl or alkali metal;and    R2,R3=1-4C alkyl.
NOVELTY - A nickel catalyst comprises nickel dendrite.    USE - Nickel catalyst is used for hydrogen generating reaction (claimed).    ADVANTAGE - The nickel catalyst has excellent durability and stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) production of nickel catalyst for hydrogen generating reaction; and    (2) method for improving catalytic activity of hydrogen generation reaction.
NOVELTY - The high pressure separator comprises a tubular upright post arranged in an inner cavity center of the separator, an outer wall of the tubular upright post fixed with a double-spiral board, an inner wall of a separator body provided with a guide groove, a hole plate arranged in a lower part of an inner cavity of the upright post, a lower pore plate in a shape of the filler in a tubular column, a section of a liquid discharging hole arranged close to an air outlet that is provided with an exhaust hole, where an upper part of the separator is provided with an air inlet.    USE - The high pressure separator is useful for compressing and liquefying super-critical carbon dioxide and marsh gas (claimed).    ADVANTAGE - The separator has improved separation efficiency, reduced energy consumption and reduced operating cost, and is convenient to operate.    DETAILED DESCRIPTION - The high pressure separator comprises a tubular upright post arranged in an inner cavity center of the separator, an outer wall of the tubular upright post fixed with a double-spiral board, an inner wall of a separator body provided with a guide groove, a hole plate arranged in a lower part of an inner cavity of the upright post, a lower pore plate in a shape of the filler in a tubular column, a section of a liquid discharging hole arranged close to an air outlet that is provided with an exhaust hole, where an upper part of the separator is provided with an air inlet. The separator is in shell shape. An upper part of a vertical cross section of the guide groove inner wall is in ladder-shape. The filler is made of a stainless steel screen and a damping tube. The working pressure range of the separator of 25 Mpa. The purity of the methane after separating is more than 95% and the purity of the carbon dioxide is more than 99.5%.
NOVELTY - Method for composting livestock excrement, involves repeating the step of moving the livestock excrement up to a fixed depth of a surface to portion of another surface until the livestock excrement gets deposited.    USE - The method is useful for composting livestock excrement, preferably excrement of cow and horse.    ADVANTAGE - The method allows movement of only those portions of the livestock excrement which are sufficiently fermented without requirement of stirring of an unnecessary portions of the excrement and also the method does not lowers temperature to wastefulness, hence fermentation process is efficiently progressed. The method does not generate any offensive odor during the fermentation and stirring processes of the portions of the excrement that are not sufficiently fermented. The method is less laborious and cost-effective as the composting method can be efficiently performed by small hydraulic shovel, hence initial installation cost and production cost of the method is also reduced to a greater extent. The fermentation time of the composting is short.
NOVELTY - The method involves comprising load circuit with a voltage monitoring circuit. The load circuit is composed of the solar energy battery board and the hydrogen-oxygen fuel cell together. A hydrogen-oxygen fuel battery and a hydrogen storage device are connected with a pipeline. The hydrogen storage device is used for collecting the hydrogen. The pipeline is provided with an electromagnetic valve. The solar panel output voltage fluctuation signal is transmitted to the single chip computer. The output power for compensating the fluctuation of the solar panel output voltage is adjusted.    USE - Method for realizing automatic control of solar energy-hydrogen energy hybrid power driving device.    ADVANTAGE - The pressure is substantially constant can be ensured. The solar energy utilization can be improved. The economical efficiency and energy efficiency can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic block diagram of the solar energy-hydrogen energy hybrid power driving device. (Drawing includes non-English language text)
NOVELTY - Recovery of phenolic compounds from berry-processing waste comprises mixing berry-processing waste with alcohol-water mixture at weight-volume ratio of 1:20 to 1:5; macerating the mixture at 40-60 degrees C for 3-24 hours under stirring, and filtering to obtain extract comprising solubilized phenolic compounds. The volume ratio of alcohol and water is 1:1 to 1:3.    USE - Method for recovering phenolic compounds (claimed) used for preventing and treating cardiovascular diseases, and treating different types of cancer.    ADVANTAGE - The process is simple and easy to implement and control; produces extract having high concentration of phenolic compounds with antioxidant capacity; decreases environmental impact generated by disposition of berry-processing-derived waste; and satisfies current market demand for potent antioxidant products, since the major part of marketed antioxidant products are whole dried ground fruit. The use of berry-processing waste to recover high nutraceutical value compounds such as antioxidants allows manufacture of product with commercial impact while limiting disposal of this waste and reducing associated costs, with low equipment requirements. The use of berry-processing waste together with high-quality of produced extract promotes high profitability for the overall process.
NOVELTY - Alcohol ether fuel comprises 35-45% denatured methanol, 10-15% eicosapentaenoic oil, 15-20% No.200 solvent oil, and 30-35% carbon. The denatured methanol is prepared by mixing 90 pts. wt. methanol, and 10 pts. wt. additive, where the additive is prepared by mixing 20 pts. wt. propanol, 10 pts. wt. ethyl acetate, 20 pts. wt. butyl butyrate, 10 pts. wt. Tween (RTM: Polysorbate), 10 pts. wt. dimethyl carbonate, 20 pts. wt. isopropyl ether, and 10 pts. wt. dimethyl ether.    USE - The fuel is used for vehicle with low oil consumption (claimed).    ADVANTAGE - The fuel is economical, does not use gasoline as raw material, and does not require any metal antiknock agent, can adjust its octane value between 93-100, is safe to use, has low oil consumption compared to the national standard No.93 gasoline, and uses easily available and economical raw materials, thus reducing the cost.
NOVELTY - The utility model claims a water electrolysis device, comprising a power supply connected with the power supply and the electrode module, further comprising a water tank main body, said water tank main body is provided with a water storage cavity and cavity, the electrode module is arranged in the electrolysis chamber, the water storage cavity and a cell cavity is connected with the multiple through holes, wherein the water tank main body is provided with a communicated water storage cavity and the water tank main body and external environment of the water inlet and an air outlet, are set as a whole structure, it can accelerate the water circulation, electrolytic chamber in existing technology, the problem of accumulating water storage cavity and an electrolytic chamber, the electrolytic chamber to maintain the temperature at 60-75 degrees centigrade, the water vapour so as to avoid possible explosion by accumulating electrolysis, at the same time, the device produced by the gas storage cavity, capable of filtering the gas, remove the impurity in the mixed gas, the generated hydrogen and oxygen purity.
NOVELTY - Producing saxagliptin involves converting trifluoro-acetic acid (1S,5S,7R)-3-((S)-1-tert-butoxycarbonylamino-2-((R)-3-cyano-2-aza-bicyclo(3.1.0)hex-2-yl)-2-oxo-ethyl)-adamantan-1-yl ester (I) in presence of isopropyl alcohol and concentrated hydrochloric acid at 50-80 degrees C, preferably 55-75 degrees C for 0.5-4 hours, into saxagliptin.    USE - For the production of saxagliptin (claimed) which is useful for treating adult type 2 diabetes patients and hyperglycemia.    ADVANTAGE - Compared with the prior art technology, the present method utilizes the compound (I) directly into the target product, which greatly improves the rate of decline in the reaction and enhances the yield of the product, simplifies post-processing method, and thus greatly reduces generation of industrial waste water. Also the method is environment-friendly.
NOVELTY - A substituted 2-oxo-azepanium as lactam alkaline ionic liquid, is new.    USE - As a lactam alkaline ionic liquid used in catalyzing waste oil for preparing biodiesel (claimed).    ADVANTAGE - The compound (I) as lactam alkaline ionic liquid is simple to prepare; has low cost; has high catalyst activity, small dosage, and low toxicity; is easy to be biodegradable; provides mild reaction condition and short reaction time; provides simple reaction process; is easy to separate; is environment friendly; and has high utilization rate.    DETAILED DESCRIPTION - A substituted 2-oxo-azepanium compound of formula (I) as lactam alkaline ionic liquid, is new.    n=1-8, preferably 1-5;    R=H or 1-12C alkyl.    An INDEPENDENT CLAIM is included for preparing the compound (I).
NOVELTY - Method for preparing mycophenolate mofetil ester involves: in dibutyl ether as solvent, under protection of inert gas, and in presence of constant boiling water, reacting mycophenolic acid (MPA) and 2-hydroxyethyl morpholine to obtain mycophenolate mofetil ester crude product.    USE - For preparing mycophenolate mofetil ester (claimed) useful as antibacterial agent, antiviral agent, anti-tumor agent, for treating psoriasis, and preventing rejection and treating kidney transplant rejection.    ADVANTAGE - The method for preparing mycophenolate mofetil ester requires short reaction time, has high product purity such as HPLC purity of more than 97%, high reaction yield of more than 70%, low production cost, improved final product color by using ionic liquid as chelating agent to decolor crude product, thus has wide industrial application prospects. The use of high boiling point ether as solvent requires short time to finish reaction. As reaction is completed in constant boiling condition, cost is low, and there is no corrosion to device. Further reaction requires low dosage of ionic liquid and can be recycled. The process cleaning does not pollute environment.
NOVELTY - Alcohol ether biological diesel oil comprises 68-92 wt.% cetane number improver, 5-8 wt.% ether, 1.5-3 wt.% surface active agent, 0.03-1 wt.% pour point depressant, 1.32-3.5 wt.% latent solvent and 0-15 wt.% modified methanol uniformly mixing to form the base liquid is the mixed liquid of alcohol and coconut oil or coconut oil, coconut oil and the alcohol and the mixed liquid of octanol weight ratio of coconut oil alcohol and octanol is any ratio, the linear ether is ether, or alkanolamide.    USE - As alcohol ether biological diesel oil (claimed).    ADVANTAGE - The biological alcohol ether diesel combustion completeness is good, the utilization rate is high; liquidity, atomizing performance, and it is not easy to generate deposition, high safety, preparation method is simple, and low cost.    DETAILED DESCRIPTION - Alcohol ether biological diesel oil comprises 68-92 wt.% cetane number improver, 5-8 wt.% ether, 1.5-3 wt.% surface active agent, 0.03-1 wt.% pour point depressant, 1.32-3.5 wt.% latent solvent and 0-15 wt.% modified methanol uniformly mixing to form the base liquid is the mixed liquid of alcohol and coconut oil or coconut oil, coconut oil and the alcohol and the mixed liquid of octanol weight ratio of coconut oil alcohol and octanol is any ratio, the linear ether is ether, or alkanolamide, the surfactant comprises a pour point depressant comprising ethylene-acid ethylene resin copolymer, methyl acrylic ester polymer or a styrene polymer, where the cosolvent is alcohol or n-butyl alcohol, the modified methanol to form methanol and 0.15-1.5% phosphine.
NOVELTY - This utility model claims a kind of solar energy generate electricity preparing hydrogen making device for reducer medium supply system, wherein the reducing medium supply system comprises a solar energy power generation device and the solar energy power generating device provides the electricity to a hydrogen of the hydrogen producing device. The hydrogen producing device is the reduction medium supply system using solar energy power generating device provides the electricity to the water electrolysis, as a reducing gas, hydrogen can be solar electric iron ore powder of iron ore powder system for reducing hydrogen making device reduced to iron powder, belonging to the direct reaction, which avoids the iron ore powder piece manufactured process, so it is not need to use coke as the framework of the supporting column, which avoids the use of the coke, at the same time, hydrogen is used as reducing medium, realizes clean production and reduces the pollution to the environment and steel, so as to realize the super-pure steel production. This utility model further claims a solar energy power generation hydrogen production of steel-making equipment, comprising the utility model provide a reduction medium supply system.
NOVELTY - The utility model claims a hydrogen-preparing system, comprising a solar battery, an energy storage battery, a power supply control circuit, an electrolytic water generator, hydrogen storage tank and a compressor. Solar energy battery generating electricity, the electric energy can be stored in the energy storage battery, or through the current voltage stabilizer and a power supply control circuit automatically or manually connected to electrolytic water generator and a compressor to compress hydrogen production and hydrogen. Energy storage battery and a current stabilizing transformer for power supply circuit controller automatically or manually connected to electrolytic water generator and a compressor to compress hydrogen production and hydrogen. This utility model is featured with simple structure, large amount of storage, environment-friendly and energy-saving and so on, which is good for promoting the popularization and application of the solar energy.
NOVELTY - This utility model claims a vehicle-mounted hydrogen generating device, comprising an air filter and an electric door lock of vehicle, is mixed with the aqueous solution of electrolyte liquid storage tank for hydrogen generated by electrolysis of the aqueous solution in the liquid storage tank of the electrolytic machine, a cooling chamber for cooling the hydrogen generated by the cooling chamber is connected with the liquid storage tank, and the power supply of the electrolysis power supply, the cooling chamber is connected with the air outlet of the air filter. This utility model the hydrogen generated in air filter of automobile, capable of giving oil in a mixed fuel of methanol and gasoline combustion increasing automobile power, running can save more than 20% oil on a highway of the highway, it can save more than 30% oil.
NOVELTY - The system has a refining portion (50) that separates the rough biogas to methane and carbon dioxide. A compression unit fits the lead-in pressure for the membrane separation of the biogas. The separated methane is passed through the membrane separation unit (510) and the high purity carbon dioxide is collected. The methane of the trace amount included in the carbon dioxide is separated and purified and passed through the membrane separation unit (520). The separated methane is separated and passed through membrane separation unit (530).    USE - Multi-stage membrane separation system for collecting methane and carbon dioxide from biogas of organic waste from sewage disposal plant and waste water disposal plant.    ADVANTAGE - The yield of methane can be improved and the consumed energy can be saved by supplying the generated methane.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for multi-stage layer separation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the multi-stage membrane separation system.(Drawing includes non-English language text)    Refining portion (50)    Membrane separation unit (510,520,530)
NOVELTY - The system has carbon dioxide recovery unit (60) that is set with compression unit (20) for liquefaction of biogas, so as to provide to the desulfurization unit (10). The refining unit (50) is set with membrane separation unit for producing the separated methane of the high purity. The separated methane is passed through membrane separation unit. The processed carbon dioxide is passed through membrane separation unit for collecting the carbon dioxide of the high purity.    USE - System for production of biomethane and recovery of carbon dioxide.    ADVANTAGE - The consumption of energy required for production of biomethane and recovery of carbon dioxide can be saved. The high purity methane and carbon dioxide can be produced effectively. The yield of methane and carbon dioxide can be improved. The energy efficiency of the production and recovery system can be improved.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for production of biomethane and recovery of carbon dioxide.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of the production and recovery system. (Drawing includes non-English language text)    Desulfurization unit (10)    Compression unit (20)    Dehumidification unit (30)    Refining unit (50)    Carbon dioxide recovery unit (60)
NOVELTY - A highly unsaturated fatty acid or highly unsaturated fatty acid ethyl ester is produced using fats and oil containing polyunsaturated fatty acid as fatty-acid component. The highly unsaturated fatty acid or highly unsaturated fatty acid ethyl ester has reduced content of environmental pollutants. Dioxin contained in highly unsaturated fatty acid or highly unsaturated fatty acid ethyl ester contains less than 0.05 pg-TEQ/g polychlorinated dibenzo-p-dioxin (PCDD) and polychlorinated dibenzofuran (PCDF), and less than 0.03 pg-TEQ/g coplanar polychlorinated biphenyl (Co-PCB).    USE - Highly unsaturated fatty acid or highly unsaturated fatty acid ethyl ester is used for pharmaceutical, supplement or foodstuff (all claimed).    ADVANTAGE - The highly unsaturated fatty acid or highly unsaturated fatty acid ethyl ester has reduced content of environmental pollutants e.g. dioxins contained in fish oil.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of highly unsaturated fatty acid or highly unsaturated fatty acid ethyl ester involves removing free fatty acid and environmental pollutant from raw material oil containing polyunsaturated fatty acid as fatty-acid component by thin film distillation, hydrolyzing or ethyl-esterifying obtained polyunsaturated fatty acid containing fats and oils, and rectifying and column-chromatography refining.
NOVELTY - A carbaldehyde compound (II) is reacted with carbaldehyde compound (III) or (IV) in presence of boron trifluoride, to obtain pregnane derivative 16,17-acetal (ketal) compound (I).    USE - Preparation of pregnane derivative acetal (ketal) compound. Uses include but are not limited to boron trifluoride tetrahydrofuran complex, boron trifluoride ether complex, boron trifluoride acetonitrile complex and boron trifluoride methanol complex.    ADVANTAGE - The method economically provides pregnane derivative 16,17-acetal (ketal) compound with reduced environmental pollution and low-energy consumption.    DETAILED DESCRIPTION - A carbaldehyde compound of formula (II) is reacted with carbaldehyde compound of formula (III) or (IV) in presence of boron trifluoride, to obtain pregnane derivative 16,17-acetal (ketal) compound of formula (I).    R=hydroxy, halo or -OCOR7;    R7=1-12C linear or branched alkyl, 3-10C cycloalkyl, 2-8C alkenyl or 2-8C alkynyl;    R1,R2=H, 1-12C linear or branched alkyl, 3-10C cycloalkyl, 2-8C alkenyl or 2-8C alkynyl in which R1, R2 bonded with C to form 3-10C cycloalkyl;    R3=H or -OCOR8;    R8=1-12C linear or branched alkyl, or 3-10C cycloalkyl;    R4=H, fluoro or chloro;    R5=H, fluoro, chloro or methyl;and    R6=1-12C linear or branched alkyl.    R1 and R2 are not simultaneously H.
NOVELTY - This utility model belongs to the technical field of environment protection, specifically to a method for processing organic waste water, wherein the system comprises a sedimentation tank, an anaerobic tank, an composite tower type ecological filter pond, an aquatic plant pond and the biogas reactor, the upper part of the sedimentation tank is provided with a water outlet, the water outlet in turn through a pipeline and an anaerobic tank, composite tower type ecological filtering pool is connected with the, at the same time, the sedimentation tank is connected with a pipeline and a biogas reactor. This utility model using composite tower type ecological filter tank and the anaerobic tank and improves the economical efficiency of the system and improves the biological energy yield, and the sewage processing process realize ecological, low cost and capable of continuously.
NOVELTY - Production of phenolic aldehyde compound (III) involves reacting at least substituted phenol compound (I) and optionally ester compound (II) with a superacid.    USE - For the production of phenolic aldehyde compounds e.g. vanillin or its derivative (claimed) used as flavoring agent in e.g. foods, beverages and pharmaceuticals.    ADVANTAGE - The present method is environment friendly one step process, which does not need a specific pressure during the reaction; and yields 5-80 molar% of the compound (III).    DETAILED DESCRIPTION - Production of phenolic aldehyde compound of formula (III) involves reacting at least substituted phenol compound of formula (I) and optionally ester compound of formula R-O-CHO (II) with a superacid.    R1=H, alkyl, alkenyl or alkoxy;    R2 to R4=H or alkyl;    R5=H, alkyl or -CHO group;    R6=H or labile group able to leave compound of formula (I) during the reaction;    R=H, alkyl or aryl.    Provided that when compound (I) is used in the reaction without the compound (II), R5 is -CHO group.
NOVELTY - Hydrogenated sugar (sugar alcohol) is subjected to dehydration reaction to convert hydrogenated sugar into anhydrous sugar alcohol. The anhydrous sugar alcohol and distilled water which is isolated through distillation process, are subjected to decolorizing process using activated carbon. Subsequently the resultant decolorized substance is contacted with ion exchange resin to obtain anhydro sugar alcohol having reduced ion content. The average granularity of resultant distillate is 0.2-10 mm.    USE - Preparation of anhydro sugar alcohol, particularly dianhydro hexitol. Uses include but are not limited to medicine and cosmetic field, heart and blood vessel treatment, adhesive of patch, oral cleaner, food industry, plastic industry, adhesive, plasticizer, and water-soluble lacquer.    ADVANTAGE - The method efficiently and economically provides high yield of anhydro sugar alcohol having reduced ion content and conductivity, and improved color characteristics and high productivity, by simple method without affecting the environment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for anhydro sugar alcohol, which has ion content of 10 ppm or less, conductivity of 10 mu S/cm, color value (b) of 0.2 or less and yellowing index value of 0.1 or less.
NOVELTY - Preparation of high-purity anhydrosugar alcohol involves converting dehydrated sugar by hydrogenation reaction, and distilling in an internal condenser thin film evaporator (1) provided with raw material input line (6), distillation residue discharge line (7), vacuum line (8) and discharge line (9).    USE - The method is useful for preparing high-purity anhydrosugar alcohol which is used in medical industry, chemistry industry and plastic industry, and for preparing medicine for heart and blood vessel disease.    ADVANTAGE - The method environmentally-friendly provides anhydrosugar alcohol having purity of 97.5% or more, pH of 3.7 or more and yield of 87% or more.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for distillation method.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining manufacture of high-purity anhydrosugar alcohol.    Internal condenser thin film evaporator (1)    Raw material input line (6)    Distillation residue discharge line (7)    Vacuum line (8)    Discharge line (9)
NOVELTY - Method of removing gas-phase potassium ions in biomass flue gas involves adding quantitative additive into a material layer of a fire grate of a boiler or into the hearth of the boiler by spraying device in a biomass combustion device, and carrying out a reaction on the additive as well as gas-phase potassium chloride and potassium carbonate in the flue gas at set temperature and generating potassium phosphate, to remove the gas-phase potassium ions in the biomass combustion flue gas.    USE - Method of removing gas-phase potassium ions in biomass flue gas (claimed).    ADVANTAGE - The method efficiently and economically provides removing gas-phase potassium ions in biomass flue gas.
NOVELTY - A biodiesel oil production method involves adding raw material grease and de-mineralized water to a hydrolysis reaction tower, and carrying out a hydrolysis reaction to obtain fatty acid and glycerol-water. The glycerol-water mixture is concentrated to obtain glycerine. The fatty acid and methanol are fed into an esterification reaction tower. Methanol and water are fed into a gas-liquid separator to obtain crude fatty acid methyl ester. The crude fatty acid methyl ester is placed in a distillation tower to obtain biodiesel oil and plant asphalt.    USE - Method for producing biodiesel oil.    ADVANTAGE - The method enables producing biodiesel oil with low reaction pressure and reaction temperature in an inexpensive and environment-friendly manner.    DETAILED DESCRIPTION - A biodiesel oil production method involves adding raw material grease and de-mineralized water to a hydrolysis reaction tower by using a metering pump, and carrying out a hydrolysis reaction at 170-190 degrees C for 2-3 hours to obtain fatty acid and glycerol-water mixture at mole ratio of 4-5:1, where reaction pressure is 1.2-1.6 MPa. The fatty acid and glycerol-water mixture are separated by using cyclone separator. The glycerol-water mixture is concentrated to obtain glycerine. The fatty acid and methanol are fed into an esterification reaction tower at mole ratio of 12-15:1, where reaction temperature is 160-180 degrees C, reaction pressure is 1.2-1.5Mpa and reaction time is 2-2.5 hours. Methanol and water are fed into a gas-liquid separator to obtain crude fatty acid methyl ester. The crude fatty acid methyl ester is placed in a distillation tower to obtain biodiesel oil and plant asphalt. An INDEPENDENT CLAIM is also included for a key preparation device.
NOVELTY - The device has a water inlet tank connected with a sewage anaerobic methane reactor through a water pump (1.1), where the anaerobic reactor is arranged at bottom of a rotational flow water distributor (1.2) that is provided with a water tank. A three-phase air collecting chamber (1.4) is connected with a water tank (1.6) through an exhaust pipe. An inner part of a cylinder reactor is provided with a mechanical stirrer (2.1). A sludge tank is provided with a sludge digestion liquid reflux pump (2.2). A methane gas pump (3.1) is provided with a flow meter (3.2).    USE - Device for treating nitrogen sewage in synchronous anaerobic ammonia oxidation and anaerobic methane oxidation mode.    ADVANTAGE - The device can solve the problem of removal of nitrogen and phosphorus in municipal sewage treatment in organic carbon source.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for treating nitrogen sewage in synchronous anaerobic ammonia oxidation and anaerobic methane oxidation mode.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a device.    Water pump (1.1)    Rotational flow water distributor (1.2)    Three-phase air collecting chamber (1.4)    Water tank (1.6)    Mechanical stirrer (2.1)    Sludge digestion liquid reflux pump (2.2)    Methane gas pump (3.1)    Flow meter (3.2)
NOVELTY - Invention relates to field of chemistry. To obtain hydrogen reaction of steam catalytic conversion of carbon-containing liquid is carried out with obtaining hydrogen-containing reaction products. Reaction products are directed on output of cathode space for electrolysis in high temperature electrolyser, on outlet from cathode space reaction flow, which contains synthesis-gas, directed on catalytic synthesis of carbon-containing liquid, is separated. Oxygen is released in anode space, separated from cathode space by electrolytic layer. Carbon-containing liquid is returned to the start of process for conversion, and hydrogen, obtained in process of carbon-containing liquid synthesis, is purified from carbon oxides.    USE - Chemistry.    ADVANTAGE - Hydrogen obtaining.11 cl, 1 dwg
NOVELTY - Production of mepiquat chloride raw medicine involves carrying out methylation and alkylation, centrifuging, obtaining crude product, adding into a vacuum dryer under -0.06 MPa to -0.04 MPa, and drying.    USE - Production of mepiquat chloride raw medicine (claimed).    ADVANTAGE - The method enables easy production of mepiquat chloride raw medicine by a simple process with high toluene recovery rate and reduced energy consumption and impurity content.
NOVELTY - The generator comprises electrode plates arranged in a row and spaced apart from each other, a sealing element that is made of elastic material with water tightness to form an accommodation space filled an electrolyte solution and is inserted between the electrode plates, an electrolyte flow hole is formed in bottom side of the electrode plates, and a mixing gas flow hole is formed in an upper side of the electrode plates. The accommodation space is not overlapped with the electrolyte flow hole of adjacent electrode plates. One of the plates includes a heat radiation frame part.    USE - The generator is useful for producing mixed gas of oxygen and hydrogen for an automotive machinery(claimed).    ADVANTAGE - The generator prevents the degradation of mixed gas of oxygen and hydrogen generation efficiency by rapidly radiating heat to outside.    DETAILED DESCRIPTION - The generator comprises electrode plates arranged in a row and spaced apart from each other, a sealing element that is made of elastic material with water tightness to form an accommodation space filled an electrolyte solution and is inserted between the electrode plates, an electrolyte flow hole is formed in bottom side of the electrode plates, and a mixing gas flow hole is formed in an upper side of the electrode plates. The accommodation space is not overlapped with the electrolyte flow hole of adjacent electrode plates. One of the plates includes a heat radiation frame part in contact with the air and protruded along circumference of the electrode plates. Oxygen and hydrogen gas in which electrolyte is supplied thorough the electrolyte flow hole is electrolyzed by voltage of cathode and anode of the electrode plate and is discharged to outside through the mixing gas flow hole. An induction element is installed at the electrolyte flow hole among electrode plates. A thickness of the sealing element is greater than the thickness of the induction element.
NOVELTY - Preparing 2-amino-5-(N-phenothiazine-yl)methyl-1,3,4-thiadiazole, involves: adding N-carboxy-methylene, amino thiourea and concentrated hydrochloric acid in reactor, and extracting under reflux reaction to obtain a reaction mixture; cooling the reaction to room temperature, adjusting pH to 8-9 by treating the reaction mixture with aqueous solution of sodium hydroxide to obtain solid particles, filtering the solid particles to obtain filter cake, washing the filter cake with ice water and then re-crystallizing the filter cake to obtain the final product.    USE - In preparing 2-amino-5-(N-phenothiazine-yl)methyl-1,3,4-thiadiazole (claimed) in preparing medicine for resisting bacteria, anxiolytic medicine, antidepressant medicine and medicine for resisting cancer.    ADVANTAGE - The method is simple, produces 2-amino-5-(N-phenothiazine-yl)methyl-1,3,4-thiadiazole with high yield; is environment-friendly, economical, and industrially amenable.
NOVELTY - A corn straw biological granulated feed comprises 96% corn straw, 2% enzymatic carrier, 2% probiotic bacteria and carrier.    USE - Corn straw biological granulated feed for cattle and sheep.    ADVANTAGE - The feed has less toxic and bacteria, high nutrition component and focus flavor, and is easy to transport and store. The feed increases animal food rate.
NOVELTY - This utility model claims a garbage recycling processing device, comprising a marsh gas furnace, a drier, a fermentation tank and the marsh gas tank, the fermentation tank comprises a tank body, a tank body top end is provided with a feeding port, a tank body is set at the bottom, the tank body is provided with a hot air device and a waste heat heating circulation device, wherein the marsh gas tank is provided with a hot water circulator and waste heat heating circulating device connected with said hot air device is provided with an air inlet and an air outlet, the air inlet is connected with air inlet pipe, wherein said dryer comprises shell body, the right end is provided with a high temperature air inlet, the left end is provided with a waste heat air outlet, the waste heat air outlet and the air inlet. This utility model of marsh gas furnace, a drier, a fermentation tank and the marsh gas pool is composed of a recycling system, the garbage generated in the process of processing a processing cycle.
NOVELTY - Realizing semi-nitrosation of domestic sewage by gallery push flow type reactor comprises inoculating nitrified sludge of sewage treatment plant, starting continuous flow nitrosation of domestic sewage by adopting sequencing batch reactor having ammonia nitrogen, ammonium sulfate and sodium bicarbonate, continuously sub-nitrifying, arranging the reactor in an aerobic/anaerobic aeration mode, monitoring the dissolved oxygen (DO) by instrument, adjusting hydraulic retention time (HRT) and aeration rate and inhibiting nitrite-oxidizing bacteria and then denitrifying into a sedimentation tank.    USE - The method is useful for realizing semi-nitrosation of domestic sewage (claimed).    DETAILED DESCRIPTION - Realizing semi-nitrosation of domestic sewage by gallery push flow type reactor comprises inoculating nitrified sludge of a sewage treatment plant at 22-25 degrees C, starting continuous flow nitrosation of domestic sewage by adopting a sequencing batch reactor having 140-160 mg/l of ammonia nitrogen with pH value of 7.7-7.9, ammonium sulfate and sodium bicarbonate under limited oxygen low-dissolved oxygen (DO) content of 0.60 mg/l, where the ammonia oxidation rate is 65-45%, continuously sub-nitrifying for more than 7 days, arranging the reactor in an aerobic/anaerobic aeration mode with reflux ratio of 50-60%, monitoring DO by an instrument, adjusting hydraulic retention time (HRT) for 7-8 hours and aeration rate and inhibiting 90-100% of nitrite-oxidizing bacteria for more than 7 days and then denitrifying into a sedimentation tank.
NOVELTY - An organic wastewater degrading method involves using dry reed as filling material and biological carrier, and treating organic wastewater by a biological fluidized bed or a fixed bed reactor, where the reed is set in the fluidized bed or fixed bed reactor as biological filler, and pH of organic waste water is 6-9.    USE - Method for degrading organic wastewater i.e. utilized in small sewage treatment.    ADVANTAGE - The method enables degrading organic wastewater without secondary pollution and providing less fluidization power consumption, good removal effect of nitrogen in wastewater and good environmental benefits in a simple and cost effective manner.
NOVELTY - An organic fertilizer producing method involves carrying out deep intelligent aerobic fermentation of biogas residue under action of solar energy. The residue is separated according to particle size, specific gravity, electric resistance and magnetic properties, followed by sieving and mixing. The residue is passed into strengthening roller crushing machine. The heat generated by a hot air furnace in negative pressure medium is passed into a dryer, followed by removing large impurities by drying, granulating to obtain organic fertilizer. The organic fertilizer is metered and packed.    USE - Method for producing organic fertilizer.    ADVANTAGE - The method enables producing organic fertilizer with high fermentation speed and high nutrient content, in an eco-friendly manner.    DETAILED DESCRIPTION - An organic fertilizer producing method involves carrying out deep intelligent aerobic fermentation of biogas residue under action of solar energy. The residue is separated according to particle size, specific gravity, electric resistance and magnetic properties, followed by sieving and mixing. The residue is passed into strengthening roller crushing machine by a belt conveyer. The heat generated by a hot air furnace in negative pressure medium is passed into a dryer under the effect of the induced draft fan, followed by remove large impurities by drying, granulating to obtain organic fertilizer. The organic fertilizer is metered and packed.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing organic fertilizer. '(Drawing includes non-English language text)'
NOVELTY - A fertilizer preparing method involves mixing ferment bacteria and rice bran at weight ratio of 1: (3-7) to obtain ferment bacteria added material that is mixed with 800-1000 parts slag produced in cassia oil production, 50-100 pts. wt. chicken manure, 100- 200 pts. wt. pig manure, 100-200 pts. wt. bagasse, 50-100 pts. wt. calcium magnesium phosphate and 3-7 pts. wt. ferment fungus additive. The mixture is stacked in a fermentation bed to obtain material stack. The obtained material stack is set on an upper cover film during composting at 60-65 degrees C for 50-70 days to obtain the fertilizer.    USE - Method for preparing fertilizer.    ADVANTAGE - The method enables preparing the fertilizer in environment-friendly manner.
NOVELTY - Preparation of esomeprazole sodium salt involves dissolving esomeprazole by using organic solvent, adding 30-80% aqueous solution of sodium hydroxide and a phase transfer catalyst at 40 degrees C for 2-4 hours, stirring at room temperature, separating esomeprazole sodium, reducing the temperature to 10 degrees C, followed by stirring for 0.5-1 hour, filtering, washing using solvent, decompressing and drying in vacuum at 20-60 degrees C, to obtain the esomeprazole sodium salt.    USE - For preparation of esomeprazole sodium salt (claimed), which is useful for reducing gastric acid secretion.    ADVANTAGE - The method has simple operation; uses recyclable solvent; provides product having high yield and high purity; and has fast reaction speed.
NOVELTY - The utility model claims a full automatic microbial inoculum continuous feeding device, wherein the device comprises water tank, chlorine-removing tank, activated domesticating pond and storage tank, wherein the device comprises an auxiliary system microbial inoculum raw liquid, solid powder feeder, a sewage tank, activating reagent, a third metering pump, nutrient substance is added, air blower and fungicide adding pump, the microbial inoculum domestication pool is connected with the activating pool, activating pool is connected with the microbial inoculum raw liquid barrel, an activator reagent barrel, a fan, a water tank for removing chlorine, solid powder feeder and domestication pool, the storage pool is connected with the domesticating pond, domesticating pond connected with nutrient substance feeding barrel and a sewage pool. This utility new type microbial inoculum method water is automatically activated, domestication, adding device uses an automatic control system for automatic control of microbial inoculum automatic feeding device using the process is completely automatic, and is realized by a corresponding control system, the heating of the heating in the tank by a metering pump, the other pump, stopping are automatic control removing agent.
NOVELTY - A hydrogen production activity determining method involves obtaining a hydrogen amount generated in an anaerobic sludge fermentation process, drawing a standard relation curve graph of the hydrogen amount and fermentation time, and calculating a maximum ratio hydrogen production activity value of the hydrogen production activity of the anaerobic sludge.    USE - Method for determining hydrogen production activity of anaerobic sludge.    ADVANTAGE - The method enables determining hydrogen production activity with high stability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for determining hydrogen production activity.
NOVELTY - This utility model claims a ecological type wetland water purifying tank, which is provided with structure, a waterproof wall side is set with a water inlet pipe and a water outlet pipe, is provided with a first water flow partition baffle plate, artificial wetland purifying tank, a filter cover plate, a sedimentation tank, an artificial wetland purifying pond is provided with an inner waterproof wall and the inner waterproof wall is connected with the water and a waterproof wall, the waterproof wall is provided with a water flow partition baffle plate, a guide tube, a water inlet and a drain outlet, a drain opening through the filter cover board and a settling tank. Waste water treatment efficiency is high, energy consumption is low;
NOVELTY - This utility model claims a method for producing marsh gas by the stirring-grinding device, comprising a stirring tank (2) and a grinding tank (2), a stirring tank (1) is connected with a feeding pipeline (8) and a water inlet pipe (7), a stirring tank (2) is provided with a stirring blade (4), a grinding tank (2) is provided with a grinding device (5), a stirring blade (4) and a grinding device (5) is driven by motor (3), a stirring tank (1) and a grinding tank (2) through a pipeline (10) is connected with the pipeline (10) is equipped with a conveying pump (6), a return pipe (9), the two ends of the through is connected to the grinding tank (2), the return pipe (9) is equipped with a conveying pump (6). This utility model can improve the marsh gas fermenting raw material utilization rate, at the same time, accelerates the fermentation process of marsh gas, shorten the period of the whole fermentation.
NOVELTY - A fertilizer base materials manufacturing method involves placing fed and screened garbage containing organic matters into a flash evaporation blasting machine. The machine is filled with steam, where temperature inside the flash machine is 210-230 degrees C, pressure is 2-3 Mpa for 80-100 seconds. The flash evaporation blasting is completed with in 0.01 seconds to obtain fertilizer base materials. The fertilizer material is placed in a drum dryer. The dried fertilizer is placed in cylinder scalping sieve of aperture 10-15 mm to obtain cleaned fertilizer base material.    USE - Method for manufacturing fertilizer base materials.    ADVANTAGE - The method enables manufacturing fertilizer base materials with strong operability, recycling property and reducing ecological problem, in environmental-friendly manner.
NOVELTY - An amino acid bio-organic fertilizer production method involves fermenting strains in a premixing way and processing the livestock and poultry manure such as pig manure and chicken manure by using a solidifyingagent, where the livestock and poultry manure are utilized as an organic raw material. Photophobic and aerobic fermentation is performed on the processed livestock and manure to obtain the amino acid bio-organic fertilizer.    USE - Method for producing an amino acid bio-organic fertilizer.    ADVANTAGE - The method enables producingthe amino acid bio-organic fertilizer in an economical manner with high output and input ratio, high stability, high-quality and better fertilizer effect, thus improving and maturing the soil. The amino acid bio-organic fertilizer is convenient for use, easy for storage and transportation, high in market competitiveness and easy for market popularization.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a method for producing an amino acid bio-organic fertilizer. '(Drawing includes non-English language text)'
NOVELTY - The device has a horizontal spiral stirring and conveying device fixed at bottom of a box body. A vertical spiral stirring and conveying device is fixed on a side of the box body. An end of the horizontal spiral stirring and conveying device is fixed with a feeding hopper. Another end of the horizontal spiral stirring and conveying device is connected to the vertical spiral stirring and conveying device. An upper end of the vertical spiral stirring and conveying device is fixed with a rotatable opening. An inner side of the box body is provided with a leveling spiral device.    USE - Horizontal organic solid, granule and powder fertilizer processing device.    ADVANTAGE - The device is simple in structure and inexpensive.    DESCRIPTION OF DRAWING(S) - The drawing shows a side view of a horizontal organic solid, granule and powder fertilizer processing device.
NOVELTY - An organic/inorganic composite fertilizer preparation method involves concentrating alcohol slops comprising 38-41% organic matters, 0.18-0.24% phosphorus pentoxide, 5.6-6.2% potassium oxide and 2.6-3.5% nitrogen, and uniformly mixing 60-70 mass% concentrated alcohol slops with 30-40 mass% inorganic fertilizer materials. The obtained mixed material is pelletized by using a rotating drum and a disk. The obtained mixture is dried to produce an organic/inorganic composite fertilizer.    USE - Method for preparing an organic/inorganic composite fertilizer for use in a sugar industry.    ADVANTAGE - The method enables preparing an organic/inorganic composite fertilizer with enhanced soil fertility, in an environment-friendly manner.
NOVELTY - An inorganic coated-type sustained-release chemical fertilizer comprises a chemical fertilizer coreand a chemical fertilizer outer coating, where the coating is a calcium carbonate coat layer or a composite coat layer comprising the calcium carbonate coat layer, a sulfur coat layer and/or an organic coat layer.    USE - Inorganic coated-type sustained-release chemical fertilizer.    ADVANTAGE - The fertilizer is inexpensive. The coating process is green and environment-friendly, and avoids harm to the environment when the fertilizer is applied for a long time.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an inorganic coated-type sustained-release chemical fertilizer.
NOVELTY - Preparing substituted tetrahydrofuran derivative (I) involves: reacting aryl diazo acetate, aldehyde and ethane compound in presence of Rhodium(II) acetate dimer.    USE - In preparing substituted tetrahydrofuran derivative (claimed) use as drug.    ADVANTAGE - The method is simple and short, requires cheap raw material and mild reaction condition, provides substituted tetrahydrofuran derivative with high yield, and is environment friendly.    DETAILED DESCRIPTION - Preparing substituted tetrahydrofuran derivative of formula (I) involves: reacting aryl diazo acetate of formula Ar1-C(=N2)-CO2CH3, aldehyde of formula R1-CHO and ethane compound of formula R2-CH=CH-R3 in presence of Rhodium(II) acetate dimer.    Ar1=optionally substituted phenyl;    R1=phenyl or cinnamoyl (both optionally substituted);    R2=optionally substituted phenyl, ester or H , and    R3=nitro or ester group.
NOVELTY - Fermenting pig excrement comprises inactivating harmful bacteria at high temperature, adding aerobic microorganism in culture solution, fermenting in a controlled temperature and humidity, culturing with adequate oxygen, repeating process in a fermentation device, and rolling the fermentation device.    USE - The method is useful for fermenting pig excrement (claimed).    ADVANTAGE - The method ferments pig excrement in simple and eco-friendly manner with convenient operation, high processing efficiency and less time consumption.
NOVELTY - A spiral absorbing biogas fertilizer device has an outer sleeve body provided with a cavity, where a bottom part of the outer sleeve body is provided with a dirt inlet, and a wall part of the outer sleeve body is provided with a drain port. A lower end of a rotating shaft is fixedly connected with a spiral shaft, where the rotating shaft passes through the spiral shaft that is arranged in the cavity, which is matched with the outer sleeve body.    USE - Spiral absorbing biogas fertilizer device.    ADVANTAGE - The fertilizer device is harmless to environment, light in weight, convenient to carry, detachable, convenient to clean, inexpensive and convenient to use.    DESCRIPTION OF DRAWING(S) - The drawing shows a side perspective view of a spiral absorbing biogas fertilizer device.
NOVELTY - An organic fertilizer production method involves taking Pleurotus eryngii and animal wastes as raw materials, adding zymophyte into the raw materials, and carrying out fermentation and crushing on the obtained mixture to obtain the organic fertilizer.    USE - Method for producing an organic fertilizer.    ADVANTAGE - The method enables producing the organic fertilizer in a simple and economical manner with wide range of application.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic illustration of a method for producing an organic fertilizer.
NOVELTY - The utility model claims a marsh gas reactor with a gradient circulation stirring system, wherein the gradient circulate stirring system comprises a suction pipe socket, a buffer return pipe, a circulating water pump, a forced circulation main pipe, forced circulating branch pipe and a spray head, wherein the suction pipe is installed in the middle upper part of the tank body through the buffer with the return pipe of the tank body is set with outer air outlet of the circulating water pump is connected with the water inlet of the circulating water pump of the water outlet is connected with a forced circulation main pipe, a forced circulation main pipe horizontally extends into the inner part of the tank body and is close to the bottom of the tank body, the upper part thereof is provided with multiple forced circulating branch pipe, the water outlet end of each branch pipe is set with a nozzle. This utility model has advantages of using a gradient stirring, it is possible to provide a process cost is low, operation is simple, safe and reliable, the intensity can be controlled, which can make up the other anaerobic reactor stirring process, and reduce energy consumption and improve biogas yield, simple operation, stable operation is marsh gas engineering
NOVELTY - The utility model claims a biogas reactor for the clear liquid collecting mechanism, comprising a liquid storage container, a liquid outlet pipe, a biogas liquid tank is provided outside of the reactor and a U-shaped pipe, the liquid storage container, a U-shaped pipe of the overflow weir and the reactor is connected with the bottom end of the liquid storage container is connected with a liquid outlet pipe, and the other end of the liquid pipe is connected with the biogas liquid tank. The advantages of the utility model is as follows: a buffer of the U-shaped tube is clear liquid in the reactor the impact, is recycled to the liquid storage container at a lower flow rate, and to the biogas liquid preparing tank for the second time;
NOVELTY - The utility model claims an anaerobic reactor, the anaerobic reactor, comprising a tank body, a marsh gas pipe and a feeding pipe, wherein the marsh gas pipe is installed on the top end of the tank body, the feed pipe is installed at the bottom of the one side of the tank, wherein the upper part and the bottom of the tank body are respectively provided with a settling zone and a flow guide cone, the periphery of the zone is provided with a weir, said weir is higher than the settling zone, the overflow weir and the outer wall of the tank body of the liquid discharge mechanism is connected with the air outlet of the mixed material in the tank body turning over a gradient circulation stirring system. This utility model has advantages of using a gradient stirring, it is possible to provide a process cost is low, operation is simple, safe and reliable, the intensity can be controlled, which can make up the other anaerobic reactor stirring process, and reduce energy consumption and improve biogas yield, simple operation, stable operation is marsh gas engineering
NOVELTY - This utility model claims a kind of bio-waste treatment device to solve the problem that bio-waste, straw cannot place quickly and efficiently produce biogas. The device comprises a cylinder body, automatic display instrument, a tap water pipe, a water input pipe, a stirrer, a material input pipe and input end, an end cover overflow pipe, a heater, a pump, a discharge hole and a sight glass window, wherein the pH value automatic display instrument, a tap water pipe, a water inlet pipe, a stirrer, a material input pipe and a waste opening are respectively set on the upper part of the cylinder body, an overflow pipe, a sight glass window are respectively installed on the side wall of the upper part of the cylinder body, a heater and a discharging port are respectively installed on the bottom of the cylinder body upper part, a material conveying pump is installed on the discharging port, a vacuum sealing body is double-layer structure. Bio-waste treatment device is mainly applied to the bio-waste and straw local produce marsh gas, marsh gas generator used with fast and high efficiency production.
NOVELTY - This utility model claims a kind of a human body, the kitchen garbage and waste water energy recycling multi-functional building, solving the problem of the city generated can effectively use the resource; This utility model comprises at least two residential building, a used for collecting human body excrement and garbage and fermentation of the marsh gas tank and the adjacent residential floor connected with the marsh gas pool of the fruit tree for grape planting farm crop and aerosol plant area for processing the marsh gas of the marsh gas purifying centre, which is connected with the marsh gas purifying and used for preparing nutrient fluid of nutrient liquid, and is connected with the nutrient liquid center. This utility model is reasonable in design, at the same time can save social investment and product flow, and the energy can be recycled, and the environment pollution is reduced.
NOVELTY - This utility model claims a kind of integrated type nitrification-denitrification microbe fuel cell. It is mainly composed of a nitrification and denitrification by the nitrifying a inoculating nitration sludge to nitrogen-containing organic waste water as fuel, organic heterotrophic bacteria decomposition releasing electrons, ammonia nitrogen by nitrifying bacteria into nitrate nitrogen and nitrite nitrogen and releasing electrons, denitrification chamber inoculating denitrifying sludge, a is water into the denitrification chamber can be further removing a denitrification electron donor is used as the cathode, the residual organic matter, nitrate nitrogen and nitrite nitrogen by denitrifying bacteria into nitrogen to finish the whole denitrification, nitration pole received electronically by denitrification cathode received by a circuit to realize generating electricity. This utility model device has compact structure, can realize nitrification and denitrification combined power generating, reduces cost, biological denitrification by using organic matter and ammonia nitrogen fuel, improves power generating efficiency, the nitrified product as electron acceptor, waste by waste, capable of effectively reduce the running cost of the microbe fuel cell.
NOVELTY - (R)-3-(1-hydroxyethyl)phenol is prepared by reacting m-hydroxyacetophenone with chiral catalyst, alkali, and hydrogen.    USE - Preparation of (R)-3-(1-hydroxyethyl)phenol for preparing (S)-3-(1-dimethylaminoethyl)phenol (claimed).    ADVANTAGE - Preparation of (R)-3-(1-hydroxyethyl)phenol is environment-friendly, has high reaction yield, greatly reduces cost, does not require resolving agent, (R)-3-(1-hydroxyethyl)phenol has high optical purity, chiral catalyst has good selectivity, and preparation (S)-3-(1-dimethylaminoethyl)phenol has high yield.    DETAILED DESCRIPTION - (R)-3-(1-hydroxyethyl)phenol is prepared by reacting m-hydroxyacetophenone with chiral catalyst of formula (I), alkali, and hydrogen.    DTB=structure of formula (II);    X=H, 1-8C alkyl, 1-8C alkoxy, Ph optionally substituted by 1-8C alkyl and/or alkoxy, 1-naphthyl, 2-naphthyl, benzyl, or heteroaryl which is furyl, thienyl, or pyridyl.    . An INDEPENDENT CLAIM is included for preparation of (S)-3-(1-dimethylaminoethyl)phenol which involves reacting (R)-3-(1-hydroxyethyl)phenol with methanesulfonyl chloride in basic conditions to form (R)-methanesulfonic acid-3-(1-methylsulfonic acid oxoethyl)phenyl ester, reacting with dimethylamine to form (S)-methanesulfonic acid-3-(1-dimethylaminoethyl)phenyl ester, and hydrolyzing under basic conditions.
NOVELTY - Preparation of chloramphenicol succinate comprises dissolving succinic anhydride in acetone, adding pyridine, heating, stirring until solution is clear, dissolving chloramphenicol in acetone, dropping clear solution, stirring, reacting, decompressing, distilling solvent to give pale yellow oil, dropping pale yellow oil in sodium bicarbonate, filtering, adding hydrochloric acid to filtrate, standing and precipitating white solid; adding white solid to ethanol, heating, dissolving and stirring, cooling, further cooling to 0-5 degrees C, crystallizing, filtering, and drying at 30 degrees C to constant weight.    USE - Method for preparing chloramphenicol succinate (claimed).    ADVANTAGE - The method is environment-friendly simple and easy, has short reaction time and recyclable solvent, and reduces cost.    DETAILED DESCRIPTION - Preparation of chloramphenicol succinate comprises dissolving succinic anhydride in acetone, adding catalyst pyridine, water bath heating and stirring until solution is clear, dissolving chloramphenicol in acetone, dropping clear solution, stirring and reacting for 30 minutes at 60 degrees C, decompressing and distilling solvent to give pale yellow oil, dropping pale yellow oil in 10% sodium bicarbonate until no turbidity, filtering, adding 10% hydrochloric acid to filtrate to 4 pH, standing and precipitating white solid; adding white solid to 1.5-2 times weight ethanol, heating to 35 degrees C, dissolving and stirring, cooling room temperature, further cooling to 0-5 degrees C, crystallizing for 2 hours, filtering, and drying obtained crystal at 30 degrees C to constant weight.
NOVELTY - Preparation of guanidinoacetic acid comprises reacting glycine and cyanamide in alkaline condition, centrifugally separating to obtain solid phase and liquid phase, where the solid phase is glycocyamine, and liquid phase is used as solvent for the reaction.    USE - Method for preparing guanidinoacetic acid (claimed).    ADVANTAGE - The method satisfies environmental protection requirement, improves yield and lowers consumption.
NOVELTY - Biodiesel is prepared by heating animal fat and vegetable oil at 60-110 degrees C, filtering to remove impurities, transesterifying with short-chain alcohol in catalyst at 65-110 degrees C for 5-30 minutes, recovering excess alcohol using cyclone separator to recycle, separating glycerol phase using centrifugal separator, and purifying by passing through ceramic packing.    USE - Method for preparing biodiesel (claimed).    ADVANTAGE - The method has low investment, simple operation, low energy consumption, and high conversion rate.
NOVELTY - The device comprises a heat transfer unit, a cleaning unit and an electric drive unit. The heat exchange unit comprises heat transfer tubes, and is provided with a water outlet and a water inlet. The cleaning unit comprises a crank mechanism and a cleaning assembly. The cleaning assembly is hingedly connected with the crank mechanism, and comprises ring plates. Each ring plate is connected with the heat transfer tubes. The electric drive unit is configured to periodically remove the dirt in the heat transfer tubes. The device further comprises a heating unit for heating a source using coal.    USE - The device is useful for producing marsh gas (claimed).    ADVANTAGE - The device is capable of producing biogas with high productivity and heat stability.    DETAILED DESCRIPTION - The device comprises a heat transfer unit, a cleaning unit and an electric drive unit. The heat exchange unit comprises heat transfer tubes, and is provided with a water outlet and a water inlet. The cleaning unit comprises a crank mechanism and a cleaning assembly. The cleaning assembly is hingedly connected with the crank mechanism, and comprises ring plates. Each ring plate is connected with the heat transfer tubes. The electric drive unit is configured to periodically remove the dirt in the heat transfer tubes. The device further comprises a heating unit for heating a source using coal, firewood, straw, electricity, solar energy, air energy or geothermal energy, explosion-proof motors operated at 3-5 Kw, DF1-Tod proof solenoid valves and a temperature sensor. The device has gear reduction ratio of 40-70.
NOVELTY - The device comprises a fixing frame, a floating rod, a carrier, a culture medium, and a balance weight block. An upper end of the fixing frame is connected with the flotation rod and the carrier. The fixing frame is a rectangular frame, and has a corrosion resistant sheet. A surface area of the fixing frame is provided with a non-woven fabric. The two ends of the flotation rod are sealed with a hollow tube or a hard foam. The carrier has melamine foam openings. The corrosion resistant sheet is stainless steel sheet or PVC plastic sheet. The culture medium is broad spectrum culture medium.    USE - The device is useful for extracting strain in sewage (claimed).
NOVELTY - Degrading straw fertilizer comprises culturing the strain in a potato dextrose agar culture medium at 28 degrees C for 48 hours.    USE - The method is useful for degrading straw fertilizer using microbial agent e.g. white rot fungi, Bacillus subtilis, Candida tropicalis and Aspergillus niger (claimed).    ADVANTAGE - The straw fertilizer is degraded in fast, simple and cost-effective manner with reduced time and increased degradation rate.
NOVELTY - Culturing microalgae comprises: taking a residue sodium hydroxide solution, adjusting the pH value, heating, adding into a high pressure sterilizing pot, heating, cooling and filtering a liquid as a micro-algae culture medium; culturing the Chlorella vulgaris, preparing a seed culture medium composition by mixing ammonium chloride, monopotassium phosphate, dipotassium phosphate, magnesium sulfate heptahydrate, glacial acetic acid, microelement and culturing; obtaining a microalgae culture base and sterilizing at high pressure; and sterilizing the medium, rotating and culturing.    USE - The method is useful for culturing microalgae using biogas residue (claimed).    DETAILED DESCRIPTION - Culturing microalgae using biogas residue comprises: taking a residue sodium hydroxide solution with the concentration of 5 mol/l, adjusting the pH value to 10, heating at 25 degrees C for 12 hours, adding into a high pressure sterilizing pot, heating at 115 degrees C for 60 minutes, cooling and filtering a liquid as a micro-algae culture medium; culturing the Chlorella vulgaris, preparing a seed culture medium composition by mixing 400 mg/l of ammonium chloride, 56 mg/l of monopotassium phosphate, 108 mg/l of dipotassium phosphate, 100mg/l of magnesium sulfate heptahydrate, 1 mg/l of glacial acetic acid, 1 ml/l of microelement, injecting the mixture into a culture box and culturing for 3-4 times at 15-30 degrees C and with the illumination intensity of 2000-4000 Lux, for 7 days; obtaining the microalgae culture base to adjust the pH to 7 with 5 mol/l hydrochloric acid solution and sterilizing at high pressure for 20 minutes; and sterilizing the microalgae culture medium without bacteria, rotating at 180 revolutions per minute, shaking and culturing at 28 degrees C and with the illumination intensity of 6000 Lux for 7 days.
NOVELTY - Low temperature lipase Lip1 (I) having an amino acid sequence of SEQ ID NO: 2 (a 294 amino acid sequence fully defined in the specification), is new.    USE - (I) is useful in long-chain fatty acid ester catalysis process (claimed) and in detergent and biologic diesel fuel.    ADVANTAGE - (I) has good activity and stability.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) a gene encoding (I); and    (2) an expression vector comprising (I) or gene.
NOVELTY - Producing volatile fatty acid comprises crushing agaricus bisporus mushroom sample and then adding alcohol, sedimentating residual sludge for 24-30 hours, discharging clear liquid to obtain a sludge sample, drying the sample at a temperature of 70 degrees C and then crushing into particles with diameter of 2 mm to obtain mushroom sample powder, putting the powder in a reaction bottle and then sealing, rotating the bottle at a speed of 100-110 revolutions per minute in a air bath shaking table, and carrying out anaerobic fermentation at a temperature of 35-38 degrees C for 1-10 days.    USE - The method is useful for producing volatile fatty acid (claimed).
NOVELTY - Producing biological diesel oil by enzyme catalysis, comprises extracting seed oil from clausenamide, taking ionic liquid as reaction medium, determining required methanol amount physical and chemical constant for oil extracted from clausenamide seeds, adding methanol and 50-400 mg of lipase with the oil to obtain a reaction product, where the ratio of methanol to oil is 1:2-10:1.    USE - The method is useful for producing biological diesel oil (claimed).    ADVANTAGE - The method is capable of producing the biological diesel oil in a cost effective manner with improved feasibility and efficiency.
NOVELTY - A liquid amino acid fertilizer comprises degraded livestock blood using Bacillus licheniformis and soybean-derived protease.    USE - A liquid amino acid fertilizer.    ADVANTAGE - The fertilizer is prepared using a simple and convenient method, thus reducing cost. The fertilizer has a long-lasting efficiency. The use amount or the preparation time of enzyme can be reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the liquid amino acid fertilizer, comprising crushing livestock blood, and degrading using B. licheniformis; and adding a treatment solution of soybean-derived protease at 50-65 degrees C, reacting for 5-24 hours, filtering, and sterilizing.
NOVELTY - Combustion of dimethyl ether (DME) comprises (A) preheating liquefied DME under reduced pressure, transporting preheated gas to heater, heating, and transmitting heated gas to cracking reactor; (B) subjecting to cracking reaction with cracking catalyst to obtain synthesis gas containing carbon monoxide and hydrogen, and transferring to methanation reactor; (C) subjecting to methanation reaction in the presence of methanation catalyst to obtain methane gas; and (D) completely converting DME to methane gas.    USE - Method for industrial combustion of dimethyl ether used as industrial gas (claimed).    ADVANTAGE - The method improves fuel heat value and achieves cost-saving and energy-saving effects.    DETAILED DESCRIPTION - Combustion of dimethyl ether (DME) comprises (A) preheating liquefied DME under reduced pressure at 350 degrees C, transporting preheated gas to heater, heating to 350-550 degrees C, and transmitting heated gas to cracking reactor; (B) subjecting to cracking reaction with cracking catalyst to obtain synthesis gas containing carbon monoxide and hydrogen, and transferring to methanation reactor; (C) subjecting to methanation reaction in the presence of methanation catalyst at 230-450 degrees C, at 0.05-0.2 MPa, and at air velocity of 500-25000/hour to obtain methane gas; and (D) completely converting DME to methane gas.
NOVELTY - This utility model claims a solar auxiliary heating high temperature rapid fermentation system, comprising a hopper for conveying the kitchen garbage for the hopper lifting electric hoist hoisting machine, is provided with a spiral conveyor is electric hoist hoisting machine, wherein the upper part is provided with a garbage buffer hopper, the buffering bucket is in the position matched with the hopper, further comprising a food waste biochemical compost, the tubular spiral conveyer is set at one end of biochemical stack machine feeding port end of the kitchen, kitchen biochemical stack machine is a water inlet and a water outlet is connected with the solar heat collector by a pipeline, a biochemical fertilizer discharge opening is provided with a belt conveyor in kitchen, wherein the belt conveyor is provided with a crusher and a vibration sieve and the air outlet is connected with a fan and a waste gas absorption tower. Providing cheap and direct heating heat source for fermenting material to realize the high temperature rapid fermentation by innovative structure, a low cost, good effect, simple structure of new-type efficient fermentation system.
NOVELTY - The utility model claims an anaerobic digester biogas integrated device, comprising an anaerobic generator, anaerobic generator is connected with solid-liquid separator connected with the inlet, a solid-liquid separator through pipeline, biogas slurry reflowing pump is connected with the anaerobic generator, solid-liquid separator through the pipeline and integrated biogas inlet of the reactor is connected with a discharging pump is connected with the automatic filling machine with integrated biogas reactor side wall lower end of the outlet pipe is set on the air outlet. This utility model has compact structure, simple operation and low cost, which reduces the scale of the biogas storage tank and reduces the engineering investment, product is convenient to store, transport and administration.
NOVELTY - This utility model claims a sow wet material groove, comprising a material cylinder, a wet material groove material tube, the bottom of the charging barrel of the discharging switch and a material cylinder, the upper side wall of the water spraying nozzle. Nozzle capable of manual switch, also can be connected with the computer so as to realize the intelligent. Discharging switch can be manual switch, also can be connected with the computer to realize the electric switch. The utility model solves the problem that the dry adding water wet, then putting for human, so as to waste a large amount of labour and a control amount is difficult to feed and water in the wet process, ratio of material to water and wet gas through fermenting mixed straw materials time is difficult to control outside the groove.
NOVELTY - A methanol liquid fuel comprises 45-60 wt.% methanol, 30-50 wt.% biological diesel oil and 4-10 wt.% additive.    USE - Methanol liquid fuel.    ADVANTAGE - The biological diesel oil improves the flash point of methanol liquid fuel.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of methanol liquid fuel comprising adding additive into methanol under room temperature and normal pressure condition, uniformly stirring to prepare modified methanol, adding biodiesel, adjusting pH to neutral using ammonia, and mixing uniformly.
NOVELTY - Prevention of biological diesel oil from corroding copper sheet comprises adding 0.01-0.2 wt.% phenolic compound, 0.01-0.2 wt.% amine compound and 0.001-0.01 wt.% metal rust inhibitor.    USE - Method for preventing biological diesel oil from corroding copper sheet (claimed).
NOVELTY - Spirulina strain ENN2201A (Desmodesmus sp.) preserved under China general microbiological culture collection center with a preservation number of CGMCC No. 5150, is new.    USE - The strain is useful for: purifying industrial wastewater or urban domestic sewage and/or industrial waste gas; and preparing bio-diesel oil and/or grease, feed including livestock, poultry or pet feed and carotenoid including zeaxanthin, canthaxanthin and carotene (all claimed).    ADVANTAGE - The strain ensures rapid growing speed, and is easy to collect.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for culturing the strain.
NOVELTY - A pigsty padding material comprises 27 wt.% peanut shells, 20 wt.% ground corncobs, 23 wt.% plant ash, 19 wt.% sawdust, and 11 wt.% plant straw. The pigsty padding material is sprinkled in a barn twice a day, once in morning and once in evening.    USE - Pigsty padding material used for degrading manure, deodorizing and purifying pig growth environment; and as organic fertilizer for crops (claimed).    ADVANTAGE - The padding material has strong absorbing and deodorizing effect, and fast pig manure degradation rate; and is suitable for different livestock.
NOVELTY - A pigsty padding material comprises 17 wt.% crushed bean trees, 21 wt.% ground corncobs, 19 wt.% plant ash, 29 wt.% sawdust, 8 wt.% shredded wheat straw, and 6 wt.% fly ash. The padding material is prepared by uniformly mixing raw materials and is sprinkled in pigsty twice a day, once in the morning and once in the evening.    USE - Pigsty padding material used for degrading pig manure and deodorizing and purifying pig growth environment, and as organic fertilizer for crops.    ADVANTAGE - The padding material has strong absorbing and deodorizing effect and fast pig manure degradation rate, and is suitable for different livestock.
NOVELTY - Organic fertilizer production comprises adding organic waste having water content of less than or equal to 95 wt.% to subcritical water reactor, adding 0-100 wt.% biomass, adjusting pH to 7.5-8.5 with sodium hydroxide, introducing steam and reacting at 150-300 degrees C and 0.5-5 MPa for 15-60 minutes, and drying or dehydrating reaction product until water content is 50-65 wt.%; and adding 0.5-1 wt.% microbial inoculum to dried or dehydrated product, uniformly mixing, heating to 60-70 degrees C after 2-3 days, maintaining at 55-65 degrees C for 5-7 days, and turning when temperature exceeds 65 degrees C until temperature remains constant.    USE - Method for producing organic fertilizer (claimed).    ADVANTAGE - The method completely kills pathogens, has no odor and heavy metal pollution, reduces processing cost, improves processing efficiency, and achieves maximum organic waste utilization.
NOVELTY - Preparing modified biological adsorbent using modified egg membrane comprises pre-processing egg shell in a solution, cleaning, drying, soaking in acid solution, taking out the egg membrane, washing with deionized water, drying, soaking in strong alkali solution, reacting, heating, hydrolyzing, separating hydrolysis liquid, adding aldehyde tanning agent, adjusting pH value, modifying, heating, condensing, curing, neutralizing, filtering, washing, and drying.    USE - The biological adsorbent is useful for recycling kitchen waste.    ADVANTAGE - The adsorbent is prepared with high adsorption property and excellent practicability in a simple, less time and cost-effective manner.    DETAILED DESCRIPTION - Preparing modified biological adsorbent using modified egg membrane comprises pre-processing egg shell in a solution, cleaning using water, drying, soaking in acid solution for 2-6 hours, taking out the egg membrane, washing with deionized water until it is neutral, drying, soaking in strong alkali solution, reacting, heating, hydrolyzing, separating hydrolysis liquid, adding aldehyde tanning agent, adjusting pH value to 6-11, modifying using modifying agent including thiourea, urea, sodium thiosulfate, mercaptan, aliphatic amine or amide substance for 6-10 hours, where the mass ratio of modifying agent to waste egg membrane is 1-35:1:10, heating, condensing, curing, neutralizing, filtering, washing, and drying.
NOVELTY - A bio-organic fertilizer is prepared by performing preliminary construction of trench, and laying initial component and composting naturally at atmospheric pressure and positive temperature of air. The initial components of composted mixture are preliminarily composted into predetermined quantities and after which they are mixed. The obtained uniform mixture is recessed into trenches, and then is moistened to 50-60% humidity. A composting is conducted for 60-65 days. The initial components comprises 40-60 wt.% tobacco dust, 20-40 wt.% soil (humus), and 10-30 wt.% lowland peat.    USE - Method for preparing bio-organic fertilizer (claimed).    DETAILED DESCRIPTION - Bio-organic fertilizer is prepared by performing preliminary construction of trench, and laying initial component and composting naturally at atmospheric pressure and positive temperature of air. The initial components of composted mixture are preliminarily composted into predetermined quantities and after which they are mixed. The obtained uniform mixture is recessed into trenches, and then is moistened to 50-60% humidity. A composting is conducted for 60-65 days at average-daily temperature of air not lower than 15 degrees C. The three times samples of uniform composted mixture are selected where content of nicotine is determined as well as value pH and cellulolytic activity. The obtained end product is finished bio-organic fertilizer after 30-35 days and at the end of process of composting mixture. The initial components comprises 40-60 wt.% tobacco dust, 20-40 wt.% soil (humus), and 10-30 wt.% lowland peat.
NOVELTY - The organic residential digester comprises a container (1) for receiving organic matter for decomposition, a worm shaft which can be driven manually or mechanically, and a bracket (20). A hermetic motor is designed for pumping gas (4), where a purifier (5) and gas mixer (6) are also included. The organic matter decomposition is performed in a container (8) having cap (9) which is inputted to system and tank. The system comprises a winch or electric motor (10) and housing (11) which are interconnected and responsible for handling the container.    USE - Organic residential digester for generating methane gas and fertilizers for use in homes, restaurants or kitchens.    ADVANTAGE - The organic residential digester comprises a container for receiving organic matter for decomposition, a worm shaft which can be driven manually or mechanically, and a bracket, and thus efficiently provides methane gas by effective separation of the decaying matter.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic front view of the organic residential digester.    Container (1)    Gas (4)    Purifier (5)    Gas mixer (6)    Container (8)    Cap (9)    Electric motor (10)    Housing (11)    Bracket (20)
NOVELTY - The fermented coffee beverage is obtained from waste generated from wet processing of coffee fruits.    USE - Fermented coffee beverage.    ADVANTAGE - The fermented coffee beverage provides greater profitability by using already discarded waste, and facilitates great convenience by adding more value to coffee and full utilization of the crop.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing fermented coffee beverage, which involves:    (A) processing dewatered pulp;    (B) filtering the processed pulp;    (C) performing sulfitation process;    (D) performing chaptalization process; and    (E) performing inoculation of yeasts for producing foot tub.
NOVELTY - Crystalline form III of pitavastatin calcium characterized by powder X-ray diffractogram comprising peaks as given in the specification, is new.    USE - The crystalline form III of pitavastatin calcium is useful for treating hypercholesterolemia (heterozygous familial and non-familial) and mixed dyslipidemia. No biological data given.    ADVANTAGE - The process is simple, cost-effective, environmentally-friendly, reproducible, scalable, and robust, to produce pitavastatin calcium with high purity.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the preparations of form III of pitavastatin calcium.
NOVELTY - Commercially viable process for the preparation of tramadol hydrochloride (I) comprises: (a) treating 3-chloroanisiole with activated magnesium in anhydrous mixture of organic solvents at reflux to give (3-methoxyphenyl)magnesium chloride (III); and (b) treating (III) with 2-((dimethylamino)methyl)-cyclohexanone at 40-45 degrees C, in a solvent to afford 2-((dimethylamino)methyl)-1-(3-methoxyphenyl)cyclohexanol, which is further subjected to the treatment of aluminum nitrate to give tramadol nitrate salt and neutralization and followed by hydrochloric acid to give (I).    USE - The process is useful for the preparation of tramadol hydrochloride (claimed) which is useful for treating pain. No biological data given.    ADVANTAGE - The commercially viable process: replaces bromides with chlorides in the preparation of Grignard reagents, in which the chlorides are less expensive and give rise to smaller amounts of salts on account of their lower molecular weights, and the effluent amount will be less when chlorides are used; utilizes cheaper raw materials to obtain the products in higher yield; is simple and easily adaptable industrially; and produces the tramadol hydrochloride which inhibits pain without the side effects which are known for opioids.
NOVELTY - Slow release fertilizer comprises 60 wt.% microbial fertilizer containing Trichoderma, 0.5-25 wt.% gibberellin, 12-15 wt.% urea, 15-18 wt.% superphosphate, 15-20 wt.% ammonium bicarbonate and 2-5 wt.% borax, where the above-mentioned components are mixed with soil in ratio of 1:80-100.    USE - As slow release fertilizer used for mountains, slop lands and dry lands.    ADVANTAGE - The fertilizer is rich in super absorbent resin, and hence water for irrigation of plants is saved, and buffer index of bed soil moisture is particularly increased, and physiologic green blight death of seedling is prevented. The fertilizer has slow release effect and thus exhibits long term effect. The slow release fertilizer increases survival rate of crops, and ensures survival rate of plants above 98% even when the plants are not watered for 30 days after transplantation.
NOVELTY - Preparation of tolfenamic acid involves mixing o-chlorobenzoic acid with excessive 3-chlorine-2-methyl aniline, adding inorganic alkaline substances, anhydrous alkali metal iodides and copper powder, stirring and heating, distilling to remove excessive 3-chlorine-2-methyl aniline, adding water to the solution, stirring and filtering, cooling solution, adding inorganic acid, stirring, filtering and drying solution, adding obtained crude product to absolute ethyl alcohol, heating the mixture, reducing the temperature, slowly stirring and crystallizing, and treating.    USE - Preparation of tolfenamic acid (claimed).    ADVANTAGE - The tolfenamic acid is economically prepared with high yield, by a simple method.    DETAILED DESCRIPTION - Preparation of tolfenamic acid involves mixing o-chlorobenzoic acid with excessive 3-chlorine-2-methyl aniline, adding inorganic alkaline substances, anhydrous alkali metal iodides and copper powder, stirring and heating at 100-150 degrees C, distilling to remove the excessive 3-chlorine-2-methyl aniline, adding water to the solution, stirring and filtering, cooling the solution at 5-10 degrees C, keeping the temperature, dropwise adding inorganic acid to adjust the pH value until the solution is acidic, stirring, filtering and drying the solution, adding obtained crude product to absolute ethyl alcohol, heating the mixture at 60-80 degrees C, reducing the temperature, slowly stirring and crystallizing, and treating.
NOVELTY - Hydrocortisone colloid and mixed solvent are mixed, heated, filtered, crystallized, centrifuged (A), mixed with ethanol and activated carbon, heated, filtered, obtained filtrate is crystallized and centrifuged, to obtain hydrocortisone product. The supernatant obtained in step (A) is concentrated, cooled, crystallized, collected, mixed with mixed solvent heated, filtered, crystallized and centrifuged, to obtain hydrocortisone having purity of more than 85%. Thus, method for recovering active components from hydrocortisone colloid is performed.    USE - Method for recovering active components from hydrocortisone colloid (claimed).    ADVANTAGE - The method effectively and economically recovers active components from hydrocortisone colloid with suppressed generation of solid waste.    DETAILED DESCRIPTION - Hydrocortisone colloid and mixed solvent in the content ratio of 1:10-20 g/ml, respectively are mixed, stirred, heated to 65-70 degrees C for 1 hour, filtered, cooled, crystallized and centrifuged (A), to obtain solid crystalline recovered product. The obtained recovered product, ethanol and activated carbon are mixed, heated to 65-70 degrees C for 1 hour, filtered, obtained filtrate is crystallized, cooled, crystallized and centrifuged, to obtain hydrocortisone product having purity of more than 99%. The supernatant obtained in step (A) is heated, solvent is evaporated and recycled, remainder product is concentrated, cooled, crystallized, collected, mixed with mixed solvent containing chloroform and ethanol in the molar ratio of 75:25, respectively, heated to 50-55 degrees C, filtered, cooled, crystallized and centrifuged, to obtain hydrocortisone having purity of more than 85%. Thus, method for recovering active components from hydrocortisone colloid is performed. The content ratio of recovered product and ethanol is 7:10 g/ml, respectively.
NOVELTY - Ventilation soil comprises 20% peanut coats or melon seed shell particles, 20% sand, 55% soil and 5% oil residues.    USE - The ventilation soil is useful for household flowers (claimed).    ADVANTAGE - The soil has excellent water absorbing and ventilation characteristics, utilizes waste as peanut coats and other fruit peels are used after being smashed, advocates citizens to cultivate flowers, and beautifies environment.
NOVELTY - A borohydride compound, a hydroxide, and a water-absorbing material are mixed uniformly in a weight ratio of 100:1-50:0.1-25. Water is added to the mixture, and the alkaline solution is absorbed by the water-absorbing material to obtain a gel-like hydrogen-storage material. A catalyst is added to the hydrogen-storage material and borohydride is hydrolyzed to obtain hydrogen.    USE - Synthesis of hydrogen fuel (claimed).    ADVANTAGE - The method provides hydrogen-storage material which has stable performance characteristics, and can be conveniently stored and transported. The releasing speed of hydrogen gas can be controlled. The prepared hydrogen gas need not be filtered.
NOVELTY - Dressing fertilizer comprises 180-240 pts. wt. farmyard manure, 15-20 pts. wt. potassium sulfate, 10-15 pts. wt. silicon-calcium-potassium fertilizer, 0.5-1 pts. wt. zinc fertilizer, 1.2-1.5 pts. wt. boron fertilizer, and 2-3 pts. wt. microbial fertilizer.    USE - As dressing fertilizer for promoting root growth of lotus planted in shallow water (claimed).    ADVANTAGE - The fertilizer has rich beneficial substances that satisfies growth demands of shallow water lotus, increases soil organics and fertility, and yield, improves pest and disease resistance and reduces application of agrochemicals.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer, which involves (a) stirring decomposed pig manure and cattle manure uniformly in a stirrer, (b) adding silicon-calcium-potassium fertilizer and potassium sulfate, and stirring uniformly, (c) adding zinc fertilizer and boron fertilizer, and stirring uniformly, and (d) adding microbial fertilizer, and stirring uniformly.
NOVELTY - Chlorophenol and alkaline liquid are added to a reactor and reacted to obtain a soluble chlorophenol salt solution. The solution is evaporated to obtain solid soluble chlorophenol salt. Chlorocarboxylic acid salt solution is added to the reactor and reacted to obtain soluble phenoxy carboxylic acid salt, with an alkali substance being additionally added during reaction. Water is added to the reactor, an acid is added, and the reaction mixture is filtered, washed and dried to obtain a phenoxy carboxylic acid type herbicide.    USE - Synthesis of phenoxy carboxylic acid type herbicide (claimed).    ADVANTAGE - The method reduces processing links, which reduces influence on production environment and water consumption, and makes the method environmentally-friendly. The method is economical.
NOVELTY - Dehydrating and alkylating aminothiazole compounds (I), comprises reacting alcohol compounds (II) and substituted aminothiazole compounds (III) in presence of alkali under inert gas protection or air, where the molar ratio of amine to alcohol in a reaction raw material is 3:1-1:3, the dosage of alkali is 5-100 mol%, and reaction temperature is 50-200 degrees C and reaction time is 5-96 hours.    USE - The method is useful for dehydrating and alkylating (I) (claimed).    ADVANTAGE - The method does not need any transition metal or a non-transition metal catalyst; utilizes (III), which can directly reacts in presence of small amount of alkali under inert gas atmosphere or air; easily separates and purifies the product; has high product recovery; utilizes easily available low-cost alcohol as alkylating agent, thus it reduces synthesis cost; is carried out under solvent free conditions, thus it is environmentally friendly; and has mild reaction conditions.    DETAILED DESCRIPTION - Dehydrating and alkylating aminothiazole compounds of formula (I), comprises reacting alcohol compounds of formula (R1-OH) (II) and substituted aminothiazole compounds of formula (III) in presence of alkali under inert gas protection or air, where the molar ratio of amine to alcohol in a reaction raw material is 3:1-1:3, the dosage of alkali is 5-100 mol%, and reaction temperature is 50-200 degrees C and reaction time is 5-96 hours.    R1 = phenyl, aryl, heteroaryl or unsaturated alkyl; and    R2, R3 = phenyl, alkyl, aryl, heteroaryl, substituted heteroaryl, cycloalkyl or R2 and R3 combines to form an optionally substituted benzo group.    Provided that R2 and R3 together with adjacent carbon atoms to form phenyl, alkyl, aryl, heteroaryl, substituted heteroaryl, cycloalkyl or optionally substituted benzo group.
NOVELTY - A chlorinating reagent is reacted N-(2,6-dichlorophenyl)phenylacetamide to obtain N-chloro-N-(2,6-dichlorophenyl)phenylacetamide. The obtained compound reacts with specified amount of Lewis acid in an organic solvent to obtain 1-(2,6-dichlorophenyl)-2-indolinone. The resultant compound is subjected to hydrolysis reaction in sodium hydroxide solution to obtain diclofenac sodium.    USE - Preparation of diclofenac sodium (claimed).    ADVANTAGE - The method efficiently and economically provides diclofenac sodium, by simple method using easily-available reagents under mild conditions.
NOVELTY - Base fertilizer comprises 10-12 wt.% human manure, 18-20 wt.% pig manure, 8 wt.% dairy manure, 12 wt.% canal mud, 10 wt.% hay, 6 wt.% leaves, 10 wt.% rape straw, 6 wt.% wheat bran, 10 wt.% rape seed cakes, 8 wt.% plant ash, 1 wt.% organic fertilizer fermenting agent, 1 wt.% organic fertilizer deodorant, 5 wt.% diammonium phosphate, 2.8 wt.% potassium sulfate and 0.2 wt.% humic acid chelating trace elements.    USE - The base fertilizer is useful for cultivating honeysuckle plant (claimed).    ADVANTAGE - The fertilizer can be prepared by simple method, improves soil quality and root growth of plant, and improves drought resistance, disease resistance and immunity of plant obviously.    DETAILED DESCRIPTION - Base fertilizer comprises 10-12 wt.% human manure, 18-20 wt.% pig manure, 8 wt.% dairy manure, 12 wt.% canal mud, 10 wt.% hay, 6 wt.% leaves, 10 wt.% rape straw, 6 wt.% wheat bran, 10 wt.% rape seed cakes, 8 wt.% plant ash, 1 wt.% organic fertilizer fermenting agent, 1 wt.% organic fertilizer deodorant, 5 wt.% diammonium phosphate, 2.8 wt.% potassium sulfate and 0.2 wt.% humic acid chelating trace elements. The base fertilizer is prepared by drying and mixing human manure, pig manure, dairy manure and canal mud, crushing the obtained mixture using a crushing machine, adding the obtained mixture in a mixing machine, adding plant ash, organic fertilizer fermenting agent, hay, leaves, rape straw and wheat bran to the obtained mixture, mixing and crushing the obtained mixture, adding the obtained mixture in a fermenting tank, adding water and stirring uniformly, sealing and fermenting for 26-28 days, opening the tank, adding organic fertilizer deodorant to the obtained product, mixing and naturally drying the obtained product, mechanically crushing the obtained mixture, adding diammonium phosphate, potassium sulfate and humic acid chelating trace element to the obtained mixture, and crushing the obtained mixture uniformly to obtain finished product.
NOVELTY - Manufacture of entacapone involves nitrating vanillin and nitrating agent, forming 3-methoxy-4-hydroxy-5-nitrobenzaldehyde, demethylating product to generate 3,4-dihydroxy-5-nitro-benzaldehyde, reacting product with N,N-diethylcyanoacetamide in presence of organic base to generate entacapone bromide salt, and dissociating entacapone bromide salt under acidic condition.    USE - Manufacture of entacapone (claimed).    ADVANTAGE - The environmentally-friendly entacapone is manufactured efficiently and economically with high yield, purity of more than 99.9% and Z-isomer content of 0.01%.
NOVELTY - A piperine hydrazone, acylhydrazone or sulfonyl hydrazone derivative substances (I) are new.    USE - Piperine hydrazone, acylhydrazone or sulfonyl hydrazone derivative substances are useful for preparing plant source insecticide (claimed), and providing antifeedant and insecticidal activity.    ADVANTAGE - The piperine hydrazone, acylhydrazone or sulfonyl hydrazone derivative substances exceeds the parent piperine as insecticidal activity of some components is higher than the commercialized botanical pesticide toosendanin, and thus prepares environmentally-friendly and less toxic botanical insecticide.    DETAILED DESCRIPTION - A piperine hydrazone, acylhydrazone or sulfonyl hydrazone derivative substances of formula (I) are new.    R=asterisk-C(=O)-asterisk, asterisk-C(=O)-CH2-CN, or groups chosen from group of formula (i)-(xxxii).    An INDEPENDENT CLAIM is included for preparation of piperine hydrazone, acylhydrazone or sulfonyl hydrazone derivative substances.
NOVELTY - A cobalt(II) metal-organic framework porous material is based on complex ligand of 3-amino-1H-1,2,4-triazole and isophthalic acid.    USE - Cobalt(II) metal-organic framework porous material used as gas storage, adsorption and separation material for adsorbing and separating carbon dioxide or methane from mixed gas of nitrogen, hydrogen, oxygen, carbon dioxide, and methane (all claimed).    ADVANTAGE - The cobalt(II) metal-organic framework porous material can be prepared by solvothermal method with high productivity and reproducibility. The porous material has a frame structure provided with two hole-passage structures of different sizes, which enables selective adsorption of carbon dioxide gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of cobalt(II) metal-organic framework porous material, which involves reacting 3-amino-1H-1,2,4-triazole, isophthalic acid, and cobalt nitrate hexahydrate to obtain a red bulk crystal of cobalt nitrate hexahydrate in double-distilled water and methanol, by solvothermal method, controlling pH to 5-6, heat-preserving at 150-160 degrees C for 3 days, cooling to room temperature, washing, and drying. The molar ratio of 3-amino-1H-1,2,4-triazole, isophthalic acid, and cobalt nitrate hexahydrate is 2-3:1:2-3. The volume of double-distilled water is 5-7 mL and the volume of methanol is 3-5 mL.
NOVELTY - Method for cultivating Agaricus bisporus involves using cultivation base material comprising 50-60 %mass mushroom dreg, 15-25 %mass crop waste, 20-30 %mass livestock excrement, 0.01-0.02 %mass auxiliary material calcium superphosphate and 0.05-0.08 %mass light calcium carbonate.    USE - The method is useful for cultivating Agaricus bisporus (claimed).    ADVANTAGE - The method solves energy waste problem solved, reduces production cost, alleviates working intensity, shortens fermentation time, improves nutritive values of the Agaricus bisporus, and is suitable for large scale production.
NOVELTY - Biological organic foliar fertilizer is prepared by pulverizing rapeseed meal broth, mixing 48 pts. pulverized rapeseed meal broth, 15 pts. yellow humic acid, 5 pts. magnesium, 5 pts. manganese, 5 pts. iron, 5 pts. boron, 2 pts. copper, 2 pts. molybdenum, 3 pts. rhamnose glycolipid biological surfactant, 2 pts. para-chloro phenoxy acetic acid (PCPA), 2 pts. 1-naphthaleneacetic acid (NAA) and 6 pts. sterile water in a reaction kettle, heating the obtained mixture to 45 degrees C for 48 hours, and adjusting pH to 3-4 to obtain the biological organic fertilizer.    USE - The biological organic foliar fertilizer is useful for promoting crop photosynthesis, activating activities of various enzymes to promote the growth, and increasing disease prevention and antibiosis of plants and increase resistance of the plants.    ADVANTAGE - The biological organic foliar fertilizer is pollution-free and harmless, has durable fertilizer efficiency, can strengthen seedlings, prevent diseases, improve soil and increase production, has no residues after use, improves quality of agricultural products, makes products appear on the market 7-15 days earlier, and increases agricultural economy benefits.
NOVELTY - Preparation of Ticagrelor intermediate 4,6-Dichloro-2-propylsulfanyl-pyrimidin-5-ylamine involves reducing nitro group of 4,6-dichloro-5-methyl-2-(propylthio)pyrimidine to amino group by performing reduction reaction using reducing agent sodium hydrosulfite.    USE - Preparation of Ticagrelor intermediate4,6-Dichloro-2-propylsulfanyl-pyrimidin-5-ylamine used in pharmaceutical field.    ADVANTAGE - The method economically and efficiently provides Ticagrelor intermediate 4,6-Dichloro-2-propylsulfanyl-pyrimidin-5-ylamine, by a simple process. The Ticagrelor intermediate 4,6-Dichloro-2-propylsulfanyl-pyrimidin-5-ylamine is environmentally-friendly.
NOVELTY - Mushroom cultivating material comprises 30-50 %mass broad bean, 30-40 %mass mushroom, 10-20 %mass wooden meal, 6-8 %mass bran, 1 %mass calcined lime powder, 1 %mass gypsum, and 1 %mass calcium superphosphate.    USE - The material is useful for cultivating oyster mushroom.    ADVANTAGE - The material has excellent compatibility and impurity, can be prepared cost-effectively with improved yield using easily available raw materials, reduces energy consumption. The bacterial residues are re-utilized, and the wastes are changed into a valuable thing to save energy and reducing emission.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the mushroom cultivating material, which involves mixing the above-mentioned raw materials, solarizing the raw material for 1-2 days using UV rays for killing fungi, wetting and pilling the obtained mixture to a height of 1-1.2 m and width of 2-3 m, where weight of each pile is 250-500 kg, fermenting the obtained product for 4 weeks, covering with grass thatch, maintaining at 60 degrees C for 24 hours, turning piles once a day, adding bacteria sequentially, adding bran and other accessories, adding water depending on the moisture content of the material, fermenting for 6-7 days, and obtaining finished product.
NOVELTY - A purified polypeptide comprising feruloyl esterase having enzymatic activity and the enzyme being obtained from symbionts of Coptotermes formosanus gut, selected from: (a) a polypeptide comprising fully defined 134 amino acids (SEQ ID NO: 2), given in the specification, which is an amino acid sequence having 61% to predicted xylanase/chitin deacetylase enzyme of butyrate-producing bacterium Accession No. CBL40699 and 87% to the polysaccharide deacetylase of Clostridium saccharolyticumi (ADL05911), is new.    USE - The polypeptide is useful for increasing the fiber digestibility of crop residue/straws (claimed); and can also be used in numerous industries for commercial production of the enzyme for various purpose which includes food industries, textile and laundry industries, agro waste treatment industries, chemical, animal feed, pulp and paper pharmaceutical.    ADVANTAGE - The protein so produced by the enzyme is non toxic to the animals; and efficiently increases the fiber digestibility of crop residue/straws.    DETAILED DESCRIPTION - A purified polypeptide comprising feruloyl esterase having enzymatic activity and the enzyme being obtained from symbionts of Coptotermes formosanus gut, selected from: (a) a polypeptide comprising fully defined 134 amino acids (SEQ ID NO: 2), given in the specification, which is an amino acid sequence having 61% to predicted xylanase/chitin deacetylase enzyme of butyrate-producing bacterium Accession No. CBL40699 and 87% to the polysaccharide deacetylase of Clostridium saccharolyticumi (ADL05911); (b) a polypeptide, which is encoded by a polynucleotide comprising of the nucleotide sequence of fully defined 1338 bp (SEQ ID NO: 1), given in the specification, or a fragment having feruloyl esterase activity, is new.
NOVELTY - Rhizosphere soil sample, is claimed. The soil sample is collected from tea growing area of Valparai (Anamallais) and shade-dried.    USE - The rhizosphere soil sample is useful as sample for isolating and exploiting solubilization efficiency of VKSB 12, preferably Pseudomonas putida which is useful for reducing synthetic potash fertilizers (all claimed).    ADVANTAGE - The rhizosphere soil sample enables isolation of strain which improves soil fertility as compared to existing chemical fertilizers and nutrient content of the tea, is environmentally-friendly, prevents depletion of beneficial microorganism in soil, enables higher productivity and ability of plants to resist e.g. diseases, insect attacks and cold, and minimizes leaching of minerals from the soil.
NOVELTY - Method for producing activated carbon from rice hull ash by solid-state fermentation of rice hull, involves inoculating white rot fungi in fermentation culture medium, inoculating Trichoderma viride, Aspergillus niger, T.reesei, T.koningii or blue mold, and carrying out dry distillation to obtain activated carbon.    USE - The method is useful for producing activated carbon from rice hull ash by solid-state fermentation of rice hull (claimed).    ADVANTAGE - The method is simple, easy to operate, and produces activated carbon having micropore structure and good adsorption capacity.
NOVELTY - Method for performing L-sorbitol fermentation, involves mechanically stirring culture comprising L-sorbose from the beginning of inoculation, stably stirring the culture in the logarithmic phase, and mixing the culture in stationary phase until the culture attains its death phase.    USE - The method is useful for performing L-sorbitol fermentation (claimed).    ADVANTAGE - The method consumes less energy and power.
NOVELTY - Preparation of 3-aryl-indolizine derivative (I) comprises taking hydrogen-substituted indolizine derivative (II), aryl boric acid compound (III), palladium catalyst, optionally nitrogen-containing ligand and alkali, pouring into reaction vessel at mol ratio of 1:1.0-3.0:0.0125-0.10:0.0125-0.3 or 0.0:1.0-5.0, adding 2.0-20 ml solvent, heating and stirring at 80-160 degrees C in oxygen atmosphere for 1-48 hours; taking reaction mixture, filtering, washing, drying, and recrystallizing or carrying out column chromatography separation to obtain solid target product.    USE - Method for preparing 3-aryl-indolizine derivative (claimed).    ADVANTAGE - The method is simple and easy, and green and environment-friendly.    DETAILED DESCRIPTION - Preparation of 3-aryl-indolizine derivative of formula (I) comprises taking hydrogen-substituted indolizine derivative of formula (II), aryl boric acid compound of formula (III), palladium catalyst, optionally nitrogen-containing ligand and alkali, pouring into reaction vessel at mol ratio of 1:1.0-3.0:0.0125-0.10:0.0125-0.3 or 0.0:1.0-5.0, adding 2.0-20 ml solvent, heating and stirring at 80-160 degrees C in oxygen atmosphere for 1-48 hours; taking reaction mixture, filtering, washing, drying, and recrystallizing or carrying out column chromatography separation to obtain solid target product.    R1=H, 5-methyl, 7-methyl, 7-N,N-dimethylamino or 7-methyl carbonyl ester;    R2=H, CN, methyl carbonyl ester, carbonyl n-butyl ester, carbonyl tert-butyl ester, carbonyl ethyl group, N,N-dimethyl-carboxamide;    R3=H, Me, phenyl, methyl carbonyl ester, or acetyl carbonyl; and    R4=H, 2-methyl, 3-methyl, 4-methyl, 4-trifluoromethyl, 4-fluoro, 4-chloro, 4-methoxy, or 3,5-dimethyl.    DESCRIPTION OF DRAWING(S) - The drawing shows a process flow diagram of preparation of 3-aryl-indolizine derivative (Drawing includes non-English language text).
NOVELTY - Preparing cefcapene pivoxil hydrochloride (I) comprises adding a sulfonic acid derivative to a solution of t-butoxycarbonyl group cephalosporin product ester to obtain cephalosporin product ester sulfonate, and transferring cefcapene pivoxil sulfonate into the cefcapene pivoxil hydrochloride.    USE - Method for preparing cefcapene pivoxil hydrochloride (claimed).    ADVANTAGE - The method has mild reaction condition, simple and convenient operation, and safe production, is environment-friendly, and can obtain a product having high quality.    DETAILED DESCRIPTION - Preparing cefcapene pivoxil hydrochloride of formula (I) comprises adding a sulfonic acid derivative of formula R-SO3H to a solution of t-butoxycarbonyl group cephalosporin product ester of formula (II) to obtain cephalosporin product ester sulfonate of formula (IV), and transferring cefcapene pivoxil sulfonate (IV) into the cefcapene pivoxil hydrochloride (I).    R=1-12C alkyl, Ph or substituted Ph, where substituents are 1-12C alkyl, 1-12C alkoxy, or unsaturated 1-12C carboxyl.    An INDEPENDENT CLAIM is also included for compounds (IV).
NOVELTY - Ambroxol hydrochloride is refined by combining crude ambroxol hydrochloride and water, heating to 70-75 degrees C, stirring to obtain crude ambroxol hydrochloride solution, adding active carbon, decoloring at 70-75 degrees C, preserving heat, filtering, stirring filtrate at 55-60 degrees C, cooling to 45-48 degrees C, controlling stirring speed at 15 rpm, adding ambroxol hydrochloride seed crystal, crystallizing while maintaining temperature and stirring speed for 1 hour, cooling to 20-25 degrees C, crystallizing for 20 minutes, cooling to 10 degrees C, crystallizing for 1.5 hours, filtering, and drying.    USE - Refining of ambroxol hydrochloride (claimed).    ADVANTAGE - Refining of ambroxol hydrochloride has short reaction route and mild reaction conditions, reduces pollution, amount of impurities, solvent consumption, and cost, and increases product purity and yield.
NOVELTY - A quinazoline derivative is prepared by performing reductive amination reaction on phenyl ether derivative using alkali and reducing agent in organic solvent.    USE - Preparation of quinazoline derivative (claimed).    ADVANTAGE - Preparation process is low cost, easy, and environment-friendly, and has reduced reaction steps, mild reaction, and high product yield.    DETAILED DESCRIPTION - A quinazoline derivative of formula (I) is prepared by performing reductive amination reaction on phenyl ether derivative of formula (II) using alkali and reducing agent in organic solvent.    R1=2-((1-8C) alkyl)amino-(2-8C) alkyl, pyrrolidin-1-yl-(2-8C) alkyl, piperazin-1-yl-(2-8C) alkyl, 4-(1-8C) alkyl piperazin-1-yl-(2-8C) alkyl, imidazol-1-yl-(2-8C) alkyl, di-((1-8C) alkoxyalkyl-(2-8C)alkyl)-amino-(2-8C) alkyl, thiomorpholino-(2-8C) alkyl, 1-oxo-thiomorpholino-(2-8C) alkyl or 1-dioxothiomorpholino-(2-8C) alkyl; and    R2=1-8C alkyl,    provided that the methylene not connected to N or O atoms in R1 is optionally substituted by OH, aryl, heteroaryl, heterocyclyl, alkyl, alkenyl, alkynyl, cycloalkyl and/or alkoxy.
NOVELTY - Paper made from biomass material comprises (in pts. wt.): active filler (40-80), polybutylene succinate (20-60), bulking agents (1-3), lubricant (0.5-2), interfacial modifier (0.3-0.5), flexibilizer (1-2), raising agents (0.3-0.5), foaming agents (0.2-0.5) and anti-oxidant (0.03-0.08).    USE - Used as a paper.    ADVANTAGE - The paper can be energy-efficiently and economically prepared in an environmentally friendly manner.    DETAILED DESCRIPTION - Preparing the paper made of biomass material, comprising drying the biomass material using alkaline solution at a temperature of 70-140 degrees C and a pressure of 3 MPa for 3 hours, and filtering the residue, preparing biomass-based succinic acid and then fermenting for 60-72 hours at a temperature of 35-42 degrees C, reacting the succinic acid and butanediol, controlling the reaction temperature to 150-260 degrees C under normal pressure, mixing zinc acetate, germanium oxide, stannous chloride, zinc stearate, propyl titanate, titanium acid methyl ester, p-toluene sulfonic acid and/or tetrabutyl titanate, and extruding and granulating the raw materials and then performing extrusion molding to obtain paper, where a mole ratio of succinic acid and butanediol is 1-3:1 and the mixing reaction is carried out for 2-8 hours.
NOVELTY - Composition comprises makgeolli yeast.    USE - The composition is useful for promoting composting (claimed).    ADVANTAGE - The composition has anti-fungal effect.
NOVELTY - Manufacturing capsiate analogs comprise reacting 100 pts. wt. mixture of vanillyl alcohol and a fatty acids in a molar ratio of 1:2-1:5 with 3-20 pts. wt. immobilized lipase by stirring at 400-600 revolutions per minute at 40-60 degrees C.    USE - The method is useful for manufacturing capsiate analogs (claimed).    ADVANTAGE - The method is environmentally friendly and has high yield.
NOVELTY - A Chlamydomonas reinhardtii strain KNUA021 capable of producing 16-18C fatty acid and hexadecenol, is new.    USE - The C.reinhardtii strain KNUA021 is useful for producing 16-18C fatty acid and hexadecenol which are used for producing biodiesel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for producing 16-18C fatty acid and hexadecenol, involves culturing C.reinhardtii strain, and extracting 16-18C fatty acid and hexadecenol from cultured product; and (2) method for producing biodiesel, involves esterifying the 16-18C fatty acid and hexadecenol.
NOVELTY - A biogas and organic fertilizer production method involves subjecting sugar beet pulp biomass to anaerobic fermentation in a biogas fermentor.    USE - Method for producing biogas and organic fertilizer from sugar beet pulp biomass.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a fermenter for production of biogas and organic fertilizer.
NOVELTY - A Nostoc species strain KNUA 003 (KCTC 12063BP), is new. The N.species strain KNUA 003 is capable of producing heptadecane, hexadecanol and fatty acid of 16-18C.    USE - The N.species strain KNUA 003 is useful for producing heptadecane, hexadecanol and fatty acid of 16-18C (all claimed), for producing biodiesel.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) method for producing heptadecane, hexadecanol and fatty acid of 16-18C, involves culturing N.species strain KNUA 003 capable of producing heptadecane, hexadecanol and fatty acid of 16-18C and extracting culture fluid from culture medium using solvent; and (2) method for producing biodiesel, involves esterifying the fatty acid of 16-18C produced by N.species strain KNUA 003 to the transformer and producing fatty acid ester.
NOVELTY - A microalgae Limnothrix sp. strain KNUA 012 (KCTC 12064BP), is new.    USE - The microalgae Limnothrix sp. strain KNUA 012 is useful for producing pentadecane, hexadecenol, and 14-16C fatty acid chosen from myristoleic acid (14:1C), palmitoleic acid (16:1C) and palmitic acid (16:0C) used for producing biodiesel (all claimed).    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following: (1) preparation of pentadecane, 14-16C fatty acid, and hexadecenol involves (a) cultivating Limnothrix sp. strain KNUA 012 and (b) extracting pentadecane, 14-16C fatty acid, and hexadecenol from culture medium; and (2) preparation of biodiesel involves esterifying 14-16C fatty acid produced by Limnothrix sp. strain KNUA 012 and producing fatty acid ester.
NOVELTY - Method for producing hydrogen using a granulated thermophilic strain mixture involves heating sludge of a digester, sewage sludge, or soil at high temperature and preparing a strain mixture including hydrogen-producing bacteria, culturing the strain mixture in a continuous stirred tank reactor (CSTR), adding the mixture strain into an expanded granular sludge bed digestion (EGSB) and granulating the strain mixture, adding a substrate to the EGSB, adding nutrients and a buffer solution to the EGSB, and performing fermentation in the EGSB.    USE - The method is useful for producing hydrogen (claimed).    ADVANTAGE - The method enables to produce product with high speed as it has reduced hydraulic retention time.
NOVELTY - Manufacture of membrane electrode assembly involves forming adhesive layer using composition containing crosslinked polymer precursor, curing agent, pore-forming agent and surfactant, forming hydrogen ion-conductive polymer electrolyte membrane on at least one side of the adhesive layer, forming interfacial adhesive layer on both sides of the hydrogen ion-conductive polymer electrolyte membrane, and forming pore in a surface of the interfacial adhesive layer and adhesive layer.    USE - Manufacture of membrane electrode assembly used for fuel cell (claimed).    ADVANTAGE - The method provides membrane electrode assembly having excellent adhesiveness between the adhesive layer and polymer electrolyte membrane. The fuel cell obtained by the membrane electrode assembly has excellent durability.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for fuel cell.
NOVELTY - The apparatus has heating unit that maintains the temperature of the stirred tank (10) while the fowl droppings are stirred with the bacteria. A port is provided with the stirred tank. A driving unit is provided for operating the mixer (20). An air outlet (16) exhausts the poison gas generated in the stirred tank and is installed with air inlet (15) for supplying air inside the stirred tank. A vent (12) is formed in the stirred tank in order to eject the fermented fowl droppings with the reverse rotation of the mixer.    USE - Apparatus for treating fowl dropping generated in stockbreeding farmhouse.    ADVANTAGE - The expenses of animal feeds saving of the farmhouse can be reduced. The processing cost of the fowl dropping treatment apparatus can be reduced effectively. The second-order product environmental contamination including the soil according to the discharge of the organic waste or ground water pollution etc. can be prevented. The growth of the hen gets raged and the shipping timing can get raged and the scattering rate can increase. The profit of the farmhouse can be increased since the prevention of infection cost can be reduced effectively. The quality of the egg is improved to the immunity enhancement. The bad small generation of the culex etc. can be prevented effectively.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating fowl dropping generated in stockbreeding farmhouse.    DESCRIPTION OF DRAWING(S) - The drawing shows the perspective view of the apparatus for treating fowl dropping generated in stockbreeding farmhouse.    Stirred tank (10)    Vent (12)    Air inlet (15)    Air outlet (16)    Mixer (20)
NOVELTY - Manufacturing compost from organic waste using hot water extract of Willow tree, comprises fermenting by adding thermophilic microorganisms extracted with hot water from Willow tree to organic waste.    USE - The method is useful for manufacturing compost from organic waste using hot water extract of Willow tree (claimed).    ADVANTAGE - The produced compost is environmentally friendly and has no odor. The method does not produce separate liquid organic waste, processes the organic waste in simple manner, reduces pollution and provides significant cost savings including electricity and fuel cost.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for:    (1) the compost prepared by the method; and    (2) purifying liquid organic waste by using hot water extract of willow tree, comprising (a) separating solid and liquid states of organic waste, and (b) fermenting by adding thermophilic microorganisms extracted with hot water from willow tree to the separated liquid state organic waste.
NOVELTY - Catalyst comprising metallic element and copper-chromium element, is new.    USE - The catalyst is useful for preparing 1,2-propanediol (claimed), which is useful for preparing biodiesel used in an engine.    ADVANTAGE - The high activation catalyst produces the 1,2-propanediol with high yield.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for the preparation of the catalyst.
NOVELTY - Preparing unsaturated polyester resin from biomass comprises reacting an oligomerglycol structure of fatty acid with unsaturated acids by an esterification reaction to prepare glycerol prepolymer, progressing the esterification reaction between the unsaturated acids and glycerol after hydrolyzing a vegetable oil under an basic catalyst existence and making mono glyceride to prepare prepolymer of oligomerglycol structure, and (c) reacting polyatomic acid with an unsaturated group in the oligomerglycol structure prepolymer and reacting the polyatomic acid with saturator and polyhydric alcohol.    USE - The method is useful for preparing unsaturated polyester resin from biomass such as vegetable oil, glycerol and fatty acid (claimed), where the unsaturated polyester resin is useful for molding a fiberglass reinforced plastic container, pipe, grating, artificial marble and non-excavating sewerage pipe.    ADVANTAGE - The method is capable of environment-friendly preparing unsaturated polyester resin with high intensity, high corrosion resistance, and high thermal resistance.    DETAILED DESCRIPTION - Preparing unsaturated polyester resin from biomass comprises (a) reacting an oligomerglycol structure of fatty acid with unsaturated acids by an esterification reaction to prepare biomass originated glycerol prepolymer, (b) progressing the esterification reaction between the unsaturated acids and glycerol after hydrolyzing a vegetable oil under an basic catalyst existence and making mono glyceride to prepare prepolymer of biomass originated oligomerglycol structure, and (c) reacting a polyatomic acid with an unsaturated group in the prepolymer of biomass originated oligomerglycol structure and reacting the polyatomic acid with saturator and polyhydric alcohol to prepare unsaturated polyester resin.
NOVELTY - Preparing fuel comprises carbonizing dehydrated tires, mixing tetra-calcium aluminate salt, tricalcium silicate and tricalcium aluminate in salt water, mixing low-grade coal having calorific value of less than 3000 Kcal, stirring to form an igniting composition, mixing paraffin, cornerstone and calcium hydroxide dihydrate to form a mixture, mixing 10-20 wt.% of hexamethylene tetramine and 2-3 wt.% of a mixture of hydrocarbons to prepare a bonding agent, and mixing the igniting composition (5-10 wt.%) and the bonding agent (2-5 wt.%) with carbide and drying the mixture.    USE - The method is useful for preparing fuel using waste tire to prepare a fertilizer (all claimed).    ADVANTAGE - The fuel is prepared by recycling the waste tire and utilizing the tire as the new energy source, thus avoiding environmental contamination and pollution. The agricultural waste can be recycled and used as an excellent fertilizer with low-grade coal having calorific value of less than 3000 Kcal so that the calorific efficiency of the fertilizer is excellent.    DETAILED DESCRIPTION - Preparing fuel comprises carbonizing dehydrated tires (40-60 wt.%), mixing tetra-calcium aluminate salt, tricalcium silicate and tricalcium aluminate in a salt water, mixing 2-3 wt.% of low-grade coal having calorific value of less than 3000 Kcal with the mixture, stirring to form an igniting composition, mixing paraffin (30-50 wt.%), cornerstone (10-20 wt.%) and calcium hydroxide dihydrate (15-25 wt.%) to form a mixture, mixing 10-20 wt.% of hexamethylene tetramine and 2-3 wt.% of a mixture of hydrocarbons to prepare a bonding agent, and mixing the igniting composition (5-10 wt.%) and the bonding agent (2-5 wt.%) with carbide and drying the mixture. An INDEPENDENT CLAIM is included for a fertilizer comprising ash of fuel.
NOVELTY - Producing a butanone comprises decarboxylizing a levulinic acid in the presence of acetoacetate decarboxylase (AADC) biocatalizer and/or AADC expression microorganism.    USE - The method is useful for producing a butanone from levulinic acid (claimed), where the butanone is presented in a form of 2-butanol as biofuel.    ADVANTAGE - The method is capable of enhancing conversion efficiency of the butanone.
NOVELTY - The device (2) has a conduit (9) whose end is connected with a container (3) by a pressurized medium. A distribution unit is connected to an end of the conduit. A dosing device is utilized for dosing predetermined amount of the substance. Two pump units (12, 13) apply the predetermined amount of the substance from another container (5) through the conduit. An adjustable control unit controls a dispensing device for a certain time period when a specified amount of the substance is dosed. A recording unit records and stores dosed quantities of substance for the certain time period.    USE - Device for applying a certain amount of a working-substance e.g. AgriMestMix (RTM: Natural mineral blend) and Compost-O (RTM: Organic matter), to manure i.e. dung (claimed) of an animal i.e. pig, in a large stable.    ADVANTAGE - The device can reduce emission of gases such as ammonia and methane in an easy manner. The device is simple in structure and high in accuracy. The device can utilize nitrogen in manure in a better way, and develops a root system of the plant in an easy manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for applying a certain amount of a working-substance manure to manure    (2) a dung.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a device for applying a certain amount of a working-substance.    Stable (1)    Device for applying a certain amount of a working-substance (2)    Containers (3, 5)    Conduit (9)    Pump units (12, 13)
NOVELTY - The chamber (10) has storage tank that is connected with induction pipe discharging sodium hypochlorite aqueous solution to chamber (11) outside. Emission tube (12) emits sodium hypochlorite and hydrogen gas within chamber main portion. Lower portion of main portion is connected to a discharge pipe (5a). Sodium hypochlorite and the electrolyzed hydrogen gas are released through hydrogen gas exhaust pipe (7). An electrolytic cell is connected to lower portion of main portion. The electrolytic cell electrolyzes salty water with direct current applied to cathode and anode.    USE - Flash chamber of electrolysis fungicide formation apparatus.    ADVANTAGE - The electrolysis fungicide formation apparatus can be used safely. Leakage of the hydrogen gas from the hydrogen gas exhaust pipe can be prevented. The hydrogen gas can be safely discharged to the outside. The efficiency of the flash chamber can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the flash chamber.    Discharge pipe (5a)    Hydrogen gas exhaust pipe (7)    Flash chamber (10)    Chamber main portion (11)    Emission tube (12)
NOVELTY - The apparatus (5) has a power supply unit (10), an electronic filter (20) and a reactor (30) which is configured for dissociating water into a hydrogen and oxygen gas mixture via an electrolytic process. The reactor is described as a variable resistance load and the power supply is configured to provide a constant current for the variable resistance load. The reactor includes an anode (32) and a cathode (34) which is formed by an outer hull fabricated from a stainless steel.    USE - Hydrogen enrichment apparatus of fuel for internal combustion.    ADVANTAGE - The production of carbon monoxide and carbon dioxide can be reduced. The hazardous storage elements for the hydrogen such as pressure tanks can be avoided. The apparatus offers the improved source of energy or fuel, and easy/stable to operate.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for hydrogen enrichment of fuel for internal combustion engine.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the for hydrogen enrichment apparatus.    Hydrogen enrichment apparatus (5)    Power supply unit (10)    Electronic filter (20)    Reactor (30)    Anode (32)    Cathode (34)
NOVELTY - The system has secondary magnetic separator (12) which is installed at upper portion of third conveyor (11). First conveyor (4) is provided for supplying raw material (2) to crusher (3). The crusher is provided for crushing raw material transferred with first conveyor to fixed level. Second conveyor (8) is arranged for supplying raw material crushed with crusher to air elutriator (7). The air elutriator is arranged for separating and removing non-ferrous metal among raw material using wind force.    USE - Recycled plastic fuel (RPF) manufacturing system for making combustible waste of paper, wood, fiber type plastic, vinyl etc into solid fuel.    ADVANTAGE - The recycled plastic fuel (RPF) manufacturing system has high efficiency.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the RPF manufacturing system. The need for pulverizing device and moisture dryer are avoided so that the manufacturing cost can be reduced.    Raw material (2)    Crusher (3)    Conveyors (4,8,11)    Air elutriator (7)    Secondary magnetic separator (12)
NOVELTY - Stick type slow-release fertilizer comprises core layer, middle layer, and shell layer. The core layer is formed by mixing inorganic fertilizer and starch, and pressing and molding the mixture. The middle layer is formed by mixing natural material or microorganism, and starch, and pressing and molding the mixture. The shell layer is formed by mixing inorganic fertilizer and starch, and pressing and molding the mixture.    USE - The stick type slow-release fertilizer is useful for providing plants with various nutrients for growth.    ADVANTAGE - The fertilizer is convenient to use.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for preparing the fertilizer which involves preparing and bonding the above-mentioned layers.
NOVELTY - The purifier (1) has an oil tank (600) which stores the vegetable oil. A de-waxing apparatus separates fat and vegetable oil. An ageing tank ages the waste oil cooled in the chill tank. A cooling tank (400) cools edible oil in vacuum tank (300). A heating tank (200) stores cooled dibble oil. The moisture contained in the waste oil is removed. A boiling water portion (100) cleanses the heated edible oil, while filtering the foreign substance included in the waste oil, and heats and precipitates foreign substance.    USE - Purifier for refining edible oil used in cooking. Uses included but are not limited to edible oil such as vegetable oil, sesame oil, perilla oil, soybean oil, olive oil, grape seed oil, canola oil, sunflower seed oil and palm oil.    ADVANTAGE - The disposable edible oil falling into disuse with illegality can be recycled efficiently as the mold lubricating oil. The edible oil can be refined at low cost.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for refinement process of edible oil.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the purifier.    Purifier (1)    Boiling water portion (100)    Heating tank (200)    Vacuum tank (300)    Cooling tank (400)    Oil tank (600)
NOVELTY - A Solid biomass fuel comprises 60-85 wt.% culled wood, 10-20 wt.% rice hulls, 4-20 wt.% binder and 1-5 wt.% additive.    USE - Solid biomass fuel (claimed).    ADVANTAGE - The solid biomass fuel has high density and low compressive strength.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of biomass solidity type fuel.
NOVELTY - Green synthesis of oxo-o-tolyl-acetic acid (I) comprises reacting 1,3-di(2-methylphenyl)propan-1,3-dione with iodine and dimethylsulfoxide and reacting the obtained 2,2-dihydroxy-1,3-di(2-methylphenyl)propan-1,3-dione with iron trichloride with iron trichloride in aqueous solution at pH 32.8-3.2 for 2-3 hours.    USE - Synthesis of oxo-o-tolyl-acetic acid used as intermediate for trifloxystrobin.    ADVANTAGE - The environmentally-friendly oxo-o-tolyl-acetic acid is manufactured efficiently with high yield and excellent workability, by simple method.
NOVELTY - Photocatalyst comprising an electroconductive film support layer (10), a sponge foam photocatalytic layer (20) and titanium dioxide holes (22) with nano size and specified value of inner hole diameter, is new.    USE - The titanium dioxide photocatalyst is useful for methane or methanol production.    ADVANTAGE - The titanium dioxide photocatalyst is economic to produce, and easy to handle.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for producing the photocatalyst.    DESCRIPTION OF DRAWING(S) - The diagram shows a schematic view of photocatalyst.    Electroconductive film support layer (10)    Sponge foam photocatalytic layer (20)    Titanium dioxide photocatalyst hole (22)    Cathode power. (30)
NOVELTY - An alcohol mixed fuel emulsifier contains esterified polyglycerine fatty acid (A) having one or more hydroxyl groups in molecule and compound (B) chosen from sorbitol, polyoxyethylene fatty acid having one or more hydroxyl groups in molecule, polyoxyethylene alkyl ether and polyoxyethylene alkyl aryl ether compound in weight ratio of 1:100-100:1.    USE - Alcohol mixed fuel emulsifier for manufacturing alcohol mixed fuel (all claimed).    ADVANTAGE - The alcohol mixed fuel emulsifier has excellent safety, and is environmentally-friendly.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) alcohol mixed fuel; and    (2) manufacture of alcohol mixed fuel.
NOVELTY - Synthesizing 2-benzothiazolyl dimethylacetal, comprises selecting benzothiazole, methanol and 2- benzothiazole as raw material and reacting the selected benzothiazole and methanol with 2-methyl-benzothiazole as an oxidizing agent.    USE - The method synthesizes is useful for synthesizing 2-benzothiazolyl dimethylacetal (claimed).    ADVANTAGE - The method synthesizes 2-benzothiazolyl dimethylacetal and 2-benzothiazol formaldehyde in a simple, convenient, cost-effective and environmental-friendly manner.    DETAILED DESCRIPTION - Synthesizing 2-benzothiazolyl dimethylacetal, comprises selecting benzothiazole, methanol and 2- benzothiazole as raw material, reacting the selected benzothiazole, methanol with 2-methyl-benzothiazole as an oxidizing agent, where the oxidizing agent is ferric trichloride, copper oxide, potassium dichromate, high manganese acid, peroxide benzoic acid anhydride, tertiary butyl alcohol, potassium mono persulfate composite salt, potassium persulfate, sodium persulfate, ammonium persulfate, ammonium ceric nitrate, benzoquinone, 2,3-dichloro-5,6-dicyano-1,4-benzoquinone, di-tert-butyl peroxide or hydrogen peroxide. An INDEPENDENT CLAIM is included for synthesizing 2-benzothiazole formaldehyde, comprising selecting benzothiazole, methanol and 2- benzothiazole as raw material, reacting the selected benzothiazole, methanol with 2-methyl-benzothiazole as the oxidizing agent.
NOVELTY - A multiblock conjugated polymer having phenylene ethylene structure (I), is new.    USE - New multiblock conjugated polymer having phenylene ethylene structure is used in cellular imaging (claimed).    ADVANTAGE - The multiblock conjugated polymer has improved water solubility, and low toxicity with respect to cells.    DETAILED DESCRIPTION - A multiblock conjugated polymer having phenylene ethylene structure of formula (I), is new.    n=1-30;    x=2, 3 or 4;    R=CyH2y+1 or (C2H4O)zCH3;    y=1-12;and    z=0-6.    INDEPENDENT CLAIMS are included for the following:    (1) preparation of multiblock conjugated polymer having phenylene ethylene structure (I); and    (2) application of multiblock conjugated polymer having phenylene ethylene structure (I) in cellular imaging, which involves dissolving multiblock conjugated polymer having phenylene ethylene structure (I) in dimethyl sulfoxide or dissolving multiblock conjugated polymer having phenylene ethylene structure (I) in mixed solvent of water and dimethyl sulfoxide, adding solution to cell culture medium, measuring material effect on cell membrane markers with fluorescence microscope.
NOVELTY - Manufacture of soil conditioner involves adding masato sludge as weathered granite, masato sludge containing organic polymer, milk processing sludge, granite talc stone, organic waste, sewage sludge, manure and livestock waste to pellet-type or vertical-type diluting agent consisting of bentonite and nutrient, mixing, heating at 50-70 degrees C, sterilizing, removing viscosity of organic polymer, fermenting for 2-4 hours, crushing, and drying.    USE - Manufacture of soil conditioner (claimed).    DETAILED DESCRIPTION - Manufacture of soil conditioner involves adding masato sludge as weathered granite, masato sludge containing organic polymer, milk processing sludge, granite talc stone, organic waste, sewage sludge, manure and livestock waste to pellet-type or vertical-type diluting agent consisting of bentonite and nutrient, mixing, heating at 50-70 degrees C, sterilizing, removing viscosity of organic polymer, fermenting for 2-4 hours, crushing, and drying. The livestock excretion comprises organic polymer including 40-60 pts. wt. sewage sludge, 20-50 pts. wt. organic waste, 5-15 pts. wt. excrement sewage sludge and 2-5 pts. wt. granite soil sludge, masato soil, oil, inorganic sludge, organic waste, diluting agent and 2-5 pts. wt. ash.
NOVELTY - A fuel pellets are obtained by mixing 50-80 wt.% sewage sludge and 5-20 wt.% primary waste obtained by mixing waste plastic film and waste plastic, fusing in a melter at 50-150 degrees C for 1-10 seconds and pelletizing to a cylindrical pellets having diameter 5~50 mm, and length 2~20 cm.    USE - Fuel pellets (claimed).
NOVELTY - Esterifying and modifying wood fiber biomass comprises drying, crushing and pre-processing the wood fiber biomass, passing the mixture in a pre-ball mill, adding esterification reagent, continuously ball milling for esterification modification reaction, washing the product, and drying.    USE - The method is useful for esterifying and modifying wood fiber biomass (claimed).    ADVANTAGE - The method provides wood fiber biomass with high resource utilization rate, without wastage and recycling solvent in a simple, cost-effective and environmental-friendly manner.
NOVELTY - Methane containing 88-92 wt.% carbon dioxide is passed through a porous membrane, and methane and 8-12 wt.% cold bed methane are separated. The pressure difference of front and rear of porous membrane is 5-7 MPa.    USE - Methane separation method (claimed).
NOVELTY - Charcoal fired brown coal is obtained by injecting a mixture into a pellet extruder and extruding. The mixture comprises (in parts weight) food waste, general wood flour (80-150), juniper wood flour (20-30), palm tree wood flour (30-50), rice-bran oil cake (10-15), complexing agent (0.05-0.1), edible molasses as organic binder (3-5), and kaolinite as inorganic clay binder (5-10).    USE - Charcoal fired brown coal.
NOVELTY - Producing (M1) an alkylbenzene product from a natural oil, comprises: deoxygenating the natural oil to form a stream comprising paraffins; dehydrogenating at least a portion of the paraffins to provide mono-olefins; alkylating benzene with the mono-olefins under alkylation conditions to provide an alkylation effluent comprising alkylbenzenes and benzene; and isolating the alkylbenzenes to provide the alkylbenzene product.    USE - The method is useful for producing: an alkylbenzene product from a natural oil (claimed) including coconut oil, babassu oil, castor oil, cooking oil, or other vegetable, nut or seed oils; and biofuels including biodiesel.    ADVANTAGE - The method provides renewable alkylbenzene products and biofuels.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for producing (M2) an alkylbenzene product from natural oil source triglycerides comprising: deoxygenating the triglycerides to form a stream comprising water, carbon dioxide, propane, a first portion of paraffins, and a second portion of paraffins; fractionating the stream to separate the first portion of paraffins and the second portion of paraffins; dehydrogenating the first portion of paraffins to provide mono-olefins; alkylating benzene with the mono-olefins under alkylation conditions to provide an alkylation effluent comprising alkylbenzenes and benzene; and isolating the alkylbenzenes to provide the alkylbenzene product.
NOVELTY - The structure has a heat exchanger which warms water in the fuel cell, while locating a conduit line. A heat exchanger (40) for a heat pump (30) is installed at a portion of multiple independent spaces. A fuel cell cools and heats the fuel cell waste heat to perform the cooling-and-heating at independent space. A heat pump is located on surface of the conduit line (60) and is arranged in the independent space for cooling and heating the independent space using the heat generated in the fuel cell.    USE - Heating and air conditioning structure of building.    ADVANTAGE - The thermal efficiency of the heating and air conditioning structure can be maximized. The resident stability nature of the heating and air conditioning structure can be guaranteed.    DESCRIPTION OF DRAWING(S) - The drawing shows a circuit diagram of the heating and air conditioning structure.    Heat pump (30)    Heat exchanger (40)    Temperature sensor (42)    Flow sensor (43)    Conduit line (60)
NOVELTY - A hydrochlorothiazide porous membrane comprises a polymer prepared by high molecular polymer and 0.5-30 wt.% nanometer oxide particle.    USE - Hydrochlorothiazide porous membrane for manufacturing fuel cell.    ADVANTAGE - The hydrochlorothiazide porous membrane is prepared in a simple and inexpensive manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are also included for the following:    (1) a method for preparing hydrochlorothiazide porous membrane    (2) a method for applying hydrochlorothiazide porous membrane.
NOVELTY - Production of natural gas involves carrying out adiabatic compression of raw material natural gas containing helium gas, separating the helium gas from the raw material natural gas by passing the adiabatically compressed raw material through a separation-membrane unit, conveying the raw material natural gas from which the helium gas is separated through a pipeline (11a) to a terminal (14), and injecting the helium gas separated from the raw material natural gas into an underground storage layer.    USE - Production of natural gas (claimed).    ADVANTAGE - The method enables economical production of natural gas.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production system (10A) of natural gas, which consists of compressor (131) which carries out the adiabatic compression of the raw material natural gas containing helium gas, separation-membrane unit which separates the helium gas from the raw material natural gas, pipeline for conveying the raw material natural gas from which the helium gas is separated towards a terminal, and underground restoration installation (16) which pressingly injects the separated helium gas in the underground storage layer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the production system of natural gas. (Drawing includes non-English language text)    Production system of natural gas (10A)    Pipeline (11a)    Terminal (14)    Underground restoration installation (16)    Compressor (131)
NOVELTY - Processing heavy oil hydrogenation and biomass liquefaction comprises using slurry-bed hydrocracking reactor, taking heavy oil and biomass as raw material, where the amount of heavy oil and biomass is 5-20 wt.%, adding a catalyst and vulcanizing agent, and controlling the temperature of hydrogenation cracking reaction at 370-430 degrees C and hydrogen partial pressure to 4-8 MPa, where the catalyst is oil-soluble dispersed hydrogenation catalyst, and the heavy oil is vacuum gas oil with distillation range of 360-540 degrees C and/or fluid catalytic cracking slurry oil.    USE - The method is useful for processing heavy oil hydrogenation and biomass liquefaction (claimed).    ADVANTAGE - The method: has uniform reaction temperature; achieves more than 90 wt.% conversion rate of the biomasses at lower hydrogen pressure (4-8 MPa) and the temperature (370-430 degrees C); achieves more than 70 wt.% oil phases yield; utilizes the dispersed hydrogenation catalyst, which greatly reduces the quantity of raw coke and has good deoxidization effect on biomasses.
NOVELTY - A prodrug of a podophyllotoxin (POD) derivative (I), where theprodrug is formed by acid-sensitive imine bond covalent combination of a medicine molecule and hydrophilic short-chain polyethylene glycol,and medicine molecule is the podophyllotoxin derivative, such as amino podophyllotoxin (NPOD), is new.    USE - Prodrug of a podophyllotoxin (POD) derivative for use innano-sized micelle or vesicle that is utilized as medicine carrier (all claimed).    ADVANTAGE - The prodrug is simple in preparation, environmental friendliness and economical benefit.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) the preparation of (I)    (2) a nano-sized micelle or vesicle, comprising the prodrug of a podophyllotoxin (POD) derivative    (3) a method for preparing nano-sized micelle or vesicle, which involves dissolving the prodrug in the solvent, to form the micelle or vesicle to a size over the course of dialysis.
NOVELTY - This utility model claims a stable structure of glass fibre reinforced plastic biomass pool, comprising an upper cover, a tank, a feeding pipe and a discharge pipe, wherein the upper cover and the lower tank by the flange I is fixedly connected with the feeding pipe and the discharging pipe are respectively located at the left and right sides of the lower tank, and is connected with the lower bottom, the feeding pipe is composed of a pipe and a pipe fitting, and are fixedly connected by a flange II, and the discharging pipe is composed of a spacing and discharging pipe, and are connected with each other through flange III, the flange II is connected with the flange I are connected by a fixing bolt, the flange with flange I is fixedly connected through a fixing bolt. With the existing marsh gas tank, the utility model using geometric theory, a feed pipe, a discharge pipe and the tank main body to form a stable triangular structure, which effectively improves the connecting strength and rigidity of the whole marsh gas tank, is convenient to install, good corrosion resistance, a large scale factory production, high reliability, and long service life.
NOVELTY - A biodiesel composition comprises biodiesel and phenol amide compound (I) or (II).    USE - Biodiesel composition for increasing oxidation stability of a biodiesel-containing fuel (claimed).    ADVANTAGE - The composition increases the oxidation stability of the poor oxidation stability biodiesel such as an acid oil biodiesel, a cottonseed oil biodiesel or a biodiesel-containing blending fuel.    DETAILED DESCRIPTION - A biodiesel composition comprises biodiesel and phenol amide compound of formula (I) or (II).    n = 1-3;    p = alkylene group, or 0-6;    R2 = H, -((CH2)xNH)y-R6, -((CH2)x1NH)y1-R7, or moiety of formula (a), where benzene ring is connected with the sub-alkyl or carbonyl carbon atoms ortho, meta or para-position;    x1 = 2 or 3;    y1 = 0-5; and    R6-R8 = 1-24C alkyl.    An INDEPENDENT CLAIM is also included for a method for increasing oxidation stability of a biodiesel-containing fuel, which involves adding biodiesel fuel containing phenolic amide compound (I) of (II).
NOVELTY - Producing marsh gas comprises crushing, sterilizing and disinfecting a crop straw and then performing acidification of the crop straw, and performing anaerobic fermentation and desulfurization on the straw with glass fiber reinforced plastic materials.    USE - The method is useful for producing marsh gas (claimed).
NOVELTY - This utility model claims a biological diesel oil methyl esterification and methanol continuous purifying device, comprising a methanol rectification kettle, a rectifying tower, a cooler and a esterification kettle, wherein the methanol rectifying kettle is provided with a stirrer, a methanol rectifying kettle is connected with the rectifying tower is connected with a cooler connected with the rectifying tower, the top outlet of the rectifying tower is connected with the biodiesel esterification kettle is connected with the supercharger is set on the rectifying tower partially or completely. The beneficial effects are: the structure is simple, which improves the rectifying efficiency of methanol, methanol volatilization loss, obviously reduces the production cost and environment pressure of the bio-diesel.
NOVELTY - A biogas production system has a storage tank for temporarily storing organic substance, methane fermentation apparatus and a hydrothermal decomposition apparatus for decomposing organic substance by fermentation using anaerobic microorganisms in absence of oxygen. Hydrogen ion contained in water is coupled with organic polymer and hydrolyzed to form low molecular weight organic acid. The decomposition is carried out using the generated acid.    USE - Biogas production system for treating organic substance (claimed).    ADVANTAGE - The system quickly enables treatment of organic substance.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating organic substance.
NOVELTY - A biomass is dissolved in room temperature ionic liquid containing cellulose, hemicellulose and lignin to dissolve cellulose. The cellulose is removed from room temperature ionic liquid by recrystallization. The cellulose is processed, to obtain glucose.    USE - Manufacture of glucose (claimed).    ADVANTAGE - The glucose is economically manufactured by simple method, without environmental pollution.
NOVELTY - The roller has a cylindrical roller (2) that is arranged on a machine frame (1). The cylindrical roller is opened on the side wall of a through-hole (3), and is driven by a power mechanism. A gear is arranged at other end of a rotating shaft. The rotating shaft is connected with power mechanism through a transmission wheel.    USE - Roller for biomass fuel granulating machine.    ADVANTAGE - Since the rotation of biomass material in the roller is pressed into pellet fuel via the through-hole, the structure of the roller can be simplified. The high heating value, strength, convenient operation, productivity, efficiency and stability of the roller can be improved. The power consumption and energy consumption of the roller can be reduced. The coal can be replaced conveniently so as to gain full use of crop straw, firewood and other biomass resources.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view of the roller for biomass fuel granulating machine.    Machine frame (1)    Cylindrical roller (2)    Through hole (3)
NOVELTY - The method involves processing a cooling hole connected along the axial direction of a machine main shaft and a pressing roller (1), to form a set of cooling loop system. A water cooling system is connected with the biomass granulator, for reducing the temperature of the pressure roller. A cooling circuit is set to carry out the heat exchange through a cooling system to reduce the temperature of oil into the oil tank (11). A temperature control device is connected on the principal shaft of granulator, to ensure the preset working temperature range of main shaft.    USE - Method for reducing operating temperature of raw material in pressure roller shaft bearings used for processing residue of straw and bamboo wood.    ADVANTAGE - The operating temperature of the pressure roller shaft bearings can be reduced to greatly extend the service life of the ring mold and pressure roller. The continuous operating time of the pellet mill can be reduced. The production cost of the biomass briquette can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows the schematic view illustrating the process for reducing operating temperature of raw material in pressure roller shaft bearings.(Drawing includes non-English language text)    Pressing roller (1)    Main shaft assembly (3)    Oil inlet passage (7)    Pressure oil pipe (10)    Oil tank (11)
NOVELTY - The method involves providing an electrolyzer (12), and receiving a series of dispatches indicating specified power consumption for a period of time. The dispatches occur for every thirty minutes. The electrolyzer is operated according to the dispatches. The hydrogen produced is discharged to a natural gas system. The hydrogen is converted into methane before hydrogen is injected into a natural gas pipeline (34). The electrolyzer is provided with a controller and an electricity meter.    USE - Method of operating electrolyzer in energy system, used for providing electrical grid services and producing hydrogen used as fuel for vehicle, as heating fuel, as industrial chemical, in wastewater treatment, as additive to natural gas.    ADVANTAGE - The electrolyzer can be operated frequently, quickly or at widely variable rates easily. The electricity consumption by the electrolyzer can be reduced, and the electrolyzer can be operated at the specified rate of power consumption easily.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) a method of marketing a virtual sale of hydrogen; and    (2) an electrolyzer.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the energy system.    Electrolyzer (12)    Natural gas pipeline (34)    Gas consumer (40)    Output valve (56)    Consumer gas meter (64)
NOVELTY - The method involves performing rubbish particles crushing, drying, extruding and preparing operations in a pyrolysis and gasification furnace. The rubbish particles are formed by solid organic matters. Gas is entered into a heat-pipe heat exchanger. Desulphurization coal gas and tar acid are removed by a draft fan. Acidic gas mist is removed in a tower by the fan. Coal gas is entered into deodorizing tower for removing toxic and harmful gas. Clean gas is generated by an engine under fan pushing condition. The furnace is fixed with a continuous batch feeding double-roller feeding device.    USE - Town domestic rubbish pyrolysis gas purifying and generating method.    ADVANTAGE - The method enables effectively realizing rubbish pyrolysis gas purifying and generating process and energy recycling process.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating a town domestic rubbish pyrolysis gas purifying and generating method.'(Drawing includes non-English language text)'
NOVELTY - The apparatus has air pipe (31) and exhaust pipe (33) that are extended upwards from a shaft inside a drum (1). A hot air generation machine is installed in an outer side of drum, and is connected with one end of pipe which introduces the air. An insertion opening door is formed in a surrounding wall of the drum. A processed material discharge port door (16) is formed in side-plate of drum. An automatic operation control circuit performs rotation control and temperature and humidity control of the drum. An outer plate covers the surroundings of a frame (41).    USE - Garbage processing apparatus for reducing quantity of organic refuse in dining room, kitchen and foodstuff sales counter.    ADVANTAGE - The organic refuse can be efficiently decomposed, and the processing time of the organic refuse can be shortened. The structure can be simplified, manufacturing cost can be reduced and the maintenance of the garbage processing apparatus can be made easy. Since the rotating drum fully stirs the refuse, the aerobic fermentation is stimulated, such that the occurrence of the offensive odor can be effectively suppressed.    DESCRIPTION OF DRAWING(S) - The drawing shows the sectional views of the rotating drum.    Drum (1)    Processed material discharge port door (16)    Air pipe (31)    Exhaust pipe (33)    Frame (41)
NOVELTY - Cooking fuel composition comprises: either dimethyl ether, and one or more 2-6C alcohols; or dimethyl ether, and one or more 2-10C hydrocarbons; or wax, and one or more 3-6C alcohols.    USE - The cooking fuel composition is useful in cylinders for residential use such as cooking and heating and as portable cylinder fuels for camping and hiking.    ADVANTAGE - The cooking fuel composition is derived from renewable resources such as biomass in an economical and environmental friendly manner.
NOVELTY - The system has solar energy mirror (2) that collects solar energy. A solar energy mirror bracket (4) is provided for supporting solar mirror. The solar mirror bracket is provided with a tracking control device (5). The tracking control device is provided to control the solar energy mirror to focus the sunshine to the solar photo-thermal converter of biomass gasification device (1). The solar energy photo-thermal converter is connected with the solar energy mirror.    USE - Fixed point array solar biomass gasification system.    ADVANTAGE - The utilization of solar energy can be improved.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the fixed point array solar biomass gasification system.    Biomass gasification device (1)    Solar energy mirror (2)    Solar energy mirror bracket (4)    Tracking control device (5)    Connecting unit (16)
NOVELTY - The apparatus (2) has a receptacle (4) that defines a flaming pyrolysis zone (34) in which first carbonaceous material is heated to generate volatile gas and second carbonaceous material. A char gasification zone (42) is defined in which second carbonaceous material is combusted to generate volatile gas and char. The air pipes (30,54) are provided to introduce air into zones. An agitator is provided for agitating carbonaceous material in flaming pyrolysis zone. Another agitator (46) mechanically reduces the size of char particles formed in char gasification zone.    USE - Gas production apparatus for producing flammable gases from e.g. carbonaceous combustible wastes, biomasses, combustible domestic and industrial wastes.    ADVANTAGE - The formation of fuel bridges can be reduced since an agitator is provided for agitating carbonaceous material in flaming pyrolysis zone. Hence, the construction of gas producing apparatus can be simplified and cost of apparatus can be reduced. The material blockage in the receptacle can be reduced since agitator mechanically reduces the size of char particles formed in char gasification zone. Hence, the apparatus can be operated continuously for longer periods and can reduce the tar content of the resulting gas. The efficiency and reliability of the apparatus can be improved since receptacle is arranged such that carbonaceous materials and char move under gravity.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing gas.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of a gas producing apparatus.    Gas producing apparatus (2)    Receptacle (4)    Air pipes (30,54)    Flaming pyrolysis zone (34)    Char gasification zone (42)    Agitator (46)
NOVELTY - Meta-dichlorobenzene and solid acid catalyst are added in a reaction kettle and stirred. Butyryl chloride is added and the temperature of reaction kettle is reduced to 90 degrees C. The reaction solution is hydrolyzed, washed and separated to obtain aqueous layer and organic layer. The aqueous layer is removed and the organic layer is transferred to a distillation kettle. The temperature in reaction kettle is raised, the organic layer is subjected to negative pressure rectification process, and decompressed to obtain 2,4-dichlorobutyrophenone.    USE - Manufacture of 2,4-dichlorobutyrophenone (claimed).    ADVANTAGE - The manufacture of 2,4-dichlorobutyrophenone is simple, and the catalyst can be used repeatedly.    DETAILED DESCRIPTION - Meta-dichlorobenzene and solid acid catalyst are added in a reaction kettle and stirred. The reaction kettle jacket is opened, butyl chloride is added slowly for 2-3 hours, addition temperature is controlled to 30-40 degrees C. Butyryl chloride is added and the temperature of reaction kettle is raised to 110-115 degrees C, the reaction mixture is maintained for 1 hour, then the temperature of reaction kettle is reduced to 90 degrees C. The reaction solution is hydrolyzed, washed and separated to obtain aqueous layer and organic layer. The aqueous layer is removed and the organic layer is transferred to a distillation kettle. The temperature in reaction kettle is raised, the organic layer is subjected to negative pressure rectification process until there is no discharge, decompressed, and the reflux ratio is controlled to obtain 2,4-dichlorobutyrophenone.
NOVELTY - The system (100) has multiple screw conveyors (140) that are arranged circumferentially around a gasifier shell (104) of a fluidized bed gasifier (102). The screw conveyors are in feed communication with a gasifier chamber (106) defined by the gasifier shell. The hoppers (126) are coupled the screw conveyors. Each hopper (126) is provided with a hopper shell that defines a hopper chamber in feed communication with the respective screw conveyor. The hoppers (116) are provided with hopper shell that defines hopper chamber (119) in feed communication with hoppers (126).    USE - System for feeding biomass material feed such as forest residues, agricultural residues, nuts, nut shells, almond shells, wood chips, pine, eucalyptus, oak, poplar, olive, grape mash and rice husks into fluidized bed gasifier.    ADVANTAGE - The pressure and temperature in a section of the gasifier chamber proximate to a screw conveyor, is similar to the temperature and pressure of a section including a screw conveyor since screw conveyors are equidistantly spaced circumferentially around the fluidized bed gasifier and biomass material feed is fed through each screw conveyor at equal flow rate. Hence, efficiency of the conversion of the biomass material feed to syngas can be increased.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a method for producing a synthesis gas from a biomass material feed in a fluidized bed gasifier.    DESCRIPTION OF DRAWING(S) - The drawing shows a top view of a biomass feed system.    Biomass feed system (100)    Fluidized bed gasifier (102)    Gasifier shell (104)    Gasifier chamber (106)    Hoppers (116,126)    Hopper chambers (119)    Screw conveyors (140)
NOVELTY - The method involves generating a hydrogen-containing-gas using the raw material of nitrogen gas and a nitrogen-containing compound with a modifier. The carbon monoxide (CO) in the hydrogen-containing-gas is reduced by oxidation reaction by CO removal device. The raw material feed rate to the modifier is increased (S1). The oxidant gas feed rate is increased (S2) so that the ratio of oxidant gas feed rate to CO removal device with respect to raw material feed rate to modifier is higher than the ratio in before increase in oxidant gas feed rate.    USE - Operating method of hydrogen generating apparatus.    ADVANTAGE - Since the ammonia discharge amount from hydrogen generating apparatus is controlled, the decline in the hydrogen generation efficiency can be suppressed.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for operating method of fuel cell system.    DESCRIPTION OF DRAWING(S) - The drawing shows a flowchart illustrating the operating method of hydrogen generating apparatus.(Drawing includes non-English language text)    Step for increasing raw material feed rate to modifier (S1)    Step for increasing oxidant gas feed rate (S2)
NOVELTY - The method involves detecting contamination values of hydrogen by a contamination sensor (15). The detected values are evaluated by a control device (16) that controls volumetric flow flowing to a hydrogen reservoir (7). Impurity concentration of substances in the hydrogen is reported to the control device. An acoustic and/or optical warning signal is not output by the control device during the impurity concentration is below a threshold value. The acoustic and/or optical warning signal is output by the control device when the impurity concentration is above the threshold value.    USE - Method for refueling a hydrogen reservoir with buffered hydrogen to operate a fuel cell for generating electrical driving power in a vehicle i.e. motor car.    ADVANTAGE - The acoustic and/or optical warning signal is output by the control device when the impurity concentration is above the threshold value, thus refueling the hydrogen reservoir with buffered hydrogen with high purity in a simple, reliable and cost-effective manner without the risk of damage to the fuel cell, and protecting a fuel cell system of the vehicles before refueling by the polluted hydrogen without the risk of malfunction in the fuel cell system.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a device for carrying out a method for refueling a hydrogen reservoir with buffered hydrogen to operate a fuel cell.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of a vehicle with a fuel cell system of a device for carrying out a method for refueling a hydrogen reservoir with buffered hydrogen to operate a fuel cell.    Fuel cell (3)    Anode chamber (5)    Hydrogen reservoir (7)    Contamination sensor (15)    Control device (16)
NOVELTY - An electric vehicle reformer has a reformer inlet, an outlet, a pre-catalyst and post-catalyst. The pre-catalyst and post-catalyst are located in the rear of the inlet, and between outlet of pre-catalyst is adjacent to the inlet. Pre-catalyst in the fuel is smaller than the width in the forward direction of the forward post-catalyst in the fuel the width direction.    USE - Electric vehicle reformer (claimed).    ADVANTAGE - The electric vehicle reformer has excellent combustion efficiency, and is capable of inhibiting oxidation reaction on the front section.
NOVELTY - Separating carbon dioxide (CO2) and methane (CH4) with high adsorption selectivity of Ramulus mori based active carbon preparation involves using wooden particles by hard material fruit shell or coal as the raw material at 450-600 degrees C, under the protection of inert gas, placing carbide and carbide material in the gasification furnace, introducing 10-80 wt.% of hydrazine hydrate water solution, decomposing a activation treatment for 1-3 hours at 700-900 degrees C, then cooling to room temperature under the protection of inert gas, boiling with water, washing and drying.    USE - For separating carbon dioxide (CO2) and methane (CH4) with high adsorption selectivity of Ramulus mori based active carbon preparation (claimed).    ADVANTAGE - The method has high adsorption performance; has high CO2/CH4 selectivity; and reaches more than 2.8 mmol/g to CO2 adsorption capacity at 25-100 degrees C under the normal temperature and normal pressure.
NOVELTY - Alcohol-based fuel combustion improver comprises 4.9-93 pts. wt.% solvent, 4.9-93 pts. wt.% bio-oil, 0.1-0.3 pts. wt.% smoke combustion supporting agent, and 1-3 pts. wt.% latent solvent.    USE - As alcohol-based fuel combustion improver (claimed).    ADVANTAGE - The alcohol-based fuel combustion improver is environment-friendly alcohol-based fuel of high heat value is 6000-10000/g, and it has good combustion performance, and alcohol-based fuel flash point, low volatility, which eliminates the potential safety hazard in the existing technology, is safe and environment-friendly, capable of regenerative, clean and sanitary, convenient use, and low cost.
NOVELTY - Fuel oil comprises active elemental metal material is iron, aluminum, magnesium, zinc, at least one of nanoparticles, for solubilizing surfactant, oil, the mass fraction of nanoparticles and the surface active agent ratio of 0.5-1, where the nano-particles and Micro surfactant were added to the fuel, where the fuel containing 50-150 mg nanoparticles.    USE - As fuel oil e.g. petroleum diesel oil, or gasoline used in diesel engine used to replace fuel such as diesel oil, biological ethanol diesel oil and emulsified fuel oil.    ADVANTAGE - The fuel oil is high efficient nano-fuel oil, promotes combustion to reduce the discharge at the same time, and it reduces cost.
NOVELTY - An organic fuel product, contains: raw organic material including straw that is ground, cleaned to remove seeds, hammered and heated to a temperature of at least 110 degrees F to form a processed material; and manure mixed with the processed material, the mixture of the processed material and manure being ground and dried to an amount that is less than ten percent of the original moisture content of the straw; where the dried mixture is compacted and compressed into a predetermined shape fuel product by a hydraulic press.    USE - The organic fuel product is useful as a source of energy.    ADVANTAGE - The organic fuel product is ecologically friendly, safe and reliable.
NOVELTY - A waste tatami mat refuse paper and plastic fuel comprises tatami mat and stylo tatami mat chosen from waste tatami mats containing combustible vegetable fiber, and waste plastic, as main raw materials.    USE - Waste tatami mat refuse paper and plastic fuel is used in thermal recycle system, industrial waste treatment and electronic manifest management.    ADVANTAGE - The waste tatami mat refuse paper and plastic fuel has excellent quality and shape stability. The thermal recycle system obtained using waste tatami mat refuse paper and plastic fuel has high efficiency and handleability, and is economical and does not contain impurities.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for manufacture of waste tatami-mat refuse paper, which involves fractionating and selecting tatami mat and stylo tatami mat by visual observation from waste tatami mats discharged from living environment plant, injecting waste tatami mat to crusher, reducing volume by performing industrial waste treatment, melting, solidifying by fractionation and selection, separating industrial waste, and mixing crushed waste plastics.
NOVELTY - Preparation of Irbesartan (I) involves: reacting cyano Irbesartan (II) with sodium azide using 1,8-diazabicyclo(5.4.0)undec-7-ene (DBU) and triethylamine hydrochloride in an organic solvent at 120-140 degrees C for 15-40 hours and isolating the compound (I) from the resulting reaction mixture; and optionally purifying the compound (I) in a polar solvent to yield the pure Irbesartan.    USE - For preparation of Irbesartan (claimed), useful in the treatment of hypertension and complications of heart failure.    ADVANTAGE - The process is an improved process which results with 98% conversion of cyano Irbesartan to Irbesartan with good yield and purity of greater than or equal to 99%. The process involves use of readily available raw materials and reagents; and avoids the use of toxic reagents such as trialkyltin azide and sodium nitrite thereby rendering the process environment friendly. The process does not involve any chromatographic purification for final product i.e. Irbesartan thereby avoiding any loss resulting in the final product in higher yield.
NOVELTY - Method for preparing a plant extract having tyrosinase inhibitor activity, involves drying leaves of Greyia radlkoferi, pulverizing the dried leaves, mixing the pulverized leaves with a solvent to allow phenolic compounds to leach into the solvent, and removing the pulverized leaves from the solvent, such that the plant extract remains in the solvent.    USE - The method is useful for preparing plant extract which is used for treating skin hyper-pigmentation. The extract is in the form of creams, lotions, aqueous solutions, balms, sunscreens, skin-oils or ointments (all claimed).    ADVANTAGE - The method reduces side effects, environmentally-friendly and cost-effective.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for plant extract, which comprises 5,7-dihidroxyflavone((2S)-pinocembrin), 2/6'-dihydroxy-4'-methoxydihydrochalcone, 2',4',6'-trihydroxyhydrochalcone, 3,5,7- trihydroxyflavone and 4',5'7-trihydroxyisoflavone.
NOVELTY - Process (P1) for separating a first reaction zone effluent, comprises: (a) separating the first reaction zone effluent in a first vapor liquid separator into a vapor stream and a liquid stream; (b) dividing the liquid stream into a recycle portion and a product portion; (c) stripping the product portion of the liquid stream in a stripping column (8) with a stripping gas into an overhead vapor stream (14) and a bottoms stream (12); (d) introducing the bottoms stream into a second reaction zone; and (e) recycling the recycle portion of the liquid stream to the first reaction zone.    USE - The process is useful for separating a first reaction zone effluent, which is useful for producing biofuel from renewable feedstocks (all claimed), where the biofuel includes green diesel from natural oils and fats.    ADVANTAGE - The process eliminates undesirable entrainment while allowing for enhanced stripping of the net liquid only.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a process (P2) for producing biofuel from renewable feedstocks, comprising: deoxygenating the renewable feedstocks in a deoxygenation reaction zone (4), and separating the deoxygenation reaction zone effluent in a first vapor-liquid separator into vapor stream and a liquid stream; steps (b) and (c) as above per se; isomerizing the bottoms stream of the stripping column in an isomerization reaction zone (22); recycling the recycle portion of the liquid stream to the deoxygenation reaction zone; and fractionating at least a portion of an effluent of the isomerization reaction zone to form at least one biofuel product stream.    DESCRIPTION OF DRAWING(S) - The figure illustrates a hydroprocessing process including an enhanced hot separator.    Deoxygenation reaction zone (4)    Stripping column (8)    Bottoms stream (12)    Overhead vapor stream (14)    Isomerization reaction zone (22)
NOVELTY - Processing of crude tall oil involves introducing crude tall oil into a flash zone (30) of a stripping column (25) to separate the crude tall oil into a liquid and a vapor, stripping the liquid in a stripping zone below the flash zone to form heavy pitch bottom stream (50) and overhead vapor stream (35), and introducing the overhead vapor stream from the stripping column into a secondary column between a stripping zone and a rectification zone, such that the overhead vapor stream is separated from the stripping column into a light pitch bottom stream (65) and a distillate stream.    USE - Processing of crude tall oil used for manufacturing biofuel.    ADVANTAGE - The crude tall oil is efficiently processed. The impurities contained in the crude tall oil are removed.    DETAILED DESCRIPTION - Processing of crude tall oil involves introducing crude tall oil into a flash zone of a stripping column to separate the crude tall oil into a liquid and a vapor, in which the stripping column is under vacuum, stripping the liquid in a stripping zone of the stripping column below the flash zone to form heavy pitch bottom stream and overhead vapor stream, in which the overhead vapor stream comprises free fatty acids, rosin acids, heads, and light pitch, and introducing the overhead vapor stream from the stripping column into a secondary column between a stripping zone and a rectification zone, where the secondary column is under vacuum, such that the overhead vapor stream is separated from the stripping column into a light pitch bottom stream and a distillate stream, where the distillate stream consists of free fatty acids, rosin acids, and heads.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining the processing method of tall oil.    Stripping column (25)    Flash zone (30)    Overhead vapor stream (35)    Heavy pitch bottom stream (50)    Light pitch bottom stream (65)
NOVELTY - Transport method of carbon dioxide involves blowing liquefied natural gas in a container containing gaseous-phase portion which includes cryogenic liquid consisting of liquefied methane, liquefied ethane, liquid nitrogen and liquid argon, and liquefaction carbon dioxide or gaseous carbon dioxide, or cryogenic liquid consisting of liquefied natural gas, liquefied methane, liquefied ethane, liquid nitrogen or liquid argon, and natural gas, methane, ethane, nitrogen and/or argon, storing the mixture in a container, and conveying container to the destination.    USE - Transport method of carbon dioxide (claimed).    ADVANTAGE - The method efficiently transfers and stores carbon dioxides.    DETAILED DESCRIPTION - Transport method of carbon dioxide involves blowing liquefied natural gas in a container containing gaseous-phase portion which includes cryogenic liquid consisting of liquefied methane, liquefied ethane, liquid nitrogen and liquid argon, and liquefaction carbon dioxide or gaseous carbon dioxide, or cryogenic liquid consisting of liquefied natural gas, liquefied methane, liquefied ethane, liquid nitrogen or liquid argon, and natural gas, methane, ethane, nitrogen and/or argon, storing the mixture in a container to which a solid carbon dioxide exists in the cryogenic liquid, and conveying container to the destination. In the destination, the mixture is unloaded from container and simultaneously separates carbon dioxide from mixture. An INDEPENDENT CLAIM is included for disposal method of carbon dioxide, which involves sending out the conveyed carbon dioxide from the system, and disposing by depth underground embedding.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view explaining transport method of carbon dioxide.    Pipe (1,5,9,10,12,13,15,17,18,19,20,21,23)    Condenser (2)    Low temperature container (3)    Pump (4,14)    Low-temperature tank (6)
NOVELTY - Wooden oil is obtained by spraying superheated steam on timber (1) and separating wooden oil from the timber extract.    USE - Wooden oil is used to prepare asphalt compound material used in road pavement method (all claimed).    ADVANTAGE - The wooden oil has excellent deodorizing effect, aromaticity, antibacterial effect, insect repellence, weed-proofing property, and contributes to environmental conservation.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) manufacture of wooden oil;    (2) asphalt compound material;    (3) manufacture of asphalt compound material, which involves mixing wooden oil and asphalt; and    (4) pavement method, which involves laying asphalt compound material on road.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of manufacturing equipment of wooden oil.    Timber (1)    Heat processing apparatus (101)    Superheated steam generator (102)    Steam collection pipe (103)    Scrubber (104)
NOVELTY - Extracting oil from a solute-bearing material containing animal material and/or vegetable material, comprises: feeding particles of the solute-bearing material to an extraction chamber; injecting globules of an extraction solvent containing 1-5C hydrocarbon into the extraction chamber to contact the particles of the solute-bearing material and extract at least a portion of the oil from the solute-bearing material; collecting a mixture of the extracted solute and solvent from the extraction chamber; and separating the solute from the solvent by vaporization.    USE - The process is useful for extracting oil from a solute-bearing material containing animal material, vegetable material (claimed), or mineral materials, including marine and waste materials, where the extracted oil is useful as a fuel or a lubricant.    ADVANTAGE - The process allows for extraction of high percentage of solute, with a very low amount of solvent remaining in the solute-bearing material.    DETAILED DESCRIPTION - Extracting oil from a solute-bearing material containing animal material and/or vegetable material, comprises: feeding particles of the solute-bearing material to an extraction chamber, where a majority of the particles fed to the extraction chamber pass through a 16 mesh sieve, but are retained by a 40 mesh sieve; injecting globules of an extraction solvent containing 1-5C hydrocarbon into the extraction chamber to contact the particles of the solute-bearing material and extract at least a portion of the oil from the solute- bearing material, where the solvent is injected into the extraction chamber at an average globule size of 400-1200 mu ; collecting a mixture of the extracted solute and solvent from the extraction chamber; and separating the solute from the solvent by vaporization.
NOVELTY - The apparatus (1000c) has a pellet mill (500) in which small engine is arranged. The exhaust gas is generated from power generator (100) passes through drying furnaces (400a,400b) to dry the biomass. The power generator drives pulverizing device (300), drying furnaces, and pellet mill. The drying furnaces are installed at one side of inner portion of compartment (200) and exhaust gas is ejected to outside. The compartment in which power generator is arranged inner portion and which is installed outside sealed compartment.    USE - Pellet manufacture apparatus used in vehicle.    ADVANTAGE - The biomass is dried by using the exhaust gas generated from the small-size engine and the apparatus can be constructed in a compact manner to improve the thermal efficiency. The exhaust gas generated from the power generator passes through drying furnaces to dry the biomass so that the drying efficiency is improved. The cooling efficiency of the power generator can be enhanced and the heat obtaining from the cooling apparatus is indirectly used for the drying of the biomass.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the apparatus. (Drawing includes non-English language text)    Power generator (100)    Compartment (200)    Pulverizing device (300)    Drying furnaces (400a,400b)    Pellet mill (500)    Pellet manufacture apparatus (1000c)
NOVELTY - The carbonizing machine (1) has a supply unit (10) that is provided to feed the biomass material. A blower section (40) is blown to a half carbonization space (22). A heating portion (30) is arranged in adjacent to the lower portion of a heater, and is provided in the lower region of porosity screen (25). An inlet port (22c) and a vent (22a) are formed in the half carbonization space. The porosity screen is provided in the lower portion of half carbonization space. A half ash process unit (20) is provided for stirring the biomass material supplied to half carbonization space.    USE - Biomass half carbonizing machine.    ADVANTAGE - The continuous input of the biomass material can be ensured effectively, by providing the biomass half carbonizing machine. The heat treatment efficiency and safety of the biomass can be improved. The dust generation of biomass can be minimized.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the biomass half carbonizing machine.    Biomass half carbonizing machine (1)    Supply unit (10)    Half ash process unit (20)    Half carbonization space (22)    Vent (22a)    Inlet port (22c)    Porosity screen (25)    Heating portion (30)    Blower section (40)
NOVELTY - The system comprises artificial wetlands aeration reactor bed provided with a water distribution matrix layer. The water distribution matrix layer is adhered with a water distributor that is connected with a sewage inlet pipe. A planting wetland plant is constructed in a wetland aeration reactor bed. A bottom of the wetland aeration reactor bed is provided with an aeration head, a gas distribution chamber and an artificial wetlands collector pipe. The gas distribution chamber provides low concentrations of methane gas through an intake pipe that is connected to the water collector pipe.    USE - The methane gas oxidation system is useful in poultry waste water treatment (claimed).    ADVANTAGE - The system meets the ecological oxygen requirement, greenhouse effect waste water, high working efficiency and low energy consumption.    DETAILED DESCRIPTION - The system comprises artificial wetlands aeration reactor bed provided with a water distribution matrix layer. The water distribution matrix layer is adhered with a water distributor that is connected with a sewage inlet pipe. A planting wetland plant is constructed in a wetland aeration reactor bed. A bottom of the wetland aeration reactor bed is provided with a uniform aeration head, a gas distribution chamber and an artificial wetlands collector pipe. The gas distribution chamber provides low concentrations of methane gas through an intake pipe that is connected to the water collector pipe. The water collector pipe is connected with a water outlet pipe of a water seal device. The water distribution matrix layer has smaller sand-like particle size. A gas distribution chamber inlet intakes the air in upward direction to the wetland. An artificial wetland spout is arranged in a sealing device.
NOVELTY - Preparation of benzbromarone (I) involves: acetylation of 3,5-dibromo-4-hydroxy-benzoic acid (II), using acetylation reagent as acetic anhydride or acetyl chloride to obtain 4-acetoxy-3,5-dibromo-benzoic acid (III) which is reacting with thionyl chloride to obtain acetic acid 2,6-dibromo-4-chlorocarbonyl-phenyl ester (IV); reacting the compound (IV) and 2-ethyl-benzofuran (V) using Friedel-Crafts reaction to obtain acetic acid 2,6-dibromo-4-(2-ethyl-benzofuran-3-carbonyl)-phenyl ester (VI); and deacetylation of the compound (VI) by hydrolysis reaction to obtain benzbromarone (I).    USE - For preparing benzbromarone (claimed) for treating gout.    ADVANTAGE - The method provides simple and safe operation, convenient post-treatment, with high product purity, low economic cost, little pollution to the environment, and is easy to realize industrialization.    DETAILED DESCRIPTION - Preparation of benzbromarone (I) involves: acetylation of 3,5-dibromo-4-hydroxy-benzoic acid (II), using acetylation reagent as acetic anhydride or acetyl chloride to obtain 4-acetoxy-3,5-dibromo-benzoic acid (III) which is reacting with thionyl chloride to obtain acetic acid 2,6-dibromo-4-chlorocar bonyl-phenyl ester (IV); reacting the compound (IV) and 2-ethyl-benzofuran (V) using Friedel-Crafts reaction using catalyst (c1) and solvent (s1) to obtain acetic acid 2,6-dibromo-4-(2-ethyl- benzofuran-3-carbonyl)-phenyl ester (VI) at 5 degrees C; and deacetylation of the compound (VI) by hydrolysis reaction using catalyst (c2) and solvent (s2) at 40-45 degrees C to obtain benzbromarone (I).
NOVELTY - A biological oil stability improving method involves preparing bio-oil raw materials by adding pine sawdust particle, and screening the particle. The screened particle is dried for 24 hours at 105 degrees C. Fluidizing gas is introduced in a rapid thermal cracking device for controlling the cracking reaction at 500 degrees C. The prepared material is added with acetic acid methyl acetate for obtaining bio-oil and improving stability of biological oil after injection molding. The obtained product is stored in a sealed container, where the fluidized gas is nitrogen.    USE - Method for improving stability of biological oil.    ADVANTAGE - The method enables improving stability of biological oil in simple, convenient and cost-effective manner.
NOVELTY - The device has a recycling device (1) provided with a receiving end (11) and an output end (12). A reaction device (2) is provided with multiple reaction kettles (21). A methanol steam pipe (212) is connected with the receiving end. The reaction kettle is provided with a raw material feeding pipe (213), a feeding pump (214) and a methanol conveying pipe (215). One end of the feeding pump is connected with the reaction kettle and another end of the pump is connected with the raw material feeding pipe. The methanol conveying pipe is connected with the output end by a liquid methanol pipe (216).    USE - Methanol recovering device for producing bio-diesel oil.    ADVANTAGE - The device has simple structure, low production cost, improved yield and utilization rate.    DESCRIPTION OF DRAWING(S) - The drawing shows a block diagram of a methanol recovering device.    Recycling device (1)    Reaction device (2)    Receiving end (11)    Output end (12)    Reaction kettle (21)    Methanol steam pipe (212)    Raw material feeding pipe (213)    Feeding pump (214)    Methanol conveying pipe (215)    Liquid methanol pipe (216)
NOVELTY - The reactor has an anaerobic reaction tank main portion (24) that includes clean liquid collecting and backflush subsystem (27), biogas storage cabin (28) and electric control system. Multiple pipeline valves, cables and wires are connected with one other. The raw liquid is purified by a suspended anaerobic granular sludge bed, and is anaerobically and biologically purified and filtered through an inner recycle filter three-phase separator.    USE - Multifunctional internal recycle anaerobic biogas generation reactor.    ADVANTAGE - The inner recycle residual sludge selector in the reaction tank can discharge residual sludge with low activity in time, so that chemical oxygen demand (COD) and suspended solids can be efficiently removed. The ammonia and nitrogen can be removed effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the multifunctional internal recycle anaerobic biogas generation reactor.    Anaerobic reaction tank main portion (24)    Clean liquid collecting and backflush subsystem (27)    Biogas storage cabin (28)    Sludge pump (56)    Clear liquid output pump (75)
NOVELTY - This utility model claims a kind of biological diesel oil production to quick esterifying device with no stirring section, comprising a reaction kettle, a recycle device, evaporator, the lower end of the reaction kettle through the first gas inlet pipe and the upper part of the evaporator is connected with the air outlet, the upper end of the reaction kettle is connected with a feeding port of the second pipeline and the recycling device. This utility model does not need to stir when the esterification reaction, methyl per ton can save about 9.25kW power, realizing the single kettle reaction, esterification speed is fast, the production efficiency is high, it can save energy.
NOVELTY - The fuel-based waste contains palm kernel shells derived from an oil palm pericarp to produce oil, where fuel contains 80.00 to 99.98 wt.% solid waste that is derived from oil palm pericarp to produce oil, 0.01 to 19.99 wt.% combustible ingredients or additives based on plants or plant products, and 0.01 to 1.00 wt.% combustible ingredients or additives, and 7 wt.% particles that are passed through a sieve mesh whose size is specified as 4.5 mm.    USE - Fuel-based waste.
NOVELTY - The electrolysis device (100) has a main structure (110), a top cover (150) which covers an upper portion of the main structure, and a bottom cover (160) which covers a lower portion of the main structure. An inner portion of the main structure is filled with raw water, when raw water is supplied through a source water supply hole (116) within the main structure. Gas generated by electrolyzing the raw water, is ejected through a gas exhaust port (117). Multiple electrolysis plates (120) are separated between an inner plate (111) and a lateral lamina (112) of main structure.    USE - Electrolysis device for electrolyzing raw water such as tap water, river water and subsurface water, and generating gas e.g. hydrogen. Can also be used in generating oxygen.    ADVANTAGE - The gas generated due to the temperature rise in the electrolysis device can be prevented from destroying due fire. The generated heat can be effectively cooled with the air circulation through the opening on the center of the main structure. The structure of the electrolysis device can be simple and the manufacturing cost of the electrolysis device can be reduced.    DESCRIPTION OF DRAWING(S) - The drawing shows a cross-sectional view of the electrolysis device.    Electrolysis device (100)    Main structure (110)    Inner plate (111)    Lateral lamina (112)    Source water supply hole (116)    Gas exhaust port (117)    Electrolysis plate (120)    Top cover (150)    Bottom cover (160)
NOVELTY - Extracting unsaturated fatty acid and aviation fuel from oil-containing microalgae comprises (i) preparing micro-algal powder, adding cosolvent, using supercritical carbon dioxide extraction to extract unsaturated fatty acid in process of cultivating microalgae powder particle to obtain mixed oil and algae, (ii) separating and enriching mixed oil to obtain unsaturated fatty acid and residual oil, and (iii) thermal cracking algal residue to obtain pyrolysis bio-oil, mixing it with residual oil, carrying out hydrogenation treatment to obtain coal oil used as aviation fuel and byproduct gasoline.    USE - The method is useful for extracting unsaturated fatty acid and aviation fuel from oil-containing microalgae (claimed).    ADVANTAGE - The method can achieve unsaturated fatty acid extraction rate of 80-95%, total oil extraction rate of 70-90%. The coal oil component can achieve aviation coal oil standards.    DETAILED DESCRIPTION - Extracting unsaturated fatty acid and aviation fuel from oil-containing microalgae, comprises (i) crushing and breaking the microalgae to prepare micro-algal powder and adding cosolvent, using supercritical carbon dioxide extraction technology to extract the unsaturated fatty acid in process of cultivating microalgae powder particle to obtain mixed oil and algae, (ii) separating and enriching the obtained mixed oil in step (i) to obtain unsaturated fatty acid and residual oil, and (iii) carrying out thermal cracking of algal residue to obtain pyrolysis bio-oil, mixing the obtained pyrolysis bio-oil with the resulting residual oil, carrying out hydrogenation treatment to obtain coal oil as main product and byproduct of gasoline and diesel oil, where the coal oil as the main product can be used as aviation fuel. An INDEPENDENT CLAIM is also included for coal oil used as the aviation fuel prepared according to the above mentioned method.
NOVELTY - Invention relates to the field of biotechnology, particularly, to a method of disposing the cellulose-containing wastes. The method of disposing the cellulose-containing wastes by using vermiculture with earthworms Eisenia fetida and culture of fungi Trichoderma viride comprises a preliminary oral inoculation of earthworm Eisenia fetida with using an insulin syringe with a sawed-off point of the needle with the suspension of mycelium and spores of a cellulose-digesting strain of week-old culture of fungi Trichoderma viride with the content in it of colony-forming units in the amount of 103 CFU/ml in amount of 0.05 ml, or daily exposure of the worms in the substrate saturated with such suspension.    USE - Agriculture.    ADVANTAGE - Invention enables to intensify the disposing of cellulose-containing wastes by producing a population of earthworms having increased cellulasic activity.1 tbl
NOVELTY - A large particle humic acid-potassium chloride fertilizer production method involves mixing sodium hydroxide solution with a humic acid raw ore in a ratio of 1: 0.25-1.5 at 10-100 degrees C, and allowing the mixture to react for 5-15 minutes to activate the humic acid raw ore. Activated slurry is dispersed and sprayed at 20-100 degrees C to a mixture of potassium chloride and the humic acid raw ore for granulating by a rotary drum followed by drying, cooling, screening and packaging.    USE - Method for producing large particle humic acid-potassium chloride fertilizer.    ADVANTAGE - The method enables producing large particle humic acid-potassium chloride fertilizer with low corrosivity, high production capacity, strong strength, friendly operating environment, improved soil and enhanced fertilizer effect and large-scale and industrialized production.    DETAILED DESCRIPTION - A large particle humic acid-potassium chloride fertilizer production method involves mixing a sodium hydroxide solution with a humic acid raw ore according in a ratio of 1: 0.25-1.5 at 10-100 degrees C, and allowing the mixture to react for 5-15 minutes to activate the humic acid raw ore. Activated slurry is dispersed and sprayed at 20-100 degrees C to a mixture of potassium chloride and the humic acid raw ore for granulating by a rotary drum followed by drying, cooling, screening and packaging, where the inlet temperature of the drum is 200-300 degrees C and outlet temperature is 50-100 degrees C, and the ratio of the mixture of potassium chloride and the humic acid raw ore is 2-10: 0-1.
NOVELTY - A Stropharia rugosoannulata cultivating method involves selecting planting field, and processing with dry straw and land plaster, before material throwing and sowing, stirring the land plaster evenly. Material throwing and sowing are conducted, the land plaster is stirred by the moderate amount of the fine soil and the sowing is conducted, and when earth covering and water immersion are conducted, thickness of the covered earth is 4-6cm, a layer of thick straw of 3-5cm covers the covered earth, and water is drained after the water immersion is conducted.    USE - Method for cultivating Stropharia rugosoannulata.    ADVANTAGE - The method enables cultivating Stropharia rugosoannulata with high and stable yields, in time-saving and labor-saving, and simple manner.    DETAILED DESCRIPTION - A Stropharia rugosoannulata cultivating method involves selecting planting field, and processing with 8000-10000 kg dry straw and 10-15 kg land plaster, before material throwing and sowing, stirring the land plaster evenly through a moderate amount of fine soil or chaff to be standby. A full-dry straw is utilized as a single raw material, and the straw is dried in the sun and standby before the material throwing and sowing are conducted. Material throwing and sowing are conducted by regularly paving straw to be rectangular pieces of land in a paddy field, width of the rectangular pieces of 40-50cm, and thickness of rectangular pieces of 15-35 cm, when the land plaster is utilized as auxiliary materials, the land plaster is stirred by the moderate amount of the fine soil and the chaff is evenly scattered on the straw and then the sowing is conducted, and when earth covering and water immersion are conducted, the thickness of the covered earth is 4-6cm, a layer of thick straw of 3-5cm covers the covered earth, and water is drained after the water immersion is conducted.
NOVELTY - This utility model claims a kind of marsh gas, mushroom integrally vegetable planting shed, comprising a planting greenhouse and marsh gas pool, further comprising a mushroom planting shed, liquid tank and a solid-liquid separating device, a mushroom planting shed planting greenhouse is set on the back and one side of the marsh gas tank is provided with planting greenhouse, marsh gas tank and the solid-liquid separating device is connected with the feeding port, liquid tank and the liquid outlet of the solid-liquid separating device is connected with the biogas pool is respectively connected with the liquid outlet of a planting greenhouse irrigation system is connected with the air outlet of a planting greenhouse and mushroom planting of the marsh gas tank to marsh gas lighting device, marsh gas heating device of greenhouse; The utility model is provided with a mushroom planting shed on the back and a planting greenhouse, at the same time, in the marsh gas tank is set on the mushroom planting shed, under the condition of not influencing the planting greenhouse lighting, which can ensure the working temperature of the marsh gas tank, at the same time, the marsh gas tank to generate the biogas can be used, increasing the economic benefit and environmental benefit.
NOVELTY - The device comprises a raw water tank, a storage basin, a fermentation and denitrification reactor, a drainage pond, an air compressor and a mud tank. The denitrification reactor is provided with a dissolved oxygen detector, a water inlet pipe, a mud inlet pipe, a gas flow meter, a water outlet pipe, an aeration pipe, a sludge discharge pipe, a stirrer, a temperature control device, an exhaust valve and an aerator pipe. The water inlet pipe is connected with the water outlet pipe. The mud tank is provided with the stirrer and the drainage pond.    USE - The device is useful for fermenting and denitrifying sludge (claimed).    ADVANTAGE - The device is capable of fermenting and denitrifying sludge with low dissolved oxygen condition and high ammonia nitrogen concentration.    DETAILED DESCRIPTION - The device comprises a raw water tank, a storage basin, fermentation and denitrification reactor, a drainage pond, an air compressor and a mud tank. The denitrification reactor is provided with a dissolved oxygen detector, a water inlet pipe, a mud inlet pipe, a gas flow meter, a water outlet pipe, an aeration pipe, a sludge discharge pipe, a stirrer, a temperature control device, an exhaust valve and an aerator pipe. The water inlet pipe is connected with the water outlet pipe. The mud tank is provided with the stirrer and the drainage pond. The drainage pond is connected with a drain valve and a drain pipe. The fermentation and denitrification reactor is connected with the mud tank and the air compressor through the gas flow meter. The mud tank is connected with a mud discharging valve, and the sludge discharging pipe. The aeration pipe is connected with the exhaust valve, a buffer tank and a gas collecting bag. An INDEPENDENT CLAIM is included for a method for fermenting and denitrifying sludge.
NOVELTY - A sawdust mushroom residue nutrition agent, is prepared by inoculating Bacillus subtilis on a mixture of sawdust mushroom residue and fresh mushroom stalk water extract.    USE - Sawdust mushroom residue nutrition agent for cultivating mozzie buster.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing sawdust mushroom residue nutrition agent, which involves preparing fermentation medium by compounding 93 pts.wt. sawdust mushroom residue, 5 pts.wt. bran, and 2 pts.wt. sucrose, where the material-to-water ratio is 1:1.2-1.3, carrying out stacking fermentation, adding 50 pts.wt. fermented mushroom residue, 25 pts.wt. garden soil, and 25 pts.wt. sand to obtain sawdust mushroom residue nutrition agent.
NOVELTY - A special biological composite bacterium fertilizer comprises 5-10 wt.% microbial inoculum, 55-60 wt.% macromolecule natural organic matter, 10-13 wt.% large granular urea, 10-12 wt.% controlled-release sulfur coated urea and 5-15 wt.% nitrogen-phosphorus-potassium compound fertilizer, where the microbial inoculum comprises Trichoderma aureoviride W2256 strain and solid culture medium in a weight ratio of 1: 20.    USE - Special biological composite bacterium fertilizer for Platycodon grandiflorum    ADVANTAGE - The fertilizer improves activity of beneficial microorganism, prevents harmful microorganism, improves physical and chemical properties of soil, increases and balances soil nutrients, reduces residues of farm chemicals and other harmful matters in the soil and improves quality and yield of Platycodon grandiflorum. The fertilizer ensures repeated plantation of Platycodon grandiflorum after applying in the soil.
NOVELTY - This utility model claims a town sewage treatment composite biological vermiculite mould system, comprising a water tank and from high to low in turn connected with the first grade, the second grade wetland and the third grade wetland, the wetland and the second grade wetland and wetland is planted with wetland plant. The composite biological vermiculite mould system to adequately utilize soil nutrient characteristic of vermiculite, reduces the floor space, which avoids a. stagnation, increase wetland oxygen content and improve the utilization of the wetland plant is provided, each level wetland to form drop, establishing a three-level drop flow type composite biological vermiculite a subsurface flow wetland, the sewage is more fully contact with oxygen in the air when the drop, which is good for complex atmospheric oxygen, the dissolved oxygen in the sewage increment of each drop of the direct current is more than 0.57mg/L, wherein the sewage level cascade process of complex oxide of 75%, oxygen increasing effect of the cascade process can improve the dissolved oxygen in the wetland bed body and the aerobic microorganism to the pollutant.
NOVELTY - An organic fertilizer comprises 50-70 wt.% carbon-containing organic matter such as straw and grass carbon, 25-45 wt.% nitrogen-containing organic waste for producing vegetable oils such as soybean oil, seasoning and sauce product, 2-5 wt.% microorganism strain raw powder containing bacteria Alternaria alternate, black spot disease bacteria, and long creep Helminthosporium cockspur grass forma spore bacteria and sharp protruding navel spore bacteria, and 1-5 wt.% auxiliary materials such as brown sugar, starch, salt and pH value conditioning agent.    USE - Organic fertilizer for weed control of organic rice.    ADVANTAGE - The fertilizer has rich nutritional ingredients required for crops and weeding function, realizes dual purposes of fertilization and weeding, and effectively solves the weed harm difficult problem that is greater in labor consumption and higher in investment.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is also included for a method for preparing an organic fertilizer, which involves utilizing carbon-containing organic matters, nitrogen-containing organic wastes, microbial strain raw powder and auxiliary materials, pre-treating and mixing the raw materials followed by fermentation and discharging to obtain the finished product.
NOVELTY - A controlled-release nutritional type soilless lawn matrix comprises 30-40 pts. wt. rice chaff powder, 25-30 pts. wt. spentmushroom compost, 10-15 pts. wt. tea cake having grain sizeless than 5 mm, 15-20 pts. wt. humic acid phosphorus-potassium fertilizer and 5-10 pts. wt. calcium sulfate. The matrix is prepared by separately fermenting spent mushroom compost and the tea cake after being mixed, adding a microbial zymophyte for fermenting, and adding the humic acid phosphorus-potassium fertilizer, the rice chaff powder and calcium sulfate, and uniformly mixing to obtain the finished product.    USE - Controlled-release nutritional type soilless lawn matrix.    ADVANTAGE - The matrix is eco-friendly, high in nutrient content and small in maintenance, reduces nutrient loss and improves the nutrient utilization rate.    DETAILED DESCRIPTION - A controlled-release nutritional type soilless lawn matrix comprises 30-40 pts. wt. rice chaff powder, 25-30 pts. wt. spentmushroom compost, 10-15 pts. wt. tea cake having grain sizeless than 5 mm, 15-20 pts. wt. humic acid phosphorus-potassium fertilizer and 5-10 pts. wt. calcium sulfate. The matrix is prepared by separately fermenting spent mushroom compost and the tea cake after being mixed, adding a microbial zymophyte for fermenting, controlling the mass content ratio of carbon to nitrogen in the material to less than 25, and adding the humic acid phosphorus-potassium fertilizer, the rice chaff powder and calcium sulfate after sufficient fermenting, and uniformly mixing to obtain the finished product. An INDEPENDENT CLAIM is also included for a method for preparing a controlled-release nutritional type soilless lawn matrix.
NOVELTY - A base fertilizer preparing method involves crushing dry pig manure, dry dairy manure, cottonseed, corn straw, dry pond sludge and organic fertilizer into powder and uniformly mixing crushed powder with water. The resulting mixture is fermented, and the fermentation product is filtered. Sterilizing deodorant is added to the filtered product, and the resulting product is dried. Urea, monoammonium phosphate, potassium sulfate, humic acid, phoxim granule and plant growth regulator are crushed and mixed to obtain a mixture, and the mixture is uniformly mixed with the dried product.    USE - Method for preparing a base fertilizer for Fraxinus.    ADVANTAGE - The method enables preparing base fertilizer in a simple and convenient manner. The fertilizer prepared using the method is odor free and is convenient to use. The fertilizer improves growth of Fraxinus and enhances drought resistance, disease resistance, insect resistance and immunity of Fraxinus.    DETAILED DESCRIPTION - A base fertilizer preparing method involves crushing 20-22 wt.% dry pig manure, 14-16 wt.% dry dairy manure, 6 wt.% cottonseed, 16 wt.% corn straw, 15 wt.% dry pond sludge and 5 wt.% organic fertilizer into powder and uniformly mixing crushed powder with water in a fermenting tank. The mixture is fermenting for 20-22 days in a sealing condition, and the resulting fermentation product is filtered. 1 wt.% Sterilizing deodorant is added to the filtered product, and the resulting product is dried until the moisture content of the product is reduced to less than 10%. 4 wt.% Urea, 6 wt.% monoammonium phosphate, 7 wt.% potassium sulfate, 1 wt.% humic acid, 1 wt.% phoxim granule and 1 wt.% plant growth regulator are crushed and mixed to obtain a mixture, and the obtained mixture is uniformly mixed with the dried product. An INDEPENDENT CLAIM is also included for a method for applying base fertilizer, which involves applying 50-60 kg of fertilizer per plant during early spring.
NOVELTY - The utility model claims a dry for removing hydrogen sulphide in marsh gas through the device, comprising a tank body are respectively provided with a marsh gas outlet hole and gas inlet pipe at one side of the top part and the bottom part of the tank body, the air outlet at the bottom of the tank body is provided with a gas distributor, the gas distributor with the marsh gas inlet pipe is corresponding to the tank body of the marsh gas and marsh gas distributor is provided with at least three stages and layer. This utility model has advantages of greatly improve desulfurizing efficiency so as to reduce the cost, can effectively reduce the filling height by fractional can lead to removing sulfureted hydrogen and carbon dioxide in marsh is more than 90%, the marsh gas user according to the mass spectrometer.
NOVELTY - This utility model claims a garbage recycling processing device, comprising a marsh gas furnace, a drier, a fermentation tank and the marsh gas tank, the fermentation tank comprises a tank body, a tank body top end is provided with a feeding port, a tank body is set at the bottom, the tank body is provided with a hot air device and a waste heat heating circulation device, wherein the marsh gas tank is provided with a hot water circulator and waste heat heating circulating device. This utility model of marsh gas furnace, a drier, a fermentation tank and the marsh gas pool is composed of a recycling system, the garbage generated in the process of processing a processing cycle.
NOVELTY - Synthesizing 5-chlorovaleryl chloride comprises (i) reacting 1-bromo-3-chloropropane and diethyl malonate in a solvent and solid potassium carbonate powder to obtain 2-(3-chloropropyl)diethyl malonate; (ii) carrying out hydrolysis and decarboxylation reaction to obtain 5-chlorovaleric acid; and (iii) reacting with thionyl chloride to obtain 5-chlorovaleryl chloride.    USE - The method is useful for synthesizing 5-chlorovaleryl chloride (claimed).    ADVANTAGE - The method is simple, utilizes raw materials which are easy to obtain, avoids the use of highly toxic chemicals including sodium hydride and potassium cyanide, ensures safe production and avoids the environmental pollution caused by cyanide wastewater.
NOVELTY - A CRX diesel oil efficiency-enhancing emission-reducing additive comprises 15-65 wt.% diesel oil, 30-70 wt.% methanol, and 10-30 wt.% CRX gasoline additive.    USE - CRX diesel oil efficiency-enhancing emission-reducing additive.
NOVELTY - Environmentally friendly type herb residue processing system comprises a filtration system comprising a dehydration device and a water purification device, where the dehydration device is connected with the water purification device. The system further comprises an anaerobic fermentation system comprising a sterilization stirring device and at least one vacuum fermentation tank devices, where the sterilization stirring device and the vacuum fermentation tank devices are connected with the filtration system.    USE - Used as an environmentally friendly type herb residue processing system.    ADVANTAGE - The processing system includes the dehydration device, which treats the herb residue and medicine waste liquid separately, the water purification device for purifying the medicine waste liquid, and anaerobic fermentation system for fermenting the herb residue into a fertilizer. The whole operation of the system is simple and convenient, waste materials can be reused.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the environmentally friendly type herb residue processing system.
NOVELTY - A ZF-30 bio-organic fertilizer comprises crop balloonflower, poultry, livestock manure, crop waste, zinc, boron, and a bio-enzyme.    USE - A ZF-30 bio-organic fertilizer used for crops.    ADVANTAGE - The fertilizer improves soil structure, removes hardening of the soil, improves crop yield, improves product quality, and is environment-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparing the ZF-30 bio-organic fertilizer, comprising mixing crop balloonflower, poultry, livestock manure, crop waste, zinc, boron, and bio-enzyme at 30 degrees C and 90% humidity; and pressing into pellets.
NOVELTY - The device comprises a photosynthetic bioreactor, a concentrated bottle, nitrogen removal device and a fermentation tank. An inlet of the photosynthetic bioreactor is provided with an air inlet and an air outlet of a transparent sealed container. The concentrated bottle is provided with a liquid inlet, a liquid outlet and a feeding port of a sealed container made of nitrogen-containing material, preferably cation exchange resin. The fermentation tank is provided with a sample inlet, a sample outlet, an air inlet, a feeding port and an air outlet.    USE - The device is useful for photosynthetic fermentation of microalgae to produce a grease and biodiesel (all claimed).    ADVANTAGE - The device improves digestive utilization rate of microalgae and reduces production cost to produce grease in an environment-friendly manner.    DETAILED DESCRIPTION - The device comprises a photosynthetic bioreactor, a concentrated bottle, nitrogen removal device and a fermentation tank. An inlet of the photosynthetic bioreactor is provided with an air inlet and an air outlet of a transparent sealed container. The concentrated bottle is provided with a liquid inlet, a liquid outlet and a feeding port of a sealed container made of nitrogen-containing material, preferably cation exchange resin. The fermentation tank is provided with a sample inlet, a sample outlet, an air inlet, a feeding port and an air outlet. The liquid outlet of the photosynthetic bioreactor is connected with the liquid inlet of the concentration bottle through a pipeline-I. The pipeline-I is provided with a three-way valve. The sample inlet is connected with an outlet of the fermentation tank via a pipeline-II and pipeline-III. An air inlet of the photosynthetic bioreactor is connected with a pipeline IV. The pipeline I-IV are provided with a pump. An INDEPENDENT CLAIM is included for use of the device for photosynthetic fermentation of microalgae to produce a grease and biodiesel.
NOVELTY - An electrolyte for photo-electro-catalytic hydrogen production system comprises inorganic strong acid, inert supporting electrolyte, and tannic acid as photosensitizer.    USE - An electrolyte for photo-electro-catalytic hydrogen production system (claimed).    ADVANTAGE - The electrolyte improves the hydrogen-producing rate and the light utilization efficiency.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for photo-electric catalytic hydrogen production system comprising a direct current voltage output device, an anode, a cathode and the electrolyte, where the electrolyte is the according to any one from claim 1 to 8, the electrolytic solution.
NOVELTY - This utility model claims a kind of using hydrogen as the main raw material, fuel oil only as a hydrogen engine starting power operation a hydrogen engine power system. Is a hydrogen by a hydrogen engine power utilization system, comprising a primary fuel oil box, wherein it is as follows: the original fuel oil box is connected with a hydrogen converter, a hydrogen converter is orderly connected with a hydrogen raw material box, an engine exhaust pipe waste heat hydrogen stimulated catalytic system, hydrogen cooling device, a hydrogen storage chamber and a hydrogen distribution system, a hydrogen distribution system raw material box is connected with a hydrogen converter is connected with a computer control system. The beneficial effect of the utility model is as follows: it saves the fuel cost of the 2/3 fuel oil engine, gas, methanol fuel cost saving, safe and environment-friendly 1/3, the combustion product is water, there is no any pollution to the human environment protection made the contribution, there is no any one kind of fuel energy compared to a hydrogen fuel, the generated value and is sufficient to influence the life pattern of human beings.
NOVELTY - An attapulgite with calcium hydroxide is prepared by performing acid treatment on natural attapulgite raw material to obtain modified attapulgite which is treated as carrier, and subjecting to high-temperature calcination.    USE - An attapulgite for heterogeneous catalyst (claimed).    ADVANTAGE - Preparation process is simple and low cost, reaction steps and industrial waste water are reduced, negative influence caused by product is avoided, and product has high catalysis efficiency, is easily separated from product after being used for catalyzing biodiesel, high in stability, and high in catalytic activity, and can be repeatedly used, and meets quality standard of existing biodiesel at home.    DESCRIPTION OF DRAWING(S) - The drawing shows a transmission electron microscope image of attapulgite with calcium hydroxide.
NOVELTY - The device has discharge pipes (940,950) which are connected to the exhausting unit for supplying the mixture to the reservoir (100). The waste water inlet pipe (910) is connected in pump (700) for transferring waste water to the waste water influx unit. The flow difference shift valve (V2) is installed in the liquefied fertilizer discharge pipe (930). A power supply device (810) supplies power source to the excrements heater (300) within the pump. The heater controller (830) is provided within tub for controlling excrements heater so as to maintain temperature of waste water.    USE - Device for manufacturing liquefied fertilizer.    ADVANTAGE - The liquefied fertilizer manufacturing time can be shortened and the mixing efficiency of the liquefied fertilizer can be enhanced. The fluid resistance is minimized and diffusion and the generation of the noise can be prevented.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the liquefied fertilizer.(Drawing includes non-English language text)    Reservoir (100)    Excrements heater (300)    Pump (700)    Power supply device (810)    Heater controller (830)    Waste water inlet pipe (910)    Liquefied fertilizer discharge pipe (930)    Discharge pipes (940,950)    Flow difference shift valve (V2)
NOVELTY - The method involves pre-precipitating municipal sewage in pre-precipitating pool. Selective efficient bioreactor is arranged in gradient biochemical aeration tank front section to treat sewage, and microbial growth accelerant is added. The gradient biochemical aeration treatment to sewage in gradient biochemical aeration tank is performed. The treated sewage is precipitated in precipitating pool. The gradient biochemical aeration treatment is performed by adjusting dissolved oxygen control gradient biochemical consumption speed of carbon source in aeration tank.    USE - Biological rotating gradient aeration (BRGA) municipal sewage treatment method.    ADVANTAGE - The high efficiency can be achieved. The processing efficiency can be improved. The sewage can be purified effectively.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the BRGA municipal sewage treatment process. (Drawing includes non-English language text)
NOVELTY - Method for preparing slurry-state fertilizer substrate, involves adding screened garbage containing organic matters to flash evaporation blaster, controlling temperature in the flash evaporation blaster to 210-230 degrees C, controlling pressure in the flash evaporation blaster to 2-3 Mpa for 80-100 seconds, and completing the flash evaporation blasting within 0.01 seconds.    USE - The method is useful for preparing slurry-state fertilizer substrate (claimed).    ADVANTAGE - The method is cost-effective, rapid and low in energy consumption, and does not produce any harmful gas, preferably dioxin (can be generated, as the maximum temperature is 230 degrees C), and has excellent operability.
NOVELTY - Organic-inorganic fertilizer binder comprises 30-40 pts. wt. rice starch, 4-6 pts. wt. selenium-enriched yeast, 4-6 pts. wt. maltose, 50-60 pts. wt. water, 0.001-0.004 pts. wt. sodium selenite, 2-3 pts. wt. potassium hydroxide, 0.2-0.4 pts. wt. borax and 0.1-0.2 pts. wt. tributyl phosphate.    USE - The organic-inorganic fertilizer binder is useful in fertilizer for tea cultivation (claimed).    ADVANTAGE - The binder ensures long-lasting property of the selenium enriched fertilizer and reduces environmental risk of selenium, allows the plant to absorb selenium and synthesis plant tissue, thus satisfies synchronization, and overcomes passive plant absorption, growth inhibition, reduced quality of agricultural products and low activity of the selenium source caused by the foliar application of organic to plant root.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the binder, which involves (a) mixing rice starch, selenium-enriched yeast and maltose with water and culturing the mixture at 28-31 degrees C for 23-25 hours, adding 4-5 pts. wt. sodium selenite for every 2-3 hours and fermenting for 40-50 hours to obtain fermented mixture, (b) adding potassium hydroxide and borax to the mixture obtained in step (a) and mixing the mixture at 30-35 degrees C for 1-1.5 hours with stirring speed of 2 times per minutes, (c) adding tributyl phosphate to the mixture obtained in step (b) and mixing uniformly to obtain semi finished product, and (d) drying the semi finished product at 80-90 degrees C, crushing the dried product, checking the crushed product and packing.
NOVELTY - Preparation of biodiesel involves esterifying the raw materials of high-acid value oil, enabling glycerol and raw materials of high-acid value oil in the molar ratio of 2-6:1 to esterify with each other under the catalyzing action of ionic liquid, obtaining mixture of low-acid value esterification product-monoglyceride, diglyceride or triglyceride, then carrying out interesterification on esterified oil, generating crude low-acid value biodiesel fatty acid methyl ester, vacuum distilling, and refining low-acid value biodiesel fatty acid methyl ester.    USE - Preparation of biodiesel (claimed).    ADVANTAGE - The biodiesel is economically and efficiently prepared with reduced energy consumption, and high yield.    DETAILED DESCRIPTION - Preparation of biodiesel involves esterifying the raw materials of high-acid value oil, enabling glycerol and raw materials of high-acid value oil in the molar ratio of 2-6:1 to esterify with each other under the catalyzing action of ionic liquid at 120-140 degrees C under pressure of 10-300 KPa for 1-3 hours, obtaining mixture of low-acid value esterification product-monoglyceride, diglyceride or triglyceride, then carrying out interesterification on esterified oil, namely carrying out interesterification on the mixture of low-acid value esterification product-monoglyceride, diglyceride or triglyceride and methanol under the action of base catalyst, generating crude low-acid value biodiesel fatty acid methyl ester for 0.5-1 hours, vacuum distilling at 180-220 degrees C under pressure of 0.5-10 KPa, and refining low-acid value biodiesel fatty acid methyl ester. The amount of alkali catalyst is 10-30 wt.%. The amount of low-acid value esterification product is 0.5-1 wt.%.
NOVELTY - Use of blue-green algae and super absorbent resin is claimed as raw materials for production of high-quality straw rotting edible mushroom concentrated culture medium.    USE - The blue-green algae and super absorbent resin is useful as raw materials for production of high-quality straw rotting edible mushroom (wood destroying fungi) concentrated culture medium (all claimed).    ADVANTAGE - The raw materials increase production of high-quality culture medium by 10-15% and reduce compost raw material cost by 50% or more. The method enables utilization of the blue-green algae discarded as waste, hence environmentally-friendly and provides high social and economic benefits.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for producing the above-mentioned culture medium, which involves using the blue-green algae and super absorbent resin as raw materials.
NOVELTY - An ((aryl-dioxolanyl)-butyryl)-oxazolidinone derivative (I) is obtained by reacting an (oxo-oxazolidinyl)-aryl-pentane-dione derivative (II) with a diol compound of formula: HO-CH2-(CH2)n-OH in the presence of a dehydrating agent in an acidic environment at a pH of less than 7.    USE - Preparation of (aryl-dioxolanyl)-butyryl-oxazolidinone derivative (claimed).    ADVANTAGE - The method is free of refluxing operation and special requirements on dehydrating agents, acids, reaction solvents, and reaction temperatures. The method is simple, economical and environmentally-friendly, and provides high yield and product purity.    DETAILED DESCRIPTION - An ((aryl-dioxolanyl)-butyryl)-oxazolidinone derivative of formula (I) is obtained by reacting an (oxo-oxazolidinyl)-aryl-pentane-dione derivative of formula (II) with a diol compound of formula: HO-CH2-(CH2)n-OH in the presence of a dehydrating agent in an acidic environment at a pH of less than 7.    Ar=substituted aryl;    n=1-4;and    R1-R3=H, isopropyl or phenyl, with at least one being phenyl.
NOVELTY - Method for preparing, separating and purifying baicalein and wogonin by enzymatic hydrolysis of endogenous baicalin and wogonoside of Scutellaria, involves obtaining traditional Chinese medicinal Scutellaria as raw material, performing e.g. endogenous enzyme induction and bioconversion, negative-pressure cavitation extraction, liquid-liquid extraction, medium-and low-pressure liquid chromatography using normal phase silica gel, and low-temperature crystallization and recrystallization, and performing extraction, separation and purification.    USE - The method is useful for preparing, separating and purifying baicalein and wogonin (claimed) which is used in development of medicines and healthcare products.    ADVANTAGE - The method is simple and economical to perform, and environmentally-friendly, provides baicalein and wogonin which are increased by 4.47 times and 2.85 times, respectively, enables high conversion rate of baicalin and wogonoside of 98.39% and 98.16%, respectively, and overcomes problem of large damaging effects on the baicalin and the wogonoside, low conversion rate and serious pollution as in the existing method. The baicalein and wogonin can be produced industrially.    DETAILED DESCRIPTION - Method for preparing, separating and purifying baicalein and wogonin by enzymatic hydrolysis of endogenous baicalin and wogonoside of Scutellaria, involves obtaining traditional Chinese medicinal Scutellaria as raw material, performing endogenous enzyme induction and bioconversion, negative-pressure cavitation extraction, liquid-liquid extraction, medium-and low-pressure liquid chromatography using normal phase silica gel, low-temperature crystallization and recrystallization and other high efficient conversion processes, and performing extraction, separation and purification to obtain baicalein and wogonin with high purity, where purity of the baicalin and the wogonoside is more than 98%, respectively.
NOVELTY - Fermenting and purifying biogas comprises inoculating microorganisms of anaerobic cellulose enzyme producing bacteria in a reaction tank of a biogas fermentation system, fermenting organic matters of straw and livestock excrements, controlling the temperature of biogas fermentation at a constant-temperature of 37 plus minus 0.2 degrees C, purifying and separating methane and carbon dioxide in biogas, comprising desulfurization treatment and drying treatment for biogas, and separating methane and carbon dioxide.    USE - The method is useful for fermenting and purifying biogas (claimed).    ADVANTAGE - The method: has high-efficiency and energy-saving effect, and is environmentally friendly (claimed); increases the fermentation efficiency of the biogas; increases the purification effect of the biogas; and reduces the fermentation cost of the biogas.
NOVELTY - This utility model claims a fully sealed production azamethiophos as a reaction device, comprising a first reaction unit, a second reaction unit and a third reaction unit. The first reaction unit comprises a rotary storage kettle, oxazole (4, 5-b)pyridine -2 (3H)-ketone material storing tank, a N, N-dimethyl formamide storage tank, a poly-formaldehyde material storage tank and a sulfoxide chloride storage tank. The first reaction unit comprises a first inlet and a first outlet a first powder-liquid mixing pump, the first powder-liquid mixing pump. The oxazole (4, 5-b)pyridine -2 (3H)-ketone material storing tank, N, N-dimethyl formamide storage tank and poly-formaldehyde material storage tank is connected with the first inlet, the first outlet is connected with the rotational flow. The rotary storage kettle comprises a first main body, the first main body is hollow to form a first reaction chamber, the first reaction chamber is an inverted conical structure. This utility model claims a reaction device, to a radically avoids harmful gas leakage, which is good for environment protection.
NOVELTY - Preparing 4-alkylamino-3-nitroquinoline and its acid addition salts, comprises: reacting 1-nitroethylene-2-amino benzoic acid with aluminum chloride and thionyl chloride in presence of a high boiling solvent to obtain 4-hydroxy-3-nitroquinoline; and halogenating the obtained 4-hydroxy-3-nitroquinoline with thionyl chloride followed by amination/alkylation in presence of a polar, aprotic high boiling solvent to yield 4-alkylamino-3-nitroquinolines.    USE - The method is useful for preparing 4-alkylamino-3-nitroquinoline and its acid addition salts (claimed) which are useful as antimalarial, antibacterial, anticonvulsant, cardiovascular and immune response modifiers (including imiquimod and resiquimod). No biological data given.    ADVANTAGE - The method: totally avoids use of acetic anhydride which requires stringent government handling restrictions being a restricted chemical; increases the yield coupled with use of polar, aprotic solvents with high boiling point which can be recycled after fractionation thus making the process cost effective and environment friendly; and provides 4-alkylamino-3-nitroquinolines and their acid salts which exhibit pre-emergence and post-emergence herbicidal activity.
NOVELTY - Substituted 4-carbethoxy piperazine compounds (A) are new.    USE - (A) are useful for preparing ranolazine (claimed) which is used to treat chronic angina. No biological data given.    ADVANTAGE - (A) provides ranolazine: by utilizing N-carbethoxy piperazine which inhibits the formation of dimer impurity in the process (claimed), thus providing highly pure ranolazine ( greater than or equal to 99.8%) with high yield; and in a safe, simple, economical and environment friendly manner.    DETAILED DESCRIPTION - Substituted 4-carbethoxy piperazine compounds (A) of formula (I) and (II) are new.    R, R1 = alkyl (preferably ethyl (preferred), CH3, propyl, isopropyl or tert-butyl), or aryl.    INDEPENDENT CLAIMS are also included for:    (1) preparing (I) and (II); and    (2) preparing ranolazine and its acid addition salts, comprising either (a) hydrolysis and concurrent decarboxylation of (I) with alkali to give 1-((2,6-dimethylphenyl)amino carbonyl methyl)piperazine, and (b) reacting 1-((2,6-dimethylphenyl)amino carbonyl methyl)piperazine with 1-(2-methoxy phenoxy)-2,3-epoxy propane in presence of an organic solvent (S3) to give ranolazine, or (a1) hydrolysis and concurrent decarboxylation of (II) with alkali to give 1-(3-(2-methoxyphenoxy)-2-hydroxypropyl)piperazine and (b1) reacting 1-(3-(2-methoxyphenoxy)-2-hydroxypropyl)piperazine with ((2,6-dimethylphenyl)-aminocarbonyl methyl) chloride in presence of an organic solvent and a base to give ranolazine.
NOVELTY - Preparing ammonium salt of thiofuroic acid, comprises (i) reacting furoyl chloride with sodium sulfide in the presence of an acid in a suitable solvent at a certain temperature and time, (ii) purging ammonia gas to the reaction mixture, and (iii) isolating ammonium salt of thiofuroic acid.    USE - The process is useful for preparing ammonium salt of thiofuroic acid, which is useful as an intermediate of furaca for preparing ceftiofur (all claimed).    ADVANTAGE - The process is capable of simply and economically preparing the ammonium salt of thiofuroic acid with high purity, stability and yield in an eco-friendly manner.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for:    (1) preparing furaca, comprising (i) reacting ammonium salt of thiofuroic acid with 7-amino cephalosporanic acid (7-ACA) in the presence of a buffering agent in a solvent at a certain temperature for time, and (ii) isolating 7-amino-3-(2-furanylcarbonytthiomethyl)-3-cephem-4-carboxylic acid (furaca); and    (2) preparing ceftiofur comprises converting the furaca to ceftiofur or its salts.
NOVELTY - On-site treatment of kitchen waste is carried out by sorting kitchen wastes including plastic, metal, ceramic, bone rod and hard waste material; dehydrating the sorted wastes, sending waste in an oil-water separation system to remove oil, and crushing solid waste material in a fermentation treatment system; adding crushed material with 2 wt.% waste degradation composite microbial inoculum, controlling initial temperature to more than 25 degrees C, and fermenting at 60-65 degrees C for 15-25 days; and discharging the fermented material and separating oil and water by gravity.    USE - Method for on-site treatment of kitchen waste (claimed).    ADVANTAGE - The method has low energy consumption, is safe to operate, and can realize waste reduction and recovery. The fermentation product can be used as organic fertilizer, or be added with functional bacteria to be made into biological organic fertilizer for agricultural production or garden greening. The separated oil can be used for producing biological diesel oil, soap, mineral flotation agent. The wastewater can be discharged through sewage pipeline.    DETAILED DESCRIPTION - On-site treatment of kitchen waste comprises:    (A) sorting kitchen wastes including plastic, metal, ceramic, bone rod and hard waste material;    (B) sending the sorted wastes into a crushing and dehydrating system, then draining water, sending waste in an oil-water separation system to remove oil, and crushing solid waste material in a fermentation treatment system;    (C) adding crushed material with 2 wt.% waste degradation composite microbial inoculum, adjusting material water content to 50-40%, controlling initial temperature to more than 25 degrees C, stirring and ventilating, fermenting for 6-10 hours, then raising temperature to 40-50 degrees C for 12-16 hours and raising to 60-65 degrees C for 15-25 days to finish fermentation; and    (D) discharging the fermented material and separating oil and wastewater by gravity.
NOVELTY - Preparation of highly pure ivabradine hydrochloride involves: (a) condensing methylamine derivative with 3-(3-chloropropyl)-7,8-dimethoxy-1,3,4,5-tetrahydro-2H-3-benzazepin-2-one; (b) treating crude ivabradine with derivatizing agent in suitable solvent; (c) treating ivabradine with hydrochloride to obtain highly pure ivabradine hydrochloride; and (d) isolating highly pure ivabradine hydrochloride.    USE - The process is useful for the preparation of highly pure ivabradine hydrochloride (claimed).    ADVANTAGE - The process is efficient, economical, less hazardous and eco-friendly.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for highly pure ivabradine hydrochloride having purity of at least 99% with the content of N-((4,5-dimethoxybenzocyclobut-1-yl)-methyl)-7N-(methyl)amine in the range of 0.03-0.15% as measured by HPLC.
NOVELTY - An alkaloid compound (I), is new.    USE - The alkaloid is useful for preparing a tumor cell multidrug-resistance reverser (claimed).    ADVANTAGE - The method utilizes microbes to perform liquid fermentation production, has simple operating technique, is performed inexpensively in short period of time, and enables guaranteed sources. The method is environmentally-friendly, as it utilizes biological synthesis method. The alkaloid reverses tumor cell multidrug resistance, and has strong reversion actions on leukemia amycin drug-resistant cells (K562/ADR), human lung adenocarcinoma/cis-platinum drug-resistant cells (A549/DDP) and human ovarian cancer/cis-platinum drug-resistant cells (SK-OV-S/DDP).    DETAILED DESCRIPTION - An alkaloid compound of formula (I), is new. An INDEPENDENT CLAIM is included for method for preparing the alkaloid, which involves obtaining biological extract from Aspergillus fumigatus SPS-02 (CCTCC M2013014).
NOVELTY - Preparation of bio-oil chemical-looping hydrogen recycled ferric oxide (Fe2O3)/aluminum oxide (Al2O3) oxygen carrier comprises mixing ferric nitrate nonahydrate and gamma -Al2O3, ultrasonically processing at 100-500 W for 15-90 minutes, drying, and calcining.    USE - Method for preparing bio-oil chemical-looping hydrogen recycled Fe2O3/Al2O3 oxygen carrier (claimed).    ADVANTAGE - The method is simple and suitable for industrial production, improves iron-based oxygen carrier body, and can obtain uniformly fined oxygen carrier particles. The oxygen carrier has high dispersion degree, and high Chemical looping hydrogen generation (CLHG) reaction activity and thermal stability.
NOVELTY - A bio-organic fertilizer comprises 50-70 pts. wt. yellow sand excrement, 30-50 pts. wt. chicken manure, 60-65 pts. wt. clay, and 35-40 pts. wt. feces of Tenebrio molitor.    USE - A bio-organic fertilizer for crops.    ADVANTAGE - The fertilizer improves crop yield and crop quality, reduces production cost, improves soil structure and agricultural ecological environment, and promotes plant sustainable development.
NOVELTY - Organic waste chosen from livestock manure, sewage sludge and food waste with moisture content of more than 80%, 50-55 wt.% urban waste including paper, and component containing iron are poured into a reactor, and blended, to obtain organic waste mixture. Mixture of organic waste and urban waste is added to the reactor, pressurized, and stirred under reduced pressure of 0.9-1.1 atm for 10-120 seconds. The organic sludge is depressurized, crushed, and dried, to obtain solid fuel with moisture content of 10-20%.    USE - Manufacture of solid fuel from organic waste (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for cogeneration system.
NOVELTY - Recycling of organic waste involves adding organic waste in raw material tank, drying in dried having kiln drier and paddle drier and recycling, supplying hydrocarbon-based gas to reactor, and obtaining hydrocarbon fuel and fertilizer.    USE - Recycling of organic waste used for producing fuel and fertilizer (all claimed).    ADVANTAGE - The method efficiently and economically recycles organic waste.    DETAILED DESCRIPTION - INDEPENDENT CLAIMS are included for the following:    (1) fuel; and    (2) fertilizer.
NOVELTY - Organic fertilizer comprises 45 plus minus 5 %mass pharmaceutical or food product factory sludge, 30 plus minus 5 %mass chicken manure, 25 plus minus 5 %mass industrially cultivated seafood mushroom residue and 5 plus minus 1 %mass plant ash.    USE - As organic fertilizer.    ADVANTAGE - The organic fertilizer is high in organic content and comprehensive in nutrition. The method overcomes low organic content, incomplete nutrition and irrational use of mushroom residue of the existing organic fertilizer and environmental pollution.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for production of the fertilizer, which involves (a) weighing the above-mentioned raw materials and mixing uniformly to obtain mixture, (b) adding the mixture to fermentation tank and performing fermentation at 55-65 degrees C for 17-22 hours using aerobic bacteria and turning the fermented material and fermenting continuously for 18-20 days, until the water content of the fermented material reaches 42-46%, (c) performing trapezoidal stack fermentation at 42-46 degrees C for 28-35 days and turning the fermented material for 4-5 times to obtain secondary fermented material, where the cross section of the trapezoidal stack bottom width is 4 m, base width is 3.5 m, and height is 1.2 m, and (d) drying the secondary fermented material, crushing the dried material mechanically and packing product.
NOVELTY - A gradient cycle stirring method in a biogas reactor, involves: (1) mixing the material in the tank body to the center of the upper part of the tank body from the bottom of the tank body; (2) the material from the upper part of the tank body is then conveyed to the bottom of the tank, reciprocating cycle; and (3) discharging clear liquid from one side of upper part of the tank body, then marsh gas is discharged from the top of the tank body.    USE - Gradient cycle stirring in a biogas reactor (claimed).    ADVANTAGE - The method is cost-effective, operation is simple, safe and reliable, the intensity can be controlled, has reduced energy consumption and improved biogas yield, simple operation, and stable operation.
NOVELTY - A long-term storage method of aerobic nitrifying granular sludge comprises measuring activity of aerobic nitrifying bacteria granular sludge before storing; monitoring aerobic nitrifying bacteria granular sludge, reducing activity by 75-80%; storing aerobic nitrifying granular sludge; activating aerobic nitrifying granular sludge every 1-2 period by dividing injection liquid into 6 parts; and controlling chemical oxygen demand.    USE - A long-term storage method of aerobic nitrifying granular sludge for wastewater treatment.    DETAILED DESCRIPTION - A long-term storage method of aerobic nitrifying granular sludge comprises measuring activity of aerobic nitrifying bacteria granular sludge before storing; monitoring aerobic nitrifying bacteria granular sludge, reducing activity by 75-80%; storing aerobic nitrifying granular sludge; activating aerobic nitrifying granular sludge every 1-2 period by dividing injection liquid into 6 parts; and controlling chemical oxygen demand at 1550-180 mg/ml, ammonium ion to 40-45 mg/l, phosphate ion to 5-6 mg/l, activating aeration amount at 0.4 m3/hour, activation temperature of 29-31 degrees C, calcium concentration of 10 mg/l, trace element of 1 ml/l, and solid content at 290-33o mg/l.
NOVELTY - Linezolid intermediate prepared by reacting an epoxide with cyanate under catalysis of dehalogenase to obtain the linezolid intermediate, the reaction temperature is 40-60 degrees C, the reaction pH is 7.0-9.0, the content in percentage by mass-water volume of the epoxide is 1-15%, and the amount of the dehalogenase is 50000U of the epoxide per gram-2 million U of the epoxide per gram.    USE - The method is useful for preparing a linezolid intermediate (claimed).    ADVANTAGE - According to the preparation method, the dehalogenase is used for a catalytic reaction, the yield can achieve 90%, and in comparison with the yield without the use of the dehalogenase, the yield is obviously greatly improved; and furthermore, chiral separation is not required, high-temperature and high-pressure conditions are not required, the reaction is mild, the safety is high, the preparation method is environment-friendly, the raw materials are low in cost and easy to obtain, the reaction yield is high, and the preparation method is further suitable for industrial production.    DETAILED DESCRIPTION - Preparation of a linezolid intermediate of formula (II), comprises reacting an epoxide represented by formula (I) with cyanate under catalysis of dehalogenase to obtain the compound of formula (II), the reaction temperature is 40-60 degrees C, the reaction pH is 7.0-9.0, the content in percentage by mass-water volume of the epoxide is 1-15%, and the amount of the dehalogenase is 50000U of the epoxide per gram-2 million U of the epoxide per gram.    R=oxygen, alkoxy, heterocyclic, heteroaryl, aryl, a substituted aryl or ester group.
NOVELTY - Processing bacterial fertilizer from domestic waste involves mixing domestic garbage and sewage sludge as raw material, inoculating mixed mixture with organic material and mixed bacterial suspension, and producing bacterial suspension, where ratio of domestic garbage and sludge is 7:3 and moisture content of mixture is 55%, ventilation quantity is 0.4 m2/minute, inoculation quantity is 1% and fermentation time is 10 days.    USE - The method is useful for processing bacterial fertilizer from domestic waste (claimed), used for inhibiting growth of harmful bacteria, accelerating vigorous growth of crops and increasing soil fertility.    ADVANTAGE - The method rapidly degrades and converts domestic garbage and sewage sludge.
NOVELTY - Bio-organic fertilizer comprises 35-45 pts. wt. rejected tobacco and tobacco waste, 40-55 pts. wt. livestock excrements and 2-5 pts. wt. microbial inoculum.    USE - As bio-organic fertilizer.    ADVANTAGE - The non-polluted bio-organic fertilizer reduces waste material, production cost, fertilizer usage amount and soil hardening and is suitable for prompting development of green agriculture.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of the fertilizer, which involves (a) drying rejected tobacco and tobacco waste and livestock excrements, until the water content reaches 20% or less, and diluting microbial inoculum and mixing with the dried mixture, adding water and stirring the mixture uniformly, and (b) adding the mixture obtained in step (a) into fermentation tank and sealing and fermenting at 55-60 degrees C for 45-50 days to obtain the product.
NOVELTY - A phenol from salicylic acid sublimation residue is prepared by (A) carrying out high-temperature pyrolysis by stirring salicylic acid sublimation residue in reaction chamber at 450-550 degrees C at vacuum degree of - 0.01 to - 0.06 MPa to obtain crude phenol, (B) distilling, purifying, placing in distillation kettle with vacuum degree of - 0.05 to - 0.07 MPa, steam heating at 0.3-0.5 MPa, purifying, cooling, and recovering.    USE - Preparation of phenol from salicylic acid sublimation residue (claimed).    ADVANTAGE - Preparation process is environment-friendly and has high yield and recyclable waste materials.
NOVELTY - A diethyl dipropylmalonate is prepared by using sodium bromide from production process of diethyl dipropylmalonate as raw material, and treating sodium bromide with a cyclic process.    USE - Preparation of diethyl dipropylmalonate for preparing valproic acid derivative.    ADVANTAGE - Preparation process reduces production costs, has high side reaction yield, and reduces pollution.    DETAILED DESCRIPTION - A diethyl dipropylmalonate of formula (CH3-(CH2)2-C(CO2Et)2-(CH2)2-CH3) (I) is prepared by using sodium bromide from production process of diethyl dipropylmalonate as raw material, and treating sodium bromide with a cyclic process provided in scheme (1). INDEPENDENT CLAIMS are included for:    (1) decomposition reaction of sodium bisulfate which involves decomposing sodium bisulfate to sodium sulfate and sulfuric acid in the presence of propanol at 48-50 degrees C;    (2) sulfuric acid waste liquid treatment which involves adding organic solvent and oxidant into sulfuric acid waste liquid, dissolving remaining waste liquid from reaction of 2-bromopropane dissolved in organic solvent, oxidizing hydrobromic acid residue into bromine, dissolving bromine with organic solvent, and recovering bromine from bromine-containing organic solvent by distilling and recycling; and    (3) preparation of 1-bromopropane which involves performing reversible reaction of propanol and hydrobromic acid in the presence of acid to produce water and 1-bromopropane and distilling.
NOVELTY - A mepivacaine and its optical enantiomer is prepared by taking N-(2,6-dimethyl phenyl)-2-piperidinecarboxamide or an optical enantiomer as starting material, adding dimethyl carbonate in alcohol solution under basic catalyst, and mixing at controlled temperature for 1-10 hours.    USE - Preparation of mepivacaine and its optical enantiomer (claimed).    ADVANTAGE - Preparation process is simple and low-cost, has commercially available raw materials, sufficient source, and mild reaction conditions, and avoids use of hazardous reagent i.e. dimethyl sulfate and sodium cyanoborohydride.    DETAILED DESCRIPTION - A mepivacaine and its optical enantiomer is prepared by taking N-(2,6-dimethyl phenyl)-2-piperidinecarboxamide or an optical enantiomer as starting material, adding dimethyl carbonate in alcohol solution under basic catalyst, mixing at controlled temperature for 1-10 hours in which reaction is represented by formula (I)..
NOVELTY - Manufacturing liquid fertilizer using fish, comprises (a) mixing rice bran, molasses or muscovado sugar, and effective microorganism (EM) and sea salt in sea water and carrying out primary fermentation process, (b) adding fish and rice-soaked water and carrying out secondary fermentation process, (c) adding EM and carrying out tertiary fermentation process, and (d) individually packing and transporting.    USE - The method is useful for manufacturing liquid fertilizer using fish (claimed).    ADVANTAGE - The method ensures complete degradation of the fish bone by carrying out natural fermentation of fish to provide the mineral component required for plant growth, utilizes effective microorganism, which do not require separate culture and thus reduces the production cost, and minimizes the smell generated during fish fermentation.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic process flow for manufacturing liquid fertilizer using fish (Drawing includes non-English language text).
NOVELTY - A nitrogenous fertilizer stabilizer composition comprises 1-60 pts. wt. nitrapyrin, 1-15 pts. wt. capsule wall material, 1-15 pts. wt. emulsifier, 2-10 pts. wt. viscosity regulator, 0.05-0.3 pt. wt. dispersant and 0.1-100 pts. wt. water.    USE - Nitrogenous fertilizer stabilizer composition.    ADVANTAGE - The composition reduces nitrogen leaching which leads to denitrification of nitrogenous fertilizer. It is compatible and can be mixed with insecticide, herbicide and bactericide.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for preparation of nitrogenous fertilizer stabilizer composition comprising heating nitrapyrin at 65-75 degrees C, melting, adding capsule wall material, stirring, adding emulsifier, stirring, high-speed homogenizing to form stable oil-in-water emulsion, reducing rotation speed, polymerizing capsule wall material at 20-80 degrees C, adding dispersant and viscosity regulator and stirring uniformly.
NOVELTY - Manufacture of higher calorific wood composite solid fuel involves pulverizing wood chip, drying in drying oven at 50-120 degrees C for 30 minutes and coating wood chips with resin and then forming polymer/wood chip mixture.    USE - Manufacture of higher calorific wood composite solid fuel (claimed).    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for higher calorific wood composite solid fuel.
NOVELTY - The method involves removing oil from small fragments of solid-state component. Debris is put in water in primary heat treatment process, such that liquid component and solid components are separated from one another. The oil is extracted from the separated liquid component from separation layer in secondary heat treatment process. A bio-diesel is manufactured from the oil. A bio-ethanol is manufactured from the oil through the saccharification and fermentation process.    USE - Method for manufacturing bio-fuel such as bio-diesel and bio-ethanol from garbage and waste of food such as noodles. Can also be used in starch crop of cane, mill, corn, potatoes, barley, ipomoea batatas, cassava, and rice straw.    ADVANTAGE - The bio-fuels are manufactured in economical and environmental-friendly manner. The bio-diesel is biodegradable, and harmless. The bio-diesel is free from sulfur or aromatic compound and cancer causing character pollution element. The expensive oxygen additive is not added. The emission of dust or carbon monoxide is reduced.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for a device for manufacturing bio-fuel.    DESCRIPTION OF DRAWING(S) - The drawing shows a flow diagram illustrating the process of manufacturing bio-fuel. (Drawing includes non-English language text)
NOVELTY - Production of glucose involves steam explosion processing biomass steam plant, immersing in water at 30-90 degrees C, stirring for 1-5 hours after filtering, mixing water, sodium hydroxide, hydrogen peroxide and methanol with a mixture and glycosylating cellulase and beta -glucosidase in the enzymatic hydrolysis.    USE - Production of glucose (claimed).    ADVANTAGE - The glucose is efficiently produced with high efficiency.
NOVELTY - Method for preparing liquid disinfectant, involves dissolving maximum solubility of citric acid in 45-55 pts. wt. hydrogen peroxide, and mixing 10 pts. wt. concentrated hydrogen peroxide, 35-45 pts. wt. water, and 45-55 pts. wt. maximum solubility of citric acid.    USE - The method is useful for preparing liquid disinfectant which is used for providing antibacterial effect (all claimed) and inhibiting foot-and-mouth disease.    ADVANTAGE - The method is environmentally-friendly.
NOVELTY - A clathrate hydrate comprises clathrate hydrate former (I), guest molecule and water as a host molecule.    USE - Clathrate hydrate (claimed).    ADVANTAGE - The clathrate hydrate has excellent water solubility, and is prepared with high purity.    DETAILED DESCRIPTION - A clathrate hydrate comprises clathrate hydrate former of formula (I), guest molecule and water as a host molecule.    R1-R4=H or 1-6C linear or branched alkyl;    X=-(CH2)n-;and    n=1-5.    An INDEPENDENT CLAIM is included for manufacture of clathrate hydrate, which involves freezing mixture of water and clathrate hydrate former, pulverizing, placing the resultant mixture into a pressure chamber, supplying guest molecule, and reacting.
NOVELTY - The system has acid fermenter (500) in which liquid which is fermented is dehydrated. The dehydrated liquid is discharged into flow control bath (400). The organic sludge is flowed in storage hopper (100). A solid material processor (300) processes solid material which is separated from dehydrator (200). The dehydrating liquid which is stored in flow control bath is injected to acid fermenter. The methane fermentation liquid is stored in stabilization bath (700). The methane fermentation liquid which is flowed into digeater (600) is temporarily saved.    USE - Anaerobic digestion system.    ADVANTAGE - The concentration of organic carbon source is maintained reliably. The inflow of methane fermentation liquid is blocked in digeater, such that excessive circulation of enriched water within stabilization bath can be reduced effectively. The stirring ability of fermenter can be improved reliably. The de-enrichment of methane fermentation liquid by digeater is suppressed by high concentration of enriched water. The biogas generation rate can be improved efficiently.    DETAILED DESCRIPTION - An INDEPENDENT CLAIM is included for method for treating organic waste using anaerobic digestion system.    DESCRIPTION OF DRAWING(S) - The drawing shows a schematic view of the anaerobic digestion system. (Drawing includes non-English language text)    Storage hopper (100)    Dehydrator (200)    Solid material processor (300)    Flow control bath (400)    Acid fermenter (500)    Digeater (600)    Stabilization bath (700)